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222-079
DA T A S U B M I T T A L C O M P L I A N C E R E P O R T AP I N o . 50 - 1 0 3 - 2 0 8 4 2 - 0 0 - 0 0 We l l N a m e / N o . KU P A R U K R I V U N I T 3 S - 6 2 5 Co m p l e t i o n S t a t u s WA G I N Co m p l e t i o n D a t e 10 / 2 6 / 2 0 2 2 Pe r m i t t o D r i l l 22 2 0 7 9 0 Op e r a t o r Co n o c o P h i l l i p s A l a s k a , I n c . MD 25 3 1 0 TV D 52 5 3 Cu r r e n t S t a t u s WA G I N 6/ 4 / 2 0 2 5 UI C Ye s We l l L o g I n f o r m a t i o n : Di g i t a l Me d / F r m t Re c e i v e d St a r t S t o p OH / CH Co m m e n t s Lo g Me d i a Ru n No El e c t r Da t a s e t Nu m b e r Na m e In t e r v a l Li s t o f L o g s O b t a i n e d : GR , R E S , D E N , D I R , A Z I , P W D , N E U , P O R , S O N I C No No Ye s Mu d L o g S a m p l e s D i r e c t i o n a l S u r v e y RE Q U I R E D I N F O R M A T I O N (f r o m M a s t e r W e l l D a t a / L o g s ) DA T A I N F O R M A T I O N Lo g / Da t a Ty p e Lo g Sc a l e DF 1/ 4 / 2 0 2 3 26 0 2 5 3 1 0 E l e c t r o n i c D a t a S e t , F i l e n a m e : 3 S - 62 5 _ D r i l l i n g _ M e c h a n i c s _ D e p t h _ R T R M _ 2 6 0 f t - 25 3 1 0 f t . l a s 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 26 0 2 5 3 1 0 E l e c t r o n i c D a t a S e t , F i l e n a m e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R T _ 2 6 0 f t - 2 5 3 1 0 f t . l a s 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 26 0 2 5 3 1 0 E l e c t r o n i c D a t a S e t , F i l e n a m e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R M _ 2 6 0 f t - 2 5 3 1 0 f t . l a s 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 44 8 1 7 4 4 8 2 0 E l e c t r o n i c D a t a S e t , F i l e n a m e : 3 S - 62 5 _ D r i l l i n g _ M e c h a n i c s _ T i m e _ R u n 0 1 . l a s 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 44 8 2 3 4 4 8 3 1 E l e c t r o n i c D a t a S e t , F i l e n a m e : 3 S - 62 5 _ D r i l l i n g _ M e c h a n i c s _ T i m e _ R u n 0 2 . l a s 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 44 8 3 6 4 4 8 5 3 E l e c t r o n i c D a t a S e t , F i l e n a m e : 3 S - 62 5 _ D r i l l i n g _ M e c h a n i c s _ T i m e _ R u n 0 3 . l a s 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 E O W L e t t e r . d o c 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 2 7 E O W C o m p a s s Su r v e y s [ C a n v a s ] . t x t 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 2 7 E O W C o m p a s s Su r v e y s [ M a c r o ] . t x t 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 2 7 E O W C o m p a s s Su r v e y s [ P e t r e l ] . t x t 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 2 7 E O W C o m p a s s Su r v e y s [ S u r v e y s ] . t x t 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 2 7 E O W C o m p a s s Su r v e y s . p d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 8 3 E O W C o m p a s s Su r v e y s [ C a n v a s ] . t x t 37 4 1 2 ED Di g i t a l D a t a We d n e s d a y , J u n e 4 , 2 0 2 5 AO G C C P a g e 1 o f 4 3S - , 625 _ V I S I ON_ S e r v i c e _ RM_2 6 0 f t - 253 10ft . l as DA T A S U B M I T T A L C O M P L I A N C E R E P O R T AP I N o . 50 - 1 0 3 - 2 0 8 4 2 - 0 0 - 0 0 We l l N a m e / N o . KU P A R U K R I V U N I T 3 S - 6 2 5 Co m p l e t i o n S t a t u s WA G I N Co m p l e t i o n D a t e 10 / 2 6 / 2 0 2 2 Pe r m i t t o D r i l l 22 2 0 7 9 0 Op e r a t o r Co n o c o P h i l l i p s A l a s k a , I n c . MD 25 3 1 0 TV D 52 5 3 Cu r r e n t S t a t u s WA G I N 6/ 4 / 2 0 2 5 UI C Ye s DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 8 3 E O W C o m p a s s Su r v e y s [ M a c r o ] . t x t 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 8 3 E O W C o m p a s s Su r v e y s [ P e t r e l ] . t x t 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 8 3 E O W C o m p a s s Su r v e y s [ S u r v e y s ] . t x t 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 N A D 8 3 E O W C o m p a s s Su r v e y s . p d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ D r i l l i n g _ M e c h a n i c s _ D e p t h _ R T R M _ 2 M D _ 2 6 0 ft - 2 5 3 1 0 f t . p d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R T _ 2 M D _ 2 6 0 f t - 25 3 1 0 f t . p d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R T _ 2 T V D _ 2 6 0 f t - 25 3 1 0 f t . p d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R T _ 5 M D _ 2 6 0 f t - 25 3 1 0 f t . p d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R T _ 5 T V D _ 2 6 0 f t - 25 3 1 0 f t . p d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R M _ 2 M D _ 2 6 0 f t - 25 3 1 0 f t . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R M _ 2 T V D _ 2 6 0 f t - 25 3 1 0 f t . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R M _ 5 M D _ 2 6 0 f t - 25 3 1 0 f t . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ V I S I O N _ S e r v i c e _ R M _ 5 T V D _ 2 6 0 f t - 25 3 1 0 f t . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ D r i l l i n g _ M e c h a n i c s _ T i m e _ R u n 0 1 . P d f 37 4 1 2 ED Di g i t a l D a t a We d n e s d a y , J u n e 4 , 2 0 2 5 AO G C C P a g e 2 o f 4 DA T A S U B M I T T A L C O M P L I A N C E R E P O R T AP I N o . 50 - 1 0 3 - 2 0 8 4 2 - 0 0 - 0 0 We l l N a m e / N o . KU P A R U K R I V U N I T 3 S - 6 2 5 Co m p l e t i o n S t a t u s WA G I N Co m p l e t i o n D a t e 10 / 2 6 / 2 0 2 2 Pe r m i t t o D r i l l 22 2 0 7 9 0 Op e r a t o r Co n o c o P h i l l i p s A l a s k a , I n c . MD 25 3 1 0 TV D 52 5 3 Cu r r e n t S t a t u s WA G I N 6/ 4 / 2 0 2 5 UI C Ye s We l l C o r e s / S a m p l e s I n f o r m a t i o n : Re c e i v e d St a r t S t o p C o m m e n t s To t a l Bo x e s Sa m p l e Se t Nu m b e r Na m e In t e r v a l IN F O R M A T I O N R E C E I V E D Co m p l e t i o n R e p o r t Pr o d u c t i o n T e s t I n f o r m a t i o n Ge o l o g i c M a r k e r s / T o p s Y Y / N A Y Mu d L o g s , I m a g e F i l e s , D i g i t a l D a t a Co m p o s i t e L o g s , I m a g e , D a t a F i l e s Cu t t i n g s S a m p l e s Y / N A Y Y / N A Di r e c t i o n a l / I n c l i n a t i o n D a t a Me c h a n i c a l I n t e g r i t y T e s t I n f o r m a t i o n Da i l y O p e r a t i o n s S u m m a r y Y Y / N A Y Co r e C h i p s Co r e P h o t o g r a p h s La b o r a t o r y A n a l y s e s Y / N A Y / N A Y / N A CO M P L I A N C E H I S T O R Y Da t e C o m m e n t s De s c r i p t i o n Co m p l e t i o n D a t e : 10 / 2 6 / 2 0 2 2 Re l e a s e D a t e : 7/ 1 8 / 2 0 2 2 DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ D r i l l i n g _ M e c h a n i c s _ T i m e _ R u n 0 2 . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 62 5 _ D r i l l i n g _ M e c h a n i c s _ T i m e _ R u n 0 3 . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 _ V I S I O N Se r v i c e _ R T R M _ 2 6 0 f t - 2 5 3 1 0 f t . d l i s 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : 3 S - 6 2 5 _ V I S I O N Se r v i c e _ R T R M _ 2 6 0 f t - 2 5 3 1 0 f t . h t m l 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : C P A I _ 3 S - 62 5 _ S o n i c S c o p e 4 7 5 _ T O C _ 1 0 0 0 _ R M . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : C P A I _ 3 S - 62 5 _ S o n i c S c o p e 4 7 5 _ T O C _ 2 0 0 _ R M . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : C P A I _ 3 S - 62 5 _ S o n i c S c o p e 4 7 5 _ T O C _ 4 0 0 0 _ R M . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : C P A I _ 3 S - 62 5 _ S o n i c S c o p e 4 7 5 _ T O C _ 5 0 0 _ R M . P d f 37 4 1 2 ED Di g i t a l D a t a DF 1/ 4 / 2 0 2 3 E l e c t r o n i c F i l e : C P A I _ 3 S - 62 5 _ S o n i c S c o p e 4 7 5 _ T O C _ 6 0 0 0 _ R M . P d f 37 4 1 2 ED Di g i t a l D a t a We d n e s d a y , J u n e 4 , 2 0 2 5 AO G C C P a g e 3 o f 4 DA T A S U B M I T T A L C O M P L I A N C E R E P O R T AP I N o . 50 - 1 0 3 - 2 0 8 4 2 - 0 0 - 0 0 We l l N a m e / N o . KU P A R U K R I V U N I T 3 S - 6 2 5 Co m p l e t i o n S t a t u s WA G I N Co m p l e t i o n D a t e 10 / 2 6 / 2 0 2 2 Pe r m i t t o D r i l l 22 2 0 7 9 0 Op e r a t o r Co n o c o P h i l l i p s A l a s k a , I n c . MD 25 3 1 0 TV D 52 5 3 Cu r r e n t S t a t u s WA G I N 6/ 4 / 2 0 2 5 UI C Ye s Co m m e n t s : Co m p l i a n c e R e v i e w e d B y : Da t e : We d n e s d a y , J u n e 4 , 2 0 2 5 AO G C C P a g e 4 o f 4 6/ 4 / 2 0 2 5 M. G u h l MEMORANDUM State of Alaska Alaska Oil and Gas Conservation Commission DATE:Wednesday, April 5, 2023 SUBJECT:Mechanical Integrity Tests TO: FROM:Austin McLeod P.I. Supervisor Petroleum Inspector NON-CONFIDENTIAL ConocoPhillips Alaska, Inc. 3S-625 KUPARUK RIV UNIT 3S-625 Jim Regg InspectorSrc: Reviewed By: P.I. Suprv Comm ________ JBR 04/05/2023 3S-625 50-103-20842-00-00 222-079-0 W SPT 5051 2220790 1500 525 525 525 525 750 785 773 771 INITAL P Austin McLeod 3/1/2023 MITIA. Producer-Injector conversion. Sundry 322-056. 30 MinPretestInitial15 Min Well Name Type Test Notes: Interval P/F Well Permit Number: Type Inj TVD PTD Test psi API Well Number Inspector Name:KUPARUK RIV UNIT 3S-625 Inspection Date: Tubing OA Packer Depth 1040 1810 1775 1770IA 45 Min 60 Min Rel Insp Num: Insp Num:mitSAM230302112921 BBL Pumped:1.3 BBL Returned:1.3 Wednesday, April 5, 2023 Page 1 of 1 9 9 9 9 9 9 9 9 9 9 9 9 James B. Regg Digitally signed by James B. Regg Date: 2023.04.05 15:48:06 -08'00' STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIONS RECEIVED By Kayla Junke at 10:32 am, Mar 28, 2023 1. Operations Susp Well Insp❑ Plug Perforations ❑ Fracture Stimulate Q Pull Tubing ❑ Operations shutdown ❑ Performed: Install Whipstock❑ Perforate ❑ Other Stimulate ❑ Alter Casing ❑ Change Approved Program ❑ Mod Artificial Lift❑ Perforate New Pool ❑ Repair Well ❑ Coiled Tubing Ops ❑ Other: ❑ 2. Operator Name 4. Well Class Before Work: 5. Permit to Drill Number: Conocophillips Alaska, Inc Development ❑ Exploratory ❑ Stratigraphic ❑ Service 0 222-079 3. Address: P.O. Box 100360, Anchorage, AK 99510 6. API Number: 50-103-20842-00-00 7. Property Designation (Lease Number): 8. Well Name and Number: ADL 025528, ADL 025544, ADL 380107 KRU 3S-625 9. Logs (List logs and submit electronic data per 20AAC25.071): 10. Field/Pool(s): Ku aruk River Unit / Torok Oil Pool 11. Present Well Condition Summary: Total Depth measured 25310 feet Plugs measured None feet true vertical 5253 feet Junk measured None feet Effective Depth measured 25247.1 feet Packer measured 12516.5 feet true vertical 5253 feet true vertical 5051.5 feet Casing Length Size MD TVD Burst Collapse Structural Conductor 94 20 131 131 Surface 2858.3 10.75 2895.3 2573.5 5210 2470 Intermediate 12248.8 7.625 12285.8 5017.9 6890 4790 Intermediate 556.2 7.625 12842 5093 10860 7850 Liner 12614 4.5 25306 5258.7 8430 7500 Perforation depth Measured depth feet Frac sleeve depths attached below True Vertical depth feet attached below Tubing (size, grade, measured and true vertical depth) 4.5 L-80 (12.6 ppf) 12701.9 5075.4 Packers and SSSV (type, measured and true vertical depth) HAL TNT Prod Packer 12516.5 5054.1 12. Stimulation or cement squeeze summary: Intervals treated (measured): Stimulation details attached below Treatment descriptions including volumes used and final pressure: Attached below 13a. Representative Daily Average Production or Injection Data Oil-BbI Gas-Mcf I Water-BbI Casing Pressure Tubing Pressure Prior to well operation: 10 10 10 10 11027 Subsequent to operation:0 10 176,193 INJECTED 10 1400 (1211) 131b. Pools active after work: Torok Oil Pool 14. Attachments (required per 20 AAC 25.070, 25.071, a 25.283) 15. Well Class after work: Daily Report of Well Operations ❑✓ Exploratory ❑ Development[] Service Stratigraphic ❑ Copies of Logs and Surveys Run ❑ 16. Well Status after work: Oil Gas WDSPL Electronic Fracture Stimulation Data ❑� GSTOR ❑ WINJ ❑ WAG 0 GINJ SUSP ❑ SPLUG 17. 1 hereby certify that the foregoing is true and correct t0 the best of my knowledge. Sundry Number or N/A if C.O. Exempt: DocuSigned by: Authorized Name and F Mar-27-2023 Digital Signature with Date: Contact Name: Contact Email: Authorized Title: Contact Phone: Sr Pet Eng: ISr Pet Geo: I 1SrResEng: DSR-3/28/23 CDW 03/29/2023 Form 10-404 Revised 1012022 Due Within 30 days of Operations Submit in PDF format to aogcc.permitting@alaska.gov RBDMS JSB 033023 u � u� ui vl N N N Yi N Vi ill vl N N Vi Yi J1 v1 N N Vi u� ui vl E p a d v C o v m E � �I �1 ti @ �i � w ti rl rr1 �i rl •i P � N � N ry N N N [QV N � N Lry F n v C o F J1 N N N N N ✓i N Vi N ill Vi N N Vi � N N ill N N N Vi N N N L W a v v n a r aN F. $ Q Ni P@ � N n M1 fi � R N �+ P P O C• M P@ n n v v D 1- q� I Y Y} Y Y Y C7 Y Y Y Y 0 � O Cl ❑ � Cl � � ^ 'n Yl V v S S v R T II h A R Q R T S R R R— 4 3— S— —= F F F F m m ry ry j �% 1- 6 4 a " 6 m v w m v v v v m v v v v v m m v v m O E N VI N N N N N �/I N N N VI N m N N N VI N N I v P ul I 0 i x 0 Y x 0 Y x 0 Y x 0 Y x 0 Y x 0 Y x ©a Y x Y x o Y x 0 Y x 0 Y x 0 Y x 0 Y x ©o Y x Y x 0 Y x 0 Y x 0 Y x 0 Y x 0 Y x 0 Y x ©o Y x Y x 0 Y x 0 Y x c P@ v c P Q Q P P P P a Q P a a a P a a Q P a a@ f V� ti o n ti o 0 0 o n o a o 0 o a a o n a o 0 0 o n o 0 v x x x x x x x x x x x x x x x x x x x x x x x x x S 0 0 V@ P V@@ P Q@ Q P P P@ Q P P Q C P@@ F�5 Q P@ 5 Q V rH O .O 2 m m2 t2 I n 'v �i I@ P V@ m m m P W m P m N P m P Na Iv, r m m m r o C a E I� m M m m� $ '� M 2 a C C O d' C O 4 C C d d' d O d' 4 C C V d• y W N W ✓i do v E v � N } N C Jai Q N n y 3 m v N� v W v W v v, �1 } N v v W 0� v� W pT! v W W �1 � W �O y E d W m LI W v u v v 4� W W u l W W W V Zfi . 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O W0 W W W W W Z a W W mm 00m C�C7 C� ���m C7 C7FfnW ��a�am UC7 u. ��w ZZ oa d a J J U y w mmm W m N J F U W m m Q 0 W w W W W w W W I Z m gaaof gaa3o(Dgao 3° a¢O »>0 »W xLLo »U O~ H rja 22MX 22 CO) Xa 2mQKU O� 3az mmrn_z mm3LLU? m0 �lJi g O r N r p r N N p 1p r Ea E" U O O O N O �O N O N O C Sq M � M V N N O E U N C C C C C 3 3 3 3 U5 d U d U d U d U d lL IL IL IL LL xO xO xO xO O 8 p t O N O N O N O N O N in5 o N r N m N rn N o M H ALLI B U RTO N Sales Order# 0908229115 Conoco Phillips 3S-625 Intervals 1-24 Kuparuk Torok Formation Harrison Bay County, AK API: 50-103-20842 Prepared for: Dustin Morrow November 29, 2022 Stimulation Treatment Post Job Report 30# Hybor G Prepared By: Keegan Lambe James Campbell Nannook Crew Notice: Although the information contained in this report is based on sound engineering practices, the copyright owner(s) does (do) not accept any responsibility whatsoever, in negligence or otherwise, for any loss or damage arising from the possession or use of the report whether in terms of correctness or otherwise. The application, therefore, by the user of this report or any part thereof, is solely at the users own risk. Nwu.�wwroN �� 5 PIM, Conoco Phillips - 35-625 TOC Engineering Executive Summary On November 16, 2022 a stimulation treatment was performed in the Torok formation on the 3S-625 well in Harrison Bay County, AK. The 35-625 was a 24 stage Horizontal Sleeve Design. The proposed treatment consisted of: 2,883,935 gallons of 30# Hybor G 451,318 gallons of 30# Linear 0 gallons of Seawater 20,000 gallons of Potassium Formate 4,800,000 pounds of Wanli 16/20 Ceramic The actual treatment fully completed 21 of 24 stages. 2 stages were skipped, 1 was cut short of design. The actual treatment consisted of: 2,731,582 gallons of 30# Hybor G 436,236 gallons of 30# Linear 32,262 gallons of Seawater 20,942 gallons of Potassium Formate 4,264,741 pounds of Wanli 16/20 Ceramic A more detailed description of the actual treatment can be found in the attached reports. The following comments were provided to summarize events and changes to the proposed treatment: The initial planned designed was adjusted based on the results of the minifrac and DFIT's performed. Adjusted the chemical loadings as needed to maintain a fluid system. Interval 3 and 5 were skipped due to no ball seat observed. Interval 9 was cut short of design due to an issue with the missile that required flushing the well. Halliburton is strongly committed to quality control on location. Before and after each job all chemicals, proppants, and fluid volumes are measured to assure the highest level of quality control. Tank fluid analysis, crosslink time, and break tests are performed before each job in order to optimize the performance of the treatment fluids. Halliburton maintains a continuous quality improvement process and appreciates any comments or suggestions that you may have. Halliburton again thanks you for the opportunity to perform service work on this well. We hope to be your solutions provider for future projects. Thank you, Keegan Lambe Senior Technical Professional Halliburton Energy Services Conoco Phillips - 35-625 Executive Summary �<aa¢a¢a¢aaaaaaaaaaaaaa ge9 zzzzizizizzzzzzzzzzzzz �e5 zzzzzzzzzzzzzzzzzzzzzz 5p— a � �C�FSe�mmm0� m$mmmmmmmmmmmm�nnnn '�= m Er — �W�m��prWrWRn::AA:B:S:"�S iFiSia^�a Ra�.�$Cm„Rge m m 3a_ s s 0 o�N$�ona$a e.nm n'�mmr'"�m m E£ v vivi�iaFa2aiaFaFaia cg assssssa<$f$f<f$<$f$f€f s o8�0.8 Sg8 -g a.g 8 g-gg �.ga.$a. ag `g i a s a s a s a a a a a a a s s s s s s s s s as e. s . .............. ... ... ... ... ... 99999999999aaaaaaaaaaaaa g aaaaaaaaaaaaaaaaaaaaaaaa x YxYxYYYYYYy�y�yxyxyxyxy R € .........y xy xy xy xy xy xy qq m nnnnyn nnm fi 269 n m am.R.^ �e nQmn�m". v.^omem�rmr. es" mam :E noon n"n"n"n" s R a s a N 2 e� 5 3 m oO0 OOOO 600 6666666.... 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ML4100t✓�BBIL� l.Y01 sVueS h-.dnN sVusS MIUW. sVueS h�ueJnN sPu TUW^N spu lm r-` BHeuaryl 611 e. oz ....l a1...l alevqul m \\ !| `§l9988e89eeg8 §{!! §!!!!|!\ !!!!!!!! ! )!!!! 1,� .................... . })!i!!!!!!!!!ii!!!;;!!;! } �!9 !!!irr !!!!! §!!,!!!! �/gggR\RRRRb/ mom zun� Start Date/Time: 11/17/22 16:02 End Date/Time: 11/17/22 17:51 Pump Time: 109 min Initial Rate (Breakdown): NA bpm Initial Surface Pressure (Breakdown): NA psi Initial BH Pressure (Breakdown): NA psi Max Rate: 37.4 bpm Max Surface Pressure: 5,162 psi Max BH Pressure: NA psi Average Rate: 32.4 bpm Average Missile Pressure: 4,308 psi Average Surface Pressure: 4,435 psi Average BH Pressure: NA psi Average Missile HHP: 3,423 hhp Initial CA Pressure: 298 psi Max OA Pressure: 521 psi Max Proppant Concentration: 5.38 Ppg Average Visc: 29.8 CID Average Temp: 72.36 F Average pH: 9.24 Proppant Summary Wanli 16/20 Ceramic Pumped: 195,931 Ibs 100M Pumped: 6,902 Ibs Total Proppant Pumped' : 202,833 Ibs Proppant in Formation: 202,833 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 209,431 gal 4,986 bbls 30# Linear Volume: 63,615 gal 1,515 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 2,640 gal 63 bbls Fluid Summary (by stage description) Pad Volume: 25,110 gal 598 bbls Conditioning Pad Volume: 22,486 gal 535 bbls Proppant Laden Fluid Volume: 72,389 gal 1,724 bbls Displacement Volume: 20,207 gal 481 bbls Flush Volume: 33,312 gal 793 bbls Freeze Protect Volume: 630 gal 15 bbls Step Rate Test Volume: 9,922 gal 236 bbls Establish Stable Fluid Volume: 62,577 gal 1,490 bbls Minifrac Volume: 25,307 gal 603 bbls Alpha Sleeve Volume: 174 gal 4 bbls Spacer and Ball Drop Volume: 1,562 gal 37 bbls Interval Status: Completed Conoco Phillips - 35-625 Interval Summary 11 Mips! prior to working on the alpha sleeve. Alpha sleeve burst at 6389psi surface pressure, assure after bursting Alpha was 1027psi. Pumped the swept. eADP would not communicate with rest of the fleet, pumped the tub of gel away manually. While dealing with the eADP the DHG ssure data was interrupted. Tried to diagnose the problem and swapped cables, but pressure idings continued to be interrupted. Shut down after flushing the surface lines from gel. Wellhead opened at 08:54am on the 17th. Opened at 607psi on wellhead. Started step rate test. After nping the minifrac the first time determined the gel loading was lower than expected. Worked a backup fluid including CL-31. Pumped a second minifrac with targeted viscosity to a better ult. Started interval 01 once confirming water on location. DH gauge box was swapped after the =d minifrac. Targeted a pH of 9.3. Pumped the first interval to proppant design. from software calculations based on Treater Greg Koester Supervisor: Greg Koester Customer Rep. Conoco Phillips - 35-625 Interval Summary 12 Start Dateffime: 11/17/22 17:51 End Date/Time: 11/18/22 13:00 Pump Time: 1149 min Initial Rate (Breakdown): 9.2 bpm Initial Surface Pressure (Breakdown): 4,829 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 37.2 bpm Max Surface Pressure: 5,714 psi Max BH Pressure: NA psi Average Rate: 26.8 bpm Average Missile Pressure: 3,624 psi Average Surface Pressure: 3,746 psi Average BH Pressure: NA psi Average Missile HHP: 2,384 hhp Initial OA Pressure: 367 psi Max CA Pressure: 616 psi Max Proppant Concentration: 4.97 Pp9 Average Visc: 31.5 cP Average Temp: 86.9 F Average pH: 9.3 Proppant Summary Wanli 16/20 Ceramic Pumped: 197,540 Ibs 100M Pumped: 7,100 Ibs Total Proppant Pumped' : 204,640 Ibs Proppant in Formation: 204,640 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 159,967 gal 3,809 bbls 30# Linear Volume: 31,303 gal 745 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 654 gal 16 bbls Fluid Summary, (by stage description) Pad Volume: 47,652 gal 1,135 bbls Conditioning Pad Volume: 24,570 gal 585 bbls Proppant Laden Fluid Volume: 78,131 gal 1,860 bbls Flush Volume: 16,338 gal 389 bbls Establish Stable Fluid Volume: 21,548 gal 513 bbls Spacer and Ball Drop Volume: 3,031 gal 72 bbls Conoco Phillips - 35-625 Interval Summary 13 Interval Status: Completed tea Interval uz on 1111 /. Uroppea the nail and aid not see a nit. Average rate was 1 /.bbdpm, rage surface pressure was 3185psi average truck pressure was 3069psi. Max rate was 15bpm, max surface pressure was 4400psi, max truckside pressure was 4287psi. Attempted to ball to seat through rate changes. decision was made to flush the well and try again the next ling. Initial CA pressure was 500psi max was 521 psi during the initial ball drop. Pumped bbl clean for the first attempt. Well was reopened on 11/18 at 10:15am to 826psi surface ;sure 2727psi. Ball was dropped off the swab. During the initial injection the blender had a raulic leak on the DA. Swapped to the ADP to displace as ball was free falling. Recovered the later and continued to displace ball. Held rate at 15bpm remainder of displacement. Did not t crosslink due until after ball seated due to lower rate and confirming ball seat. All proppant sped. During the slowdown and waiting on ball seat the primary IFS server crashed. No ball t was observed. flushed the well from the crosslink at low rate. Shut down and diagnosed IFS rer while also vac out tree to check for ball in wellhead. No ball observed in wellhead, dropped kuo ball on the swab. for proppant are taken from software calculations based on multiple variables. it is billed off of weight ticket volumes and may vary slightly from this number. tngmeer. Keegan Lambe Treater Greg Koester Supervisor: Greg Koester Customer Engineer: Customer Rep: Conoco Phillips - 35-625 Interval Summary 14 3S-625 - Kuparuk - Interval 3 Interval Summary Start Dateffime: 11/18/22 14:44 End Date/Time: 11/19/22 14:58 Pump Time: 1454 min Initial Rate (Breakdown): NA bpm Initial Surface Pressure (Breakdown): NA psi Initial BH Pressure (Breakdown): NA psi Max Rate: 21.7 bpm Max Surface Pressure: 3,785 psi Max BH Pressure: NA psi Average Rate: 16.2 bpm Average Missile Pressure: 2,759 psi Average Surface Pressure: 2,871 psi Average BH Pressure: NA psi Average Missile HHP: 1,098 hhp Initial CA Pressure: 492 psi Max CA Pressure: 590 psi Max Proppant Concentration: 0.00 PP9 Fluid Summary (by fluid description) 30# Hybor G Volume: 16,940 gal 403 bbls 30# Linear Volume: 65,350 gal 1,556 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 1,102 gal 26 bbls Fluid Summary (by stage description) Pad Volume: 16,940 gal 403 bbls Conditioning Pad Volume: 0 gal 0 bbls Proppant Laden Fluid Volume: 0 gal 0 bbls Displacement Volume: 45,893 gal 1,093 bbls Flush Volume: 18,248 gal 434 bbls Freeze Protect Volume: 504 gal 12 bbls Spacer and Ball Drop Volume: 1,209 gal 29 bbls Interval Status: Skipped mat Dan nit ooservea, aroppea oacKup Dan