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Page 1

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Engineer :

Dataset : 4225535696_20191026.snp

Title : SAMPLE

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Important Note: Review page 3 of this report for actual and potential problems.

Solution Rate: 2586 mscf/ Pvc Bottom Bellows: 615

GL Design Press: 786 Solution fbhp: 1002 psia Operating Pressure: 862

Wellhead Pressure: 183 Flwg Wh Temp (Twh): 120 Casing DP: 142

SNAP IPR function Top Valve Flwg Temp: 120 Orifice DP: 147

Static BHP(Pws): 6100 Static BH Temp: 160 KO Gas Gradient : 0.0228

SNAP 2.699 11/11/2019 Tubing Size: 1.995 Operating Gas Grd: 0.0243

11/12/19 11:46:43 Design GL Rate: 1000 Watercut: 63.9 %

Model: HagedornBrown Unloading Gradient: 0.433 Liquid Yield: 229

Design QO: 214 stbf/d Design QW: 378 stbf/d Design QFmGas:2586 mscf/d

Rn Sta Depth Depth Valve Valve Valve Port Valve Valve Flwg

Or # TVD MD OD Type Model Size Ap/Ab Ppef Tmp

12 1 1961 1961 1.0 Bellows Camco_BK 0.2500 0.7000 0.1976 120

11 2 2941 2941 1.0 Bellows Camco_BK 0.2500 0.7000 0.1976 120

10 3 3663 3663 1.0 Bellows Camco_BK 0.2500 0.7000 0.1976 120

9 4 4287 4287 1.0 Bellows Camco_BK 0.2500 0.7000 0.1976 120

8 5 4939 4939 1.0 Bellows Camco_BK 0.2500 0.7000 0.1976 120

7 6 5590 5591 1.0 Bellows Camco_BK 0.2500 0.7000 0.1976 120

6 7 6242 6245 1.0 Orifice Camco_BK 0.3125 0.0000 0.0000 120

5 8 6889 6902 1.0 Dummy 120

4 9 7529 7559 1.0 Dummy 120

3 10 8164 8214 1.0 Dummy 120

2 11 8816 8871 1.0 Dummy 120

1 12 9460 9523 1.0 Orifice Camco_BK 0.2500 0.0000 0.0000 120

Rn Sta Ppd Pwf Qg* TGLR Qgi(req) Qgi(VPC) Qgi(ThH) Qgi(Wnk) Ptro60 Ptro

Or # Prs psia mscf/d scf/b mscf mscf mscf mscf calc Instld

12 1 305 1604 2499 200 0 0 920 0 798 1215

11 2 375 1575 2504 200 0 0 951 0 808 1205

10 3 429 1506 2516 200 0 0 978 0 805 1190

9 4 479 1394 2534 200 0 0 994 0 799 1175

8 5 532 1289 2550 200 0 0 1015 0 793 1165

7 6 587 1180 2565 200 0 0 1036 0 788 1150

6 7 643 1002 2586 200 0 1 1612 1973

5 8 700 Dummy

4 9 758 Dummy

3 10 817 Dummy

2 11 879 Dummy

1 12 941 1002 2586 1000 1000 999 951 1067

Rn Sta Pgd GLD GLD GLD Pvc Ppd-Pmin

Or # Prs Piod Pvcd PpTran Ct Pio Psc DP psia

12 1 831 831 752 353 0.886 788 715 20 48

11 2 853 822 762 461 0.886 754 695 20 87

10 3 870 810 759 498 0.886 727 675 20 68

9 4 884 807 753 481 0.886 709 655 20 2

8 5 899 801 748 476 0.886 689 635 20 -56

7 6 914 796 743 470 0.886 669 615 20 -116

6 7 929 667 -1230

5 8 944 Dummy

4 9 958 Dummy

3 10 973 Dummy

2 11 988 Dummy

1 12 1002 1088 147

* Qliq values represent the minimum liquid rate that occurs during KO

as gas begins to push around the next valve downhole.

Page 2

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WARNING 1:Tubing Prs is not 100 psi less than PTMin at Station 1

PROBLEM: You will not be able to transfer to the next lower station

SOLUTION: Either move the next lower valve up, or increase KO pressure

WARNING 2:Tubing Prs is not 100 psi less than PTMin at Station 3

PROBLEM: You will not be able to transfer to the next lower station

SOLUTION: Either move the next lower valve up, or increase KO pressure