on swan. uispiacea wim nnear get to mini ze engineer. Keegan Lamt displacement of previous stage. Restarted interval 3 at 14:44, no ball hit was observed on the Treater Greg Koester id drop. On 11/19 a second riser was rigged up on the surface lines. Dropped the third ball gh the ball launcher mimicking between stage drops. Well opened at 13:57 to 815psi. No ball Supervisor: Greg Koester as observed. dropped ball for interval 4 and skipped interval 3. Conoco Phillips - 3S-625 Interval Summary 15 3S-625 - Kuparuk - Interval 4 Interval Summary Start Date/Time: 11/19/22 14:58 End Date/Time: 11/19/22 17:13 Pump Time: 135 min Initial Rate (Breakdown): 9.4 bpm Initial Surface Pressure (Breakdown): 5,024 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 37.2 bpm Max Surface Pressure: 5,266 psi Max BH Pressure: NA psi Average Rate: 30.5 bpm Average Missile Pressure: 3,692 psi Average Surface Pressure: 3,804 psi Average BH Pressure: NA psi Average Missile HHP: 2,760 hhp Initial CA Pressure: 589 psi Max CA Pressure: 689 psi Max Proppant Concentration: 5.01 PPg Average Visc: 35 cP Average Temp: 82.5 F Average pH: 9 Proppant Summary Wanli 16120 Ceramic Pumped: 202,041 Its 100M Pumped: 7,100 Ibs Total Proppant Pumped' : 209,141 Ibs Proppant in Formation: 209,141 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 131,445 gal 3,130 bbls 30# Linear Volume: 16,584 gal 395 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 0 gal 0 bbls Fluid Summary (by stage description) Pad Volume: 25,159 gal 599 bbls Conditioning Pad Volume: 25,203 gal 600 bbls Proppant Laden Fluid Volume: 74,413 gal 1,772 bbls Displacement Volume: 15,834 gal 377 bbls Establish Stable Fluid Volume: 5,431 gal 129 bbls Spacer and Ball Drop Volume: 1,989 gal 47 bbls Interval Status: Completed rate responses from the pumps. Gel viscosity had creeped up significantly, reduced gel visc pumps started to line out. Proppant pumped to design for proppant are taken from software calculations based on multiple variables. it is billed off of weight ticket volumes and may vary slightly from this number. Treater. Greg Koester Supervisor: Greg Koester Customer Engineer: Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 16 3S-625 - Kuparuk - Interval 5 Interval Summary Start DateTrime: 11/19/22 17:13 End Date/Time: 11/20/22 13:37 Pump Time: 1224 min Initial Rate (Breakdown): NA bpm Initial Surface Pressure (Breakdown): NA psi Initial BH Pressure (Breakdown): NA psi Max Rate: 21.2 bpm Max Surface Pressure: 3,512 psi Max BH Pressure: NA psi Average Rate: 10.5 bpm Average Missile Pressure: 1,757 psi Average Surface Pressure: 1,887 psi Average BH Pressure: NA psi Average Missile HHP: 453 hhp Initial CA Pressure: 391 psi Max CA Pressure: 603 psi Max Proppant Concentration: NA Pp9 Proppant Summary Wanli 16/20 Ceramic Pumped: 0 Ibs 100M Pumped: 0 Ibs Total Proppant Pumped* : 0 Ibs Proppant in Formation: 0 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 17,280 gal 411 bbls 30# Linear Volume: 48,380 gal 1,152 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 798 gal 19 bbls Fluid Summary (by stage description) Pad Volume: 17,280 gal 411 bbls Conditioning Pad Volume: 0 gal 0 bbls Proppant Laden Fluid Volume: 0 gal 0 bbls Displacement Volume: 31,473 gal 749 bbls Flush Volume: 14,925 gal 355 bbls Spacer and Ball Drop Volume: 1,982 gal 47 bbls DFIT Volume: 0 gal 0 bbls Interval Status: Skipped uroppea Dail Tor stage o, no Dail Tin odservea. i-lusnea the well ana snut down. vvenneaa engineer. Keegan Lambe reopened at 12:20 to 922psi. Rate was established and the backup ball was launched. Backup Treater Greg Koester backup ball loaded and launched. Backup Backup ball was not observed landing. Moved on to interval 6 Supervisor: Greg Koester Customer Engineer. `Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 17 35-625 - Kuparuk - interval 6 Interval Summary Start DatelTime: 11/20/22 13:37 End Date/Time: 11/20/22 15:53 Pump Time: 136 min Initial Rate (Breakdown): 10.0 bpm Initial Surface Pressure (Breakdown): 5,129 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 36.6 bpm Max Surface Pressure: 4,700 psi Max BH Pressure: NA psi Average Rate: 32.6 bpm Average Missile Pressure: 3,493 psi Average Surface Pressure: 3,623 psi Average BH Pressure: NA psi Average Missile HHP: 2,793 hhp Initial CIA Pressure: 603 psi Max CA Pressure: 673 psi Max Proppant Concentration: 5.26 Pp9 Average Visc: 28 CID Average Temp: 82.8 F Average pH: 9.1 Proppant Summary Wanli 16/20 Ceramic Pumped: 191,822 Ibs 100M Pumped: 6,836 Ibs Total Proppant Pumped* : 198,658 Ibs Proppant in Formation: 198,658 Ibs Fluid Summary (by Fluid description) 30# Hybor G Volume: 136,818 gal 3,258 bbls 30# Linear Volume: 15,568 gal 371 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 0 gal 0 bbls Fluid Summary (by stage description) Pad Volume: 25,254 gal 601 bbls Conditioning Pad Volume: 28,927 gal 689 bbls Proppant Laden Fluid Volume: 71,898 gal 1,712 bbls Displacement Volume: 13,880 gal 330 bbls Establish Stable Fluid Volume: 10,739 gal 256 bbls Spacer and Ball Drop Volume: 1,688 gal 40 bbls DFIT Volume: 0 gal 0 bbls Interval Status: Completed stall seat was observed [tsool early. Interval pumped to design. Lngineer. Keegan Lambe Treater Greg Koester Supervisor: Greg Koester *Values for proppant are taken from software calculations based on multiple variables. Customer Engineer. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 18 3S-625 - Kuparuk - Interval 7 Interval Summary Start Date/Time: 11/20/22 15:53 End Date/Time: 11/20/22 17:50 Pump Time: 117 min Initial Rate (Breakdown): 9.2 bpm Initial Surface Pressure (Breakdown): 5,170 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 37.1 bpm Max Surface Pressure: 4,598 psi Max BH Pressure: NA psi Average Rate: 33.8 bpm Average Missile Pressure: 3,518 psi Average Surface Pressure: 3,653 psi Average BH Pressure: NA psi Average Missile HHP: 2,916 hhp Initial CA Pressure: 633 psi Max CA Pressure: 696 psi Max Proppant Concentration: 5.25 PPg Average Visc: 27 cP Average Temp: 85.7 F Average pH: 9 Proppant Summary Wanli 16120 Ceramic Pumped: 198,180 Its 100M Pumped: 7,195 Ibs Total Proppant Pumped' : 205,375 Ibs Proppant in Formation: 205,375 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 141,641 gal 3,372 bbls 30# Linear Volume: 28,866 gal 687 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 0 gal 0 bbls Fluid Summary (by stage description) Pad Volume: 25,084 gal 597 bbls Conditioning Pad Volume: 29,481 gal 702 bbls Proppant Laden Fluid Volume: 76,217 gal 1,815 bbls Displacement Volume: 14,956 gal 356 bbls Flush Volume: 13,910 gal 331 bbls Establish Stable Fluid Volume: 10,859 gal 259 bbls Interval Status: Completed LA. During 3ppg Had issues after swapping with the CT pump but was able to transfer al to complete the interval. Held 3ppg long until samples were confirmed. Little Red Freeze well after frac. for proppant are taken from software calculations based on multiple variables. it is billed off of weight ticket volumes and may vary slightly from this number. Treater. Greg Koester Supervisor: Greg Koester Customer Engineer: Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 19 3S-625 - Kuparuk - Interval 8 Interval Summary Start Date/Time: 11/21/22 14:04 End Date/Time: 11/21/22 16:21 Pump Time: 137 min Initial Rate (Breakdown): 10.0 bpm Initial Surface Pressure (Breakdown): 5,130 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 38.8 bpm Max Surface Pressure: 4,427 psi Max BH Pressure: NA psi Average Rate: 34.2 bpm Average Missile Pressure: 3,574 psi Average Surface Pressure: 3,651 psi Average BH Pressure: NA psi Average Missile HHP: 2,995 hhp Initial CA Pressure: 421 psi Max CA Pressure: 622 psi Max Proppant Concentration: 5.18 PPg Average Visc: 28 CID Average Temp: 80.3 F Average pH: 9.1 Proppant Summary Wanli 16120 Ceramic Pumped: 189,620 Its 100M Pumped: 6,939 Ibs Total Proppant Pumped' : 196,559 Ibs Proppant in Formation: 196,559 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 144,831 gal 3,448 bbls 30# Linear Volume: 14,976 gal 357 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 641 gal 15 bbls Fluid Summary (by stage description) Pad Volume: 26,558 gal 632 bbls Conditioning Pad Volume: 29,419 gal 700 bbls Proppant Laden Fluid Volume: 81,604 gal 1,943 bbls Displacement Volume: 12,787 gal 304 bbls Establish Stable Fluid Volume: 7,250 gal 173 bbls Spacer and Ball Drop Volume: 2,189 gal 52 bbls Interval Status: Completed stepped back into stage. After running 4ppg stage out, added a 4.5ppg stage to make up the ,pant missed in 3ppg. for proppant are taken from software calculations based on multiple variables. it is billed off of weight ticket volumes and may vary slightly from this number. Treater. Greg Koester Supervisor: Greg Koester Customer Engineer: Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 20 3S-625 - Kuparuk - Interval 9 Interval Summary Start Date/Time: 11/21/22 16:21 End Date/Time: 11/21/22 17:47 Pump Time: 86 min Initial Rate (Breakdown): 12.6 bpm Initial Surface Pressure (Breakdown): 5,106 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 36.9 bpm Max Surface Pressure: 4,080 psi Max BH Pressure: NA psi Average Rate: 33.7 bpm Average Missile Pressure: 3,487 psi Average Surface Pressure: 3,412 psi Average BH Pressure: NA psi Average Missile HHP: 2,882 hhp Initial CA Pressure: 622 psi Max CA Pressure: 688 psi Max Proppant Concentration: 3.07 PPg Average Visc: 27 cP Average Temp: 79.9 F Average pH: 9.1 Proppant Summary Wanli 16120 Ceramic Pumped: 78,546 Its 100M Pumped: 7,203 Ibs Total Proppant Pumped' : 85,749 Ibs Proppant in Formation: 85,749 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 113,942 gal 2,713 bbls 30# Linear Volume: 25,865 gal 616 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 0 gal 0 bbls Fluid Summary (by stage description) Pad Volume: 35,068 gal 835 bbls Conditioning Pad Volume: 28,830 gal 686 bbls Proppant Laden Fluid Volume: 42,327 gal 1,008 bbls Displacement Volume: 12,320 gal 293 bbls Flush Volume: 13,545 gal 323 bbls Establish Stable Fluid Volume: 7,717 gal 184 bbls Interval Status: Cut Short ige, a bracket on the low pressure side of the missile was noticed to be broken. Cut sand at the pper and cleaned up. During flush lost a right angle drive on a pump. Continued to Flush the well 30bpm. flues for proppant are taken from software calculations based on multiple variables. fppant is billed off of weight ticket volumes and may vary slightly from this number. Treater. Greg Koester Supervisor: Greg Koester Customer Engineer: Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 21 35-625 - Kuparuk - Interval 10 Interval Summary Start DatelTime: 11/22/22 19:03 End Date/Time: 11/23/22 14:02 Pump Time: 1139 min Initial Rate (Breakdown): 10.9 bpm Initial Surface Pressure (Breakdown): 5,322 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 36.1 bpm Max Surface Pressure: 4,612 psi Max BH Pressure: NA psi Average Rate: 32.6 bpm Average Missile Pressure: 3,542 psi Average Surface Pressure: 3,559 psi Average BH Pressure: NA psi Average Missile HHP: 2,827 hhp Initial CA Pressure: 453 psi Max CA Pressure: 603 psi Max Proppant Concentration: 7.56 PP9 Average Visc: 29 CP Average Temp: 82 F Average pH: 9.2 Proppant Summary Wanli 16/20 Ceramic Pumped: 198,239 Ibs 100M Pumped: 6,833 Ibs Total Proppant Pumped' : 205,072 Ibs Proppant in Formation: 205,072 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 134,310 gal 3,198 bbls 30# Linear Volume: 14,775 gal 352 bbls Seawater Volume: 20,460 gal 487 bb/s Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 1,632 gal 39 bbls Fluid Summary (by stage description) Pad Volume: 24,931 gal 594 bbls Conditioning Pad Volume: 30,230 gal 720 bbls Proppant Laden Fluid Volume: 66,788 gal 1,590 bbls Displacement Volume: 32,821 gal 781 bbls Establish Stable Fluid Volume: 12,361 gal 294 bbls Spacer and Ball Drop Volume: 2,414 gal 57 bbls DFIT Volume: 0 gal 0 bbls Interval Status: Completed on i wzz, aunng the preparation Tor interval I a water tanK was compromsea out not spilling Lngmeer. Keegan Lambe water. While getting ready to go downhole the chemical lines were found to be frozen. Seawater Treater Abdon Gamez was pumped downhole to remove the water from the problem tank. Wellhead was opened to 952 si. During the pump down the blender lost its tub due to a communication error between the Supervisor: Abdon Gamez `Values for proppant are taken from software calculations based on multiple variables. Customer Engineer. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 22 35-625 - Kuparuk - Interval 11 Interval Summary Start DatelTime: 11/23/22 14:02 End Date/Time: 11/23/22 16:24 Pump Time: 142 min Initial Rate (Breakdown): 9.6 bpm Initial Surface Pressure (Breakdown): 5,164 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 35.3 bpm Max Surface Pressure: 4,420 psi Max BH Pressure: NA psi Average Rate: 24.1 bpm Average Missile Pressure: 2,643 psi Average Surface Pressure: 2,896 psi Average BH Pressure: NA psi Average Missile HHP: 1,558 hhp Initial CA Pressure: 603 psi Max CA Pressure: 648 psi Max Proppant Concentration: 6.76 Pp9 Average Visc: 30 CID Average Temp: 82.7 F Average pH: 9.3 Proppant Summary Wanli 16/20 Ceramic Pumped: 204,110 Ibs 100M Pumped: 7,427 Ibs Total Proppant Pumped* : 211,537 Ibs Proppant in Formation: 211,537 Ibs Fluid Summary (by Fluid description) 30# Hybor G Volume: 116,769 gal 2,780 bbls 30# Linear Volume: 16,818 gal 400 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 0 gal 0 bbls Fluid Summary (by stage description) Pad Volume: 24,982 gal 595 bbls Conditioning Pad Volume: 28,859 gal 687 bbls Proppant Laden Fluid Volume: 55,393 gal 1,319 bbls Displacement Volume: 14,815 gal 353 bbls Establish Stable Fluid Volume: 7,535 gal 179 bbls Spacer and Ball Drop Volume: 916 gal 22 bbls DFIT Volume: 1,087 gal 26 bbls Interval Status: Completed ball seat observed. -jumped linear tluld Into tormatlon at 2bbpm for a ut-I I. z5nut down and Lngineer. Keegan Lambe observed pressure response. Came offline at 14:08 and restarted pumping at 14:40.Restablished Treater Abdon Gamez injection, stable crosslink and resumed frac. Supervisor: Abdon Gamez Customer Engineer. *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 23 3S-625 - Kuparuk - Interval 12 Interval Summary Start Date/Time: 11/23/22 16:24 End Date/Time: 11/23/22 17:45 Pump Time: 81 min Initial Rate (Breakdown): 10.5 bpm Initial Surface Pressure (Breakdown): 5,510 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 35.5 bpm Max Surface Pressure: 4,714 psi Max BH Pressure: NA psi Average Rate: 34.5 bpm Average Missile Pressure: 3,597 psi Average Surface Pressure: 3,597 psi Average BH Pressure: NA psi Average Missile HHP: 3,042 hhp Initial CA Pressure: 635 psi Max CA Pressure: 674 psi Max Proppant Concentration: 7.99 ppg Average Visc: 29 CID Average Temp: 83.1 F Average pH: 9.3 Proppant Summary Wanli 16120 Ceramic Pumped: 217,509 Ibs 100M Pumped: 6,934 Ibs Total Proppant Pumped' : 224,443 Ibs Proppant in Formation: 224,443 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 105,332 gal 2,508 bbls 30# Linear Volume: 12,605 gal 300 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 1,302 gal 31 bbls Fluid Summary (by stage description) Pad Volume: 24,204 gal 576 bbls Conditioning Pad Volume: 29,538 gal 703 bbls Proppant Laden Fluid Volume: 51,590 gal 1,228 bbls Displacement Volume: 0 gal 0 bbls Flush Volume: 12,605 gal 300 bbls Freeze Protect Volume: 1,302 gal 31 bbls Interval Status: Completed Treater. Abdon Gamez Supervisor: Abdon Gamez for proppant are taken from software calculations based on multiple variables. Customer Engineer: it is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 24 35-625 - Kuparuk - Interval 13 Interval Summary Start DatelTime: 11/24/22 13:11 End Date/Time: 11/24/22 15:16 Pump Time: 125 min Initial Rate (Breakdown): 9.8 bpm Initial Surface Pressure (Breakdown): 5,460 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 35.3 bpm Max Surface Pressure: 4,167 psi Max BH Pressure: NA psi Average Rate: 31.1 bpm Average Missile Pressure: 3,067 psi Average Surface Pressure: 3,045 psi Average BH Pressure: NA psi Average Missile HHP: 2,340 hhp Initial CA Pressure: 491 psi Max CA Pressure: 686 psi Max Proppant Concentration: 7.41 Pp9 Average Visc: 30 CP Average Temp: 84.3 F Average pH: 9 Proppant Summary Wanli 16/20 Ceramic Pumped: 200,942 Ibs 100M Pumped: 7,132 Ibs Total Proppant Pumped* : 208,074 Ibs Proppant in Formation: 208,074 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 111,791 gal 30# Linear Volume: 13,892 gal Seawater Volume: 0 gal Freeze Protect Volume: 0 gal Potassium Formate Volume: 588 gal Fluid Summary (by stage description) Pad Volume: 24,205 gal Conditioning Pad Volume: 29,034 gal Proppant Laden Fluid Volume: 51,214 gal Displacement Volume: 0 gal Flush Volume: 12,708 gal Establish Stable Fluid Volume: 5,875 gal Spacer and Ball Drop Volume: 2,647 gal DFIT Volume: 0 gal Interval Status: Completed 2,662 bbls 331 bbls 0 bbls 0 bbls 14 bbls 576 bbls 691 bbls 1,219 bbls 0 bbls 303 bbls 140 bbls 63 bbls 0 bbls vvenneaa openea to ozopsl. rnor to dropping the ball for interval 14, the aaa pump master Lngineer. Keegan Lambe discharge failed to open. Flushed interval 13 with linear gel. After flushing the stage acid pumper Treater NDaon uamevuralg was recovered and the ball was launched. Kaminski Supervisor: Abdon Gamez Customer Engineer. *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 25 35-625 - Kuparuk - Interval 14 Interval Summary Start DatelTime: 11/24/22 15:16 End Date/Time: 11/24/22 16:40 Pump Time: 84 min Initial Rate (Breakdown): 11.3 bpm Initial Surface Pressure (Breakdown): 5,387 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 37.5 bpm Max Surface Pressure: 4,159 psi Max BH Pressure: NA psi Average Rate: 34.9 bpm Average Missile Pressure: 3,205 psi Average Surface Pressure: 3,229 psi Average BH Pressure: NA psi Average Missile HHP: 2,743 hhp Initial CA Pressure: 685 psi Max CA Pressure: 732 psi Max Proppant Concentration: 7.31 PP9 Average Visc: 29 CID Average Temp: 84.5 F Average pH: 9 Proppant Summary Wanli 16/20 Ceramic Pumped: 194,303 Ibs 100M Pumped: 7,791 Ibs Total Proppant Pumped' : 202,094 Ibs Proppant in Formation: 202,094 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 113,294 gal 2,697 bbls 30# Linear Volume: 11,943 gal 284 bbls Seawater Volume: 0 gal 0 bb/s Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 1,134 gal 27 bbls Fluid Summary (by stage description) Pad Volume: 24,168 gal 575 bbls Conditioning Pad Volume: 32,044 gal 763 bbls Proppant Laden Fluid Volume: 50,637 gal 1,206 bbls Flush Volume: 11,943 gal 284 bbls Freeze Protect Volume: 1,134 gal 27 bbls Establish Stable Fluid Volume: 6,445 gal 153 bbls Interval Status: Completed ball was Displaced at zuopm due to linear welloore nusn of previous stage. luuM castle Din naa Lngineer. Keegan Lambe trouble closing at the end of the stage leading to longer volume run than planned. Had issues with Treater ADDon uamevuralg pumps during the stage, lost a pump to a valve issue in 6ppg, Adjusted rate on other pumps. Karninski Supervisor: Abdon Gamez Customer Engineer. Baskoro Tejo `Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 26 3S-625 - Kuparuk - Interval 15 Interval Summary Start Date/Time: 11/25/22 11:28 End Date/Time: 11/25/22 13:13 Pump Time: 105 min Initial Rate (Breakdown): 9.3 bpm Initial Surface Pressure (Breakdown): 5,136 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 36.2 bpm Max Surface Pressure: 3,897 psi Max BH Pressure: NA psi Average Rate: 33.5 bpm Average Missile Pressure: 3,037 psi Average Surface Pressure: 3,036 psi Average BH Pressure: NA psi Average Missile HHP: 2,492 hhp Initial CA Pressure: 500 psi Max CA Pressure: 669 psi Max Proppant Concentration: 7.22 PPg Average Visc: 30 cP Average Temp: 84.8 F Average pH: 9 Proppant Summary Wanli 16/20 Ceramic Pumped: 195,675 Ibs 100M Pumped: 7,656 Ibs Total Proppant Pumped' : 203,331 Ibs Proppant in Formation: 203,331 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 110,254 gal 2,625 bbls 30# Linear Volume: 963 gal 23 bbls Seawater Volume: 0 gal 0 bb/s Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 1,344 gal 32 bbls Fluid Summary (by stage description) Pad Volume: 24,167 gal 575 bbls Conditioning Pad Volume: 29,404 gal 700 bbls Proppant Laden Fluid Volume: 50,597 gal 1,205 bbls Establish Stable Fluid Volume: 5,224 gal 124 bbls Spacer and Ball Drop Volume: 1,825 gal 43 bbls Interval Status: Completed vvenneao was opened at azupsl. Interval pumped to design. tngmeer. Keegan Lambe Treater: ,vodon uamezncralg Karninski Supervisor. Abdon Gamez 'Values for proppant are taken from software calculations based on multiple variables. Customer Engineer., Baskoro Tejo Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 3S-625 Interval Summary 27 3S-625 - Kuparuk - Interval 16 Interval Summary Start Date/Time: 11/25/22 13:13 End Date/Time: 11/25/22 14:35 Pump Time: 82 min Initial Rate (Breakdown): 9.4 bpm Initial Surface Pressure (Breakdown): 5,129 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 37.2 bpm Max Surface Pressure: 3,735 psi Max BH Pressure: NA psi Average Rate: 33.5 bpm Average Missile Pressure: 2,922 psi Average Surface Pressure: 2,924 psi Average BH Pressure: NA psi Average Missile HHP: 2,399 hhp Initial CA Pressure: 659 psi Max OA Pressure: 717 psi Max Proppant Concentration: 7.27 PPg Average Visc: 30 cP Average Temp: 86.6 F Average pH: 9.3 Proppant Summary Wanli 16/20 Ceramic Pumped: 198,200 Ibs 100M Pumped: 6,945 Ibs Total Proppant Pumped* : 205,145 Ibs Proppant in Formation: 205,145 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 104,890 gal 2,497 bbls 30# Linear Volume: 0 gal 0 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 0 gal 0 bbls Fluid Summary (by stage description) Pad Volume: 24,184 gal 576 bbls Conditioning Pad Volume: 29,432 gal 701 bbls Proppant Laden Fluid Volume: 50,355 gal 1,199 bbls Spacer and Ball Drop Volume: 919 gal 22 bbls Interval Status: Completed ball seat observed, Interval pumped to design. tngmeer. Keegan Lambe Treater: HDaon uamezncralg Karninski Supervisor. Abdon Gamez *Values for proppant are taken from software calculations based on multiple variables. Customer Engineer., Baskoro Tejo Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 3S-625 Interval Summary 28 3S-625 - Kuparuk - Interval 17 Interval Summary Start Date/Time: 11/25/22 14:35 11 /25/22 15:51 Pump Time: 76 min Initial Rate (Breakdown): 8.4 bpm Initial Surface Pressure (Breakdown): 5,131 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 38.0 bpm Max Surface Pressure: 3,882 psi Max BH Pressure: NA psi Average Rate: 35.5 bpm Average Missile Pressure: 2,989 psi Average Surface Pressure: 2,997 psi Average BH Pressure: NA psi Average Missile HHP: 2,601 hhp Initial CA Pressure: 754 psi Max OA Pressure: 754 psi Max Proppant Concentration: 7.66 PPg Average Visc: 30 cP Average Temp: 86.9 F Average pH: 9.2 Proppant Summary Wanli 16/20 Ceramic Pumped: 196,945 Ibs 100M Pumped: 8,353 Ibs Total Proppant Pumped' : 205,298 Ibs Proppant in Formation: 205,298 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 103,035 gal 30# Linear Volume: 10,931 gal Seawater Volume: 0 gal Freeze Protect Volume: 0 gal Potassium Formate Volume: 1,470 gal Fluid Summary (by stage description) Pad Volume: 24,196 gal Conditioning Pad Volume: 29,378 gal Proppant Laden Fluid Volume: 49,461 gal Flush Volume: 10,931 gal Freeze Protect Volume: 1,470 gal Interval Status: Completed 2,453 bbls 260 bbls 0 bb/s 0 bbls 35 bbls 576 bbls 699 bbls 1,178 bbls 260 bbls 35 bbls ball seat observed, Interval pumped to design. tngmeer. Keegan Lambe Treater: HDaon uamezncralg Karninski Supervisor. Abdon Gamez 'Values for proppant are taken from software calculations based on multiple variables. Customer Engineer., Baskoro Tejo Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 3S-625 Interval Summary 29 35-625 - Kuparuk - Interval 18 Interval Summary Start DatelTime: 11/27/22 11:18 End Date/Time: 11/27/22 14:14 Pump Time: 176 min Initial Rate (Breakdown): 8.2 bpm Initial Surface Pressure (Breakdown): 4,591 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 39.9 bpm Max Surface Pressure: 3,988 psi Max BH Pressure: NA psi Average Rate: 32.4 bpm Average Missile Pressure: 3,025 psi Average Surface Pressure: 3,040 psi Average BH Pressure: NA psi Average Missile HHP: 2,399 hhp Initial CA Pressure: 505 psi Max CA Pressure: 684 psi Max Proppant Concentration: 7.29 Pp9 Average Visc: 31 CP Average Temp: 89 F Average pH: 9.2 Proppant Summary Wanli 16/20 Ceramic Pumped: 192,828 Ibs 100M Pumped: 6,794 Ibs Total Proppant Pumped* : 199,622 Ibs Proppant in Formation: 199,622 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 114,089 gal 2,716 bbls 30# Linear Volume: 1,621 gal 39 bbls Seawater Volume: 11,802 gal 281 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 2,079 gal 50 bbls Fluid Summary (by stage description) Pad Volume: 24,145 gal 575 bbls Conditioning Pad Volume: 29,970 gal 714 bbls Proppant Laden Fluid Volume: 51,186 gal 1,219 bbls Displacement Volume: 11,802 gal 281 bbls Establish Stable Fluid Volume: 6,875 gal 164 bbls Spacer and Ball Drop Volume: 2,914 gal 69 bbls DFIT Volume: 620 gal 15 bbls Interval Status: Completed vvenneaa openea to io[psl. vvnlle alsplacing the oall gel lines could not oe openea. ulsplacea the Lngineer. Keegan Lambe ball with seawater and shut down for a DFIT. Swapped eADP gel hoses and resumed pumping. Treater ADaon uamevuralg Interval pumped to design. Kaminski Supervisor: Abdon Gamez Customer Engineer. Baskoro Tejo `Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 30 35-625 - Kuparuk - Interval 19 Interval Summary Start Datelrime: 11/27/22 14:14 End Date/Time: 11/27/22 15:36 Pump Time: 82 min Initial Rate (Breakdown): 8.5 bpm Initial Surface Pressure (Breakdown): 5,004 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 37.0 bpm Max Surface Pressure: 3,594 psi Max BH Pressure: NA psi Average Rate: 33.6 bpm Average Missile Pressure: 2,939 psi Average Surface Pressure: 2,931 psi Average BH Pressure: NA psi Average Missile HHP: 2,418 hhp Initial OA Pressure: 656 psi Max CA Pressure: 724 psi Max Proppant Concentration: 7.29 PPg Average Visc: 31 CID Average Temp: 90.1 F Average pH: 9.1 Proppant Summary Wanli 16/20 Ceramic Pumped: 196,256 Ibs 100M Pumped: 7,445 Ibs Total Proppant Pumped' : 203,701 Ibs Proppant in Formation: 203,701 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 105,625 gal 2,515 bbls 30# Linear Volume: 0 gal 0 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 0 gal 0 bbls Fluid Summary (by stage description) Pad Volume: 24,226 gal 577 bbls Conditioning Pad Volume: 29,410 gal 700 bbls Proppant Laden Fluid Volume: 50,818 gal 1,210 bbls Spacer and Ball Drop Volume: 1,171 gal 28 bbls Interval Status: Completed for proppant are taken from software calculations based on multiple variables. it is billed off of weight ticket volumes and may vary slightly from this number. Treater ADaon uamevuralg Kaminski Supervisor: Abdon Gamez Customer Engineer. Baskoro Tejo Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 31 3S-625 - Kuparuk - Interval 20 Interval Summary Start Date/Time: 11/27/22 15:36 End Date/Time: 11/27/22 16:54 Pump Time: 78 min Initial Rate (Breakdown): 9.6 bpm Initial Surface Pressure (Breakdown): 4,055 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 36.6 bpm Max Surface Pressure: 3,673 psi Max BH Pressure: NA psi Average Rate: 35.4 bpm Average Missile Pressure: 3,020 psi Average Surface Pressure: 2,987 psi Average BH Pressure: NA psi Average Missile HHP: 2,623 hhp Initial CA Pressure: 691 psi Max CA Pressure: 745 psi Max Proppant Concentration: 7.46 PPg Average Visc: 30 cP Average Temp: 89.1 F Average pH: 9.1 Proppant Summary Wanli 16/20 Ceramic Pumped: 197,514 Ibs 100M Pumped: 7,249 Ibs Total Proppant Pumped' : 204,763 Ibs Proppant in Formation: 204,763 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 104,230 gal 30# Linear Volume: 10,002 gal Seawater Volume: 0 gal Freeze Protect Volume: 0 gal Potassium Formate Volume: 840 gal Fluid Summary (by stage description) Pad Volume: 24,211 gal Conditioning Pad Volume: 29,098 gal Proppant Laden Fluid Volume: 50,921 gal Flush Volume: 10,002 gal Freeze Protect Volume: 840 gal Interval Status: Completed 2,482 bbls 238 bbls 0 bb/s 0 bbls 20 bbls 576 bbls 693 bbls 1,212 bbls 238 bbls 20 bbls Interval pumped to design. tngmeer. Keegan Lambe Treater: ,vodon uamezncralg Karninski Supervisor. Abdon Gamez 'Values for proppant are taken from software calculations based on multiple variables. Customer Engineer., Baskoro Tejo Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 3S-625 Interval Summary 32 35-625 - Kuparuk - Interval 21 Interval Summary Start DatelTime: 11/28/22 13:04 End Date/Time: 11/28/22 15:36 Pump Time: 152 min Initial Rate (Breakdown): 9.8 bpm Initial Surface Pressure (Breakdown): 3,865 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 35.9 bpm Max Surface Pressure: 3,135 psi Max BH Pressure: NA psi Average Rate: 31.4 bpm Average Missile Pressure: 2,529 psi Average Surface Pressure: 2,511 psi Average BH Pressure: NA psi Average Missile HHP: 1,943 hhp Initial CA Pressure: 557 psi Max CA Pressure: 718 psi Max Proppant Concentration: 7.27 Pp9 Average Visc: 30 CID Average Temp: 89.3 F Average pH: 9.1 Proppant Summary Wanli 16/20 Ceramic Pumped: 195,843 Ibs 100M Pumped: 6,950 Ibs Total Proppant Pumped* : 202,793 Ibs Proppant in Formation: 202,793 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 112,161 gal 2,671 bbls 30# Linear Volume: 11,702 gal 279 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 966 gal 23 bbls Fluid Summary (by stage description) Pad Volume: 24,209 gal 576 bbls Conditioning Pad Volume: 28,720 gal 684 bbls Proppant Laden Fluid Volume: 50,780 gal 1,209 bbls Displacement Volume: 9,269 gal 221 bbls Establish Stable Fluid Volume: 7,243 gal 172 bbls Spacer and Ball Drop Volume: 2,602 gal 62 bbls DFIT Volume: 1,040 gal 25 bbls Interval Status: Completed stall aroppea ana alsplacea with linear gel. Arter oan seat pertormea uF1 I with linear gel. Interval Lngineer. Keegan Lambe pumped to design. Treater ADaon uamevuralg Kaminski Supervisor: Abdon Gamez Customer Engineer. *Values for proppant are taken from software calculations based on multiple variables. Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 33 35-625 - Kuparuk - Interval 22 Interval Summary Start Date/Time: 11/28/22 15:36 End Date/Time: 11/28/22 16:55 Pump Time: 79 min Initial Rate (Breakdown): 10.0 bpm Initial Surface Pressure (Breakdown): 4,257 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 34.8 bpm Max Surface Pressure: 3,199 psi Max BH Pressure: NA psi Average Rate: 33.9 bpm Average Missile Pressure: 2,586 psi Average Surface Pressure: 2,578 psi Average BH Pressure: NA psi Average Missile HHP: 2,151 hhp Initial CA Pressure: 718 psi Max CA Pressure: 762 psi Max Proppant Concentration: 7.36 PPg Average Visc: 31 cP Average Temp: 89.1 F Average pH: 9.2 Proppant Summary Wanli 16/20 Ceramic Pumped: 191,432 Ibs 100M Pumped: 6,979 Ibs Total Proppant Pumped' : 198,411 Ibs Proppant in Formation: 198,411 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 103,593 gal 2,467 bbls 30# Linear Volume: 9,331 gal 222 bbls Seawater Volume: 0 gal 0 bb/s Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 2,030 gal 48 bbls Fluid Summary (by stage description) Pad Volume: 24,230 gal 577 bbls Conditioning Pad Volume: 28,815 gal 686 bbls Proppant Laden Fluid Volume: 50,548 gal 1,204 bbls Flush Volume: 9,331 gal 222 bbls Freeze Protect Volume: 2,030 gal 48 bbls Interval Status: Completed wart drop and seat observed. Interval proppant pumped to aeslgn. when trying to load the dart Tor tngmeer. Keegan Lambe interval 23 the dart hung up in the launcher and couldn't shut the top launch valve. Flushed the Treater: HDaon uani well on linear. Karninski Supervisor. Abdon Gamez `Values for proppant are taken from software calculations based on multiple variables. Customer Engineer., Proppant is billed off of weight ticket volumes and may vary slightly from this number. Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 34 3S-625 - Kuparuk - Interval 23 Interval Summary Start Dateffime: 11/29/22 11:55 End Date/Time: 11/29/22 13:39 Pump Time: 104 min Initial Rate (Breakdown): 9.8 bpm Initial Surface Pressure (Breakdown): 4,052 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 35.8 bpm Max Surface Pressure: 3,280 psi Max BH Pressure: NA psi Average Rate: 33.4 bpm Average Missile Pressure: 2,434 psi Average Surface Pressure: 2,563 psi Average BH Pressure: NA psi Average Missile HHP: 1,991 hhp Initial CA Pressure: 545 psi Max CA Pressure: 683 psi Max Proppant Concentration: 7.60 ling Average Visc: 30 CP Average Temp: 86.4 F Average pH: 9.2 Proppant Summary Wanli 16/20 Ceramic Pumped: 211,352 Ibs 100M Pumped: 8,157 Ibs Total Proppant Pumped* : 219,509 Ibs Proppant in Formation: 219,509 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 114,253 gal 2,720 bbls 30# Linear Volume: 2,513 gal 60 bbls Seawater Volume: 0 gal 0 bbls Freeze Protect Volume: 0 gal 0 bbls Potassium Formate Volume: 756 gal 18 bbls Fluid Summary (by stage description) Pad Volume: 24,185 gal 576 bbls Conditioning Pad Volume: 31,602 gal 752 bbls Proppant Laden Fluid Volume: 53,374 gal 1,271 bbls Establish Stable Fluid Volume: 5,092 gal 121 bbls Spacer and Ball Drop Volume: 2,513 gal 60 bbls Interval Status: Completed erty for proppant are taken from software calculations based on multiple variables. it is billed off of weight ticket volumes and may vary slightly from this number. Treater ADaon uamevuralg Kaminski Supervisor: Abdon Gamez Customer Engineer: Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 35 3S-625 - Kuparuk - Interval 24 Interval Summary Start Datelrime: 11/29/22 13:39 End Date/Time: 11/29/22 15:05 Pump Time: 86 min Initial Rate (Breakdown): 9.7 bpm Initial Surface Pressure (Breakdown): 4,226 psi Initial BH Pressure (Breakdown): NA psi Max Rate: 36.5 bpm Max Surface Pressure: 3,126 psi Max BH Pressure: NA psi Average Rate: 34.2 bpm Average Missile Pressure: 2,416 psi Average Surface Pressure: 2,538 psi Average BH Pressure: NA psi Average Missile HHP: 2,023 hhp Initial OA Pressure: 683 psi Max CA Pressure: 726 psi Max Proppant Concentration: 7.77 ppg Average Visc: 29 CID Average Temp: 87.8 F Average pH: 9.3 Proppant Summary Wanli 16/20 Ceramic Pumped: 219,913 Ibs 100M Pumped: 7,197 Ibs Total Proppant Pumped' : 227,110 Ibs Proppant in Formation: 227,110 Ibs Fluid Summary (by fluid description) 30# Hybor G Volume: 105,661 gal 30# Linear Volume: 8,633 gal Seawater Volume: 0 gal Freeze Protect Volume: 0 gal Potassium Formate Volume: 966 gal Fluid Summary (by stage description) Pad Volume: 24,236 gal Conditioning Pad Volume: 28,803 gal Proppant Laden Fluid Volume: 52,622 gal Flush Volume: 8,633 gal Freeze Protect Volume: 966 gal Interval Status: Completed for proppant are taken from software calculations based on multiple variables. it is billed off of weight ticket volumes and may vary slightly from this number. 2,516 bbls 206 bbls 0 bbls 0 bbls 23 bbls 577 bbls 686 bbls 1,253 bbls 206 bbls 23 bbls Treater ADaon uamevuralg Kaminski Supervisor: Abdon Gamez Customer Engineer: Customer Rep: Greg Clayton Conoco Phillips - 35-625 Interval Summary 36 3 KR-■f!!7§9!!: \}/\!:;:l:lnB:§: nlE;El /\ ! STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIONS RECEIVED By Kayla Junks at 10:01 am, Mar 24, 2023 1. Operations Susp Well Insp ❑ Plug Perforations ❑ Fracture Stimulate ❑ Pull Tubing ❑ Operations shutdown ❑ Performed: Install Whipstock ❑ Perforate ❑ Other Stimulate ❑ Alter Casing ❑ Change Approved Program ❑ Mod Artificial Lift ❑ Perforate New Pool ❑ Repair Well ❑ Coiled Tubing Ops ❑ Other: Convert to WAG 0 2. Operator Name 4. Well Class Before Work: 5. Permit to Drill Number: ConocoPhillips Alaska, Inc. Development O Exploratory❑ Stratigraphic ❑ Service❑ 222-079 3. Address: P.O. Box 100360 6. API Number: Anchorage, AK 99510 50-103-20842-00-00 7. Property Designation (Lease Number): 8. Well Name and Number: ADL0025528, ADL00255", ADL0380107 KRU 3S-625 9. Logs (List logs and submit electronic data per 20AAC25.071): 10. Field/Pool(s): NIA Kuparuk River Field/ Torok Oil Pool 11. Present Well Condition Summary: Total Depth measured 25310' feet Plugs measured None feet true vertical 5253' feel Junk measured None feet Effective Depth measured 25310' feel Packer measured 12516', 12692' feet true vertical 5253' feel true vertical 5051', 5074' feet Casing Length Size MD TVD Burst Collapse Conductor 94' 20" 131, 131' Surface 2859' 10-3/4" 2895' 2572' Intermediate 12807T 7-5/8" 12842' 5090' Production Liner 12614' 4-1/2" 25306' 5253' Perforation depth Measured depth Frac Sleeves altemating:12891-25247' True Vertical depth Frac Sleeves a0emating: 5094-5253' Tubing (size, grade, measured and true vertical depth) 4-1/2" L-80 12702' MD 5075' TVD Packers and SSSV (type, measured and true vertical depth) Packer: HAL TNT Prod Packer 12516' MD 5051' TVD Packer: ZXP w/TieBK Sleeve LTP 12692' MD 5074' TVD SSSV: None N/A NIA 12. Stimulation or cement squeeze summary: Intervals treated (measured): N/A Treatment descriptions including volumes used and final pressure: N/A 13a. Representative Daily Average Production or Injection Data Oil-Bbl Gas-Mcf Water-Bbl Casing Pressure Tubing Pressure Prior to well operation: 1088 1383 5602 1454 251 Subsequent to operation: Injector - 4686 790 511 131b. Pools active after work: Torok Oil Pool 14. Attachments (required per 20 AAC 25.070, 25.071, & 25.283) 15. Well Class after work: Daily Report of Well Operations 0 Exploratory ❑ Development ❑ Servicep Stratigraphic ❑ Copies of Logs and Surveys Run ❑ 16. Well Status after work: Oil ❑ Gas ❑ WDSPL ❑ Electronic Fracture Stimulation Data ❑ GSTOR ❑ WINJ ❑ WAG p GINJ ❑ SUSP❑ SPLUG ❑ 17. 1 hereby certify that the foregoing is true and correct to the best of my knowledge. Sundry Number or N/A if C.O. Exempt: 322-056 Digitally.Lynnre Lynn A Authorized Name and es IreDate:202303.2408:55:20 -08'00' Digital Signature with Date: Contact Name: Lynn Aleshlre Contact Email: Ivnn.aleshire(vv)conocoohillios.com Authorized Title: Surveillance Reservoir Engineer Contact Phone: (907) 265-5525 Sr Pet Eng: Sr Pet Geo: I Isr Res Eng: RBDMS JSB 033023 Form 10404 Revised 10/2022 Due Within 30 days of Operations Submit in PDF format to aogcc.permifting@alaska.gov 3S-625 DESCRIPTION OF WORK COMPLETED SUMMARY Date Event Summary 02/11/23 Set RBP @ 6714' RKB. Pull OV, set DP HFCV @ 6668' RKB. Circ out and FP. 02/12/23 Pull HFCV and set DV @ 6668' RKB. MITIA to 2500 psi - PASS. Pull RBP & catcher. 02/13/23 Well BOL 03/01/23 State witnessed (Austin McLeod) MIT -IA PASSED to 1820 psi. WELL KUP INJ WELLNANIE 3S-625 WELLBORE 3S-626 CUnocoPhillip5 Alaska, Inc. mina®; 33.7-2 Deans Imam lees, IrNmedWa: umr 11,602 MXieD- Well Attributes I Max AngleBMD TO now Name WNIbore APWVA Wellhore Statue Id(°) Mn(a-1 MBrm grand TRACT PERATI NM RTR 1 2 2 IN 3.15 18,825.]5 25,310.0 comment H23(ppm) DRe Mmte ion Entl pNe KBGN go RRDak Ater Ekv... 3677 10271202 t-ast-ptuvRm via AnnWalion WeIINrt Entl Date Lasl Mok By Rev Reason: Pulled Our 8 Set DV 35E25 2I12I2023 zembaej Casing Strings set Depth sM Diane Cap Des OD lint ID lint Top Pass, gtKBI (WD)(.KB) WlhenpbigWL�UjHydbg�3 To Conductor 20 19.12 37.0 131.0 131.0 154.340314 9.95 35J 2895.3 2,5]1.9 45.WHYDIntermediate 1Sts b.88 35.1 128420 5,090.3 29.]0 Liner 41121 3.95 12,692.4 25,3(6.0 1 5,253.0 12.ut L-80 I HYD563 Tubing Strings: string max indicates LONGEST segment of string Top lftKBl Sat Dep[M1... SttDeptM1._ String Ma... Tubing De¢vigion Wt llbMl Grade Top Conrrtdion Might 32.9 12J01.9 5,0]5.3 4112 Tubing- Completion Upper 12.60 L-80 Hydril5fi3 3.96 Completion Details: excludes tubing, pup, space out, thread, RKB... OD Top(TVD) Topinal Nominal Nominal Top(..) (XK9) F) hem Des (in) Core Make Mader ID (in) 32.9 32.9 C.00 Hanger 10.850 Stbamfio 4-112"Tubing Hanger, StreamF 3020227 3.958 H563 l0 9 2,034.2 1.966.6 30.23 Nipple- 4.925 NIPPLE, Lending, HAL 3.813' X, HAL 3.990 Landing Nickel 2,]]8.2 2.500.9 51.43 GAS LIFT 6.000 Cameo 127141- 3.965 01_VCS 6,667.9 3.683.2 75.98 GAS LIFT 6.000 Cameo 127141- 3.965 01SI2 12,452.4 5,042.1 81.35 Gauge l Pump 5.694 HAL ROC DHGa Mandrel, 4-112" HAL ORS- 3.925 Sensor 12.64 L40 Hyd 563 001786 ADD 12,516.5 5,051.5 81.88 Packer 6.000 HAL TNT Production Packer HAL 1027226 3.958 4.5"x7.63"T-Blue 15 12,591.3 5,061.5 82.60 Nipple- 4.925 NIPPLE,LANDING,4-112",DBS, HAL 4402228 3.908 Lending Nickel,3.562",11563 BXP -01 12,692.9 5,074.2 83.08 Locator Baker Shear Type Locator sub- Baker above locating shoulder 12,698.7 5,074.9 83.11 Shoe - Mule 5.210 Hallibudon Ratcheting Muleshoe Baker 3.920 Mandrel Inserts : excludes pulled ins at al Top (TVD) Top on VaM LahM1 OD TRO Run Targets) (M(B) Ind l°) No Sery Typa Type (in) Ipep Run Date pM Co. Make an" Ste (In) 2]]8.2 2,500.9 51.43 GAS LIFT DMY BK 6 0.0 12I612022 Cao KBG 0.000 6,667.9 3,683.2 ]5.98 2 GAS LIFT DMY BN 6 0.0 2I12I2023 Cme amco KBG B.000 Liner Details: Excludes Liner, Pup, Joints, casing, float, sub, shoe... ToplrvD) Topmd OD Nominal NnmlmllD Tap DtKB) IM e) I°) Rem Des bad Cam Make Motel (in) 12,692.4 5,074.1 83.08 Packer 6.540 5.5"X7-51E ZXP Packer wl ZXP LTP H29645026 4.810 11.29'x 5J5"ID TmBK Sleeve- 5 UP @ -12692' 12,712.4 5,076.5 83.17 Nipple-RS 6.050 RS Rackoff Seal Nipple R15 10553458 4.250 Nipple 12,724.0 5,0]].9 83.23 XO Reducing 6.060 5.5" Hyd 563 box X pin 4.5" Hit 3.900 563 cross over 12,891.1 5,093.7 86.54 Sleeve - Free 5.000 Advanced Upstream Frac Sleeve Frac 10739 3.500 824 Locator -not freed- sleeve W0027 13,453.9 5,140.6 84.74 Racket - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSYk24 Swell 3124 13,635.7 5,157.3 84.78 Biases -Frac 5.000 AMancetl Upstream Frac Sleeve Frac 107390. 3.500 M23 sleeve M026 13,918.9 5,183.3 84.71 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSYR23 Swell 3123 14,181.9 5,207.3 84.75 Sleeve -Frac 5.000 Advanced Upstream Frac Sleeve Frac 107394- 3.500 822 sleeve 000025 14,333.6 5,225.6 84.95 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSYk22 Swell 3122 14,684.5 5,247.2 86.69 Sleeve -Frac 5.000 Advanced Upstream Frac Sleeve Frac 107390. 3.500 Qi sleeve 000024 14,927.8 5,261.0 86.80 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSYp21 Swell 3121 15,189.8 5,272.0 88.15 Sleeve- Frac 4.500 BAKER Frac Sleeve (3.3]5"ball) Frac H80908039 3.323 M20, HYD563 sleeve 2 15,432.7 5,278.1 89.19 Packer -Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSYp20 Swell 3120 15,695.2 5,279.7 89s) Sleeve -Frac 4.500 BAKER Frac Blame (3.313" ball) Frac H809OK39 3.260 #19, HYD563 sleeve 3 15,940.3 5,278.9 90.26 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSYp19 Swell 3119 16,202.5 5,276.8 90.88 Sleeve -Frac 4.500 BAKER Frac Sleeve (3.250" ball) Frac H80908039 3.198 R18, HYD563 sleeve 4 16,524.9 5,272.7 90.96 Packer - Swell 4.500 Samil Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSY418 Swell 3118 16,707.3 5,266.6 92.30 Sleeve-Frac 4.500 BAKER Frac Sleeve (3.188" ball) Frac H90908039 3.135 X17, HYD563 sleeve 5 16,871.0 5,261.4 91.37 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSYp17 Swell 3117 17,214.1 5,258.4 90.34 Sleeve-Frac 4.500 BAKER Free Sleeve (3.125" ball) Frac H80908039 3.073 M16, HYD563 sleeve 6 17,498.9 5,256.2 90.34 Packer - Swell 4.500 Swell Packer 5,80"OD HYD563 Water H30187052 3.900 P110S ASSYNI6 Swul 3116 17,719.6 5,256.2 89.93 Sleeve -Frac 4.500 BAKER Frac Sleeve (3.063" ball) Frac H80908039 3.010 X15, HYD563 sleeve ] 17,962.4 5,256.0 90.36 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSYk15 Swell 3115 18,224.7 5,254.7 90.09 Sleeve -Frac 4.500 BAKER Frac Sleeve(3.00"bell) Frac H809080]2 2.955 I %14, HYD563 Sleeve 9 KUP INJ WELLNAME 3S-626 WELLBORE 3S_625 v Oxio ;Phillips Alaska, Inc. 57.0 Liner Details: Excludes Liner, Pup, Joints, tarsi XOMmNTA r3ss2s, 3r2On623 s 32.5] PM v.mmaanem.ae 0_4 Top508.9 Top lT) To I-) MF al) Nominal (ln) Mar Nominal lb I3. """"""""""""""""XanPor; 33.o - 18,508.9 5,254 5,254.] 0. 90.16 Pacft.ker Packer - Swell 4.500 Swell Packer 80 HYD563 Water 1870Mode 052 3.900 ...... _.. ............. ......... ASSY.80"OD P110S ASSY AI4 Swell 3114 3114 18,730.6 5,249.2 92.F] Sleeve - Free 4.500 BAKER Frac Sleeve (2.945"bell) Frac H80908072 2.905 #13, HYD563 sleeve ] comvamr. m.ni3io 18,935.2 5,238.5 9284 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 s,an®sorry c.m.rs as.e - P110S ASSY#13 Swell 3113 apple-brdln.,3e a.0 19,238.7 5,231.5 90.01 Sleeve-Frac 4.500 BAKER Frac Sleeve (2.895" ball) #12. HYD563 Frac sleeve H80908072 8 2.855 19,522.8 5,231.7 90.01 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 GA. LIFT,p]e.2 P110S ASSY#12 Swell 3112 19,744.6 5,231.8 89.95 Sleeve - Free 4.500 BAKER Frec Sleeve (2.845" ball) Frac 1180908026 2.805 - #11, HYD563 .leave 4 s,ara®;x.]-zees3- 19,985.8 5,231.9 89.8] Packer -Swell 4.500 Swell Packer 5,80"OD HYD563 Water H30187052 3.900 P110S ASSY#11 Swell 3111 Gee LIFT. 6. PS 20,248.6 5,232.4 89.93 Sleeve -Frac 4.500 BAKER Frac Sleeve (2J95"bell) Frac H80908039 2.755 Imerme no, splM1p 1 camera. #10, HYD563 sleeve 8 2aB9'p nNB 20,493.5 5,232.8 89.93 Packer -Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 BauPo IPump saran.,; rzasza P110S ASSY#10 Swell 3110 20,716.3 5,233.2 89.96 Sleeve - Free 4.500 BAKER Free Sleeve (2.]45"ball) Frac H80908039 2J05 #9, HYD563 sleeve ] Packer. 12516s TO960.7 5,233E 8995 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSY#9 Swell 3109 Nippi-Lenaira uset.a 21,223.1 5,233.8 89.98 Sleeve -Frac 4.500 BAKER Frac Sleeve(2.695"bell) Frac H80908039 2.655 NB, HYD563 sleeve 6 21,545.8 5,234.4 89.86 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSY#8 Swell 3108 sore-MJe: I3Foa1 21728.0 5,234.7 89.86 Sleeve-Frac 4.500 BAKER Frac Blame (2.645" ball) #],HYD563 Frac sleeve H8090K39 5 2.605 22,013.2 5,235.1 89J7 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSY#] Swell 3107 22,231.3 5,237.4 88.97 Sleeve - Fret 4.500 BAKER Free Blame. (2.595"bell) Frac H809OW39 2.555 #6, HYD563 sleeve 4 22,476.3 5,241.7 88.95 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 limmaawas.vu.eu'0 P 110S ASSY#6 Swell 3106 22,708.6 5,245.2 89.46 Sleeve-Frac 4.500 BAKER Frac Sleeve (2.545" ball) Frac H80908039 2.505 XS. HYD563 sleeve 3 22,983.4 5,248.0 89.45 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSY#5 Swell 3105 23,246.4 5,249.5 89.97 Sleeve - Free 4.500 BAKER Free Sleeve (2A95"ball) Frac H80908039 2.465 114, HYD563 sleeve 2 23,409.0 5,249.6 89.91 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P 110S ASSY#4 Swell 3104 23,753.1 5,250.0 89.92 Sleeve -Frac 4.500 BAKER Frac Sleeve (2.455"bell) Frac H80908039 2.425 #3, HYD563 sleeve 1 24,118.4 5,250.6 89.86 Packer -Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSY#3 Swell 3103 24,260.1 5,251.0 89.88 Sleeve - Free 4.500 BAKER Free Sleeve (2.415" ball) Frac H809ON39 2.385 #2, HYD563 sleeve 0 24,464.4 5,251.2 89.95 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSY#2 Swell 3102 24,767.0 5,251.6 89.99 Sleeve -Frac 4.500 BAKER Frac Sleeve (2.3]5"ball) Frac H8090SOM 2.345 111, HYD563 sleeve 9 25,011.1 5,252.2 89.85 Packer - Swell 4.500 Swell Packer 5.80"OD HYD563 Water H30187052 3.900 P110S ASSY#1 Swell 3101 25,243.4 5,253.0 89.98 Sleeve -Frac 5.620 Alpha Pressure Sleeve 4 lZ Alpha H81047006 3.000 HYD56313.5#O125 sleeve 8 25,247.1 5,253.0 89.99 Sleeve -Frac 5.630 WIV-4112" 13.5#P110HYD563 WIV H80914004 1.250 -2 pins IT 990 PSI -1,25" ball 2 25,306.01 5,253.01 90.00 5.200 Niiiiiii 1�1 f r� N,ar, 12,6e2.125aa6r 1. Type of Request: Abandon Plug Perforations Fracture Stimulate Repair Well Operations shutdown Suspend Perforate Other Stimulate Pull Tubing Change Approved Program Plug for Redrill Perforate New Pool Re-enter Susp Well Alter Casing Other: Convert to WAG 2. Operator Name: 4. Current Well Class: 5. Permit to Drill Number: Exploratory Development 3. Address: Stratigraphic Service 6. API Number: 7. If perforating:8. Well Name and Number: What Regulation or Conservation Order governs well spacing in this pool? Will planned perforations require a spacing exception? Yes No 9. Property Designation (Lease Number): 10. Field: Current Pools: 11. Total Depth MD (ft): Total Depth TVD (ft): Effective Depth MD: Effective Depth TVD: MPSP (psi): Plugs (MD): Junk (MD): 25310'None Casing Collapse Structural Conductor Surface Intermediate Production Liner Packers and SSSV Type: Packers and SSSV MD (ft) and TVD (ft): 12. Attachments: Proposal Summary Wellbore schematic 13. Well Class after proposed work: Detailed Operations Program BOP Sketch Exploratory Stratigraphic Development Service 14. Estimated Date for 15. Well Status after proposed work: Commencing Operations: OIL WINJ WDSPL Suspended 16. Verbal Approval: Date: GAS WAG GSTOR SPLUG AOGCC Representative: GINJ Op Shutdown Abandoned Contact Name: Contact Email: Contact Phone: Authorized Title: Conditions of approval: Notify AOGCC so that a representative may witness Sundry Number: Plug Integrity BOP Test Mechanical Integrity Test Location Clearance Other: Post Initial Injection MIT Req'd? Yes No Spacing Exception Required? Yes No Subsequent Form Required: APPROVED BY Approved by: COMMISSIONER THE AOGCC Date: Comm. Comm. Sr Pet Eng Sr Pet Geo Sr Res Eng 17. I hereby certify that the foregoing is true and the procedure approved herein will not be deviated from without prior writt en approval. Authorized Name and Digital Signature with Date: AOGCC USE ONLY Lynn Aleshire lynn.aleshire@conocophillips.com (907) 265-6525 Surveillance Reservoir Engineer Tubing Grade: Tubing MD (ft): 12516' MD and 5051' TVD 12692' MD and 5074' TVD N/A Perforation Depth TVD (ft): Tubing Size: L-80 12702' MD 3/1/2023 Packer: HAL TNT Prod Packer Packer: ZXP w/TieBK Sleeve LTP SSSV: None STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION APPLICATION FOR SUNDRY APPROVALS 20 AAC 25.280 ADL0025528, ADL0025544, ADL0380107 222-079 P.O. Box 100360, Anchorage, AK 99510 50-103-20842-00-00 ConocoPhillips Alaska, Inc. KRU 3S-625 Torok Oil PoolTorok Oil PoolKuparuk River Field N/A Length Size Proposed Pools: TVD Burst PRESENT WELL CONDITION SUMMARY 5253' 25310' 5253' None MD 131' 2572' 5090' 131' 2895' 12842' 20" 10-3/4" 94' 2859' Perforation Depth MD (ft): 7-5/8"12807' None 4-1/2" None 25306'12614' 4-1/2" 5253' Form 10-403 Revised 10/2022 Approved application valid for 12 months from date of approval.Submit PDF to aogcc.permitting@alaska.gov By Meredith Guhl at 7:14 am, Jan 31, 2023 322-056 Lynn Aleshire Digitally signed by Lynn Aleshire Date: 2023.01.30 15:36:06 -09'00' MGR13FEB23 X DLB 02/03/2023 DSR-2/1/23 10-404 GCW 02/13/23 JLC 2/13/2023 2/13/23 Brett W. Huber, Sr. Digitally signed by Brett W. Huber, Sr. Date: 2023.02.13 14:35:57 -09'00' RBDMS JSB 021423 1 ConocoPhillips Alaska, Inc. 700 G St. Anchorage, AK 99501-3448 January 30, 2023 AOGCC Commissioner State of Alaska, Oil & Gas Conservation Commission 333 W. 7th Ave., Ste. 100 Anchorage, AK 99501 Re: KRU 3S-625 (PTD 222-079) Conversion to Injection Dear Commissioner, ConocoPhillips Alaska, Inc. requests approval to convert Kuparuk River Unit Well 3S-625 from Production to Water-Alternating Gas Service. A 10-404 was recently submitted to inform of our intention to flow back this injector for more than 30 days, effectively, converting it to a producer. The required flowback will be complete soon and the well should be placed in water injection service. Attached you will find the 10-403 Application for Sundry Approval for ConocoPhillips Alaska, Inc. for conversion of KRU 3S-625 to WAG service. If you have any questions regarding this matter, please contact me at 907-265-6525 or by email at lynn.aleshire@cop.com. Sincerely, Lynn Aleshire Surveillance Reservoir Engineer ConocoPhillips Alaska, Inc. Attachments: Sundry applications Lynn Aleshire Digitally signed by Lynn Aleshire Date: 2023.01.30 15:36:37 -09'00' 3S-625 DESCRIPTION SUMMARY OF PROPOSAL ConocoPhillips Alaska Inc. requests approval to convert Kuparuk River Unit Well 3S-625 from Oil Production service to Water Alternating Gas Injection service now that the post-drill flowback has been completed. Area of Review: KRU Well 3S-625 was originally completed as a WAG injector in the Torok reservoir in December 2022. The flowback period required to clean up the completion exceded the 30 day window for flowback and the well was converted to production. The top of the Torok sand in 3S-625 is at 13,337' MD / 5070' TVDSS Area Map with 1/4 mile radius around target injection zone (see attached) The attached map shows that the only KRU well located within the 1/4 mile radius is 3S-615, the Torok producer 3S-625 was drilled to support. Mechanical Condition of Well to be Converted: The mechanical condition of 3S-625 is good. The injection tubing / casing annulus is isolated with a Halliburton TNT Prod Packer set at 12,516' MD / 5052' TVD. A NON-witnessed MITIA will be performed prior to injection. After injection has stablized a State-witnessed SW MITIA will be performed. CBL and interpretation of cement quality All hydrocarbon zones penetrated by the well are isolated. See attached Area of Review Detail for offset producer 3S-615. The 10-3/4" Surface Casing was cemented with 452 bbls of 10.7 ppg lead cement and 57 bbls of 15.8 ppg tail cement. The 7-5/8" Intermediate was cemented with 264 bbls of 15.3 ppg lead cement and 33 bbls of 15.3 ppg tail cement. CBL indicates top of cement at 7850' MD / 3970' TVD. KRU 3S-625 AREA OF REVIEWPTD API WELL NAME STATUSTop of Torok Oil Pool (MD)Top of Torok Oil Pool (TVDSS)Top of Cement (MD)Top of Cement (TVDSS)Top of Cement Determined ByReservoir Status Zonal Isolation Cement Operations Summary Mechanical Integrity222-101 50-103-20844 3S-615 Producing 11,749' 5080' 5620' 3340' CBLFrac sleeves open to productionZXP Packer @ 11,531' MD10-3/4": 501 bbls 10.7 ppg lead cement & 58 bbls 15.8 ppg tail cement. 7-5/8": 237 bbls of 15.3 ppg.12/30/22 CMIT -TxIA TO 3850 PASS Last Rev Reason Annotation Wellbore End Date Last Mod By Rev Reason: Set DV / GLV & Pulled catcher/RBP 3S-625 12/6/2022 zembaej Casing Strings Csg Des OD (in) ID (in) Top (ftKB) Set Depth (ftKB) Set Depth (TVD) (ftKB) Wt/Len (lb/ft) Grade Top Thread Conductor 20 19.12 37.0 131.0 131.0 154.34 GRX-65 Surface 10 3/4 9.95 36.7 2,895.3 2,571.9 45.50 L-80 HYD 563 Intermediate 7 5/8 6.88 35.1 12,842.0 5,090.3 29.70 L-80 Hyd 563 Liner 4 1/2 3.95 12,692.4 25,306.0 5,253.0 12.60 L-80 HYD 563 Tubing Strings: string max indicates LONGEST segment of string Top (ftKB) 32.9 Set Depth … 12,701.9 Set Depth … 5,075.3 String Ma… 4 1/2 Tubing Description Tubing – Completion Upper Wt (lb/ft) 12.60 Grade L-80 Top Connection Hydril 563 ID (in) 3.96 Completion Details: excludes tubing, pup, space out, thread, RKB... Top (ftKB) Top (TVD) (ftKB) Top Incl (°) Item Des OD Nominal (in)Com Make Model Nominal ID (in) 32.9 32.9 0.00 Hanger 10.850 Streamflo 4-1/2" Tubing Hanger, H563 StreamF lo 3020227 9 3.958 2,034.2 1,966.6 30.23 Nipple - Landing 4.925 NIPPLE, Landing, HAL 3.813" X, Nickel HAL 3.980 2,778.2 2,500.9 51.43 GAS LIFT 6.000 4-1/2" x 1" Camco KBG 4-5 GLM Camco 127141- 01_VCS 3.865 6,667.9 3,683.2 75.98 GAS LIFT 6.000 4-1/2" x 1" Camco KBMG GLM Camco 127141- 01-SL2 3.865 12,452.4 5,042.1 81.35 Gauge / Pump Sensor 5.694 HAL ROC DHG + Mandrel, 4-1/2" 12.6# L-80 Hyd 563 HAL OPS- 001786 ADD 3.925 12,516.5 5,051.5 81.88 Packer 6.000 HAL TNT Production Packer 4.5"x7.63" T-Blue HAL 1027226 15 3.958 12,591.3 5,061.5 82.60 Nipple - Landing 4.925 NIPPLE,LANDING,4-1/2",DB-6, Nickel,3.562",H563 BXP HAL 4402228 -01 3.908 12,692.9 5,074.2 83.08 Locator Baker Shear Type Locator sub - above locating shoulder Baker 12,698.7 5,074.9 83.11 Shoe - Mule 5.210 Halliburton Ratcheting Muleshoe Baker 3.920 Mandrel Inserts : excludes pulled inserts Top (ftKB) Top (TVD) (ftKB) Top Incl (°) St ati on No /S Serv Valve Type Latch Type OD (in) TRO Run (psi) Run Date Com Make Model Port Size (in) 2,778.2 2,500.9 51.43 1 GAS LIFT DMY BK 6 0.0 12/6/2022 Camco KBG 0.000 6,667.9 3,683.2 75.98 2 GAS LIFT OV BK 6 0.0 12/6/2022 Camco KBG 0.438 Liner Details: Excludes Liner, Pup, Joints, casing, float, sub, shoe... Top (ftKB) Top (TVD) (ftKB) Top Incl (°) Item Des OD Nominal (in)Com Make Model Nominal ID (in) 12,692.4 5,074.1 83.08 Packer 6.540 5.5" X 7-5/8" ZXP Packer w/ 11.29' x 5.75" ID TieBK Sleeve - LTP @ ~12,692' ZXP LTP H29645026 5 4.810 12,712.4 5,076.5 83.17 Nipple - RS 6.050 RS Packoff Seal Nipple R/S Nipple 10553458 4.250 12,724.0 5,077.9 83.23 XO Reducing 6.060 5.5" Hyd 563 box X pin 4.5" Hyd 563 cross over 3.900 12,891.1 5,093.7 86.54 Sleeve - Frac 5.000 Advanced Upstream Frac Sleeve #24 Locator - not frac'd - Frac sleeve 107394- 000027 3.500 13,453.9 5,140.6 84.74 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #24 Water Swell H30187052 3/ 24 3.900 13,635.7 5,157.3 84.78 Sleeve - Frac 5.000 Advanced Upstream Frac Sleeve #23 Frac sleeve 107394- 000026 3.500 13,918.9 5,183.3 84.71 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #23 Water Swell H30187052 3/ 23 3.900 14,181.9 5,207.3 84.75 Sleeve - Frac 5.000 Advanced Upstream Frac Sleeve #22 Frac sleeve 107394- 000025 3.500 14,383.6 5,225.6 84.95 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #22 Water Swell H30187052 3/ 22 3.900 14,684.5 5,247.2 86.69 Sleeve - Frac 5.000 Advanced Upstream Frac Sleeve #21 Frac sleeve 107394- 000024 3.500 14,927.8 5,261.0 86.80 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #21 Water Swell H30187052 3/ 21 3.900 15,189.8 5,272.0 88.15 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.375" ball) #20, HYD563 Frac sleeve H80908039 2 3.323 15,432.7 5,278.1 89.19 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #20 Water Swell H30187052 3/ 20 3.900 15,695.2 5,279.7 89.80 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.313" ball) #19, HYD563 Frac sleeve H80908039 3 3.260 15,940.3 5,278.9 90.26 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #19 Water Swell H30187052 3/ 19 3.900 16,202.5 5,276.8 90.88 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.250" ball) #18, HYD563 Frac sleeve H80908039 4 3.198 16,524.9 5,272.7 90.96 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #18 Water Swell H30187052 3/ 18 3.900 16,707.3 5,266.6 92.30 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.188" ball) #17, HYD563 Frac sleeve H80908039 5 3.135 16,871.0 5,261.4 91.37 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #17 Water Swell H30187052 3/ 17 3.900 17,214.1 5,258.4 90.34 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.125" ball) #16, HYD563 Frac sleeve H80908039 6 3.073 17,498.9 5,256.2 90.34 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #16 Water Swell H30187052 3/ 16 3.900 17,719.6 5,256.2 89.93 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.063" ball) #15, HYD563 Frac sleeve H80908039 7 3.010 17,962.4 5,256.0 90.36 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #15 Water Swell H30187052 3/ 15 3.900 18,224.7 5,254.7 90.09 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.00" ball) #14, HYD563 Frac sleeve H80908072 9 2.955 HORIZONTAL, 3S-625, 1/18/2023 2:29:15 PM Vertical schematic (actual) Liner; 12,692.4-25,306.0 Intermediate; 35.1-12,842.0 Shoe - Mule; 12,698.7 Nipple - Landing; 12,591.3 Packer; 12,516.5 Gauge / Pump Sensor; 12,452.3 Intermediate String 1 Cement; 7,389.0 ftKB GAS LIFT; 6,667.9 Surface; 36.7-2,895.3 GAS LIFT; 2,778.2 Nipple - Landing; 2,034.2 Surface String Cement; 39.8 ftKB Conductor; 37.0-131.0 Hanger; 33.0 KUP PROD KB-Grd (ft) 36.77 RR Date 10/27/202 2 Other Elev… 3S-625 ... TD Act Btm (ftKB) 25,310.0 Well Attributes Field Name TRACT OPERATION MORTR05 Wellbore API/UWI 501032084200 Wellbore Status PROD Max Angle & MD Incl (°) 93.15 MD (ftKB) 18,825.75 WELLNAME WELLBORE3S-625 Annotation End DateH2S (ppm) DateComment Liner Details: Excludes Liner, Pup, Joints, casing, float, sub, shoe... Top (ftKB) Top (TVD) (ftKB) Top Incl (°) Item Des OD Nominal (in)Com Make Model Nominal ID (in) 18,508.9 5,254.7 90.16 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #14 Water Swell H30187052 3/ 14 3.900 18,730.6 5,249.2 92.77 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.945" ball) #13, HYD563 Frac sleeve H80908072 7 2.905 18,935.2 5,238.5 92.84 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #13 Water Swell H30187052 3/ 13 3.900 19,238.7 5,231.5 90.01 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.895" ball) #12, HYD563 Frac sleeve H80908072 8 2.855 19,522.8 5,231.7 90.01 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #12 Water Swell H30187052 3/ 12 3.900 19,744.6 5,231.8 89.95 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.845" ball) #11, HYD563 Frac sleeve H80908026 4 2.805 19,985.8 5,231.9 89.87 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #11 Water Swell H30187052 3/ 11 3.900 20,248.6 5,232.4 89.93 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.795" ball) #10, HYD563 Frac sleeve H80908039 8 2.755 20,493.5 5,232.8 89.93 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #10 Water Swell H30187052 3/ 10 3.900 20,716.3 5,233.2 89.96 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.745" ball) #9, HYD563 Frac sleeve H80908039 7 2.705 20,960.7 5,233.5 89.95 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #9 Water Swell H30187052 3/ 09 3.900 21,223.1 5,233.8 89.98 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.695" ball) #8, HYD563 Frac sleeve H80908039 6 2.655 21,545.8 5,234.4 89.86 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #8 Water Swell H30187052 3/ 08 3.900 21,728.0 5,234.7 89.86 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.645" ball) #7, HYD563 Frac sleeve H80908039 5 2.605 22,013.2 5,235.1 89.77 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #7 Water Swell H30187052 3/ 07 3.900 22,231.3 5,237.4 88.97 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.595" ball) #6, HYD563 Frac sleeve H80908039 4 2.555 22,476.3 5,241.7 88.95 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #6 Water Swell H30187052 3/ 06 3.900 22,738.6 5,245.2 89.46 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.545" ball) #5, HYD563 Frac sleeve H80908039 3 2.505 22,983.4 5,248.0 89.45 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #5 Water Swell H30187052 3/ 05 3.900 23,246.4 5,249.5 89.97 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.495" ball) #4, HYD563 Frac sleeve H80908039 2 2.465 23,409.0 5,249.6 89.91 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #4 Water Swell H30187052 3/ 04 3.900 23,753.1 5,250.0 89.92 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.455" ball) #3, HYD563 Frac sleeve H80908039 1 2.425 24,118.4 5,250.6 89.86 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #3 Water Swell H30187052 3/ 03 3.900 24,260.1 5,251.0 89.88 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.415" ball) #2, HYD563 Frac sleeve H80908039 0 2.385 24,464.4 5,251.2 89.95 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #2 Water Swell H30187052 3/ 02 3.900 24,767.0 5,251.6 89.99 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.375" ball) #1, HYD563 Frac sleeve H80908038 9 2.345 25,011.1 5,252.2 89.85 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #1 Water Swell H30187052 3/ 01 3.900 25,243.4 5,253.0 89.98 Sleeve - Frac 5.620 Alpha Pressure Sleeve 4 1/2" HYD 563 13.5# Q125 Alpha sleeve H81047006 8 3.000 25,247.1 5,253.0 89.99 Sleeve - Frac 5.630 WIV - 4 1/2" 13.5# P110 HYD563 - 2 pins @ 990 PSI - 1.25" ball WIV H80914004 2 1.250 25,306.0 5,253.0 90.00 5.200 HORIZONTAL, 3S-625, 1/18/2023 2:29:16 PM Vertical schematic (actual) Liner; 12,692.4-25,306.0 Intermediate; 35.1-12,842.0 Shoe - Mule; 12,698.7 Nipple - Landing; 12,591.3 Packer; 12,516.5 Gauge / Pump Sensor; 12,452.3 Intermediate String 1 Cement; 7,389.0 ftKB GAS LIFT; 6,667.9 Surface; 36.7-2,895.3 GAS LIFT; 2,778.2 Nipple - Landing; 2,034.2 Surface String Cement; 39.8 ftKB Conductor; 37.0-131.0 Hanger; 33.0 KUP PROD 3S-625 ... WELLNAME WELLBORE3S-625 2T12NR8ET12NR7ET12NR8E T13NR7E T12NR7E T13NR7E ADL380107ADL390697 ADL355032 ADL380106 ADL393883 ADL025528 ADL025544 4 ADL390434 2 18 712 1923 14 6 13 11 24 1 PALM 1 MORAINE 1 3S - 6 1 1 P B 1 3S-620 3S- 6 1 3 3S - 6 1 1 3S- 6 1 2 3S-6153S 1/26/2023 3S-625 Injection Sundry 3S-625 Open Interval 32-625 Well Trajectory 3S-625 OI Quarter Mile Radius Other Active Well P&A Well Exploration Well BHL CPAI Leases ADNR Section Unit Boundary Roads and Pads 3S-62500.50.25 Milesk 1. Operations Susp Well Insp Plug Perforations Fracture Stimulate Pull Tubing Operations shutdown Performed: Install Whipstock Perforate Other Stimulate Alter Casing Change Approved Program Mod Artificial Lift Perforate New Pool Repair Well Coiled Tubing Ops Other: Convert to PROD Development Exploratory Stratigraphic Service 6. API Number: 7. Property Designation (Lease Number): 8. Well Name and Number: 9. Logs (List logs and submit electronic data per 20AAC25.071): 10. Field/Pool(s): 11. Present Well Condition Summary: Total Depth measured 25310'feet None feet true vertical 5253'feet None feet Effective Depth measured 25310'feet 12516', 12692'feet true vertical 5253'feet 5051', 5074'feet Perforation depth Measured depth True Vertical depth Tubing (size, grade, measured and true vertical depth) 4-1/2" L-80 12702' MD 5075' TVD Packers and SSSV (type, measured and true vertical depth) 12516' MD 12692' MD N/A 5051' TVD 5074' TVD N/A 12. Stimulation or cement squeeze summary: Intervals treated (measured): Treatment descriptions including volumes used and final pressure: N/A 13a. Prior to well operation: Subsequent to operation: 13b. Pools active after work: Torok Oil Pool 15. Well Class after work: Daily Report of Well Operations Exploratory Development Service Stratigraphic Copies of Logs and Surveys Run 16. Well Status after work: Oil Gas WDSPL Electronic Fracture Stimulation Data GSTOR GINJ SUSP SPLUG Sundry Number or N/A if C.O. Exempt: Authorized Name and Digital Signature with Date: Contact Name: Contact Email: Authorized Title: Contact Phone: 2895' 2572' Burst Collapse Production Liner 12807' 12614' Casing 5090' 4-1/2" 12842' 25306' 5253' 2859' 131'Conductor Surface Intermediate 20" 10-3/4" 94' measured TVD 7-5/8" STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION REPORT OF SUNDRY WELL OPERATIONS 222-079 50-103-20842-00-00 P.O. Box 100360 Anchorage, AK 99510 3. Address: ConocoPhillips Alaska, Inc. N/A 5. Permit to Drill Number:2. Operator Name N 4. Well Class Before Work: ADL0025528, ADL0025544, ADL0380107 Kuparuk River Field/ Torok Oil Pool KRU 3S-625 Plugs Junk measured Length measured true vertical Packer Representative Daily Average Production or Injection Data Casing Pressure Tubing Pressure 14. Attachments (required per 20 AAC 25.070, 25.071, & 25.283) Gas-Mcf MD ~ Size 131' Injector ~~ N/A Sr Pet Eng: Sr Pet Geo: Sr Res Eng: WINJ WAG ~ Water-BblOil-Bbl 17. I hereby certify that the foregoing is true and correct to the best of my knowledge. N/A Packer: HAL TNT Prod Packer Packer: ZXP w/TieBK Sleeve LTP SSSV: None Lynn Aleshire lynn.aleshire@conocophillips.com (907) 265-6525Surveillance Reservoir Engineer Frac Sleeves alternating:12891-25247' Frac Sleeves alternating: 5094-5253' Form 10-404 Revised 10/2022 Due Within 30 days of Operations Submit in PDF format to aogcc.permitting@alaska.gov 1131 481 3177 5341578 By Samantha Carlisle at 9:05 am, Jan 19, 2023 DTTMSTART JOBTYP SUMMARYOPS 12/21/2022 SUPPORT OTHER OPERATIONS LRS CONTINUE R/U, SCAFFOLDERS TO BUILD HOOCHES, WELL SUPPORT TYING IN TANKS 12/22/2022 SUPPORT OTHER OPERATIONS WALK DOWN PERFORMED WITH OPERATIONS. BUILDING AND WRAPING OF HOOCHES COMPLETE.CHEMICAL PUMP AND VAC TRUCKS NOT AVAILABLE UNTIL TOMORROW MORNING.START INJECTING .4MMSCF/D G/L. DOWN I/A. 12/23/2022 SUPPORT OTHER OPERATIONS VAC TRUCKS ARRIVED ON LOCATION. CHEMICAL PUMP ON SITE AND RIGGED UP. HOLD PRE-JOB SAFETY MEETING. DHD PERFORM I/A FLUID LEVEL SHOT, I/A IS CLEAR OF DIESEL, GAS AT THE OV. POP 3S-625.AT 14:45.SHIPPING FLUID RETURNS TO TANKS, GAS RETURNS TO PLANT. UNLOAD WELL PER PROCEDURE. 12/24/2022 SUPPORT OTHER OPERATIONS LRS CONTINUED TO UNLOAD THE WELL. THE WELL STARTED PRODUCING OIL DURING THE DAY WITH FLUID MEETING SPEC. 16:00 LRS CO-MINGLE THE FLUID RETURNS WITH THE GAS BEING SENT TO THE PLANT. SCALE INHIBITOR IS BEING INJECTED INTO THE FLUID STREAM AT A RATE OF 10 GALLONS PER DAY. ALL TANKS ON LOCATION ARE EMPTY. 12/25/2022 SUPPORT OTHER OPERATIONS LRS CONTINUE TO UNLOAD THE WELL PER PROCEDURE. 12/26/2022 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 12/27/2022 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 12/28/2022 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 12/29/2022 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 12/30/2022 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 12/31/2022 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 1/1/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 1/2/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 3S-625 Convert to Production Summary of Operations 1/3/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 1/4/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 1/5/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 1/6/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 1/7/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 1/8/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE. 1/9/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL PER PROCEDURE, SI WELL TO BEGIN BLOW DOWN AND RIG DOWN. 1/10/2023 SUPPORT OTHER OPERATIONS RIGGED DOWN COMPLETE JOB, STAGED EQUIPMENT AT 3T. CALLED BACK TO RIG UP ON WELL TO PRODUCE. 1/11/2023 SUPPORT OTHER OPERATIONS RIGGED EQUIPMENT BACK UP POPPED 3S-325 THRU TEST SEPARATOR OUTLET WELL 3S-19 1/12/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL THRU SEPARATOR AND DOWN 3S-19 FLOWLINE 1/13/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL THRU SEPARATOR AND DOWN 3S-19 FLOWLINE 1/14/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL THRU SEPARATOR AND DOWN 3S-19 FLOWLINE 1/15/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL THRU SEPARATOR AND DOWN 3S-19 FLOWLINE 1/16/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL THRU SEPARATOR AND DOWN 3S-19 FLOWLINE 1/17/2023 SUPPORT OTHER OPERATIONS LRS CONTINUE TO FLOW WELL THRU SEPARATOR AND DOWN 3S-19 FLOWLINE, SI WELL @ 03:00 BEGIN BLOWDOWN/RIG DOWN Last Rev Reason Annotation Wellbore End Date Last Mod By Rev Reason: Set DV / GLV & Pulled catcher/RBP 3S-625 12/6/2022 zembaej Casing Strings Csg Des OD (in) ID (in) Top (ftKB) Set Depth (ftKB) Set Depth (TVD) (ftKB) Wt/Len (lb/ft) Grade Top Thread Conductor 20 19.12 37.0 131.0 131.0 154.34 GRX-65 Surface 10 3/4 9.95 36.7 2,895.3 2,571.9 45.50 L-80 HYD 563 Intermediate 7 5/8 6.88 35.1 12,842.0 5,090.3 29.70 L-80 Hyd 563 Liner 4 1/2 3.95 12,692.4 25,306.0 5,253.0 12.60 L-80 HYD 563 Tubing Strings: string max indicates LONGEST segment of string Top (ftKB) 32.9 Set Depth 12,701.9 Set Depth 5,075.3 String Ma 4 1/2 Tubing Description Tubing Completion Upper Wt (lb/ft) 12.60 Grade L-80 Top Connection Hydril 563 ID (in) 3.96 Completion Details: excludes tubing, pup, space out, thread, RKB... Top (ftKB) Top (TVD) (ftKB) Top Incl (°) Item Des OD Nominal (in)Com Make Model Nominal ID (in) 32.9 32.9 0.00 Hanger 10.850 Streamflo 4-1/2" Tubing Hanger, H563 StreamF lo 3020227 9 3.958 2,034.2 1,966.6 30.23 Nipple - Landing 4.925 NIPPLE, Landing, HAL 3.813" X, Nickel HAL 3.980 2,778.2 2,500.9 51.43 GAS LIFT 6.000 4-1/2" x 1" Camco KBG 4-5 GLM Camco 127141- 01_VCS 3.865 6,667.9 3,683.2 75.98 GAS LIFT 6.000 4-1/2" x 1" Camco KBMG GLM Camco 127141- 01-SL2 3.865 12,452.4 5,042.1 81.35 Gauge / Pump Sensor 5.694 HAL ROC DHG + Mandrel, 4-1/2" 12.6# L-80 Hyd 563 HAL OPS- 001786 ADD 3.925 12,516.5 5,051.5 81.88 Packer 6.000 HAL TNT Production Packer 4.5"x7.63" T-Blue HAL 1027226 15 3.958 12,591.3 5,061.5 82.60 Nipple - Landing 4.925 NIPPLE,LANDING,4-1/2",DB-6, Nickel,3.562",H563 BXP HAL 4402228 -01 3.908 12,692.9 5,074.2 83.08 Locator Baker Shear Type Locator sub - above locating shoulder Baker 12,698.7 5,074.9 83.11 Shoe - Mule 5.210 Halliburton Ratcheting Muleshoe Baker 3.920 Mandrel Inserts : excludes pulled inserts Top (ftKB) Top (TVD) (ftKB) Top Incl (°) St ati on No /S Serv Valve Type Latch Type OD (in) TRO Run (psi) Run Date Com Make Model Port Size (in) 2,778.2 2,500.9 51.43 1 GAS LIFT DMY BK 6 0.0 12/6/2022 Camco KBG 0.000 6,667.9 3,683.2 75.98 2 GAS LIFT OV BK 6 0.0 12/6/2022 Camco KBG 0.438 Liner Details: Excludes Liner, Pup, Joints, casing, float, sub, shoe... Top (ftKB) Top (TVD) (ftKB) Top Incl (°) Item Des OD Nominal (in)Com Make Model Nominal ID (in) 12,692.4 5,074.1 83.08 Packer 6.540 5.5" X 7-5/8" ZXP Packer w/ 11.29' x 5.75" ID TieBK Sleeve - LTP @ ~12,692' ZXP LTP H29645026 5 4.810 12,712.4 5,076.5 83.17 Nipple - RS 6.050 RS Packoff Seal Nipple R/S Nipple 10553458 4.250 12,724.0 5,077.9 83.23 XO Reducing 6.060 5.5" Hyd 563 box X pin 4.5" Hyd 563 cross over 3.900 12,891.1 5,093.7 86.54 Sleeve - Frac 5.000 Advanced Upstream Frac Sleeve #24 Locator - not frac'd - Frac sleeve 107394- 000027 3.500 13,453.9 5,140.6 84.74 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #24 Water Swell H30187052 3/ 24 3.900 13,635.7 5,157.3 84.78 Sleeve - Frac 5.000 Advanced Upstream Frac Sleeve #23 Frac sleeve 107394- 000026 3.500 13,918.9 5,183.3 84.71 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #23 Water Swell H30187052 3/ 23 3.900 14,181.9 5,207.3 84.75 Sleeve - Frac 5.000 Advanced Upstream Frac Sleeve #22 Frac sleeve 107394- 000025 3.500 14,383.6 5,225.6 84.95 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #22 Water Swell H30187052 3/ 22 3.900 14,684.5 5,247.2 86.69 Sleeve - Frac 5.000 Advanced Upstream Frac Sleeve #21 Frac sleeve 107394- 000024 3.500 14,927.8 5,261.0 86.80 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #21 Water Swell H30187052 3/ 21 3.900 15,189.8 5,272.0 88.15 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.375" ball) #20, HYD563 Frac sleeve H80908039 2 3.323 15,432.7 5,278.1 89.19 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #20 Water Swell H30187052 3/ 20 3.900 15,695.2 5,279.7 89.80 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.313" ball) #19, HYD563 Frac sleeve H80908039 3 3.260 15,940.3 5,278.9 90.26 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #19 Water Swell H30187052 3/ 19 3.900 16,202.5 5,276.8 90.88 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.250" ball) #18, HYD563 Frac sleeve H80908039 4 3.198 16,524.9 5,272.7 90.96 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #18 Water Swell H30187052 3/ 18 3.900 16,707.3 5,266.6 92.30 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.188" ball) #17, HYD563 Frac sleeve H80908039 5 3.135 16,871.0 5,261.4 91.37 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #17 Water Swell H30187052 3/ 17 3.900 17,214.1 5,258.4 90.34 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.125" ball) #16, HYD563 Frac sleeve H80908039 6 3.073 17,498.9 5,256.2 90.34 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #16 Water Swell H30187052 3/ 16 3.900 17,719.6 5,256.2 89.93 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.063" ball) #15, HYD563 Frac sleeve H80908039 7 3.010 17,962.4 5,256.0 90.36 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #15 Water Swell H30187052 3/ 15 3.900 18,224.7 5,254.7 90.09 Sleeve - Frac 4.500 BAKER Frac Sleeve (3.00" ball) #14, HYD563 Frac sleeve H80908072 9 2.955 HORIZONTAL, 3S-625, 1/18/2023 2:29:15 PM Vertical schematic (actual) Liner; 12,692.4-25,306.0 Intermediate; 35.1-12,842.0 Shoe - Mule; 12,698.7 Nipple - Landing; 12,591.3 Packer; 12,516.5 Gauge / Pump Sensor; 12,452.3 Intermediate String 1 Cement; 7,389.0 ftKB GAS LIFT; 6,667.9 Surface; 36.7-2,895.3 GAS LIFT; 2,778.2 Nipple - Landing; 2,034.2 Surface String Cement; 39.8 ftKB Conductor; 37.0-131.0 Hanger; 33.0 KUP PROD KB-Grd (ft) 36.77 RR Date 10/27/202 2 Other Elev 3S-625 ... TD Act Btm (ftKB) 25,310.0 Well Attributes Field Name TRACT OPERATION MORTR05 Wellbore API/UWI 501032084200 Wellbore Status PROD Max Angle & MD Incl (°) 93.15 MD (ftKB) 18,825.75 WELLNAME WELLBORE3S-625 Annotation End DateH2S (ppm) DateComment Liner Details: Excludes Liner, Pup, Joints, casing, float, sub, shoe... Top (ftKB) Top (TVD) (ftKB) Top Incl (°) Item Des OD Nominal (in)Com Make Model Nominal ID (in) 18,508.9 5,254.7 90.16 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #14 Water Swell H30187052 3/ 14 3.900 18,730.6 5,249.2 92.77 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.945" ball) #13, HYD563 Frac sleeve H80908072 7 2.905 18,935.2 5,238.5 92.84 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #13 Water Swell H30187052 3/ 13 3.900 19,238.7 5,231.5 90.01 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.895" ball) #12, HYD563 Frac sleeve H80908072 8 2.855 19,522.8 5,231.7 90.01 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #12 Water Swell H30187052 3/ 12 3.900 19,744.6 5,231.8 89.95 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.845" ball) #11, HYD563 Frac sleeve H80908026 4 2.805 19,985.8 5,231.9 89.87 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #11 Water Swell H30187052 3/ 11 3.900 20,248.6 5,232.4 89.93 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.795" ball) #10, HYD563 Frac sleeve H80908039 8 2.755 20,493.5 5,232.8 89.93 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #10 Water Swell H30187052 3/ 10 3.900 20,716.3 5,233.2 89.96 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.745" ball) #9, HYD563 Frac sleeve H80908039 7 2.705 20,960.7 5,233.5 89.95 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #9 Water Swell H30187052 3/ 09 3.900 21,223.1 5,233.8 89.98 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.695" ball) #8, HYD563 Frac sleeve H80908039 6 2.655 21,545.8 5,234.4 89.86 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #8 Water Swell H30187052 3/ 08 3.900 21,728.0 5,234.7 89.86 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.645" ball) #7, HYD563 Frac sleeve H80908039 5 2.605 22,013.2 5,235.1 89.77 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #7 Water Swell H30187052 3/ 07 3.900 22,231.3 5,237.4 88.97 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.595" ball) #6, HYD563 Frac sleeve H80908039 4 2.555 22,476.3 5,241.7 88.95 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #6 Water Swell H30187052 3/ 06 3.900 22,738.6 5,245.2 89.46 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.545" ball) #5, HYD563 Frac sleeve H80908039 3 2.505 22,983.4 5,248.0 89.45 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #5 Water Swell H30187052 3/ 05 3.900 23,246.4 5,249.5 89.97 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.495" ball) #4, HYD563 Frac sleeve H80908039 2 2.465 23,409.0 5,249.6 89.91 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #4 Water Swell H30187052 3/ 04 3.900 23,753.1 5,250.0 89.92 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.455" ball) #3, HYD563 Frac sleeve H80908039 1 2.425 24,118.4 5,250.6 89.86 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #3 Water Swell H30187052 3/ 03 3.900 24,260.1 5,251.0 89.88 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.415" ball) #2, HYD563 Frac sleeve H80908039 0 2.385 24,464.4 5,251.2 89.95 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #2 Water Swell H30187052 3/ 02 3.900 24,767.0 5,251.6 89.99 Sleeve - Frac 4.500 BAKER Frac Sleeve (2.375" ball) #1, HYD563 Frac sleeve H80908038 9 2.345 25,011.1 5,252.2 89.85 Packer - Swell 4.500 Swell Packer 5.80" OD HYD563 P110S ASSY #1 Water Swell H30187052 3/ 01 3.900 25,243.4 5,253.0 89.98 Sleeve - Frac 5.620 Alpha Pressure Sleeve 4 1/2" HYD 563 13.5# Q125 Alpha sleeve H81047006 8 3.000 25,247.1 5,253.0 89.99 Sleeve - Frac 5.630 WIV - 4 1/2" 13.5# P110 HYD563 - 2 pins @ 990 PSI - 1.25" ball WIV H80914004 2 1.250 25,306.0 5,253.0 90.00 5.200 HORIZONTAL, 3S-625, 1/18/2023 2:29:16 PM Vertical schematic (actual) Liner; 12,692.4-25,306.0 Intermediate; 35.1-12,842.0 Shoe - Mule; 12,698.7 Nipple - Landing; 12,591.3 Packer; 12,516.5 Gauge / Pump Sensor; 12,452.3 Intermediate String 1 Cement; 7,389.0 ftKB GAS LIFT; 6,667.9 Surface; 36.7-2,895.3 GAS LIFT; 2,778.2 Nipple - Landing; 2,034.2 Surface String Cement; 39.8 ftKB Conductor; 37.0-131.0 Hanger; 33.0 KUP PROD 3S-625 ... WELLNAME WELLBORE3S-625 WELL NAME API #SERVICE ORDER # FIELD NAMESERVICE DESCRIPTION DELIVERABLE DESCRIPTION DATA TYPE DATE LOGGED CDDirectional Survey3S-625 50-103-20842-00-00 222-079 KRU MWD/LWD/DD VISION SERVICES FINAL FIELD 1#REF! #REF! #REF! #REF! #REF! #REF! #REF! #REF!Transmittal Receipt________________________________ X____________________________________________Print Name Signature DatePlease return via courier or sign/scan and email a copy to Schlumberger.VTuong@slb.comSLB Auditor -A Transmittal Receipt signature confirms that a package (box, envelope, etc.) has been received and the contents of the package have been verified to match the media noted above. The specific content of the CDs and/or hardcopy prints may or may not have been verified for correctness or quality level at this point.# Schlumberger-PrivateBy Meredith Guhl at 8:48 am, Jan 04, 2023222-079T37412Meredith GuhlDigitally signed by Meredith Guhl Date: 2023.01.04 08:48:48 -09'00' 1a. Well Status:Oil SPLUG Other Abandoned Suspended 1b. Well Class: 20AAC 25.105 20AAC 25.110 Development Exploratory GINJ WINJ WDSPL No. of Completions: __________________ Service Stratigraphic Test 2. Operator Name:6. Date Comp., Susp., or 14.Permit to Drill Number / Sundry: Aband.: 3. Address: 7. Date Spudded: 15. API Number: 4a. Location of Well (Governmental Section): 8. Date TD Reached: 16. Well Name and Number: Surface: Top of Productive Interval: 3663' FSL, 4154' FWL SESW S14 T12N R7E 9. Ref Elevations: KB: 17. Field / Pool(s): GL: 23.9 BF: Total Depth: 10.Plug Back Depth MD/TVD: 18.Property Designation: 4b. Location of Well (State Base Plane Coordinates, NAD 27): 11. Total Depth MD/TVD: 19. DNR Approval Number: Surface: x- y- Zone- 4 TPI: x- y- Zone- 4 12. SSSV Depth MD/TVD: 20. Thickness of Permafrost MD/TVD: Total Depth: x- y- Zone- 4 5. Directional or Inclination Survey: Yes (attached) No 13. Water Depth, if Offshore: 21. Re-drill/Lateral Top Window MD/TVD: Submit electronic information per 20 AAC 25.050 N/A (ft MSL) 22.Logs Obtained: 23. BOTTOM 20" GRX-65 131'10 yards 10 3/4" L-80 2,574' 7 5/8" L-80 5,025' 7 5/8" TN11OS 5,030' 4 1/2" L-80 5,259' 24.Open to production or injection? Yes No 25. 26. Was hydraulic fracturing used during completion? Yes No DEPTH INTERVAL (MD) AMOUNT AND KIND OF MATERIAL USED 27. Date First Production: Method of Operation (Flowing, gas lift, etc.): Hours Tested: Production for Gas-MCF: Test Period Casing Press: Calculated Gas-MCF: Oil Gravity - API (corr): Press. 24-Hour Rate ACID, FRACTURE, CEMENT SQUEEZE, ETC. CASING, LINER AND CEMENTING RECORD List all logs run and, pursuant to AS 31.05.030 and 20 AAC 25.071, submit all electronic data within 90 days of completion, 9.875" TUBING RECORD 25,306' Lead: 297 bbls 15.3 ppg Class G 5,074' 9.875" 6.5" 12,702'4.5 12,516' MD/5,051'TVD 12,692' MD/ 5,074'TVD BOTTOM 13.5" Lead: 452bbls 10.7ppg Class G Tail: 57 bbl 15.8ppg Class G CASING 501-103-20842-00-00 KRU 3S-625 9/12/2022 25,310'MD/5,253'TVD N/A 60.7 P.O.Box 100360, Anchorage, AK 99510-0360 475974 2711' FSL, 3521' FWL SESW S18 T12N R8E 4712' FSL, 1161' FWL SESW S2 T12N R7E STATE OF ALASKA ALASKA OIL AND GAS CONSERVATION COMMISSION WELL COMPLETION OR RECOMPLETION REPORT AND LOG ConocoPhillips Alaska, Inc. WAG Gas 10/26/2022 222-079 10/10/2022 CEMENTING RECORD 5994838 1,593'MD/1,567'TVD SETTING DEPTH TVD 6006460 TOP HOLE SIZE AMOUNT PULLEDTOP SETTING DEPTH MD PACKER SET (MD/TVD) 12,692' 42" 12.6 5993847 Kuparuk River Field/ Torok Oil Pool ADL 380107, ADL 025544, ADL 025528 LONS 01-01103 40' 33.7 40' 12,342' 2,895' If Yes, list each interval open (MD/TVD of Top and Bottom; Perforation Size and Number; Date perf'd or liner run): WT. PER FT.GRADE 466052 463102 If Yes, list each interval open (MD/TVD of Top and Bottom; Perforation Size and Number; Date perf'd or liner run): Liner: 12,692'MD/5,074'TVD to 25,306' MD/5,259'TVD Gas-Oil Ratio:Choke Size: suspension, or abandonment; or within 90 days of acquisition of the log, whichever occurs first. Types of logs to be listed include, but are not limited to: mud log, spontaneous potential, gamma ray, caliper, resistivity, porosity, magnetic resonance, dipmeter, formation tester, temperature, cement evaluation, casing collar locator, jewelry, and perforation record. Acronyms may be used. Attach a separate page only if necessary. N/A GR, RES, DEN, DIR, AZI, PWD, NEU, POR,SONIC, 40' 40' Per 20 AAC 25.283 (i)(2) attach electronic information 29.7 12,842' 40' 5,025' 154.34 45.5 131' 40' 12,342' SIZE DEPTH SET (MD) Sr Res EngSr Pet GeoSr Pet Eng N/A Oil-Bbl: Water-Bbl: Water-Bbl: PRODUCTION TEST Date of Test: Oil-Bbl: Flow Tubing Form 10-407 Revised 10/2022 Due within 30 days of Completion, Suspension, or Abandonment By James Brooks at 12:09 pm, Nov 23, 2022 Completed 10/26/2022 JSB RBDMS JSB 120622 50- G KRU 3S-625 10/26/2022 Date Comp DSR-12-12-22 G Permit to Drill Number Service Kuparuk River Field/ Torok Oil Pool 222-079 Conventional Core(s): Yes No Sidewall Cores: 30. MD TVD Surface Surface 1593 1567 Ugnu B 1658 1627 1796 1755 2088 2013 C-80 2962 2612 C-50 5274 3348 Coyote/K3 8415 4108 Torok Shales 9557 4387 13307 5127 25310 5253 31. List of Attachments: Directional Survey, Well Schematic, Cement Operations, Operations Summary 32. I hereby certify that the foregoing is true and correct to the best of my knowledge. Contact Name: Jenna Taylor Digital Signature with Date: Contact Phone:907-265-4522 General: Item 1a: Item 1b: Item 4b: Item 9: Item 15: Item 19: Item 20: Item 22: Item 23: Item 24: Item 27: Item 28: Item 30: Item 31: If Yes, list formations and intervals cored (MD/TVD, From/To), and briefly summarize lithology and presence of oil, gas or water (submit separate pages if needed). Submit detailed descriptions, core chips, photographs, and all subsequent laboratory analytical results per 20 AAC 25.071 no matter when acquired. Formation Name at TD: Torok Yes No Well tested? Yes No 28. CORE DATA If Yes, list intervals and formations tested, briefly summarizing test results for each. Attach separate pages if needed and submit detailed test info including reports and Excel or ASCII tables per 20 AAC 25.071. NAME Permafrost - Top Permafrost - Base 29. GEOLOGIC MARKERS and POOL BOUNDARIES: (list all encountered) FORMATION TESTS Top of Productive Interval (Torok) Well Class - Service wells: Gas Injection, Water Injection, Water-Alternating-Gas Injection, Salt Water Disposal, Water Supply for Injection, Observation, or Other. Ugnu A Report the Division of Oil & Gas / Division of Mining Land and Water: Plan of Operations (LO/Region YY-123), Land Use Permit (LAS 12345), and/or Easement (ADL 123456) number. The Kelly Bushing, Ground Level, and Base Flange elevations in feet above Mean Sea Level. Use same as reference for depth measurements given in other spaces on this form and in any attachments. The API number reported to AOGCC must be 14 digits (ex: 50-029-20123-00-00). This form and the required attachments provide a complete and concise record for each well drilled in Alaska. Submit a current well schematic diagram with each 10-407. Submit 10-407 and attachments in PDF format to aogcc.permitting@alaska.gov. All laboratory analytical reports from a well must be submitted to the AOGCC, no matter when the analyses are conducted per 20 AAC 25.071. Information to be attached includes, but is not limited to: summary of daily operations, wellbore schematic, directional or inclination survey, as-built, core analysis, paleontological report, production or well test results, per 20 AAC 25.070. Multiple completion is defined as a well producing from more than one pool with production from each pool completely segregated. Each segregated pool is a completion. TPI (Top of Producing Interval). Authorized Name and INSTRUCTIONS Contact Email: jenna.l.taylor@conocophillips.com Authorized Title: Senior Wells Analyst West Sak Pursuant to 20 AAC 25.070, attach to this form: well schematic diagram, summary of daily well operations, directional or inclination survey, and other tests as required including, but not limited to: core analysis, paleontological report, production or well test results. Report measured depth and true vertical thickness of permafrost. Provide MD and TVD for the top and base of permafrost in Box 29. Attached supplemental records should show the details of any multiple stage cementing and the location of the cementing tool. If this well is completed for separate production from more than one interval (multiple completion), so state in item 1, and in item 23 show the producing intervals for only the interval reported in item 26. (Submit a separate form for each additional interval to be separately produced, showing the data pertinent to such interval). Provide a listing of intervals cored and the corresponding formations, and a brief description in this box. Pursuant to 20 AAC 25.071, submit detailed descriptions, core chips, photographs, and all subsequent laboratory analytical results, including, but not limited to: porosity, permeability, fluid saturation, fluid composition, fluid fluorescence, vitrinite reflectance, geochemical, or paleontology. Method of Operation: Flowing, Gas Lift, Rod Pump, Hydraulic Pump, Submersible, Water Injection, Gas Injection, Shut-in, or Other (explain). Provide a listing of intervals tested and the corresponding formation, and a brief summary in this box. Submit detailed test and analytical laboratory information required by 20 AAC 25.071. Review the reporting requirements of 20 AAC 25.071 and, pursuant to AS 31.05.030, submit all electronic data within 90 days of completion, suspension, or abandonment; or 90 days after log acquisition, whichever occurs first. 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rom:McLellan, Bryan J (OGC) To:AOGCC Records (CED sponsored) Subject:FW: [EXTERNAL]RE: 3S-625 (PTD 222-079) Fracture Stimulation Sundry Date:Monday, November 14, 2022 9:08:28 AM For the wellfile… Bryan McLellan Senior Petroleum Engineer Alaska Oil & Gas Conservation Commission 333 W 7th Ave Anchorage, AK 99501 Bryan.mclellan@alaska.gov +1 (907) 250-9193 From: Morrow, Dustin W <Dustin.W.Morrow@conocophillips.com> Sent: Friday, November 11, 2022 11:34 AM To: McLellan, Bryan J (OGC) <bryan.mclellan@alaska.gov> Subject: RE: [EXTERNAL]RE: 3S-625 Fracture Stimulation Sundry Mr. McLellan, Our reservoir engineer’s estimate is the following: Here is the reservoir pressure and depth for the Moraine. 2,300 psi at 5,175' TVD (subsea) Which would give us 1783psi at 0.1psi/ft gas gradient Thank you, Dustin W. Morrow Staff Completions Engineer ConocoPhillips Alaska Cell: 832-493-9141 Office: 907-263-4752 From: McLellan, Bryan J (OGC) <bryan.mclellan@alaska.gov> Sent: Thursday, November 10, 2022 2:01 PM To: Morrow, Dustin W <Dustin.W.Morrow@conocophillips.com> Subject: RE: [EXTERNAL]RE: 3S-625 Fracture Stimulation Sundry So that would give a MPSP = reservoir pressure minus .1 psi/ft gas gradient = 2205 psi. Bryan McLellan Senior Petroleum Engineer Alaska Oil & Gas Conservation Commission th 333 W 7 Ave Anchorage, AK 99501 Bryan.mclellan@alaska.gov +1 (907) 250-9193 From: Morrow, Dustin W <Dustin.W.Morrow@conocophillips.com> Sent: Thursday, November 10, 2022 12:41 PM To: McLellan, Bryan J (OGC) <bryan.mclellan@alaska.gov> Subject: RE: [EXTERNAL]RE: 3S-625 Fracture Stimulation Sundry Mr. McLellan, I asked the reservoir engineer for their most recent downhole pressure estimate after receiving your question. I just want to let you know I am working on it and want you to have the most accurate information. While we wait… We ended the drilling with 10.0ppg brine in the well to kill so we are looking at approximately 5250 * .052 * 10.0 = 2730psi formation pressure. Thank you, Dustin W. Morrow Staff Completions Engineer ConocoPhillips Alaska Cell: 832-493-9141 Office: 907-263-4752 From: McLellan, Bryan J (OGC) <bryan.mclellan@alaska.gov> Sent: Thursday, November 10, 2022 10:33 AM To: Morrow, Dustin W <Dustin.W.Morrow@conocophillips.com> Subject: RE: [EXTERNAL]RE: 3S-625 Fracture Stimulation Sundry Dustin, The MPSP box was left blank on the 10-403 form, and I couldn’t find the reservoir pressure to calculate it. Could you send over reservoir pressure/TVD for the MPSP calculation? 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ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϳ ϯϬη,LJďŽƌ' DŝŶŝĨƌĂĐ ϭϱ ϭϮ͕ϲϬϬ ϯϬϬ ϯϬϬ Ϭ͗ϮϬ͗ϬϬ ϭ͗ϰϵ͗ϮϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϴ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϰϬ ϭϲ͕ϭϯϲ ϯϴϰ ϯϴϰ Ϭ͗Ϭϵ͗ϯϲ ϭ͗Ϯϵ͗ϮϮ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬϬ͘Ϯϱ Ϭ͘ϭϱϭͲϵ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϵ͗ϰϲϭͲϭϬ ϯϬη,LJďŽƌ' ƐƚĂďůŝƐŚ^ƚĂďůĞ&ůƵŝĚ ϭϱ ϰ͕ϮϬϬ ϭϬϬ ϭϬϬ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϵ͗ϰϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϭϭ ϯϬη,LJďŽƌ' WĂĚ ϰϬ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϯ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϭϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϰϬ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϳ͗ϮϬ ϭ͗Ϭϲ͗Ϯϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϭϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϰϬ ϭϮ͕ϬϬϬ Ϯϴϲ Ϯϵϵ ϭϮ͕ϬϬϬ Ϭ͗Ϭϳ͗Ϯϴ Ϭ͗ϰϵ͗Ϭϲ Ϯ͘ϬϬϬ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϭϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϰϬ ϭϴ͕ϬϬϬ ϰϮϵ ϰϲϳ ϯϲ͕ϬϬϬ Ϭ͗ϭϭ͗ϰϭ Ϭ͗ϰϭ͗ϯϴ Ϯ͘ϬϬϬ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϭϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϰϬ ϭϴ͕ϬϬϬ ϰϮϵ ϰϴϳ ϱϰ͕ϬϬϬ Ϭ͗ϭϮ͗ϭϭ Ϭ͗Ϯϵ͗ϱϲ Ϯ͘ϬϬϬ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϭϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϰϬ ϭϮ͕ϬϬϬ Ϯϴϲ ϯϯϳ ϰϴ͕ϬϬϬ Ϭ͗Ϭϴ͗Ϯϳ Ϭ͗ϭϳ͗ϰϱ Ϯ͘ϬϬϬ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϭϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϰϬ ϭϬ͕ϬϬϬ Ϯϯϴ ϮϵϮ ϱϬ͕ϬϬϬ Ϭ͗Ϭϳ͗ϭϵ Ϭ͗Ϭϵ͗ϭϵ Ϯ͘ϬϬϬ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭͲϭϴ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬϬϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮͲϭϬ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϯͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗ϭϲ͗Ϯϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϱϯͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ ϭ͗Ϭϵ͗ϭϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϯͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϱϬ͗Ϯϳ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϯͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϰϲ͗Ϯϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϯͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϰϮ͗ϭϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϯͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗ϯϳ͗Ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϯͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϯϬ͗ϱϵ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϯͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗Ϯϰ͗ϰϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϮϱϬ͘ϭϱϯͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗ϭϴ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϮϱϬ͘ϭϱϯͲϭϬ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϯϳ ϭϱ͕ϱϬϳ ϯϲϵ ϯϲϵϬ͗Ϭϵ͗ϱϵ Ϭ͗ϭϯ͗Ϭϵ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬϬ͘ϮϱϬ͘ϱϬϬ͘ϭϱϯͲϭϭ &ƌĞĞnjĞWƌŽƚĞĐƚ &ƌĞĞnjĞWƌŽƚĞĐƚ ϭϱ Ϯ͕ϬϬϬ ϰϴ ϰϴ Ϭ͗Ϭϯ͗ϭϬ Ϭ͗Ϭϯ͗ϭϬ ϭϬϬϬ͘ϬϬϯͲϭϮ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷ>ŝƋƵŝĚĚĚŝƚŝǀĞƐƌLJĚĚŝƚŝǀĞƐϱϬͲϭϬϯͲϮϬϴϰϮ,QWHUYDO.XSDUXN6DQGV#IW),QWHUYDO.XSDUXN6DQGV#IW),QWHUYDO.XSDUXN6DQGV#IW)ŽŶŽĐŽWŚŝůůŝƉƐͲϯ^dĞƐƚĂƐĞWůĂŶŶĞĚĞƐŝŐŶϭ h^dKD ZŽŶŽĐŽWŚŝůůŝƉƐ&>^ W/ &;ůďͬŐĂůͿϴ͘ϱϰ>dϳϬ͘ϯϵϰϬϭϴϴϴ> ^ ϯ^ͲϲϮϱ^> ^KZ Z,^d;Σ&Ϳϭϰϱ>KE'ͲϭϱϬ͘ϭϵϴϲϭϱ&KZDd/KE<ƵƉĂƌƵŬd DĂdžWƌĞƐƐƵƌĞ;ƉƐŝͿϵϬϬϬΎ džĐĞĞĚƐϴϬйŽĨďƵƌƐƚƉƌĞƐƐƵƌĞΎWƌŽƉ ^ůƵƌƌLJ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶ^ůƵƌƌLJ ĞƐŝŐŶWƌŽƉ ^ƚĂŐĞ/ŶƚĞƌǀĂů >ͲϮϴD >Ͳϯϭ >ŽƐƵƌĨͲϯϬϬ DKͲϲϳ >sdͲϮϬϬ t'Ͳϯϲ KƉƚŝ&ůŽͲ/// KƉƚŝ&ůŽͲ// ^WƌĞĂŬĞƌ ͲϲdƌĞĂƚŵĞŶƚ^ƚĂŐĞ &ůƵŝĚ ^ƚĂŐĞ WƌŽƉƉĂŶƚ ŽŶĐ ZĂƚĞ sŽůƵŵĞ sŽůƵŵĞ sŽůƵŵĞ dŽƚĂů dŝŵĞ dŝŵĞ/ŶƚĞƌǀĂů EƵŵďĞƌ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ;ƉƉŐͿ ;ďƉŵͿ ;ŐĂůͿ ;ďďůͿ ;ďďůͿ ;ůďƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ>ŝƋƵŝĚĚĚŝƚŝǀĞƐƌLJĚĚŝƚŝǀĞƐϱϬͲϭϬϯͲϮϬϴϰϮϰͲϭ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϰͲϮ &ƌĞĞnjĞWƌŽƚĞĐƚ WƌŝŵĞhƉWƌĞƐƐƵƌĞdĞƐƚ ϭ͕ϬϬϬ Ϯϰ Ϯϰ ϭ͗ϭϯ͗ϱϱϰͲϯ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϰͲϰ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ ϭ͗ϭϯ͗ϱϱϮ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϱ ϯϬη,LJďŽƌ' ƐƚĂďůŝƐŚ^ƚĂďůĞ&ůƵŝĚ ϭϱ ϰ͕ϮϬϬ ϭϬϬ ϭϬϬ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϭ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϲ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϳ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϭϬ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϭϭ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϭϮ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϭϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϭϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϰͲϭϱ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϱͲϭϬ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗ϭϱ͗ϰϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ ϭ͗Ϭϴ͗ϯϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϰϵ͗ϰϵ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϰϱ͗ϰϳ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϰϭ͗ϯϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗ϯϲ͗Ϯϳ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϯϬ͗ϮϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗Ϯϰ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗ϭϳ͗ϯϳ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϭϬ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϯϳ ϭϰ͕ϱϯϰ ϯϰϲ ϯϰϲϬ͗Ϭϵ͗Ϯϭ Ϭ͗ϭϮ͗ϯϮ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϲͲϭϭ &ƌĞĞnjĞWƌŽƚĞĐƚ &ƌĞĞnjĞWƌŽƚĞĐƚ ϭϱ Ϯ͕ϬϬϬ ϰϴ ϰϴ Ϭ͗Ϭϯ͗ϭϬ Ϭ͗Ϭϯ͗ϭϬ ϭϬϬϬ͘ϬϬϲͲϭϮ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷ,QWHUYDO.XSDUXN6DQGV#IW),QWHUYDO.XSDUXN6DQGV# IW),QWHUYDO.XSDUXN6DQGV#IW)ŽŶŽĐŽWŚŝůůŝƉƐͲϯ^dĞƐƚĂƐĞWůĂŶŶĞĚĞƐŝŐŶϮ h^dKD ZŽŶŽĐŽWŚŝůůŝƉƐ&>^ W/ &;ůďͬŐĂůͿϴ͘ϱϰ>dϳϬ͘ϯϵϰϬϭϴϴϴ> ^ ϯ^ͲϲϮϱ^> ^KZ Z,^d;Σ&Ϳϭϰϱ>KE'ͲϭϱϬ͘ϭϵϴϲϭϱ&KZDd/KE<ƵƉĂƌƵŬd DĂdžWƌĞƐƐƵƌĞ;ƉƐŝͿϵϬϬϬΎ džĐĞĞĚƐϴϬйŽĨďƵƌƐƚƉƌĞƐƐƵƌĞΎWƌŽƉ ^ůƵƌƌLJ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶ^ůƵƌƌLJ ĞƐŝŐŶWƌŽƉ ^ƚĂŐĞ/ŶƚĞƌǀĂů >ͲϮϴD >Ͳϯϭ >ŽƐƵƌĨͲϯϬϬ DKͲϲϳ >sdͲϮϬϬ t'Ͳϯϲ KƉƚŝ&ůŽͲ/// KƉƚŝ&ůŽͲ// ^WƌĞĂŬĞƌ ͲϲdƌĞĂƚŵĞŶƚ^ƚĂŐĞ &ůƵŝĚ ^ƚĂŐĞ WƌŽƉƉĂŶƚ ŽŶĐ ZĂƚĞ sŽůƵŵĞ sŽůƵŵĞ sŽůƵŵĞ dŽƚĂů dŝŵĞ dŝŵĞ/ŶƚĞƌǀĂů EƵŵďĞƌ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ;ƉƉŐͿ ;ďƉŵͿ ;ŐĂůͿ ;ďďůͿ ;ďďůͿ ;ůďƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ>ŝƋƵŝĚĚĚŝƚŝǀĞƐƌLJĚĚŝƚŝǀĞƐϱϬͲϭϬϯͲϮϬϴϰϮϳͲϭ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϳͲϮ &ƌĞĞnjĞWƌŽƚĞĐƚ WƌŝŵĞhƉWƌĞƐƐƵƌĞdĞƐƚ ϭ͕ϬϬϬ Ϯϰ Ϯϰ ϭ͗ϭϯ͗ϱϱϳͲϯ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϳͲϰ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ ϭ͗ϭϯ͗ϱϱϮ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϱ ϯϬη,LJďŽƌ' ƐƚĂďůŝƐŚ^ƚĂďůĞ&ůƵŝĚ ϭϱ ϰ͕ϮϬϬ ϭϬϬ ϭϬϬ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϭ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϲ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϳ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϭϬ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϭϭ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϭϮ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϭϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϭϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϳͲϭϱ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϴͲϭϬ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϵͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗ϭϱ͗Ϭϵ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϱϵͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ ϭ͗Ϭϳ͗ϱϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϵͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϰϵ͗ϭϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϵͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϰϱ͗ϭϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϵͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϰϬ͗ϱϳ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϵͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗ϯϱ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϵͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗Ϯϵ͗ϰϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϵͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗Ϯϯ͗Ϯϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϮϱϬ͘ϭϱϵͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗ϭϳ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬϮ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϮϱϬ͘ϭϱϵͲϭϬ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϯϳ ϭϯ͕ϱϲϲ ϯϮϯ ϯϮϯϬ͗Ϭϴ͗ϰϰ Ϭ͗ϭϭ͗ϱϰ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬϬ͘ϮϱϬ͘ϱϬϬ͘ϭϱϵͲϭϭ &ƌĞĞnjĞWƌŽƚĞĐƚ &ƌĞĞnjĞWƌŽƚĞĐƚ ϭϱ Ϯ͕ϬϬϬ ϰϴ ϰϴ Ϭ͗Ϭϯ͗ϭϬ Ϭ͗Ϭϯ͗ϭϬ ϭϬϬϬ͘ϬϬϵͲϭϮ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷ,QWHUYDO .XSDUXN6DQGV#IW),QWHUYDO.XSDUXN6DQGV#IW ),QWHUYDO.XSDUXN6DQGV#IW)ŽŶŽĐŽWŚŝůůŝƉƐͲϯ^dĞƐƚĂƐĞWůĂŶŶĞĚĞƐŝŐŶϯ h^dKD ZŽŶŽĐŽWŚŝůůŝƉƐ&>^ W/ &;ůďͬŐĂůͿϴ͘ϱϰ>dϳϬ͘ϯϵϰϬϭϴϴϴ> ^ ϯ^ͲϲϮϱ^> ^KZ Z,^d;Σ&Ϳϭϰϱ>KE'ͲϭϱϬ͘ϭϵϴϲϭϱ&KZDd/KE<ƵƉĂƌƵŬd DĂdžWƌĞƐƐƵƌĞ;ƉƐŝͿϵϬϬϬΎ džĐĞĞĚƐϴϬйŽĨďƵƌƐƚƉƌĞƐƐƵƌĞΎWƌŽƉ ^ůƵƌƌLJ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶ^ůƵƌƌLJ ĞƐŝŐŶWƌŽƉ ^ƚĂŐĞ/ŶƚĞƌǀĂů >ͲϮϴD >Ͳϯϭ >ŽƐƵƌĨͲϯϬϬ DKͲϲϳ >sdͲϮϬϬ t'Ͳϯϲ KƉƚŝ&ůŽͲ/// KƉƚŝ&ůŽͲ// ^WƌĞĂŬĞƌ ͲϲdƌĞĂƚŵĞŶƚ^ƚĂŐĞ &ůƵŝĚ ^ƚĂŐĞ WƌŽƉƉĂŶƚ ŽŶĐ ZĂƚĞ sŽůƵŵĞ sŽůƵŵĞ sŽůƵŵĞ dŽƚĂů dŝŵĞ dŝŵĞ/ŶƚĞƌǀĂů EƵŵďĞƌ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ;ƉƉŐͿ ;ďƉŵͿ ;ŐĂůͿ ;ďďůͿ ;ďďůͿ ;ůďƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ>ŝƋƵŝĚĚĚŝƚŝǀĞƐƌLJĚĚŝƚŝǀĞƐϱϬͲϭϬϯͲϮϬϴϰϮϭϬͲϭ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϭϬͲϮ &ƌĞĞnjĞWƌŽƚĞĐƚ WƌŝŵĞhƉWƌĞƐƐƵƌĞdĞƐƚ ϭ͕ϬϬϬ Ϯϰ Ϯϰ ϭ͗ϭϯ͗ϱϱϭϬͲϯ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϭϬͲϰ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ ϭ͗ϭϯ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϱ ϯϬη,LJďŽƌ' ƐƚĂďůŝƐŚ^ƚĂďůĞ&ůƵŝĚ ϭϱ ϰ͕ϮϬϬ ϭϬϬ ϭϬϬ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϭ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϲ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϳ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϭϬ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϭϭ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϭϮ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϭϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϭϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϬͲϭϱ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϭͲϭϬ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗ϭϰ͗ϯϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϱϭϮͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ ϭ͗Ϭϳ͗ϮϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϰϴ͗ϯϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϰϰ͗ϯϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϰϬ͗ϮϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗ϯϱ͗ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗Ϯϵ͗Ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϮϮ͗ϰϵ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗ϭϲ͗Ϯϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϮͲϭϬ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϯϳ ϭϮ͕ϲϮϭ ϯϬϬ ϯϬϬ Ϭ͗Ϭϴ͗Ϭϳ Ϭ͗ϭϭ͗ϭϴ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϱϬ Ϭ͘ϭϱϭϮͲϭϭ &ƌĞĞnjĞWƌŽƚĞĐƚ &ƌĞĞnjĞWƌŽƚĞĐƚ ϭϱ Ϯ͕ϬϬϬ ϰϴ ϰϴ Ϭ͗Ϭϯ͗ϭϬ Ϭ͗Ϭϯ͗ϭϬ ϭϬϬϬ͘ϬϬϭϮͲϭϮ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷ,QWHUYDO.XSDUXN6DQGV# IW),QWHUYDO.XSDUXN6DQGV# IW),QWHUYDO.XSDUXN6DQGV#IW)ŽŶŽĐŽWŚŝůůŝƉƐͲϯ^dĞƐƚĂƐĞWůĂŶŶĞĚĞƐŝŐŶϰ h^dKD ZŽŶŽĐŽWŚŝůůŝƉƐ&>^ W/ &;ůďͬŐĂůͿϴ͘ϱϰ>dϳϬ͘ϯϵϰϬϭϴϴϴ> ^ ϯ^ͲϲϮϱ^> ^KZ Z,^d;Σ&Ϳϭϰϱ>KE'ͲϭϱϬ͘ϭϵϴϲϭϱ&KZDd/KE<ƵƉĂƌƵŬd DĂdžWƌĞƐƐƵƌĞ;ƉƐŝͿϵϬϬϬΎ džĐĞĞĚƐϴϬйŽĨďƵƌƐƚƉƌĞƐƐƵƌĞΎWƌŽƉ ^ůƵƌƌLJ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶ^ůƵƌƌLJ ĞƐŝŐŶWƌŽƉ ^ƚĂŐĞ/ŶƚĞƌǀĂů >ͲϮϴD >Ͳϯϭ >ŽƐƵƌĨͲϯϬϬ DKͲϲϳ >sdͲϮϬϬ t'Ͳϯϲ KƉƚŝ&ůŽͲ/// KƉƚŝ&ůŽͲ// ^WƌĞĂŬĞƌ ͲϲdƌĞĂƚŵĞŶƚ^ƚĂŐĞ &ůƵŝĚ ^ƚĂŐĞ WƌŽƉƉĂŶƚ ŽŶĐ ZĂƚĞ sŽůƵŵĞ sŽůƵŵĞ sŽůƵŵĞ dŽƚĂů dŝŵĞ dŝŵĞ/ŶƚĞƌǀĂů EƵŵďĞƌ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ;ƉƉŐͿ ;ďƉŵͿ ;ŐĂůͿ ;ďďůͿ ;ďďůͿ ;ůďƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ>ŝƋƵŝĚĚĚŝƚŝǀĞƐƌLJĚĚŝƚŝǀĞƐϱϬͲϭϬϯͲϮϬϴϰϮϭϯͲϭ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϭϯͲϮ &ƌĞĞnjĞWƌŽƚĞĐƚ WƌŝŵĞhƉWƌĞƐƐƵƌĞdĞƐƚ ϭ͕ϬϬϬ Ϯϰ Ϯϰ ϭ͗ϭϯ͗ϱϱϭϯͲϯ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϭϯͲϰ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ ϭ͗ϭϯ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϱ ϯϬη,LJďŽƌ' ƐƚĂďůŝƐŚ^ƚĂďůĞ&ůƵŝĚ ϭϱ ϰ͕ϮϬϬ ϭϬϬ ϭϬϬ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϭ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϲ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϳ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϭϬ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϭϭ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϭϮ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϭϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϭϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϯͲϭϱ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϰͲϭϬ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗ϭϯ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϱϭϱͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ ϭ͗Ϭϲ͗ϰϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϰϳ͗ϱϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϰϯ͗ϱϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϵ͗ϰϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗ϯϰ͗ϯϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗Ϯϴ͗ϯϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϮϮ͗ϭϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗ϭϱ͗ϰϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϱͲϭϬ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϯϳ ϭϭ͕ϲϰϵ Ϯϳϳ Ϯϳϳ Ϭ͗Ϭϳ͗ϯϬ Ϭ͗ϭϬ͗ϰϬ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϱϬ Ϭ͘ϭϱϭϱͲϭϭ &ƌĞĞnjĞWƌŽƚĞĐƚ &ƌĞĞnjĞWƌŽƚĞĐƚ ϭϱ Ϯ͕ϬϬϬ ϰϴ ϰϴ Ϭ͗Ϭϯ͗ϭϬ Ϭ͗Ϭϯ͗ϭϬ ϭϬϬϬ͘ϬϬϭϱͲϭϮ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷ,QWHUYDO.XSDUXN6DQGV# IW),QWHUYDO.XSDUXN6DQGV#IW),QWHUYDO.XSDUXN6DQGV#IW)ŽŶŽĐŽWŚŝůůŝƉƐͲϯ^dĞƐƚĂƐĞWůĂŶŶĞĚĞƐŝŐŶϱ h^dKD ZŽŶŽĐŽWŚŝůůŝƉƐ&>^ W/ &;ůďͬŐĂůͿϴ͘ϱϰ>dϳϬ͘ϯϵϰϬϭϴϴϴ> ^ ϯ^ͲϲϮϱ^> ^KZ Z,^d;Σ&Ϳϭϰϱ>KE'ͲϭϱϬ͘ϭϵϴϲϭϱ&KZDd/KE<ƵƉĂƌƵŬd DĂdžWƌĞƐƐƵƌĞ;ƉƐŝͿϵϬϬϬΎ džĐĞĞĚƐϴϬйŽĨďƵƌƐƚƉƌĞƐƐƵƌĞΎWƌŽƉ ^ůƵƌƌLJ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶ^ůƵƌƌLJ ĞƐŝŐŶWƌŽƉ ^ƚĂŐĞ/ŶƚĞƌǀĂů >ͲϮϴD >Ͳϯϭ >ŽƐƵƌĨͲϯϬϬ DKͲϲϳ >sdͲϮϬϬ t'Ͳϯϲ KƉƚŝ&ůŽͲ/// KƉƚŝ&ůŽͲ// ^WƌĞĂŬĞƌ ͲϲdƌĞĂƚŵĞŶƚ^ƚĂŐĞ &ůƵŝĚ ^ƚĂŐĞ WƌŽƉƉĂŶƚ ŽŶĐ ZĂƚĞ sŽůƵŵĞ sŽůƵŵĞ sŽůƵŵĞ dŽƚĂů dŝŵĞ dŝŵĞ/ŶƚĞƌǀĂů EƵŵďĞƌ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ;ƉƉŐͿ ;ďƉŵͿ ;ŐĂůͿ ;ďďůͿ ;ďďůͿ ;ůďƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ>ŝƋƵŝĚĚĚŝƚŝǀĞƐƌLJĚĚŝƚŝǀĞƐϱϬͲϭϬϯͲϮϬϴϰϮϭϲͲϭ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϭϲͲϮ &ƌĞĞnjĞWƌŽƚĞĐƚ WƌŝŵĞhƉWƌĞƐƐƵƌĞdĞƐƚ ϭ͕ϬϬϬ Ϯϰ Ϯϰ ϭ͗ϭϯ͗ϱϱϭϲͲϯ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϭϲͲϰ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ ϭ͗ϭϯ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϱ ϯϬη,LJďŽƌ' ƐƚĂďůŝƐŚ^ƚĂďůĞ&ůƵŝĚ ϭϱ ϰ͕ϮϬϬ ϭϬϬ ϭϬϬ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϭ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϲ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϳ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϭϬ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϭϭ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϭϮ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϭϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϭϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϲͲϭϱ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϳͲϭϬ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗ϭϯ͗ϭϳ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ ϭ͗Ϭϲ͗Ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϰϳ͗ϮϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϰϯ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϵ͗Ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗ϯϯ͗ϱϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗Ϯϳ͗ϱϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗Ϯϭ͗ϯϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗ϭϱ͗Ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϴͲϭϬ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϯϳ ϭϬ͕ϲϳϵ Ϯϱϰ Ϯϱϰ Ϭ͗Ϭϲ͗ϱϮ Ϭ͗ϭϬ͗Ϭϯ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϱϬ Ϭ͘ϭϱϭϴͲϭϭ &ƌĞĞnjĞWƌŽƚĞĐƚ &ƌĞĞnjĞWƌŽƚĞĐƚ ϭϱ Ϯ͕ϬϬϬ ϰϴ ϰϴ Ϭ͗Ϭϯ͗ϭϬ Ϭ͗Ϭϯ͗ϭϬ ϭϬϬϬ͘ϬϬϭϴͲϭϮ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷ,QWHUYDO.XSDUXN6DQGV# IW),QWHUYDO.XSDUXN6DQGV#IW),QWHUYDO.XSDUXN6DQGV#IW)ŽŶŽĐŽWŚŝůůŝƉƐͲϯ^dĞƐƚĂƐĞWůĂŶŶĞĚĞƐŝŐŶϲ h^dKD ZŽŶŽĐŽWŚŝůůŝƉƐ&>^ W/ &;ůďͬŐĂůͿϴ͘ϱϰ>dϳϬ͘ϯϵϰϬϭϴϴϴ> ^ ϯ^ͲϲϮϱ^> ^KZ Z,^d;Σ&Ϳϭϰϱ>KE'ͲϭϱϬ͘ϭϵϴϲϭϱ&KZDd/KE<ƵƉĂƌƵŬd DĂdžWƌĞƐƐƵƌĞ;ƉƐŝͿϵϬϬϬΎ džĐĞĞĚƐϴϬйŽĨďƵƌƐƚƉƌĞƐƐƵƌĞΎWƌŽƉ ^ůƵƌƌLJ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶůĞĂŶ ĞƐŝŐŶ^ůƵƌƌLJ ĞƐŝŐŶWƌŽƉ ^ƚĂŐĞ/ŶƚĞƌǀĂů >ͲϮϴD >Ͳϯϭ >ŽƐƵƌĨͲϯϬϬ DKͲϲϳ >sdͲϮϬϬ t'Ͳϯϲ KƉƚŝ&ůŽͲ/// KƉƚŝ&ůŽͲ// ^WƌĞĂŬĞƌ ͲϲdƌĞĂƚŵĞŶƚ^ƚĂŐĞ &ůƵŝĚ ^ƚĂŐĞ WƌŽƉƉĂŶƚ ŽŶĐ ZĂƚĞ sŽůƵŵĞ sŽůƵŵĞ sŽůƵŵĞ dŽƚĂů dŝŵĞ dŝŵĞ/ŶƚĞƌǀĂů EƵŵďĞƌ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ ĞƐĐƌŝƉƚŝŽŶ;ƉƉŐͿ ;ďƉŵͿ ;ŐĂůͿ ;ďďůͿ ;ďďůͿ ;ůďƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ ;ŚŚ͗ŵŵ͗ƐƐͿ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ŐƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ ;ƉƉƚͿ>ŝƋƵŝĚĚĚŝƚŝǀĞƐƌLJĚĚŝƚŝǀĞƐϱϬͲϭϬϯͲϮϬϴϰϮϭϵͲϭ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϭϵͲϮ &ƌĞĞnjĞWƌŽƚĞĐƚ WƌŝŵĞhƉWƌĞƐƐƵƌĞdĞƐƚ ϭ͕ϬϬϬ Ϯϰ Ϯϰ ϭ͗ϭϯ͗ϱϱϭϵͲϯ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϭϵͲϰ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ ϭ͗ϭϯ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϱ ϯϬη,LJďŽƌ' ƐƚĂďůŝƐŚ^ƚĂďůĞ&ůƵŝĚ ϭϱ ϰ͕ϮϬϬ ϭϬϬ ϭϬϬ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϭ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϲ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϳ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϭϬ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϭϭ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϭϮ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϭϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϭϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϭϵͲϭϱ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϬͲϭϬ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗ϭϮ͗ϯϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ ϭ͗Ϭϱ͗Ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϰϲ͗ϯϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϰϮ͗ϯϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϴ͗Ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗ϯϯ͗ϭϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗Ϯϳ͗Ϭϵ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϮϬ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗ϭϰ͗Ϯϰ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϭͲϭϬ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϯϳ ϵ͕ϱϰϮ ϮϮϳ ϮϮϳϬ͗Ϭϲ͗Ϭϴ Ϭ͗Ϭϵ͗ϭϵ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬϬ͘ϮϱϬ͘ϱϬϬ͘ϭϱϮϭͲϭϭ &ƌĞĞnjĞWƌŽƚĞĐƚ &ƌĞĞnjĞWƌŽƚĞĐƚ ϭϱ Ϯ͕ϬϬϬ ϰϴ ϰϴ Ϭ͗Ϭϯ͗ϭϬ Ϭ͗Ϭϯ͗ϭϬ ϭϬϬϬ͘ϬϬϮϭͲϭϮ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/ŶϮϮͲϭ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϮϮͲϮ &ƌĞĞnjĞWƌŽƚĞĐƚ WƌŝŵĞhƉWƌĞƐƐƵƌĞdĞƐƚ ϭ͕ϬϬϬ Ϯϰ Ϯϰ ϭ͗ϭϯ͗ϱϱϮϮͲϯ ^ŚƵƚͲ/Ŷ ^ŚƵƚͲ/Ŷϭ͗ϭϯ͗ϱϱϮϮͲϰ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ ϭ͗ϭϯ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϱ ϯϬη,LJďŽƌ' ƐƚĂďůŝƐŚ^ƚĂďůĞ&ůƵŝĚ ϭϱ ϰ͕ϮϬϬ ϭϬϬ ϭϬϬ Ϭ͗Ϭϲ͗ϰϬ ϭ͗ϭϭ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϲ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϳ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϭϬ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϭϭ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϭϮ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϭϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϭϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϮͲϭϱ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗Ϭϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ Ϭ͗ϱϴ͗ϬϮ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϯϵ͗ϭϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϯϱ͗ϭϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϭ͗Ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗Ϯϱ͗ϱϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗ϭϵ͗ϱϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϭϯ͗ϯϭ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗Ϭϳ͗Ϭϲ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϯͲϭϬ ϯϬη,LJďŽƌ' ^ƉĂĐĞƌĂŶĚĂůůƌŽƉ ϭϱ ϭ͕ϮϲϬ ϯϬ ϯϬ Ϭ͗ϬϮ͗ϬϬ Ϭ͗ϬϮ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϭ ϯϬη,LJďŽƌ' WĂĚ ϯϳ ϭϭ͕ϮϬϬ Ϯϲϳ Ϯϲϳ Ϭ͗Ϭϳ͗ϭϮ ϭ͗ϭϭ͗ϱϳ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϮ ϯϬη,LJďŽƌ' ŽŶĚŝƚŝŽŶŝŶŐWĂĚ ϭϬϬD Ϭ͘Ϯϱ ϯϳ Ϯϴ͕ϴϬϬ ϲϴϲ ϲϴϲ ϳ͕ϮϬϬ Ϭ͗ϭϴ͗ϰϱ ϭ͗Ϭϰ͗ϰϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϯ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϭ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϰϵ ϲ͕ϬϬϬ Ϭ͗Ϭϰ͗ϬϮ Ϭ͗ϰϲ͗ϬϬ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϰ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ Ϯ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϱϲ ϭϮ͕ϬϬϬ Ϭ͗Ϭϰ͗ϭϯ Ϭ͗ϰϭ͗ϱϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϱ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϯ͘ϬϬ ϯϳ ϳ͕ϬϬϬ ϭϲϳ ϭϴϵ Ϯϭ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϳ Ϭ͗ϯϳ͗ϰϱ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϲ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϰ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ ϮϮϱ ϯϮ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϭϱ Ϭ͗ϯϮ͗ϯϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϳ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϱ͘ϬϬ ϯϳ ϴ͕ϬϬϬ ϭϵϬ Ϯϯϰ ϰϬ͕ϬϬϬ Ϭ͗Ϭϲ͗ϭϵ Ϭ͗Ϯϲ͗ϯϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϴ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϲ͘ϬϬ ϯϳ ϳ͕ϴϯϯ ϭϴϳ Ϯϯϳ ϰϳ͕ϬϬϬ Ϭ͗Ϭϲ͗Ϯϱ Ϭ͗ϮϬ͗ϭϯ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϵ ϯϬη,LJďŽƌ' WƌŽƉƉĂŶƚ>ĂĚĞŶ&ůƵŝĚ tĂŶůŝϭϲͬϮϬĞƌĂŵŝĐ ϳ͘ϬϬ ϯϳ ϲ͕ϬϬϬ ϭϰϯ ϭϴϴ ϰϮ͕ϬϬϬ Ϭ͗Ϭϱ͗Ϭϲ Ϭ͗ϭϯ͗ϰϴ Ϯ͘ϬϬ Ϭ͘ϭϬ ϭ͘ϬϬ Ϭ͘ϴϬ ϯϬ͘ϬϬ Ϯ͘ϬϬ Ϭ͘Ϯϱ Ϭ͘Ϯϱ Ϭ͘ϭϱϮϰͲϭϬ ϯϬη>ŝŶĞĂƌ &ůƵƐŚ ϯϳ ϴ͕ϲϬϬ ϮϬϱ ϮϬϱϬ͗Ϭϱ͗ϯϮ Ϭ͗Ϭϴ͗ϰϯ ϭ͘ϬϬ ϯϬ͘ϬϬ Ϯ͘ϬϬϬ͘ϮϱϬ͘ϱϬϬ͘ϭϱϮϰͲϭϭ &ƌĞĞnjĞWƌŽƚĞĐƚ &ƌĞĞnjĞWƌŽƚĞĐƚ ϭϱ Ϯ͕ϬϬϬ ϰϴ ϰϴ Ϭ͗Ϭϯ͗ϭϬ Ϭ͗Ϭϯ͗ϭϬ ϭϬϬϬ͘ϬϬϮϰͲϭϮ ^ŚƵƚͲ/Ŷ 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DtͿ͘>ŽǁĞƌĐŽŶĨŝŶŝŶŐnjŽŶĞƐ͗^ŝůƚƐƚŽŶĞĂŶĚƐŚĂůĞŽĨƚŚĞƵŶĚĞƌůLJŝŶŐůŽǁĞƌdŽƌŽŬ͕,Z͕ĂŶĚ<ĂůƵďŝŬŝŶƚĞƌǀĂůƐƚŚĂƚŚĂǀĞĂŶĂŐŐƌĞͲŐĂƚĞdsdŽĨŵŽƌĞƚŚĂŶϱϬϬ͛dsŝŶƚŚĞŶĞĂƌďLJWĂůŵϭǁĞůů;ůŽĐĂƚĞĚΕϴ͕ϲϬϬ͛ƚŽƚŚĞĞĂƐƚͿ͘&ƌĂĐƚƵƌĞŐƌĂĚŝĞŶƚĞdžƉĞĐƚĞĚƚŽƌĂŶŐĞĨƌŽŵĂďŽƵƚϬ͘ϳϴƚŽϬ͘ϵϰƉƐŝͬĨƚ;ϭϱƚŽϭϴƉƉŐ DtͿ͘^&ϭϭͬϰͬϮϬϮϮ^&ϭϭͬϰͬϮϬϮϮ;ĂͿ;ϭϬͿ>ŽĐĂƚŝŽŶ͕ŽƌŝĞŶƚĂƚŝŽŶ͕ƌĞƉŽƌƚŽŶŵĞĐŚĂŶŝĐĂůĐŽŶĚŝƚŝŽŶŽĨĞĂĐŚǁĞůůĞŵĞŶƚƌĞƉŽƌƚƐĨŽƌϯ^ͲϲϭϮ͕ϯ^Ͳϲϭϯ͕ϯ^ϭϵ͕EƵŶĂϭĂŶĚEƵŶĂϭWϭŝŶĐůƵĚĞĚ͕ǁŚŝĐŚǁĞƌĞƚŚĞϱǁĞůůƐŝĚĞŶƚŝĨŝĞĚŝŶƐĞĐƚŝŽŶ;ĂͿ;ϮͿ;ĐͿĂƐďĞŝŶŐǁŝƚŚŝŶƚŚĞĨƌĂĐƉŽŝŶƚЪŵŝůĞƌĂĚŝƵƐ͘:DϭϭͬϵͬϮϮ;ĂͿ;ϭϬͿ^ƵĨĨŝĐŝĞŶƚŝŶĨŽƌŵĂƚŝŽŶƚŽĚĞƚĞƌŵŝŶĞǁĞůůƐǁŝůůŶŽƚŝŶƚĞƌĨĞƌĞǁŝƚŚĐŽŶƚĂŝŶŵĞŶƚǁŝƚŚŝŶЪŵŝůĞ<Zhϯ^ͲϲϭϮ͕<Zhϯ^Ͳϲϭϯ͕EƵŶĂϭ͕ĂŶĚEƵŶĂϭWϭ;ĞdžŝƐƚŝŶŐͿ͖<Zhϯ^Ͳϲϭϱ;ƉůĂŶŶĞĚͿ͗tĞůůƌĞĐŽƌĚƐŝŶĚŝĐĂƚĞƚŚĞdŽƌŽŬKŝůWŽŽůŝƐŝƐŽůĂƚĞĚďLJĐĞŵĞŶƚŝŶĞĂĐŚŽĨƚŚĞƚŚƌĞĞĞdžŝƐƚŝŶŐǁĞůůƐĂŶĚŽŶĞƉůƵŐŐĞĚͲďĂĐŬǁĞůůďŽƌĞĐƵƌƌĞŶƚůLJůŽĐĂƚĞĚǁŝƚŚŝŶЪŵŝůĞŽĨ<Zhϯ^ͲϲϮϱĂŶĚǁŝůůŶŽƚŝŶƚĞƌĨĞƌĞǁŝƚŚĐŽŶƚĂŝŶŵĞŶƚŽĨŝŶũĞĐƚĞĚĨůƵŝĚƐ͘/ĨĐŽŶƐƚƌƵĐƚĞĚĂƐƉůĂŶŶĞĚ͕ƚŚĞdŽƌŽŬKŝůWŽŽůŝŶ<Zhϯ^ͲϲϭϱǁŝůůďĞŝƐŽůĂƚĞĚĂŶĚǁŝůůŶŽƚŝŶƚĞƌĨĞƌĞǁŝƚŚĐŽŶƚĂŝŶŵĞŶƚ͘^&ϭϭͬϳͬϮϬϮϮƌůŐ ŶŐ ϮϬϮϱ͘Ϯϴϯ,LJĚƌĂƵůŝĐ&ƌĂĐƚƵƌŝŶŐƉƉůŝĐĂƚŝŽŶʹŚĞĐŬůŝƐƚ<Zhϯ^ͲϲϮϱ;WdEŽ͘ϮϮϮͲϬϳϵ͖^ƵŶĚƌLJEŽ͘ϯϮϮͲϲϯϮͿWĂƌĂŐƌĂƉŚ^ƵďͲWĂƌĂŐƌĂƉŚ^ĞĐƚŝŽŶŽŵƉůĞƚĞ͍K' WĂŐĞϰ EŽǀĞŵďĞƌϭϬ͕ϮϬϮϮ;ĂͿ;ϭϭͿ&ĂƵůƚƐĂŶĚĨƌĂĐƚƵƌĞƐ͕>ŽĐĂƚŝŽŶ͕ŽƌŝĞŶƚĂƚŝŽŶ;ĂͿ;ϭϭͿ&ĂƵůƚƐĂŶĚĨƌĂĐƚƵƌĞƐ͕^ƵĨĨŝĐŝĞŶƚŝŶĨŽƌŵĂƚŝŽŶƚŽĚĞƚĞƌŵŝŶĞŶŽŝŶƚĞƌĨĞƌĞŶĐĞǁŝƚŚĐŽŶƚĂŝŶŵĞŶƚǁŝƚŚŝŶЪŵŝůĞEŽŶĞ͗dŚĞŽƉĞƌĂƚŽƌŚĂƐŶŽƚŝĚĞŶƚŝĨŝĞĚĂŶLJĨĂƵůƚƐŽƌĨƌĂĐƚƵƌĞnjŽŶĞƐŽŶƐĞŝƐŵŝĐĚĂƚĂǁŝƚŚŝŶĂЪͲŵŝůĞƌĂĚŝƵƐŽĨ<Zhϯ^ͲϲϮϱ͘/ƚŝƐƵŶůŝŬĞůLJƚŚĂƚĂŶLJĨĂƵůƚƐǁŝůůŝŶƚĞƌĨĞƌĞǁŝƚŚĐŽŶƚĂŝŶŵĞŶƚŽĨƚŚĞŝŶũĞĐƚĞĚĨƌĂĐƚƵƌŝŶŐĨůƵŝĚƐ͖ŚŽǁĞǀĞƌ͕ŝĨƚŚĞƌĞĂƌĞŝŶĚŝĐĂƚŝŽŶƐƚŚĂƚĂĨƌĂĐƚƵƌĞŚĂƐŝŶƚĞƌƐĞĐƚĞĚĂĨĂƵůƚŽƌŶĂƚƵƌĂůͲĨƌĂĐƚƵƌĞŝŶƚĞƌǀĂůĚƵƌŝŶŐĨƌĂĐŽƉĞƌĂƚŝŽŶƐ͕ƚŚĞŽƉĞƌĂƚŽƌǁŝůůŐŽƚŽĨůƵƐŚĂŶĚƚĞƌŵŝŶĂƚĞƚŚĞƐƚĂŐĞŝŵŵĞĚŝĂƚĞůLJ͘^&ϭϭͬϳͬϮϬϮϮ;ĂͿ;ϭϮͿWƌŽƉŽƐĞĚƉƌŽŐƌĂŵĨŽƌĨƌĂĐƚƵƌŝŶŐŽƉĞƌĂƚŝŽŶWƌŽǀŝĚĞĚǁŝƚŚĂƉƉůŝĐĂƚŝŽŶ͘ϮϰŝŶƚĞƌǀĂůƐ͕ŵƵůƚŝƐƚĂŐĞ͕ĨƌĂĐĚĂƌƚƐĂŶĚďĂůůĚƌŽƉ͘tϭϭͬϬϴͬϮϬϮϮ ;ĂͿ;ϭϮͿ;Ϳ ƐƚŝŵĂƚĞĚǀŽůƵŵĞWƌŽǀŝĚĞĚǁŝƚŚĂƉƉůŝĐĂƚŝŽŶ͘ϲϭ͕ϵϴϳďďůƚŽƚĂůĚŝƌƚLJǀŽů͘ϰ͘ϵDŝůůŝŽŶůďƚŽƚĂůƉƌŽƉƉĂŶƚtϭϭͬϬϴͬϮϬϮϮ;ĂͿ;ϭϮͿ;ͿĚĚŝƚŝǀĞƐ͗ŶĂŵĞƐ͕ƉƵƌƉŽƐĞƐ͕ĐŽŶĐĞŶƚƌĂƚŝŽŶƐWƌŽǀŝĚĞĚǁŝƚŚĂƉƉůŝĐĂƚŝŽŶ͘tϭϭͬϬϴͬϮϬϮϮ;ĂͿ;ϭϮͿ;ͿŚĞŵŝĐĂůŶĂŵĞĂŶĚ^ŶƵŵďĞƌŽĨĞĂĐŚWƌŽǀŝĚĞĚǁŝƚŚĂƉƉůŝĐĂƚŝŽŶ͘^ŝŶĨŽƌŵĂƚŝŽŶŽŶ,ĂůůŝďƵƌƚŽŶƉƌŽƉƌŝĞƚĂƌLJĐŚĞŵŝĐĂůƐƉƌĞǀŝŽƵƐůLJƉƌŽǀŝĚĞĚtϭϭͬϬϴͬϮϬϮϮ;ĂͿ;ϭϮͿ;Ϳ/ŶĞƌƚƐƵďƐƚĂŶĐĞƐ͕ǁĞŝŐŚƚŽƌǀŽůƵŵĞŽĨĞĂĐŚWƌŽǀŝĚĞĚǁŝƚŚĂƉƉůŝĐĂƚŝŽŶ͘tϭϭͬϬϴͬϮϬϮϮ;ĂͿ;ϭϮͿ; 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EŽǀĞŵďĞƌϭϬ͕ϮϬϮϮďƵƚŶŽƚƚŚƌŽƵŐŚ͕ƚŚĞŽǀĞƌůLJŝŶŐĐŽŶĨŝŶŝŶŐŵƵĚƐƚŽŶĞĂŶĚƐŝůƚƐƚŽŶĞŽĨƚŚĞdŽƌŽŬƚŚĂƚŝƐĂďŽƵƚϳϯϮ͛ƚŚŝĐŬŝŶƚŚŝƐĂƌĞĂ͘;ĂͿ;ϭϯͿWƌŽƉŽƐĞĚƉƌŽŐƌĂŵĨŽƌƉŽƐƚͲĨƌĂĐƚƵƌŝŶŐǁĞůůĐůĞĂŶƵƉĂŶĚĨůƵŝĚƌĞĐŽǀĞƌLJtĞůůĐůĞĂŶŽƵƚĂŶĚĨůŽǁďĂĐŬƉƌŽĐĞĚƵƌĞƉƌŽǀŝĚĞĚǁŝƚŚĂƉƉůŝĐĂƚŝŽŶ͘EŽĚŝƐƉŽƐĂůƐƉĞĐŝĨŝĐĂůůLJŝĚĞŶƚŝĨŝĞĚďƵƚW/ŚĂƐŶƵŵĞƌŽƵƐůĂƐƐ/ĂŶĚůĂƐƐ//ǁĞůůƐĂǀĂŝůĂďůĞ͘tϭϭͬϬϴͬϮϬϮϮ;ďͿdĞƐƚŝŶŐŽĨĐĂƐŝŶŐŽƌŝŶƚĞƌŵĞĚŝĂƚĞĐĂƐŝŶŐdĞƐƚĞĚхϭϭϬйŽĨŵĂdžĂŶƚŝĐŝƉĂƚĞĚƉƌĞƐƐƵƌĞyyϬϬƉƐŝďĂĐŬƉƌĞƐƐƵƌĞ͕ƉůĂŶƚŽƚĞƐƚƚŽyyϬϬƉƐŝ͕ƉŽƉŽĨĨƐĞƚĂƐyyϬϬƉƐŝtϭϭͬϬϴͬϮϬϮϮ;ĐͿ&ƌĂĐƚƵƌŝŶŐƐƚƌŝŶŐ;ĐͿ;ϭͿWĂĐŬĞƌхϭϬϬ͛ďĞůŽǁdKŽĨƉƌŽĚƵĐƚŝŽŶŽƌŝŶƚĞƌŵĞĚŝĂƚĞĐĂƐŝŶŐϰ͘ϱ͟ƚƵďŝŶŐǁŝůůďĞĂŶĐŚŽƌĞĚǁŝƚŚĂdEdƉĂĐŬĞƌĂƚϭϮϱϭϲĨƚĂŶĚĂůŝŶĞƌƚŽƉƉĂĐŬĞƌĂƚϭϮϲϵϮĨƚ͘WĞƌĨŽƌĂƚŝŽŶƐͬĨƌĂĐƐůĞĞǀĞƐƚĂƌƚƐĂƚϭϯϰϱϯĨƚ͘ϭϬ͘ϳϱ͟ƐƵƌĨĂĐĞĐĂƐŝŶŐĐĞŵĞŶƚĞĚƚŽƐƵƌĨĂĐĞ͘/ŶƚĞƌŵĞĚŝĂƚĞϳͲϱͬϴ͟dKϳϴϱϬĨƚDďLJ>tϭϭͬϬϴͬϮϬϮϮ;ĐͿ;ϮͿdĞƐƚĞĚхϭϭϬйŽĨŵĂdžĂŶƚŝĐŝƉĂƚĞĚƉƌĞƐƐƵƌĞĚŝĨĨĞƌĞŶƚŝĂůdƵďŝŶŐƚĞƐƚŽĨϰϱϱϬƉƐŝ͘DĂdžƉƌĞƐƐƵƌĞĚŝĨĨĞƌĞŶƚŝĂůŝƐĞƐƚŝŵĂƚĞĚĂƐϯϳϱϱƉƐŝ;ϳϯϱϱǁŝƚŚϯϲϬϬƉƐŝďĂĐŬƉƌĞƐƐƵƌĞͿƐŽƚĞƐƚŽĨϰϭϯϬƉƐŝƐĂƚŝƐĨŝĞƐϭϭϬйtϭϭͬϬϴͬϮϬϮϮ;ĚͿWƌĞƐƐƵƌĞƌĞůŝĞĨǀĂůǀĞ>ŝŶĞƉƌĞƐƐƵƌĞфсƚĞƐƚƉƌĞƐƐƵƌĞ͕ƌĞŵŽƚĞůLJĐŽŶƚƌŽůůĞĚƐŚƵƚͲŝŶĚĞǀŝĐĞϵϱϬϬƉƐŝůŝŶĞƉƌĞƐƐƵƌĞƚĞƐƚ͕ƉƵŵƉŬŶŽĐŬŽƵƚϳϴϱϱƉƐŝǁŝƚŚŵĂdž͘ŐůŽďĂůŬŝĐŬŽƵƚϴϰϱϱƉƐŝ͘/WZsƐĞƚĂƐϯϲϬϬƉƐŝ͘tϭϭͬϬϴͬϮϬϮϮ;ĞͿŽŶĨŝŶĞŵĞŶƚ&ƌĂĐĨůƵŝĚƐĐŽŶĨŝŶĞĚƚŽĂƉƉƌŽǀĞĚĨŽƌŵĂƚŝŽŶƐWƌŽǀŝĚĞĚǁŝƚŚĂƉƉůŝĐĂƚŝŽŶ͘tϭϭͬϬϴͬϮϬϮϮ;ĨͿ^ƵƌĨĂĐĞĐĂƐŝŶŐƉƌĞƐƐƵƌĞƐDŽŶŝƚŽƌĞĚǁŝƚŚŐĂƵŐĞĂŶĚƉƌĞƐƐƵƌĞƌĞůŝĞĨĚĞǀŝĐĞ/WZsƐĞƚĂƚϯϲϬϬƉƐŝ͘^ƵƌĨĂĐĞĂŶŶƵůƵƐŽƉĞŶ͘&ƌĂĐƉƌĞƐƐƵƌĞƐĐŽŶƚŝŶƵŽƵƐůLJŵŽŶŝƚŽƌĞĚ͘tϭϭͬϬϴͬϮϬϮϮ;ŐͿŶŶƵůƵƐƉƌĞƐƐƵƌĞŵŽŶŝƚŽƌŝŶŐΘŶŽƚŝĨŝĐĂƚŝŽŶϱϬϬƉƐŝĐƌŝƚĞƌŝĂƵƌŝŶŐŚLJĚƌĂƵůŝĐĨƌĂĐƚƵƌŝŶŐŽƉĞƌĂƚŝŽŶƐ͕ĂůůĂŶŶƵůƵƐƉƌĞƐƐƵƌĞƐŵƵƐƚďĞĐŽŶƚŝŶƵŽƵƐůLJŵŽŶŝƚŽƌĞĚĂŶĚƌĞĐŽƌĚĞĚ͘/ĨĂƚĂŶLJƚŝŵĞĚƵƌŝŶŐŚLJĚƌĂƵůŝĐĨƌĂĐƚƵƌŝŶŐŽƉĞƌĂƚŝŽŶƐƚŚĞĂŶŶƵůƵƐƉƌĞƐƐƵƌĞŝŶĐƌĞĂƐĞƐŵŽƌĞƚŚĂŶϱϬϬƉƐŝŐĂďŽǀĞƚŚŽƐĞĂŶƚŝĐŝƉĂƚĞĚŝŶĐƌĞĂƐĞƐĐĂƵƐĞĚďLJƉƌĞƐƐƵƌĞŽƌƚŚĞƌŵĂůƚƌĂŶƐĨĞƌ͕ƚŚĞŽƉĞƌĂƚŽƌƐŚĂůů͗tϭϭͬϬϴͬϮϬϮϮ ;ŐͿ;ϭͿEŽƚŝĨLJK'ǁŝƚŚŝŶϮϰŚŽƵƌƐ ;ŐͿ;ϮͿŽƌƌĞĐƚŝǀĞĂĐƚŝŽŶŽƌƐƵƌǀĞŝůůĂŶĐĞ ;ŐͿ;ϯͿ^ƵŶĚƌLJƚŽK' 1 Regg, James B (OGC) From:Brooks, Phoebe L (OGC) Sent:Wednesday, November 9, 2022 1:58 PM To:Rig 19 Cc:Regg, James B (OGC) Subject:RE: Doyon Rig 19 BOPE Test 3S-625 10-17-22 Attachments:Doyon 19 10-17-22 Revised.xlsx Attached is a revised report changing the Misc. Inspections/Misc. field to “NA” and bottle precharge of 1050 in remarks. Please update your copy. Thank you, Phoebe Phoebe Brooks Research Analyst Alaska Oil and Gas Conservation Commission Phone: 907‐793‐1242 CONFIDENTIALITY NOTICE: This e-mail message, including any attachments, contains information from the Alaska Oil and Gas Conservation Commission (AOGCC), State of Alaska and is for the sole use of the intended recipient(s). It may contain confidential and/or privileged information. The unauthorized review, use or disclosure of such information may violate state or federal law. If you are an unintended recipient of this e-mail, please delete it, without first saving or forwarding it, and, so that the AOGCC is aware of the mistake in sending it to you, contact Phoebe Brooks at 907-793-1242 or phoebe.brooks@alaska.gov. From: Rig 19 <rig19@doyondrilling.com> Sent: Monday, October 17, 2022 3:00 PM To: Regg, James B (OGC) <jim.regg@alaska.gov> Cc: DOA AOGCC Prudhoe Bay <doa.aogcc.prudhoe.bay@alaska.gov>; Brooks, Phoebe L (OGC) <phoebe.brooks@alaska.gov>; D19 Company Man <d19cm@conocophillips.com>; David Coates <coates.coates@conocophillips.com>; Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com>; Operations Engineer, Doyon 19 <d19opseng@conocophillips.com>; Ben Wedin <bwedin@doyondrilling.com> Subject: FW: Doyon Rig 19 BOPE Test 3S‐625 10‐17‐22 Resend with chart Thank you Orville Williams Rig 19 Toolpusher 907 670‐6098 907 306‐4467 From: Rig 19 Sent: Monday, October 17, 2022 2:13 PM To: Jim Regg <jim.regg@alaska.gov> Cc: AOGCC.Inspectors@alaska.gov; phoebe. brooks (phoebe.brooks@alaska.gov) <phoebe.brooks@alaska.gov>; D19 Company Man <d19cm@conocophillips.com>; David Coates <coates.coates@conocophillips.com>; Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com>; Operations Engineer, Doyon 19 <d19opseng@conocophillips.com>; Ben Wedin KRU 3S-625 PTD 2220790 2 <bwedin@doyondrilling.com> Subject: Doyon Rig 19 BOPE Test 3S‐625 10‐17‐22 Test report. Thank you Orville Williams Rig 19 Toolpusher 907 670‐6098 907 306‐4467 From: Doyon 19, Co‐Man <d19cm@conocophillips.com> Sent: Monday, October 17, 2022 1:31 PM To: Doyon 19, Toolpusher <d19tp@conocophillips.com>; Rig 19 <rig19@doyondrilling.com> Subject: FW: [EXTERNAL]RE: Permit #222‐079 ‐ 3S‐625 ‐ Doyon 19 Ken Harding / Dusty Pickworth Doyon 19 Company Man 907‐670‐6099 From: Coates, David <Coates.Coates@conocophillips.com> Sent: Friday, October 14, 2022 1:42 PM To: Doyon 19, Co‐Man <d19cm@conocophillips.com> Subject: FW: [EXTERNAL]RE: Permit #222‐079 ‐ 3S‐625 ‐ Doyon 19 Dave Coates Doyon 19 Drilling Superintendent ConocoPhillips Alaska Office: 907‐2634933 Cell: 907‐715‐4974 From: Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com> Sent: Friday, October 14, 2022 1:41 PM To: Coates, David <Coates.Coates@conocophillips.com> Cc: Operations Engineer, Doyon 142 <Doyon142.OperationsEngineer@conocophillips.com> Subject: FW: [EXTERNAL]RE: Permit #222‐079 ‐ 3S‐625 ‐ Doyon 19 FYI 3 From: Regg, James B (OGC) <jim.regg@alaska.gov> Sent: Friday, October 14, 2022 1:27 PM To: Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com>; Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov> Cc: DOA AOGCC Prudhoe Bay <doa.aogcc.prudhoe.bay@alaska.gov> Subject: [EXTERNAL]RE: Permit #222‐079 ‐ 3S‐625 ‐ Doyon 19 CAUTION:This email originated from outside of the organization. Do not click links or open attachments unless you recognize the sender and know the content is safe. AOGCC concurs with completing steps 1‐3 before testing BOPE, acknowledging the test may not start with the required 14 days since the last test. Jim Regg Supervisor, Inspections AOGCC 333 W. 7th Ave, Suite 100 Anchorage, AK 99501 907‐793‐1236 From: Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com> Sent: Friday, October 14, 2022 1:10 PM To: Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; Regg, James B (OGC) <jim.regg@alaska.gov> Subject: Permit #222‐079 ‐ 3S‐625 ‐ Doyon 19 Victoria and Jim, Currently Doyon 19 is backreaming its way out of the 6.5” production open hole at 14,140’ MD at approximately 100 feet per hour. Hole conditions while pulling out of hole have considerably slowed our progress and have increased our predicted time to pull out hole to the shoe by 2 days. The 7‐5/8” casing shoe is at 12,842’ MD and we are projected to reach the shoe later tonight if hole conditions allow. Doyon 19 is due for its 2‐week BOPE test tomorrow, September 15. Our current plan is as follows: 1.Continue to work pipe out of hole to the 7‐5/8” casing shoe. 2.Circulate the casing clean to ensure any formation cuttings/cavings generated while drilling or backreaming out for hole are removed from the well. 3.Shut down and monitor well for flow/breathing until static. 4.Remove wear bushing and install BOPE test plug, hanging off drillpipe on the test plug. 5.Test BOPE as per the PTD. Should hole conditions not allow start of the test by the end of our 14 day interval at 2400 hours 10/15/22, we ask concurrence that we have the time to complete steps one through three above prior to planned hangoff and testing. Thank‐you, Greg Greg Hobbs, P.E. CAUTION: This email originated from outside the State of Alaska mail system. Do not click links or open attachments unless you recognize the sender and know the content is safe. 4 Regulatory Engineer | Wells Team ConocoPhillips Alaska Inc. STATE OF ALASKA OIL AND GAS CONSERVATION COMMISSION *All BOPE reports are due to the agency within 5 days of testing* Submit to:jim.regg@alaska.gov; AOGCC.Inspectors@alaska.gov; phoebe.brooks@alaska.gov Rig Owner:Rig No.:19 DATE:10/17/22 Rig Rep.:Rig Email: Operator: Operator Rep.:Op. Rep Email: Well Name:PTD #2220790 Sundry # Operation:Drilling: X Workover:Explor.: Test:Initial:Weekly:Bi-Weekly:X Other: Rams:250/4000 Annular:250/2500 Valves:250/4000 MASP:2024 MISC. INSPECTIONS:TEST DATA FLOOR SAFETY VALVES: Test Result/Type Test Result Quantity Test Result Housekeeping P Well Sign P Upper Kelly 1 P Permit On Location P Hazard Sec.P Lower Kelly 1 P Standing Order Posted P Misc.NA Ball Type 1 P Test Fluid Water Inside BOP 1 P FSV Misc 0 NA BOP STACK:Quantity Size/Type Test Result MUD SYSTEM:Visual Alarm Stripper 0 NA Trip Tank P P Annular Preventer 1 13-5/8"P Pit Level Indicators P P #1 Rams 1 3.5" X 6"P Flow Indicator P P #2 Rams 1 Blinds P Meth Gas Detector P P #3 Rams 1 3.5" X 6"P H2S Gas Detector P P #4 Rams 0 NA MS Misc 0 NA #5 Rams 0 NA #6 Rams 0 NA ACCUMULATOR SYSTEM: Choke Ln. Valves 1 3.125 P Time/Pressure Test Result HCR Valves 2 3.125 P System Pressure (psi)2925 P Kill Line Valves 1 3.125 P Pressure After Closure (psi)1350 P Check Valve 0 NA 200 psi Attained (sec)32 P BOP Misc 1 4" Kill line Demco P Full Pressure Attained (sec)178 P Blind Switch Covers:All stations Yes CHOKE MANIFOLD:Bottle Precharge:P Quantity Test Result Nitgn. Bottles # & psi (Avg.):4 @ 2325 P No. Valves 14 FP ACC Misc 0 NA Manual Chokes 1 P Hydraulic Chokes 1 P Control System Response Time:Time (sec)Test Result CH Misc 0 NA Annular Preventer 17 P #1 Rams 7 P Coiled Tubing Only:#2 Rams 16 P Inside Reel valves 0 NA #3 Rams 8 P #4 Rams 0 NA Test Results #5 Rams 0 NA #6 Rams 0 NA Number of Failures:1 Test Time:5.0 HCR Choke 1 P Repair or replacement of equipment will be made within days. HCR Kill 1 P Remarks: AOGCC Inspection 24 hr Notice Yes Date/Time 10/13/22 11:16AM Waived By Test Start Date/Time:10/17/2022 4:00 (date)(time)Witness Test Finish Date/Time:10/17/2022 9:00 BOPE Test Report Notify the AOGCC of repairs with written confirmation to: AOGCC.Inspectors@alaska.gov Bob Noble Doyon Test all BOPE components tested with a 4" and 4.5" test joint. F-P on choke valve #1 grease port. Replaced grease port- test, passed. (Tested past due date due to hole conditions. Pre-Approved from Jim Regg). Bottle Precharge 1050 psi. Orville Williams / Sean Tower CPAI K . Harding / D. Pickworth KRU 3S-625 Test Pressure (psi): rig19@doyondrilling.com d19cm@conocophillips.com Form 10-424 (Revised 08/2022)2022-1017_BOP_Doyon19_KRU_3S-625 jbr J. Regg; 11/22/2022 Doyon 19 - BOPE Test KRU 3S-625 PTD 2220790 10/17/2022 J. Regg; 11/22/2022 From:Regg, James B (OGC) To:AOGCC Records (CED sponsored) Subject:RE: BOP - Doyon 19 Date:Tuesday, November 22, 2022 3:47:49 PM Attachments:2022-1017_BOP_Doyon19_KRU_3S-625.pdf Disregard previous report; corrected report attached Jim Regg Supervisor, Inspections AOGCC 333 W. 7th Ave, Suite 100 Anchorage, AK 99501 907-793-1236 From: Regg, James B (OGC) Sent: Tuesday, November 22, 2022 3:38 PM To: AOGCC Records (CED sponsored) <aogcc.records@alaska.gov> Subject: BOP - Doyon 19 KRU 3S-625 (PTD 2220790) Jim Regg Supervisor, Inspections AOGCC 333 W. 7th Ave, Suite 100 Anchorage, AK 99501 907-793-1236 )URP 0RUURZ'XVWLQ: 7R 0F/HOODQ%U\DQ- 2*& 6XEMHFW 5( >(;7(51$/@5( 6)UDFWXUH6WLPXODWLRQ6XQGU\ 'DWH :HGQHVGD\1RYHPEHU 30 $WWDFKPHQWV LPDJHSQJ Dƌ͘DĐ>ĞůůĂŶ͕ dŚĞƌĞƉŽƌƚŽŶϭϬͬϮϲƐŚŽǁƐĂϮϱϬƉƐŝƚĞƐƚĨŽƌϱŵŝŶƐĨŽůůŽǁĞĚďLJĂϱ͕ϬϬϬƉƐŝƚĞƐƚĨŽƌϭϱŵŝŶƐ͕ďŽƚŚŐŽŽĚ͘ZĞƉŽƌƚƐŚŽǁŶďĞůŽǁ͘ KŶĐĞƚŚĞĨƌĂĐƐƉƌĞĂĚŝƐƌŝŐŐĞĚƵƉǁĞǁŝůůƚĞƐƚƐƵƌĨĂĐĞƚƌĞĂƚŝŶŐŝƌŽŶƚŽϭϬ͕ϬϬϬƉƐŝĂŶĚƚŚĞŶƚĞƐƚƚŚĞƚƌĞĞƚŽ;ĂƚůĞĂƐƚͿƚŚĞDtWŽĨ ϴ͕ϵϬϬƉƐŝŽƌƚŽĂŵĂdžŽĨϵ͕ϱϬϬƉƐŝ͘ dŚĂŶŬLJŽƵ͕ ƵƐƚŝŶt͘DŽƌƌŽǁ ^ƚĂĨĨŽŵƉůĞƚŝŽŶƐ ŶŐŝŶĞĞƌ ŽŶŽĐŽWŚŝůůŝƉƐůĂƐŬĂ Ğůů͗ϴϯϮͲϰϵϯͲϵϭϰϭ KĨĨŝĐĞ͗ϵϬϳͲϮϲϯͲϰϳϱϮ &ƌŽŵ͗DĐ>ĞůůĂŶ͕ƌLJĂŶ:;K'ͿфďƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀх ^ĞŶƚ͗tĞĚŶĞƐĚĂLJ͕EŽǀĞŵďĞƌϵ͕ϮϬϮϮϰ͗ϱϬWD dŽ͗DŽƌƌŽǁ͕ƵƐƚŝŶtфƵƐƚŝŶ͘t͘DŽƌƌŽǁΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх ^ƵďũĞĐƚ͗Z ͗ yd ZE>Z ͗ϯ^ͲϲϮϱ&ƌĂĐƚƵƌĞ^ƚŝŵƵůĂƚŝŽŶ^ƵŶĚƌLJ KŶĞŵŽƌĞƋƵĞƐƚŝŽŶ͙ /ĚŝĚŶ͛ƚƐĞĞĂŶLJŵĞŶƚŝŽŶŽĨƚĞƐƚŝŶŐƚŚĞĨƌĂĐƚƌĞĞ͘/͛ŵĂƐƐƵŵŝŶŐŝƚǁĂƐƚĞƐƚĞĚĂůƌĞĂĚLJ͘tŚĂƚǁĂƐƚŚĞƚĞƐƚƉƌĞƐƐƵƌĞ͍ ƌLJĂŶDĐ>ĞůůĂŶ ^ĞŶŝŽƌWĞƚƌŽůĞƵŵ ŶŐŝŶĞĞƌ ůĂƐŬĂKŝůΘ'ĂƐŽŶƐĞƌǀĂƚŝŽŶŽŵŵŝƐƐŝŽŶ ϯϯϯtϳƚŚǀĞ <RXGRQ WRIWHQJHWHPDLOIURPGXVWLQZPRUURZ#FRQRFRSKLOOLSVFRP/HDUQZK\WKLVLVLPSRUWDQW ŶĐŚŽƌĂŐĞ͕<ϵϵϱϬϭ ƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀ нϭ;ϵϬϳͿϮϱϬͲϵϭϵϯ &ƌŽŵ͗DŽƌƌŽǁ͕ƵƐƚŝŶtфƵƐƚŝŶ͘t͘DŽƌƌŽǁΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх ^ĞŶƚ͗tĞĚŶĞƐĚĂLJ͕EŽǀĞŵďĞƌϵ͕ϮϬϮϮϰ͗ϰϵWD dŽ͗DĐ>ĞůůĂŶ͕ƌLJĂŶ:;K'ͿфďƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀх ^ƵďũĞĐƚ͗ZĞ͗ yd ZE>Z ͗ϯ^ͲϲϮϱ&ƌĂĐƚƵƌĞ^ƚŝŵƵůĂƚŝŽŶ^ƵŶĚƌLJ &ŽƌĐŽƵƌƐĞ͕ĞŵĂŝůŽƌĐĂůůĂŶLJƚŝŵĞ͘ dŚĂŶŬLJŽƵĨŽƌƌĞǀŝĞǁŝŶŐƚŚĞƐƵŶĚƌLJƐŽƋƵŝĐŬůLJ͘ 'ĞƚKƵƚůŽŽŬĨŽƌŝK^ &ƌŽŵ͗DĐ>ĞůůĂŶ͕ƌLJĂŶ:;K'ͿфďƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀх ^ĞŶƚ͗tĞĚŶĞƐĚĂLJ͕EŽǀĞŵďĞƌϵ͕ϮϬϮϮϰ͗ϰϯ͗ϬϯWD dŽ͗DŽƌƌŽǁ͕ƵƐƚŝŶtфƵƐƚŝŶ͘t͘DŽƌƌŽǁΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх ^ƵďũĞĐƚ͗Z ͗ yd ZE>Z ͗ϯ^ͲϲϮϱ&ƌĂĐƚƵƌĞ^ƚŝŵƵůĂƚŝŽŶ^ƵŶĚƌLJ dŚĂŶŬƐĨŽƌƚŚĞƋƵŝĐŬƌĞƐƉŽŶƐĞ͘ ƌLJĂŶDĐ>ĞůůĂŶ ^ĞŶŝŽƌWĞƚƌŽůĞƵŵ ŶŐŝŶĞĞƌ ůĂƐŬĂKŝůΘ'ĂƐŽŶƐĞƌǀĂƚŝŽŶŽŵŵŝƐƐŝŽŶ ϯϯϯtϳƚŚǀĞ ŶĐŚŽƌĂŐĞ͕<ϵϵϱϬϭ ƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀ нϭ;ϵϬϳͿϮϱϬͲϵϭϵϯ &ƌŽŵ͗DŽƌƌŽǁ͕ƵƐƚŝŶtфƵƐƚŝŶ͘t͘DŽƌƌŽǁΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх ^ĞŶƚ͗tĞĚŶĞƐĚĂLJ͕EŽǀĞŵďĞƌϵ͕ϮϬϮϮϰ͗ϰϮWD dŽ͗DĐ>ĞůůĂŶ͕ƌLJĂŶ:;K'ͿфďƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀх ^ƵďũĞĐƚ͗ZĞ͗ yd ZE>Z ͗ϯ^ͲϲϮϱ&ƌĂĐƚƵƌĞ^ƚŝŵƵůĂƚŝŽŶ^ƵŶĚƌLJ zĞƐƐŝƌ͕ƚŚĂƚŝƐĐŽƌƌĞĐƚ͘ tĞŚĂǀĞĂϭϬŬĨƌĂĐƚƌĞĞŽŶƚŚĞǁĞůůŶŽǁ͘ dŚĂŶŬƐ ƵƐƚŝŶ ϴϯϮͲϰϵϯͲϵϭϰϭ 'ĞƚKƵƚůŽŽŬĨŽƌŝK^ &ƌŽŵ͗DĐ>ĞůůĂŶ͕ƌLJĂŶ:;K'ͿфďƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀх ^ĞŶƚ͗tĞĚŶĞƐĚĂLJ͕EŽǀĞŵďĞƌϵ͕ϮϬϮϮϰ͗Ϯϴ͗ϱϲWD dŽ͗DŽƌƌŽǁ͕ƵƐƚŝŶtфƵƐƚŝŶ͘t͘DŽƌƌŽǁΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх ^ƵďũĞĐƚ͗ yd ZE>Z ͗ϯ^ͲϲϮϱ&ƌĂĐƚƵƌĞ^ƚŝŵƵůĂƚŝŽŶ^ƵŶĚƌLJ CAUTION:This email originated from outside of the organization. Do not click links or open attachments unless you recognize the sender and know the content is safe. ƵƐƚŝŶ͕ ƌĞLJŽƵƉůĂŶŶŝŶŐƚŽƌĞƉůĂĐĞƚŚĞƉƌŽĚƵĐƚŝŽŶƚƌĞĞǁŝƚŚƚŚĞϭϬŬĨƌĂĐƚƌĞĞ͕ƚŚĞŶƌĞƉůĂĐĞƚŚĞĨƌĂĐƚƌĞĞǁŝƚŚƉƌŽĚƵĐƚŝŽŶƚƌĞĞĂĨƚĞƌƚŚĞũŽď͍ ƌLJĂŶDĐ>ĞůůĂŶ ^ĞŶŝŽƌWĞƚƌŽůĞƵŵ ŶŐŝŶĞĞƌ ůĂƐŬĂKŝůΘ'ĂƐŽŶƐĞƌǀĂƚŝŽŶŽŵŵŝƐƐŝŽŶ ϯϯϯtϳƚŚǀĞ &$87,21 7KLVHPDLORULJLQDWHGIURPRXWVLGHWKH6WDWHRI$ODVNDPDLOV\VWHP'RQRWFOLFNOLQNVRURSHQ DWWDFKPHQWVXQOHVV\RXUHFRJQL]HWKHVHQGHUDQGNQRZWKHFRQWHQWLVVDIH 6RPHSHRSOHZKRUHFHLYHGWKLVPHVVDJHGRQ WRIWHQJHWHPDLOIURPGXVWLQZPRUURZ#FRQRFRSKLOOLSVFRP/HDUQZK\WKLVLVLPSRUWDQW ŶĐŚŽƌĂŐĞ͕<ϵϵϱϬϭ ƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀ нϭ;ϵϬϳͿϮϱϬͲϵϭϵϯ &ƌŽŵ͗DŽƌƌŽǁ͕ƵƐƚŝŶtфƵƐƚŝŶ͘t͘DŽƌƌŽǁΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх ^ĞŶƚ͗dƵĞƐĚĂLJ͕EŽǀĞŵďĞƌϭ͕ϮϬϮϮϱ͗ϮϬWD dŽ͗DĐ>ĞůůĂŶ͕ƌLJĂŶ:;K'ͿфďƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀх͖ZŝdžƐĞ͕DĞůǀŝŶ';K'ͿфŵĞůǀŝŶ͘ƌŝdžƐĞΛĂůĂƐŬĂ͘ŐŽǀх͖K'WĞƌŵŝƚƚŝŶŐ; ƐƉŽŶƐŽƌĞĚͿфĂŽŐĐĐ͘ƉĞƌŵŝƚƚŝŶŐΛĂůĂƐŬĂ͘ŐŽǀх Đ͗DĞƚnjŐĂƌ͕<LJůĞEф<LJůĞ͘E͘DĞƚnjŐĂƌΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх͖>ŽĞƉƉ͕sŝĐƚŽƌŝĂd;K'ͿфǀŝĐƚŽƌŝĂ͘ůŽĞƉƉΛĂůĂƐŬĂ͘ŐŽǀх͖dĂLJůŽƌ͕:ĞŶŶĂ ф:ĞŶŶĂ͘>͘dĂLJůŽƌΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх͖ŽŶŬůŝŶ͕ŵLJфŵLJ͘͘ŽŶŬůŝŶΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх ^ƵďũĞĐƚ͗Z ͗ϯ^ͲϲϮϱ&ƌĂĐƚƵƌĞ^ƚŝŵƵůĂƚŝŽŶ^ƵŶĚƌLJ ZĞƐĞŶĚŝŶŐƚŽŝŶĐůƵĚĞƚŚĞƉĞƌŵŝƚƚŝŶŐĞŵĂŝůĂĚĚƌĞƐƐ͘ dŚĂŶŬLJŽƵ͕ ƵƐƚŝŶt͘DŽƌƌŽǁ ^ƚĂĨĨŽŵƉůĞƚŝŽŶƐ ŶŐŝŶĞĞƌ ŽŶŽĐŽWŚŝůůŝƉƐůĂƐŬĂ Ğůů͗ϴϯϮͲϰϵϯͲϵϭϰϭ KĨĨŝĐĞ͗ϵϬϳͲϮϲϯͲϰϳϱϮ &ƌŽŵ͗DŽƌƌŽǁ͕ƵƐƚŝŶt ^ĞŶƚ͗dƵĞƐĚĂLJ͕EŽǀĞŵďĞƌϭ͕ϮϬϮϮϯ͗ϱϳWD dŽ͗ďƌLJĂŶ͘ŵĐůĞůůĂŶΛĂůĂƐŬĂ͘ŐŽǀ͖ŵĞůǀŝŶ͘ƌŝdžƐĞΛĂůĂƐŬĂ͘ŐŽǀ Đ͗DĞƚnjŐĂƌ͕<LJůĞEф<LJůĞ͘E͘DĞƚnjŐĂƌΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх͖ǀŝĐƚŽƌŝĂ͘ůŽĞƉƉΛĂůĂƐŬĂ͘ŐŽǀ͖dĂLJůŽƌ͕:ĞŶŶĂ ф:ĞŶŶĂ͘>͘dĂLJůŽƌΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх͖ŽŶŬůŝŶ͕ŵLJфŵLJ͘͘ŽŶŬůŝŶΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх ^ƵďũĞĐƚ͗ϯ^ͲϲϮϱ&ƌĂĐƚƵƌĞ^ƚŝŵƵůĂƚŝŽŶ^ƵŶĚƌLJ ůů͕ WůĞĂƐĞĨŝŶĚĂƚƚĂĐŚĞĚƚŚĞϯ^ͲϲϮϱ&ƌĂĐ^ƵŶĚƌLJƌĞƋƵĞƐƚ͘ dŚĂŶŬLJŽƵĨŽƌLJŽƵƌƚŝŵĞĂŶĚƉůĞĂƐĞůĞƚŵĞŬŶŽǁŝĨLJŽƵŚĂǀĞĂŶLJƋƵĞƐƚŝŽŶƐŽƌŝĨ/ŵŝƐƐĞĚĂŶLJƚŚŝŶŐ͘ dŚĂŶŬLJŽƵ͕ ƵƐƚŝŶt͘DŽƌƌŽǁ ^ƚĂĨĨŽŵƉůĞƚŝŽŶƐ ŶŐŝŶĞĞƌ ŽŶŽĐŽWŚŝůůŝƉƐůĂƐŬĂ Ğůů͗ϴϯϮͲϰϵϯͲϵϭϰϭ KĨĨŝĐĞ͗ϵϬϳͲϮϲϯͲϰϳϱϮ CAUTION: This email originated from outside the State of Alaska mail system. Do not click links or open attachments unless you recognize the sender and know the content is safe. From:Regg, James B (OGC) To:AOGCC Records (CED sponsored) Subject:FW: Permit #222-079 - 3S-625 - Doyon 19 Date:Friday, October 14, 2022 1:29:42 PM KRU 3S-625 (PTD 2220790) Jim Regg Supervisor, Inspections AOGCC 333 W. 7th Ave, Suite 100 Anchorage, AK 99501 907-793-1236 From: Regg, James B (OGC) Sent: Friday, October 14, 2022 1:27 PM To: Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com>; Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov> Cc: aogcc.inspectors@alaska.gov Subject: RE: Permit #222-079 - 3S-625 - Doyon 19 AOGCC concurs with completing steps 1-3 before testing BOPE, acknowledging the test may not start with the required 14 days since the last test. Jim Regg Supervisor, Inspections AOGCC 333 W. 7th Ave, Suite 100 Anchorage, AK 99501 907-793-1236 From: Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com> Sent: Friday, October 14, 2022 1:10 PM To: Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov>; Regg, James B (OGC) <jim.regg@alaska.gov> Subject: Permit #222-079 - 3S-625 - Doyon 19 Victoria and Jim, Currently Doyon 19 is backreaming its way out of the 6.5” production open hole at 14,140’ MD at approximately 100 feet per hour. Hole conditions while pulling out of hole have considerably slowed our progress and have increased our predicted time to pull out hole to the shoe by 2 days. The 7- 5/8” casing shoe is at 12,842’ MD and we are projected to reach the shoe later tonight if hole conditions allow. Doyon 19 is due for its 2-week BOPE test tomorrow, September 15. Our current plan is as follows: 1. Continue to work pipe out of hole to the 7-5/8” casing shoe. 2. Circulate the casing clean to ensure any formation cuttings/cavings generated while drilling or backreaming out for hole are removed from the well. 3. Shut down and monitor well for flow/breathing until static. 4. Remove wear bushing and install BOPE test plug, hanging off drillpipe on the test plug. 5. Test BOPE as per the PTD. Should hole conditions not allow start of the test by the end of our 14 day interval at 2400 hours 10/15/22, we ask concurrence that we have the time to complete steps one through three above prior to planned hangoff and testing. Thank-you, Greg Greg Hobbs, P.E. Regulatory Engineer | Wells Team ConocoPhillips Alaska Inc. 5HJJ-DPHV% 2*& )URP %URRNV3KRHEH/ 2*& 6HQW )ULGD\2FWREHU $0 7R 5LJ &F 5HJJ-DPHV% 2*& 6XEMHFW 5( 'R\RQ5LJ %23(WHVWUHSRUW $WWDFKPHQWV 'R\RQ 5HYLVHG[OV[ /͛ǀĞĂƚƚĂĐŚĞĚĂƌĞǀŝƐĞĚƌĞƉŽƌƚĂĚĚŝŶŐƚŚĞǀĂůǀĞƐŝnjĞƐ͕ĐŚĂŶŐŝŶŐƚŚĞD^WƚŽƌĞĨůĞĐƚϮϬϮϰďĂƐĞĚŽŶWdηϮϮϮϬϳϵϬ͕ ĐŚĂŶŐŝŶŐƚŚĞDŝƐĐ͘ĨŝĞůĚƚŽ͞E͕͟ĂŶĚŵŽǀŝŶŐƚŚĞďŽƚƚůĞƉƌĞĐŚĂƌŐĞŽĨϭϬϱϬƚŽƚŚĞƌĞŵĂƌŬƐ;ĂƐƚŚŝƐŝƐĂWͬ&ĨŝĞůĚͿ͘WůĞĂƐĞ ƵƉĚĂƚĞLJŽƵƌĐŽƉLJŽƌůĞƚŵĞŬŶŽǁŝĨLJŽƵĚŝƐĂŐƌĞĞ͘ dŚĂŶŬLJŽƵ͕ WŚŽĞďĞ WŚŽĞďĞƌŽŽŬƐ ZĞƐĞĂƌĐŚŶĂůLJƐƚ ůĂƐŬĂKŝůĂŶĚ'ĂƐŽŶƐĞƌǀĂƚŝŽŶŽŵŵŝƐƐŝŽŶ WŚŽŶĞ͗ϵϬϳͲϳϵϯͲϭϮϰϮ CONFIDENTIALITY NOTICE: This e-mail message, including any attachments, contains information from the Alaska Oil and Gas Conservation Commission (AOGCC), State of Alaska and is for the sole use of the intended recipient(s). It may contain confidential and/or privileged information. The unauthorized review, use or disclosure of such information may violate state or federal law. If you are an unintended recipient of this e-mail, please delete it, without first saving or forwarding it, and, so that the AOGCC is aware of the mistake in sending it to you, contact Phoebe Brooks at 907-793-1242 or phoebe.brooks@alaska.gov. &ƌŽŵ͗ZŝŐϭϵфƌŝŐϭϵΛĚŽLJŽŶĚƌŝůůŝŶŐ͘ĐŽŵх ^ĞŶƚ͗dŚƵƌƐĚĂLJ͕KĐƚŽďĞƌϲ͕ϮϬϮϮϱ͗ϬϰWD dŽ͗ƌŽŽŬƐ͕WŚŽĞďĞ>;K'ͿфƉŚŽĞďĞ͘ďƌŽŽŬƐΛĂůĂƐŬĂ͘ŐŽǀх ^ƵďũĞĐƚ͗Z ͗ŽLJŽŶZŝŐϭϵKW ƚĞƐƚƌĞƉŽƌƚϵͲϭϴͲϮϮ ŽƌƌĞĐƚϯ͘ϭϮϱͬǁŽƵůĚLJŽƵůŝŬĞŵĞĐŽƌƌĞĐƚŚŝƐƌĞƉŽƌƚĂŶĚƌĞƐĞŶĚŝƚ &ƌŽŵ͗ƌŽŽŬƐ͕WŚŽĞďĞ>;K'ͿфƉŚŽĞďĞ͘ďƌŽŽŬƐΛĂůĂƐŬĂ͘ŐŽǀх ^ĞŶƚ͗dŚƵƌƐĚĂLJ͕KĐƚŽďĞƌϲ͕ϮϬϮϮϰ͗ϰϲWD dŽ͗ZŝŐϭϵфƌŝŐϭϵΛĚŽLJŽŶĚƌŝůůŝŶŐ͘ĐŽŵх ^ƵďũĞĐƚ͗Z ͗ŽLJŽŶZŝŐϭϵKW ƚĞƐƚƌĞƉŽƌƚϵͲϭϴͲϮϮ dŚĞǀĂůǀĞƐŝnjĞƐĂƌĞŵŝƐƐŝŶŐĨƌŽŵƚŚĞKWƐƚĂĐŬ͖ƐŚŽƵůĚƚŚĞLJďĞϯ͘ϭϮϱ͍ WŚŽĞďĞƌŽŽŬƐ ZĞƐĞĂƌĐŚŶĂůLJƐƚ ůĂƐŬĂKŝůĂŶĚ'ĂƐŽŶƐĞƌǀĂƚŝŽŶŽŵŵŝƐƐŝŽŶ WŚŽŶĞ͗ϵϬϳͲϳϵϯͲϭϮϰϮ CONFIDENTIALITY NOTICE: This e-mail message, including any attachments, contains information from the Alaska Oil and Gas Conservation Commission (AOGCC), State of Alaska and is for the sole use of the intended recipient(s). It may contain confidential and/or privileged information. The unauthorized review, use or disclosure of such information may violate state or federal law. If you .5786 37' ƌĞǀŝƐĞĚƌĞƉŽƌƚĂ ǀĂůǀĞƐŝnjĞƐ͕ĐŚĂŶŐŝŶŐƚŚĞD^Wƚ ĐŚĂŶŐŝŶŐƚŚĞDŝƐĐ͘ĨŝĞůĚƚ ŵŽǀŝŶŐƚŚĞďŽƚƚůĞƉƌĞĐŚĂƌŐĞŽĨϭϬϱϬƚŽƚŚĞƌĞŵĂƌŬƐ are an unintended recipient of this e-mail, please delete it, without first saving or forwarding it, and, so that the AOGCC is aware of the mistake in sending it to you, contact Phoebe Brooks at 907-793-1242 or phoebe.brooks@alaska.gov. &ƌŽŵ͗ZŝŐϭϵфƌŝŐϭϵΛĚŽLJŽŶĚƌŝůůŝŶŐ͘ĐŽŵх ^ĞŶƚ͗^ƵŶĚĂLJ͕^ĞƉƚĞŵďĞƌϭϴ͕ϮϬϮϮϱ͗ϱϵWD dŽ͗KK'WƌƵĚŚŽĞĂLJфĚŽĂ͘ĂŽŐĐĐ͘ƉƌƵĚŚŽĞ͘ďĂLJΛĂůĂƐŬĂ͘ŐŽǀх͖ƌŽŽŬƐ͕WŚŽĞďĞ>;K'Ϳ фƉŚŽĞďĞ͘ďƌŽŽŬƐΛĂůĂƐŬĂ͘ŐŽǀх͖ZĞŐŐ͕:ĂŵĞƐ;K'Ϳфũŝŵ͘ƌĞŐŐΛĂůĂƐŬĂ͘ŐŽǀх͖ϭϵŽŵƉĂŶLJDĂŶ фĚϭϵĐŵΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх͖ĂǀŝĚŽĂƚĞƐфĐŽĂƚĞƐ͘ĐŽĂƚĞƐΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх͖,ŽďďƐ͕'ƌĞŐ^ ф'ƌĞŐ͘^͘,ŽďďƐΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх͖KƉĞƌĂƚŝŽŶƐ ŶŐŝŶĞĞƌ͕ŽLJŽŶϭϵфĚϭϵŽƉƐĞŶŐΛĐŽŶŽĐŽƉŚŝůůŝƉƐ͘ĐŽŵх Đ͗ĞŶtĞĚŝŶфďǁĞĚŝŶΛĚŽLJŽŶĚƌŝůůŝŶŐ͘ĐŽŵх͖ŝůůtĂůƚĞƌфďǁĂůƚĞƌΛĚŽLJŽŶĚƌŝůůŝŶŐ͘ĐŽŵх͖^ĂŵƵĞůLJĞ фƐĚLJĞΛĚŽLJŽŶĚƌŝůůŝŶŐ͘ĐŽŵх ^ƵďũĞĐƚ͗ŽLJŽŶZŝŐϭϵKW ƚĞƐƚƌĞƉŽƌƚϵͲϭϴͲϮϮ dŚĂŶŬLJŽƵ KƌǀŝůůĞtŝůůŝĂŵƐ ZŝŐϭϵdŽŽůƉƵƐŚĞƌ ϵϬϳϲϳϬͲϲϬϵϴ ϵϬϳϯϬϲͲϰϰϲϳ &$87,21 7KLVHPDLORULJLQDWHGIURPRXWVLGHWKH6WDWHRI$ODVNDPDLOV\VWHP'RQRWFOLFNOLQNVRURSHQ DWWDFKPHQWVXQOHVV\RXUHFRJQL]HWKHVHQGHUDQGNQRZWKHFRQWHQWLVVDIH STATE OF ALASKA OIL AND GAS CONSERVATION COMMISSION BOPE Test Report for: Reviewed By: P.I. Suprv Comm ________KUPARUK RIV UNIT 3S-625 JBR 12/09/2022 MISC. INSPECTIONS: FLOOR SAFTY VALVES:CHOKE MANIFOLD:BOP STACK: ACCUMULATOR SYSTEM:MUD SYSTEM: P/F P/F P/FP/FP/F Visual Alarm QuantityQuantity Time/Pressure SizeQuantity Number of Failures:1 CMV # 4 had to be serviced, passed retest Test Results TEST DATA Rig Rep:Kelly Haug/Einar FleaglOperator:ConocoPhillips Alaska, Inc.Operator Rep:Lundale/Brown Rig Owner/Rig No.:Doyon 19 PTD#:2220790 DATE:10/1/2022 Type Operation:DRILL Annular: 250/2500Type Test:BIWKLY Valves: 250/4000 Rams: 250/4000 Test Pressures:Inspection No:bopAGE221003210002 Inspector Adam Earl Inspector Insp Source Related Insp No: INSIDE REEL VALVES: Quantity P/F (Valid for Coil Rigs Only) Remarks: Test Time 7 MASP: 2024 Sundry No: Control System Response Time (sec) Time P/F Housekeeping:P PTD On Location P Standing Order Posted P Well Sign P Hazard Sec.P Test Fluid W Misc NA Upper Kelly 1 P Lower Kelly 1 P Ball Type 1 P Inside BOP 1 P FSV Misc 0 NA 14 FPNo. Valves 1 PManual Chokes 1 PHydraulic Chokes 0 NACH Misc Stripper 0 NA Annular Preventer 1 13 5/8 P #1 Rams 1 3 1/2 X 6 P #2 Rams 1 Blind P #3 Rams 1 3 1/2 X 6 P #4 Rams 0 NA #5 Rams 0 NA #6 Rams 0 NA Choke Ln. Valves 1 3 1/8 P HCR Valves 2 3 1/8 P Kill Line Valves 1 3 1/8 P Check Valve 0 NA BOP Misc 1 4" kill demco P System Pressure P2950 Pressure After Closure P1400 200 PSI Attained P30 Full Pressure Attained P172 Blind Switch Covers:PAll Stations Bottle precharge P Nitgn Btls# &psi (avg)P4@2325 ACC Misc NA0 P PTrip Tank P PPit Level Indicators P PFlow Indicator P PMeth Gas Detector P PH2S Gas Detector 0 NAMS Misc Inside Reel Valves 0 NA Annular Preventer P20 #1 Rams P8 #2 Rams P8 #3 Rams P8 #4 Rams NA0 #5 Rams NA0 #6 Rams NA0 HCR Choke P2 HCR Kill P2 FP CMV # 4 had to be serviced, passed retest STATE OF ALASKA OIL AND GAS CONSERVATION COMMISSION *All BOPE reports are due to the agency within 5 days of testing* SSu bm it t o :jim.regg@alaska.gov; AOGCC.Inspectors@alaska.gov; phoebe.brooks@alaska.gov Rig Owner: Rig No.:19 DATE: 9/18/22 Rig Rep.: Rig Email: Operator: Operator Rep.: Op. Rep Email: Well Name:PTD #2220790 Sundry # Operation: Drilling: X Workover: Explor.: Test: Initial: X Weekly: Bi-Weekly: Other: Rams:250/4000 Annular:250/2500 Valves:250/4000 MASP:2024 MISC. INSPECTIONS: TEST DATA FLOOR SAFETY VALVES: Test Result/Type Test Result Quantity Test Result Housekeeping P Well Sign P Upper Kelly 1P Permit On Location P Hazard Sec.P Lower Kelly 1P Standing Order Posted P Misc.NA Ball Type 1P Test Fluid Water Inside BOP 1P FSV Misc 0NA BOP STACK:Quantity Size/Type Test Result MUD SYSTEM:Visual Alarm Stripper 0NATrip Tank PP Annular Preventer 1 13-5/8"P Pit Level Indicators PP #1 Rams 1 3.5" X 6"P Flow Indicator PP #2 Rams 1 Blinds P Meth Gas Detector PP #3 Rams 1 3.5" X 6"P H2S Gas Detector PP #4 Rams 0NAMS Misc 0NA #5 Rams 0NA #6 Rams 0NAACCUMULATOR SYSTEM: Choke Ln. Valves 1 3.125 P Time/Pressure Test Result HCR Valves 2 3.125 P System Pressure (psi)3000 P Kill Line Valves 1 3.125 P Pressure After Closure (psi)1400 P Check Valve 0NA200 psi Attained (sec)30 P BOP Misc 1 4" Kill line Demco P Full Pressure Attained (sec)172 P Blind Switch Covers: All stations Yes CHOKE MANIFOLD:Bottle Precharge:P Quantity Test Result Nitgn. Bottles # & psi (Avg.): 2400 P No. Valves 14 P ACC Misc 0NA Manual Chokes 1P Hydraulic Chokes 1P Control System Response Time:Time (sec) Test Result CH Misc 0NA Annular Preventer 17 P #1 Rams 7 P Coiled Tubing Only:#2 Rams 16 P Inside Reel valves 0NA #3 Rams 8 P #4 Rams 0 NA Test Results #5 Rams 0 NA #6 Rams 0 NA Number of Failures:0 Test Time:4.5 HCR Choke 1 P Repair or replacement of equipment will be made within days. HCR Kill 1 P Remarks: AOGCC Inspection 24 hr Notice Yes Date/Time 9/15/22 11:15 Waived By Test Start Date/Time:9/17/2022 23:00 (date) (time)Witness Test Finish Date/Time:9/18/2022 3:30 BOPE Test Report Notify the AOGCC of repairs with written confirmation to: AOGCC.Inspectors@alaska.gov Sully Sullivan Doyon Test all BOPE components tested with a 5" test joint. Bottle precharge - 1050. Orville Williams / Sean Tower CPAI Charles Brown / Kevin Hinrichs KRU 3S-625 Test Pressure (psi): rig19@doyondrilling.com d19cm@conocophillips.com Form 10-424 (Revised 08/2022)2022-0918_BOP_Doyon19_KRU_3S-625 9 9 9 9 9 9 99 9 9 9 9 9 -5HJJ STATE OF ALASKA OIL AND GAS CONSERVATION COMMISSION DIVERTER Test Report for: Reviewed By: P.I. Suprv Comm ________KUPARUK RIV UNIT 3S-625 JBR 10/05/2022 MISC. INSPECTIONS: GAS DETECTORS: DIVERTER SYSTEM:MUD SYSTEM: P/F P/F P/F Alarm Visual Alarm Visual Time/Pressure Size Number of Failures:0 Remarks:Tested 20" Annular with 5" DP. The rig called later and said they had to replace Knife valve due to leaking. Non witnessed times were as follows: Annular-25sec. Knife-13sec. TEST DATA Rig Rep:Hawg/TowerOperator:ConocoPhillips Alaska, Inc.Operator Rep:Lundale/Pickworth Contractor/Rig No.:Doyon 19 PTD#:2220790 DATE:9/11/2022 Well Class:DEV Inspection No:divAGE220912194613 Inspector Adam Earl Inspector Insp Source Related Insp No: Test Time:2 ACCUMULATOR SYSTEM: Location Gen.:P Housekeeping:P Warning Sign P 24 hr Notice:P Well Sign:P Drlg. Rig.P Misc:NA Methane:P P Hydrogen Sulfide:P P Gas Detectors Misc:0 NA Designed to Avoid Freeze-up?P Remote Operated Diverter?P No Threaded Connections?P Vent line Below Diverter?P Diverter Size:20 P Hole Size:13.5 P Vent Line(s) Size:16 P Vent Line(s) Length:116.5 P Closest Ignition Source:96 P Outlet from Rig Substructure:113 P Vent Line(s) Anchored:P Turns Targeted / Long Radius:NA Divert Valve(s) Full Opening:P Valve(s) Auto & Simultaneous: Annular Closed Time:35 P Knife Valve Open Time:17 P Diverter Misc:0 NA Systems Pressure:P2900 Pressure After Closure:P1450 200 psi Recharge Time:P28 Full Recharge Time:P151 Nitrogen Bottles (Number of):P4 Avg. Pressure:P2350 Accumulator Misc:NA0 P PTrip Tank: P PMud Pits: P PFlow Monitor: 0 NAMud System Misc: 5(9,6(' 9 9 9 9 9 9 'LYHUWHUVL]HUHYLVHG 9 9 STATE OF ALASKA OIL AND GAS CONSERVATION COMMISSION DIVERTER Test Report for: Reviewed By: P.I. Suprv Comm ________KUPARUK RIV UNIT 3S-625 JBR 09/21/2022 MISC. INSPECTIONS: GAS DETECTORS: DIVERTER SYSTEM:MUD SYSTEM: P/F P/F P/F Alarm Visual Alarm Visual Time/Pressure Size Number of Failures:0 Remarks:Tested 20" Annular with 5" DP. The rig called later and said they had to replace Knife valve due to leaking. Non witnessed times were as follows: Annular-25sec. Knife-13sec. TEST DATA Rig Rep:Hawg/TowerOperator:ConocoPhillips Alaska, Inc.Operator Rep:Lundale/Pickworth Contractor/Rig No.:Doyon 19 PTD#:2220790 DATE:9/11/2022 Well Class:DEV Inspection No:divAGE220912194613 Inspector Adam Earl Inspector Insp Source Related Insp No: Test Time:2 ACCUMULATOR SYSTEM: Location Gen.:P Housekeeping:P Warning Sign P 24 hr Notice:P Well Sign:P Drlg. Rig.P Misc:NA Methane:P P Hydrogen Sulfide:P P Gas Detectors Misc:0 NA Designed to Avoid Freeze-up?P Remote Operated Diverter?P No Threaded Connections?P Vent line Below Diverter?P Diverter Size:20 P Hole Size:13.5 P Vent Line(s) Size:16 P Vent Line(s) Length:116.5 P Closest Ignition Source:96 P Outlet from Rig Substructure:113 P Vent Line(s) Anchored:P Turns Targeted / Long Radius:NA Divert Valve(s) Full Opening:P Valve(s) Auto & Simultaneous: Annular Closed Time:35 P Knife Valve Open Time:17 P Diverter Misc:0 NA Systems Pressure:P2900 Pressure After Closure:P1450 200 psi Recharge Time:P28 Full Recharge Time:P151 Nitrogen Bottles (Number of):P4 Avg. Pressure:P2350 Accumulator Misc:NA0 P PTrip Tank: P PMud Pits: P PFlow Monitor: 0 NAMud System Misc: 9 9 9 9 9 9 9 9 replace Knife valve due to leaking.Non witnessed times were as Annular-25sec. Knife-13sec. Alaska Oil and Gas Conservation Commission 333 West Seventh Avenue Anchorage, Alaska 99501-3572 Main: 907.279.1433 Fax: 907.276.7542 www.aogcc.alaska.gov Chris Brillon Drilling Manager ConocoPhillips Alaska, Inc. PO Box 100360 Anchorage, AK 99510-0360 Re: Kuparuk River Field, Torok Oil Pool, KRU 3S-625 ConocoPhillips Alaska, Inc. Permit to Drill Number: 222-079 Surface Location: 2569' FNL, 1285' FEL, SESW, Sec. 18, T12N, R8E, UM Bottomhole Location: 659' FNL, 1181' FWL, NWNW, Sec. 2, T12N, R7E, UM Dear Mr. Brillon: Enclosed is the approved application for the permit to drill the above referenced well. Per Statute AS 31.05.030(d)(2)(B) and Regulation 20 AAC 25.071, composite curves for well logs run must be submitted to the AOGCCwithin 90 days after completion, suspension or abandonment of this well. This permit to drill does not exempt you from obtaining additional permits or an approval required by law from other governmental agencies and does not authorize conducting drilling operations until all other required permits and approvals have been issued. In addition, the AOGCC reserves the right to withdraw the permit in the event it was erroneously issued. Operations must be conducted in accordance with AS 31.05 and Title 20, Chapter 25 of the Alaska Administrative Code unless the AOGCC specifically authorizes a variance. Failure to comply with an applicable provision of AS 31.05, Title 20, Chapter 25 of the Alaska Administrative Code, or an AOGCC order, or the terms and conditions of this permit may result in the revocation or suspension of the permit. Sincerely, Jessie L. Chmielowski Commissioner DATED this ___ day of July, 2022. 18 Jessie L. Chmielowski Digitally signed by Jessie L. Chmielowski Date: 2022.07.18 09:27:28 -08'00' ! 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Chmielowski Date: 2022.07.18 09:25:42 -08'00' GMTU KRU 3S-625 Conditions of Approval: Approval is granted to run the LWD-Sonic on upcoming well with the following provisions: 1. CPAI will provide a written log evaluation/interpretation to the AOGCC along with the log as soon as they become available. The evaluation is to include/highlight the intervals of competent cement that CPAI is using to meet the objective requirements for annular isolation, reservoir isolation, or confining zone isolation etc. Providing the log without an evaluation/interpretation is not acceptable. 2. LWD sonic logs must show free pipe and Top of Cement, just as the e-line log does. CPAI must start the log at a depth to ensure the free pipe above the TOC is captured as well as the TOC. Starting the log below the actual TOC based on calculations predicting a different TOC will not be acceptable. 3. CPAI will provide a cement job summary report and evaluation along with the cement log and evaluation to the AOGCC when they become available 4. CPAI will provide the results of the FIT when available. 5. Depending on the cement job results indicated by the cement job report, the logs and the FIT, remedial measures or additional logging may be required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'+( = '+( 4 " += '+( , $, , $,0 '+( '+( > , ';( - "3 . / '+( 5&&&"&& " "$ 053$0"$3 " & "&000" & "&&'"9 & "& &"& "3300"'9 '" - 2@ <05 50&&"&& "& $ 9"' 05$9'"' " &"&00"$' & "&0"3 & "& &"& "'0"03'"$9 - 2@ <05 50&"03"3$ $"' 5&0"'& "9$ & "&00'"& & "&0"&9 &"& &"& 9"&0"&0 " - 2@ <05 5&&"& & "9 0"' 5&" "9$ & "&00'"& & "&0"&9 &"& &"& 9"&0"&0 " - 2@ <05 5&&"&& 3"'$ "0 50'"93 " & "&03"'& & "&0"00&"& &"& 9"93"9& '"3$ - 2 # A # <#- 5 5'&&"&& '&"3 $"9 50"& "3 & "&0$"0 & "&0"& &"& &"& $"'$"0 "0- 2# A # <#- 5 5&&"&& '"3 '" 539"& '"& &"&00&"&3 &"&0"3$ & "& &"& '"&&0&"3 "'0 - 2 # A # <#- 5 5&&"& & ''"'9 ' "9$ 5 $"$ '"' & "&000"&0 &"&0"3 & "& &"& ''"'000" "9 - 2# A # <#- 5 5$"3 '"'3 '3"'9 5''"'& '"' & "&00"& &"&" & "& &"& '"30"9 "$ - 2# A # <#- 5 59&&"&& '" '3"$ 5'$"90 '"' & "&00"& &"&" & "& &"& '"30"9 "$ - 2# A # <#- 5 59' "0'9" '$"$ 5'& "'& '" &"&00"& &"&"3 & "& &"& '9"$0" "& - 2# A # <#- 5 59 "0'9" '$"$ 5'9"39 '" & "&00"9& & "&"3 & "& &"& '9"0"0 " - 2@ < 5 53&&"& & '3"' & "3 5'$9"0$'" & "&00"$ & "&"39 & "& &"& '3"&00"9$ " - 2@ < 5 5$&&"&& &"90 "' 5 "&' '"'0 & "&00'"0&"&"$ & "& &"& 0"0"& " - 2@ < 5 5$99"33 " "0 50&"'& '"' &"&00"& &"&9"& &"& &"& "&0"33 9"& - 2@ < 5 5&&&"&& "&' "3 5"93 '"' &"&00"& &"&9"& &"& &"& "&0"33 9"& - 2@ < 5 50&&"&& "' 3"&3 53" '"9 & "&003"' &"&9"09&"& &"& &"0$"& 9"'9 - 2 @ < 5 5&&"&& 9"3' & "0 599"' '"$$ & "&00"'$ & "&9" & "& &"& '""0 9"$& - 2@ < 5 5&&"&& &"$ " 5933" "0 & "&0'"3 & "&9"$ &"& &"& 9"3 "' 3"0 - 2@ < 5 5'&&"& & "99 '"0'53" "$ & "&03"'3 & "&9"39 & "& &"& 9&"$" 3"$ - 2@ < 5 5&&"&& "9 "$3 533& "0"0&"&0"'& & "&3"0$&"&0 &"& 9"&"0$$"& - 2@ < 5 5'"' "' "9' 53$9"& " & "&0'"0&"&3" & "&0 &"& 9"$0'"$' $"0$- 2@ < 5 5&&"& & 9"$' 9"' 5$0$"39 " & "&0"3 &"&3"& &"&0 &"& 9"&9"'& $"3 - 2@ < 5 59&&"&& 9&"9 3" 5$"09"0&"&0'& "$$ & "&3"30 & "&0 &"& 9"3&'0"3' $"$ - 2@ < 5 53&&"& & 9" 0 $"3 5$3 "39 9"9 & "&0' "9 &"&$"0&"&0 &"& 93"'"' $"$3 - 2@ < 5 533'" 9"39 9& "93 5&&3"0$3"' & "&0'$" &"&$"' & "&0 &"& 9$"'$&"'$ 0&"& - 2@ < 5 5$&&"&& 9"39 9& "93 5&00"$ 3" & "&0&" & "&$" &"&0 &"& 9$"30"' 0&"' - 2@ < 5 '5&&&"&& 9"39 9& "93 5&"9 3"$9 & "&0"& & "&0&"03&"&0 &"& 3&"3"000&"'9 - 2 @ < 5 '50&&"&& 9"39 9& "93 5&&"93 $" & "&0& "& & "&0&"3 & "&0 &"& 30"990"& 0&"$ - 2@ < 5 '5&&"&& 9"39 9& "93 5&3"0$0&"& & "&0 " & "&00"'3 & "&0 &"& 3" "$3 0&"3$ - 2 @ < 5 '5&&"&& 9"39 9& "93 50&$"& 9" &"&0"$ &"&3"'' & "&0 &"& 9$"&'"0$0&"& - 2# A # <#- 5 '5'&&"&& 9"39 9& "93 50'"& 9"$ & "&0 "99 & "&3"9$ & "&0 &"& 3&"''"0 0&" - 2# A # <#- 5 '5&&"&& 9"39 9& "93 503"' 3"$ & "&09"$9 & "&$"0&"&0 &"& 30"3"' 0&"0 - 2# A # <#- 5 '5&&"&& 9"39 9& "93 503"3' 3" & "&0'& "03&"&$"0 &"&0 &"& 30"$'& " 0&" - 2# A # <#- 5 '59&&"&& 9"39 9& "93 5& 9" $"&' &"&0'"'& & "&$"3$ & "&0 &"& 3"'"30 0&"9$ - 2# A # <#- 5 '53&&"&& 9"39 9& "93 50" $"' & "&0''" & "&0&"9 & "&0 &"& 3"0&' "&0 0&"$ - 2# A # <#- 5 '5$&&"&& 9"39 9& "93 5 "&9 $"3 & "&0'"39 & "&0&" & "&0 &"& 3"3'9" 00"&' - 2# A # <#- 5 5&&&"&& 9"39 9& "93 53& "'3 0&"0 & "&0'$"00&"&00"&' &"&0 &"& 3'"&&'$"'' 00"09- 2# A # <#- 5 50&&"&& 9"39 9& "93 5& '"3$ 0&"0 & "&00" & "&00"'' & "&0 &"& 3'"30"9 00"$ - 2# A # <#- 5 5&&"&& 9"39 9& "93 5$"& 00"&0 &"&0" & "&00"3 & "&0 &"& 3'"9"$0 00"'0 - 2 # A # <#- 5 5&&"&& 9"39 9& "93 5 "90 00"'0 & "&0"33 & "&0"' & "&0 &"& 3"&"000" - 2# A # <#- 5 5'&&"&& 9"39 9& "93 593"000"3 & "&03"0'&"&0"' & "&0 &"& 3"03"'& 00"' - 2# A # <#- 5 5&&"&& 9"39 9& "93 5'& " 0" & "&0& "'0 & "&0"& &"&0 &"& 3"& " 00"9 - 2# A # <#- 5 5&&"&& 9"39 9& "93 5'"$' 0"' & "&0"3 & "&0"' & "&0 &"& 3"9$"$0 00"39 - 2 # A # <#- 5 59&&"&& 9"39 9& "93 5' 0" 0"& &"&0'"$ & "&0"39 & "&0 &"& 3"&& "0900"$$ - 2# A # <#- 5 53&&"&& 9"39 9& "93 5'9 "9 0"' & "&09" & "&0'"$ & "&0 &"& 3"&9"'' 0"0&- 2# A # <#- 5 5$&&"&& 9"39 9& "93 5&&"090"33 & "&0$"0 &"&0'"90 & "&0 &"& 3"3$"90 0" - 2# A # <#- 5 5&&&"&& 9"39 9& "93 5'"3 0'"$ & "&090"9$ & "&0"0&"&0 &"& 3"90"$3 0"' - 2# A # <#- 5 50&&"&& 9"39 9& "93 5 '3"$$ 0'"90 & "&09'"&9 &"&0" &"&0 &"& 3"9&9'" 0"' - 2 # A # <#- 5 5&&"&& 9"39 9& "93 5 9"'& 0"0&"&09" & "&0"$9 & "&0 &"& 3"3'9" 0"9 - 2# A # <#- 5 5&&"&& 9"39 9& "93 5 $9"30 0" &"&093"' & "&0"$ & "&0 &"& 3"$393"30 0"$ - 2# A # <#- 5 5'&&"&& 9"39 9& "93 5" 0"$9 & "&03& "$ & "&0"3 & "&0 &"& 39"0&30"&$ 0"3& - 2 # A # <#- 5 5&&"&& 9"39 9& "93 5'" 0"$ & "&03" & "&09" & "&0 &"& 39"3"3 0"$ - 2# A # <#- 5 5&&"&& 9"39 9& "93 590"&' 0"30 & "&03 "0 &"&09"9 & "&0 &"& 39"3 " 0"&' - 2# A # <#- 5 * $ " + # ! ,# "#"$%& "'& ( -./+ #! ) * 0# "#"$%& "'& ( /+ #! + # , 1 + # 2 # -. . ) "# 2 3 # / 0/ 4#5 "&&1. /3#2,0 + < 4 " " / '+( '+( = '+( > , ';( ';( * '+( = '+( . '+( = '+( 4 " += '+( , $, , $,0 '+( '+( > , ';( - "3 . / '+( 59&&"&& 9"39 9& "93 5$ "' 09"' & "&039"3& & "&03"0&&"&0 &"& 39"'39"$ 0"0- 2# A # <#- 5 53&&"&& 9"39 9& "93 590$"3 09" & "&0$& "&$ &"&03" &"&0 &"& 39"$& " 0"$ - 2# A # <#- 5 5$&&"&& 9"39 9& "93 59''"9 03"&3 &"&0$"$ & "&03"$ & "&0 &"& 39"$" 0"'0 - 2 # A # <#- 5 95&&&"&& 9"39 9& "93 593"3 03"0 &"&0$'"3 & "&0$"'& & "&0 &"& 39"90$'"30 0" - 2# A # <#- 5 950&&"&& 9"39 9& "93 59$"&$ 03"$' & "&0$"$9 & "&0$"3 & "&0 &"& 39"9$$9"0&0" - 2# A # <#- 5 95&&"&& 9"39 9& "93 5309"& 0$" & "&0$$"9 & "&& " & "&0 &"& 39"39$$"$ 0"93 - 2# A # <#- 5 95&&"&& 9"39 9& "93 53'0"$0 0$"9$ & "&00&0"9 &"&& "9& & "&0 &"& 39"$'0&0"$ 0"$& - 2# A # <#- 5 95'&&"&& 9"39 9& "93 53" & " & "&00&"3 & "&0"0&"&0 &"& 33"&00&"$3 0'"& - 2# A # <#- 5 95&&"&& 9"39 9& "93 53$& "9 & " & "&00&"0&"&0"9 &"&0 &"& 33"&30&"3 0'"0- 2# A # <#- 5 95&&"&& 9"39 9& "93 5$0"0'0"&9 &"&00&3"' & "&"&& &"&0 &"& 33"0'0&3"9 0'"$ - 2# A # <#- 5 959&&"&& 9"39 9& "93 5$$" 0"& &"&000&"9 & "&"'' & "&0 &"& 33"&00&"39 0'"' - 2 # A # <#- 5 953&&"&& 9"39 9& "93 5$"$ 0"$ & "&000"& &"&"33 & "&0 &"& 33"00"00'" - 2# A # <#- 5 95$&&"&& 9"39 9& "93 5$33"9 " & "&000" & "&"0 & "&0 &"& 33"00"' 0'"3 - 2# A # <#- 5 35&&&"&& 9"39 9& "93 '5&0"93 "9$ & "&0009" & "&"9 & "&0 &"& 33"9009"9 0'"30 - 2 # A # <#- 5 350&&"&& 9"39 9& "93 '5&9"0$ " & "&000$"$ & "&'"0$&"&0 &"& 33"'0& "& 0'"$ - 2# A # <#- 5 35&&"&& 9"39 9& "93 '5&0"& " & "&00" & "&'" & "&0 &"& 33"'90" 0"&3 - 2# A # <#- 5 35&&"&& 9"39 9& "93 '5&3"&0 '"&3 &"&00'" &"& "&9 &"&0 &"& 33"00'" 0" - 2# A # <#- 5 35'&&"&& 9"39 9& "93 '500&"' '"0 &"&00"3 & "& "0 &"&0 &"& 33"0"$ 0" - 2# A # <#- 5 35'0"9 9 "39 9& "93 '50 "'& '"$ & "&00$"0&"& "$ & "&0 &"& 33"&0$" 0"'$ - 2 # A # <#- 5 35&&"&& 9"39 9& "93 '50'"3 '"$ & "&00$"0&"& "$ & "&0 &"& 33"&0$" 0"'$ - 2 # A # <#- 5 35&&"&& 9"39 9& "93 '50$"' "3 & "&000"' & "&"$ & "&0 &"& 33"'00" 0" - 2# A # <#- 5 359&&"&& 9"39 9& "93 '503" "30 & "&00"99 & "&"3 & "&0 &"& 33"30"3 0"99 - 2# A # <#- 5 353&&"&& 9"39 9& "93 '5& 3"& "' & "&00"&9 &"&9"9 & "&0 &"& 33"90"00"$0 - 2# A # <#- 5 35$&&"&& 9"39 9& "93 '5"'9 "9 & "&003"9 & "&9"90 & "&0 &"& 33"903"' 0"& - 2# A # <#- 5 $5&&&"&& 9"39 9& "93 '5 "33 9"00&"&00'& "3 & "&3"0&"&0 &"& 33"9$0'& "9 0"0$- 2# A # <#- 5 $50&&"&& 9"39 9& "93 '530"$ 9"' &"&00'"$3 & "&3"& & "&0 &"& 33"30'"& 0" - 2# A # <#- 5 $5&&"&& 9"39 9& "93 '5& "9& 9"$9 & "&00' "3 & "&$"&' &"&0 &"& 33"30' "9 0"'3 - 2 # A # <#- 5 $5&&"&& 9"39 9& "93 '5& "003"'& & "&00'9"$ &"&$"'3 & "&0 &"& 33"3$0'9"9 0" - 2# A # <#- 5 $5'&&"&& 9"39 9& "93 '5 '" 3"3' & "&00'$"3$ & "&$"$ & "&0 &"& 33"$0'$"$9 0"99 - 2# A # <#- 5 $5&&"&& 9"39 9& "93 '593"$ $"9 & "&00"& & "&& "9 & "&0 &"& 33"$0"9 0"$0 - 2# A # <#- 5 $50'"0 9 "39 9& "93 '53"'& $"9& & "&00'"& &"&& "30 & "&0 &"& 33"$30'"3 09"& - 2# A # <#- 5 $5&&"&& 9"39 9& "93 '5'& "' $"9& & "&00'"& &"&& "30 & "&0 &"& 33"$30'"3 09"& - 2# A # <#- 5 $59&&"&& 9"39 9& "93 '5'9"9 & "0'&"&00"30 & "&0" & "&0 &"& 3$"&&0"33 09"0 - 2# A # <#- 5 $53&&"&& 9"39 9& "93 '5' "0&"9 &"&00$"00&"&0"9& & "&0 &"& 3$"&0$"0$09" - 2# A # <#- 5 $5$&&"&& 9"39 9& "93 '5'9"9 0"&0 &"&000"' & "&"0'&"&0 &"& 3$"&00"'$ 09"0 - 2# A # <#- 5 0&5&&&"&& 9"39 9& "93 '5&&"$3 0"'' & "&00"9 & "&"$ &"&0 &"& 3$"&30"3& 09" - 2# A # <#- 5 0&50&&"&& 9"39 9& "93 '5"$ 0"39 & "&00"& &"&"& &"&0 &"& 3$"0&0"0&09"30 - 2 # A # <#- 5 0&5&&"&& 9"39 9& "93 '5'$"3& "0 & "&003"' & "&"'9 & "&0 &"& 3$"003"'& 09"$ - 2# A # <#- 5 0&5&&"&& 9"39 9& "93 '59'"0 "9' & "&009& "' & "&"$ & "&0 &"& 3$"009& "90 03"00- 2# A # <#- 5 0&5'&&"&& 9"39 9& "93 '5$3" "03&"&009"$ & "&'" & "&0 &"& 3$"0909"& 03"9 - 2# A # <#- 5 0&5&&"&& 9"39 9& "93 '5"& "0 & "&009 " & "&'"30 & "&0 &"& 3$"0$09 " 03"' - 2 # A # <#- 5 0&50"& 9"39 9& "93 '5 "'$ "3' & "&009"' & "& "&' &"&0 &"& 3$"009"& 03"& - 2# A # <#- 5 0&5&&"&& 9"3 9"$ '5'9"' '"& &"&0099"3 & "& " & "&0 &"& 3$"099" 03"3 - 2# A # <#- 5 0&59&&"&& 9"3 9 "3 '590"$ '"'3 & "&0093"$ & "&"0&&"&0 &"& 3$"309$"$' 03"9 - 2# A # <#- 5 0&53&&"&& 9"3 93"'3 '5$"$ '"$ & "&009$"$$ & "&"$$ & "&0 &"& 3$"303" 03"3$ - 2 # A # <#- 5 0&5$&&"&& 9"$0 30"9 '59& "9$ " & "&003& "' &"&3"&& &"&0 &"& 3$"003'"9 0$"& - 2# A # <#- 5 005&&&"&& 9"& 0 3'" '59' "& "9$ & "&003& "9 &"&$"00&"&0 &"& 3$"303"3 0$" - 2# A # <#- 5 0050&&"&& 9"039"9 '59$"0 " & "&003& "&3 &"&'& "3 & "&0 &"& 3$"3$03$"0&0$"3 - 2# A # <#- 5 005&&"& & 9" $& "3 '59$"$0 " & "&009$"&9 &"&'0"& &"&0 &"& $&"00$0"& 0$" - 2# A # <#- 5 005&&"& & 9" ' $"$0 '530" 9"&$ &"&0099" &"&'"9 & "&0 &"& $&"30$"' 0$"90 - 2# A # <#- 5 005'&&"& & 9"3& $"$3 '53$"' 9" &"&009 "0 &"&'"$' & "&0 &"& $&"90$ " 0$"39 - 2 # A # <#- 5 005&&"& & 99"&$ &&"& '53"& 9"$ & "&009"$ & "&' "00&"&0 &"& $&"$30$9"9 &"&' - 2# A # <#- 5 005&&"&& 99"'0 & "00'533'"&$ 3"'& & "&00$"$0 & "&'"& & "&0 &"& $0"00$$"0 &"& - 2# A # <#- 5 0059&&"& & 99"99 & "0'5$& "3 3"3 & "&00" & "&'9"& & "&0 &"& $0"& 0"9 & "9 - 2# A # <#- 5 * $ " + # ! ,# "#"$%& "'& ( -./+ #! ) * 0# "#"$%& "'& ( /+ #! + # , 1 + # 2 # -. . ) "# 2 3 # / 0/ 4#5 "&&1. /3#2,0 + < 4 " " / '+( '+( = '+( > , ';( ';( * '+( = '+( . '+( = '+( 4 " += '+( , $, , $,0 '+( '+( > , ';( - "3 . / '+( 0053&&"&& 93"09&$"& '5$"' $"9 & "&00"' & "&'3"&$ &"&0 &"& $"&& "0'&" - 2# A # <#- 5 005$&&"&& 93"$ 0" '5$'" 3 $"90 & "&009"3' & "&'3"3' & "&0 &"& $"'&& '"30 & "9 - 2# A # <#- 5 05&&&"& & 9$"& 0" '5$ "$9 '& "0'&"&00"3$ & "&'$"' & "&0 &"& $"93& "3 & "$0 - 2# A # <#- 5 050&&"&& 9$"' 03" '5$3'" '&"3 &"&00'9"& &"&'$"$' & "&0 &"& $"09& 9"3 0"00- 2# A # <#- 5 05&&"&& 3&"& 0"9 5&&"3 '0"& &"&00'0"$ & "&&" & "&0 &"& $"9& $"0 0" - 2# A # <#- 5 05&&"&& 3&" $ '" 5&0$"&$ '0"' & "&00 "'3 & "&&"'' & "&0 &"& $"$90&"'9 0"' - 2# A # <#- 5 05'&&"&& 30"0 9"' 5&'"$ '0"$& & "&003"33 & "&&"'9 & "&0 &"& $'"00"0 0"93 - 2# A # <#- 5 05&&"&& 30"9 & " 5&'$"3 '" & "&000"$0 & "&&"3 & "&0 &"& $'"90" "& - 2# A # <#- 5 05&&"&& 3" "035&" '"99 & "&000'"0 & "&&"09&"&0 &"& $"0'0"3 "' - 2# A # <#- 5 059&&"&& 3"$$ "0'5& 9"'& '"0 & "&00&9"&& &"&'$"3 & "&0 &"& $"00'"'& " - 2# A # <#- 5 053&&"&& 3"' $"&$ 5& 33"&' '" & "&0$$"00&"&'$"'$ & "&0 &"& $"330"0 "&0 - 2# A # <#- 5 05$&&"& & 3'"0 '"& 5&$3" ' ''"&$ &"&0$& "$9 & "&'$"&9 &"&0 &"& $"0"9' "$ - 2# A # <#- 5 05$9"' 3'"3& ''"050&"'& ''"0 & "&03" & "&'3"' & "&0 &"& $"&09"&& 0"$ - 2@ < 5' 05&&&"& & 3'"$$ ''"$ 50&9"3 ''"0 & "&03" & "&'3"' & "&0 &"& $"&09"&& 0"$ - 2@ < 5' 05&&0"' 3 "&& '"&& 50&9"$9 ''"0 & "&03"00&"&'3"'0 & "&0 &"& $"&09"& 0"$0 - 2@ < 5' 050&&"&& 3"&& '"&& 500" 3 ''" & "&03"3$ & "&'3"' & "&0 &"& $"309"$ "9 - 2@ < 5' 05&&"&& 3"&& '"&& 50 "$ ''" & "&03"3' & "&'3"' & "&0 &"& $"3909" 9 "0'- 2@ < 5' 05& 0"' 3 "&& '"&& 50 "'& ''" & "&03"3 & "&'3"' & "&0 &"& $"3909"9 "0- 2@ < 5' 05&&"&& 3"&& '"&& 50'"& 0 ''"$ & "&03'"$' & "&'3"'3 & "&0 &"& $9"&909"3 '"' - 2 @ < 5' 05'&&"&& 3"&& '"&& 50'"9 ''" & "&03"0$&"&'3" &"&0 &"& $9"303"09 "0'- 2@ < 5' 05&&"&& 3"&& '"&& 500"'' ''"' & "&039"$ &"&'3"& & "&0 &"& $9"003"'3 3"0- 2@ < 5' 05&&"&& 3"&& '"&& 50& "0 ''"& &"&03$"0&"&'3"9 & "&0 &"& $9"903"30 & "9 - 2@ < 5' 059&&"&& 3"&& '"&& 503"39 ''"& & "&0$& "9$ & "&'3"9 & "&0 &"& $3"&&0$"0 "9$ - 2@ < 5' 053&&"&& 3"&& '"&& 5099" $ ''"90 & "&0$"9 &"&'3"3 & "&0 &"& $3"0$"0 "9 - 2@ < 5' 05$&&"&& 3"&& '"&& 503"& ''"3 & "&0$'"'9 & "&'3"$9 & "&0 &"& $3"0$"33 3"& - 2@ < 5' 0'5&&&"&& 3"&& '"&& 50$ "& ''"$ & "&0$"'3 & "&'$"0&&"&0 &"& $3"3& "9 '& "3 - 2 @ < 5' 0'50&&"&& 3"&& '"&& 5& "9 ' "00&"&0$3"$ &"&'$" & "&0 &"& $$"0& "9 '" - 2@ < 5' 0'5&&"&& 3"&& '"&& 50"' ' "3 & "&00&&"3& & "&'$"3 & "&0 &"& $$"''0"&$ '"' - 2@ < 5' 0'5& 0"' 3 "&& '"&& 50" '"3 & "&00&&"3 & "&'$"$ & "&0 &"& $$"''0"&$ '"3 - 2@ < 5' 0'5&&"&& 3"'$ ' "& 5& "9' ' "' & "&00&"$ & "&'3"$& & "&0 &"& $$"990" '$"'9 - 2 @ < 5' 0'5'&&"&& 3"$$ ' "0053"09'"' & "&00&"0'&"&'3"' & "&0 &"& 0&&"000"$9 "' - 2 @ < 5' 0'5&&"&& 3"'3 ' "095'"9' ''"99 & "&033"0'&"&'9"&3 &"&0 &"& $9"003"& 0"$9 - 2# A # <#-'5' 0'5&&"&& 3"$3 ' " 5'& "'' ''"3' & "&033" & "&'"' & "&0 &"& $9"&03" "0&- 2# A # <#-'5' 0'59&&"&& 39"'3 ' "$ 5' "9 ''"$ & "&03$"0$&"&'"9 & "&0 &"& $9"$03"9 '" - 2# A # <#-'5' 0'53&&"&& 39"$9 ' "' 5'$"' ' "&& &"&03$"9 & "&' "$ & "&0 &"& $9"9303"39 "' - 2 # A # <#-'5' 0'5$&&"& & 33"'9 ' "'& 5 "' ' "&$ &"&0$& "' & "&' "90 & "&0 &"& $9"330$"&& "9 - 2# A # <#-'5' 05&&&"& & 33"$9 ' "' 5 '"3 '"03&"&0$& "$ & "&' " &"&0 &"& $9"$30$"0 9"$& - 2# A # <#-'5' 050&&"&& 3$"' ' "0 5"$' ' "3 & "&0$0"& & "&' "' & "&0 &"& $3"&$0$"9 $"0- 2# A # <#-'5' 05&&"&& 3$"$ ' "9 5 "' ' "3 & "&0$"9 & "&' "$ & "&0 &"& $3"0$0$"'& '& "' - 2 # A # <#-'5' 053'"& $& "3 ' " 5 "0$'"' & "&0$"3 & "&' "'0 & "&0 &"& $3"30$" '0"& - 2# A # <#-'5' 05&&"&& $&"3 ' " 5 "&$ '"'3 & "&0$"$$ & "&' "' & "&0 &"& $3"&0$"' '0"9& - 2# A # <#-'5' 05'&&"&& $&"3 ' " 5"' ' "$ &"&0$"3$ & "&' " &"&0 &"& $3"'00$"3 '"&& - 2# A # <#-'5' 05&&"&& $&"3 ' " 5 '"9 ' "9& & "&0$'"3& & "&' "' & "&0 &"& $3"0$"3 ''"0 - 2# A # <#-'5' 05&&"&& $&"3 ' " 5 '"0&'"3 & "&0$ "9 & "&' "9 & "&0 &"& $3"'0$"$9 ' " - 2# A # <#-'5' 059&&"&& $&"3 ' " 5 "'' ' "$' & "&0$"$ & "&' "33 & "&0 &"& $3"9& "0'"$ - 2# A # <#-'5' 053&&"&& $&"3 ' " 5 "99 '"& &"&0$9" & "&'"&0 &"&0 &"& $3"33& "9 '3"& - 2# A # <#-'5' 05$&&"&& $&"3 ' " 5 "00'"0$&"&0$3" & "&'"0'&"&0 &"& $$"&0& "' '$"' - 2# A # <#-'5' 05&&&"&& $&"3 ' " 5 0"' '" & "&0$$"9 & "&'"9 & "&0 &"& $$"0'& "3 0"&& - 2# A # <#-'5' 050&&"&& $&"3 ' " 5 & "93 '"' & "&00&&"9& & "&'"'0 & "&0 &"& $$"9& "9' " - 2# A # <#-'5' 05&&"&& $&"3 ' " 5 & "0'"0 & "&00&0"9 & "&'" &"&0 &"& $$"'&& "$0 "9 - 2# A # <#-'5' 05&&"&& $&"3 ' " 5'$"' '"9 & "&00&"30 & "&'"$ & "&0 &"& $$"'0"&9 "&$ - 2# A # <#-'5' 05'&&"&& $&"3 ' " 5'3"3& '"$& & "&00&"3$ & "&'"3' & "&0 &"& $$"30"' "' - 2 # A # <#-'5' 05&&"&& $&"3 ' " 5'3"0'9"& &"&00&'"$3 & "&'9"&& &"&0 &"& $$"30"'0 9"3 - 2 # A # <#-'5' 05&&"&& $&"3 ' " 5'9"'9 '9"0 & "&00&"0&&"&'9"0&"&0 &"& $$"$90"$ $"0 - 2# A # <#-'5' * $ " + # ! ,# "#"$%& "'& ( -./+ #! ) * 0# "#"$%& "'& ( /+ #! + # , 1 + # 2 # -. . ) "# 2 3 # / 0/ 4#5 "&&1. /3#2,0 + < 4 " " / '+( '+( = '+( > , ';( ';( * '+( = '+( . 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State of Alaska mail system. Do not click links or open attachments unless you recognize the sender and know the content is safe. From:Smith, Matt To:Loepp, Victoria T (OGC) Cc:Hobbs, Greg S Subject:RE: [EXTERNAL]KRU 3S-625 Cement Calc detail Date:Monday, July 11, 2022 3:39:47 PM Attachments:3S-625 Detailed Cement Calcs and KT.docx Hi Victoria, please find attached document with cement volume details as well as Kick Tolerance calculation. At our minimum LOT of 11.5ppg, we maintain ~31 bbl kick tolerance, which is ConocoPhillips recommended kick tolerance for development wells around this hole size. I also wanted to mention, since submitting this we have discussed our intermediate cement job and have elected to go with a 15.3ppg system instead of the 15.8ppg system as noted in the permit. The 15.3ppg pilot lab tests show good results compared to the 15.8ppg and it gives us some additional flexibility in terms of ECD’s while circulating, to ensure we don’t induce any losses and get a good cement top above the Coyote interval during the job. We have had good success with the 15.8ppg previously, but with this being one of the longer intermediate sections on the pad, we wanted to give ourselves a little extra room to operate, and do not see a detriment in going with the slightly lighter slurry. Thank you, Matt Smith Drilling Engineer – Alaska Kuparuk 700 G ST ANCHORAGE ALASKA, ATO-1704 OFFICE: +1.907.263.4324 CELL: +1.432.269.6432 MATT.SMITH2@COP.COM From: Loepp, Victoria T (OGC) <victoria.loepp@alaska.gov> Sent: Friday, July 08, 2022 10:04 AM To: Smith, Matt <Matt.Smith2@conocophillips.com> Cc: Hobbs, Greg S <Greg.S.Hobbs@conocophillips.com> Subject: [EXTERNAL]KRU 3S-625 Cement Calc detail CAUTION:This email originated from outside of the organization. Do not click links or open attachments unless you recognize the sender and know the content is safe. Matt, Please provide the level of detail in cement calculations as outlined in the attached table. Also, please provide kick tolerance calculations for the SC shoe. Thanx, Victoria Victoria Loepp Senior Petroleum Engineer State of Alaska Oil & Gas Conservation Commission 333 W. 7th Ave Anchorage, AK 99501 Work: (907)793-1247 Victoria.Loepp@alaska.gov CONFIDENTIALITY NOTICE:This e-mail message, including any attachments, contains information from the Alaska Oil and Gas Conservation Commission (AOGCC), State of Alaska and is for the sole use of the intended recipient(s). It may contain confidential and/or privileged information. The unauthorized review, use or disclosure of such information may violate state or federal law. If you are an unintended recipient of this e-mail, please delete it, without first saving or forwarding it, and, so that the AOGCC is aware of the mistake in sending it to you, contact Victoria Loepp at (907)793-1247 or Victoria.Loepp@alaska.gov 10-3/4” Surface Casing Cement Job 10.7 ppg Surface Lead Slurry from 2,245’ MD to surface Conductor (119’ – 0’) x 0.243 bbl/ft x 1.0 (0% excess) = 28.9 bbls Base of Permafrost to Conductor (1,784’ – 119’) x 0.0648 bbl/ft x 3.50 (250% excess) = 377.6 bbls Top of Tail to Base of Permafrost (2,245’ – 1,784’) x 0.0648 bbl/ft x 1.50 (50% excess) = 48.6 bbls Total Volume = 455.1 bbls = 2,555 ft 3 =>887 sx of 10.7 ppg Lead @ 2.88 ft 3 /sk 15.8 ppg Surface Tail slurry from 2,745’ MD to 2,245 MD Shoe to Top of Tail (2,745’ – 2,245’) x 0.0648 bbl/ft x 1.50 (50% excess) = 48.6 bbls Shoe Track (80’) x 0.0962 bbl/ft x 1.0 (0% excess) = 7.7 bbls Total Volume = 56.3 bbls = 316 ft3 =>280 sx of 15.8 ppg Tail @ 1.16 ft 3/sk 7-5/8” Intermediate Casing Cement Job Slurry from 12,967 MD to 7,435’ MD (3,875’ TVD) with 15.3 ppg Class G + additives (250’ TVD above Coyote) Shoe to Top of Cement (12,967’ – 7,435’) X 0.0383 bbl/ft X 1.4 (40% excess) = 296.6 bbls Shoe Joint (80’) X 0.0444 bbl//ft X 1.0 (0% excess) = 3.6 bbls Total Volume = 300.2 bbls = 1683 ft 3 => 1370 sx of 15.3 ppg Class G @ 1.23 ft 3/sk Kick Tolerance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ompanyConocoPhillips Alaska, Inc.Well Name:KUPARUK RIV UNIT 3S-625Initial Class/TypeSER / PENDGeoArea890Unit11160On/Off ShoreOnProgramSERField & PoolWell bore segAnnular DisposalPTD#:2220790KUPARUK RIVER, TOROK OIL - 490169NA1Permit fee attachedYes2Lease number appropriateYes3Unique well name and numberYes4Well located in a defined poolYes5Well located proper distance from drilling unit boundaryYes6Well located proper distance from other wellsYes7Sufficient acreage available in drilling unitYesDirectional plan view included, no land plat.8If deviated, is wellbore plat includedYes9Operator only affected partyYes10Operator has appropriate bond in forceNo11Permit can be issued without conservation orderYes12Permit can be issued without administrative approvalYes13Can permit be approved before 15-day waitYesAIO No. 2C14Well located within area and strata authorized by Injection Order # (put IO# in comments) (ForYes15All wells within 1/4 mile area of review identified (For service well only)Yes3S-625 will be pre-produced for approximately 2 weeks to clean up the wellbore.16Pre-produced injector: duration of pre-production less than 3 months (For service well only)NA17Nonconven. gas conforms to AS31.05.030(j.1.A),(j.2.A-D)Yes59.6' conductor provided18Conductor string providedYesSet to 2745' MD19Surface casing protects all known USDWsYes187% excess20CMT vol adequate to circulate on conductor & surf csgNo21CMT vol adequate to tie-in long string to surf csgNoProductive interval will be completed with uncemented frac sleeves and swell packers22CMT will cover all known productive horizonsYes23Casing designs adequate for C, T, B & permafrostYesRig has steel tanks; all wsste to approved disposal wells24Adequate tankage or reserve pitNA25If a re-drill, has a 10-403 for abandonment been approvedYesAnti-collision analysis complete; no major risk failures26Adequate wellbore separation proposedYes27If diverter required, does it meet regulationsYesMax formation pressure is 2543 psig(9.4 ppg EMW); will drill w/ 9-10.5 ppg EMW28Drilling fluid program schematic & equip list adequateYes29BOPEs, do they meet regulationYesMPSP is 2024 psig; will test BOPs to 3500 psig30BOPE press rating appropriate; test to (put psig in comments)Yes31Choke manifold complies w/API RP-53 (May 84)Yes32Work will occur without operation shutdownYesH2S measures required33Is presence of H2S gas probableNANuna plug back34Mechanical condition of wells within AOR verified (For service well only)NoH2S is present in reservoir, measures required. Well 3S-620 measured 60 ppm H2S on 12/15/17.35Permit can be issued w/o hydrogen sulfide measuresYes36Data presented on potential overpressure zonesNA37Seismic analysis of shallow gas zonesNA38Seabed condition survey (if off-shore)NA39Contact name/phone for weekly progress reports [exploratory only]ApprDLBDate6/20/2022ApprVTLDate7/13/2022ApprDLBDate6/20/2022AdministrationEngineeringGeologyGeologic Commissioner:Date:Engineering Commissioner:DatePublic CommissionerDateJLC 7/18/2022
