Surge Force Calculation

Line number

Area

System

Fluid density

Fluid properties Fluid bulk Upstream Steady modulus static state fluid pressure velocity

N/m2 K 1.55E+09 1.55E+09

Pa P1 4.31E+06 4.31E+06

m/s v 1.41 2.01

N/m2 Eml 2.00E+11 2.00E+11

inch Dext 30 18

mm Dext 762 457.2

mm T 16 12.7

Young's modulus of main pipe

Main pipe properties Outside diameter of Pipe wall Schedule pipe thickness 40 pipe (actual) wall thickness

Actual length of pipeline

Length of pipeline between changes in direction

Sonic velocity

Maximum Maximum surge out-ofpressure balance force

Actual valve closure time

mm T40 17.48 14.27

m L 2400 700

m Lup 250 250

m/s C 1350 1350

Pa Pmax 1.62E+06 2.31E+06

kN Fmax 677.3 337.8

sec Tsud 3.6 1.0

sec Tclose 7.5 7.5

Valve type and characteristic Full bore Reduced Butterfly Globe ball bore ball

Gate

Selected valve characteri stic

Valve factor

Peak Maximum outsurge of-balance pressure force (inc valve characteristic)

Calculation of limit force Selected Wall Limit support thickness/ force stiffness schedule 40 wall

IP-P-201/211-0647 IP-P-010/211-0003

AVU AVU

Crude feed to AVU Crude feed to AVU

kg/m3 ρ 850 850

IP-P-010/211-0023 IP-P-030/211-0313

AVU

Vacuum residue to DCU

993

1.55E+09

3.69E+06

1.10

2.00E+11

18

457.2

14.27

14.27

601.7

250

1249

1.36E+06

196.9

1.0

7.5

-0.4408

-0.62213 -0.76967 -0.62213

-4.60E-02

1.74E+05

25.1

4

1.0

149

IP-P-010/211-0022 IP-P-203/211-0659

AVU AVU

Vacuum residue to storage

993 993

1.55E+09 1.55E+09

3.69E+06 3.69E+06

1.73 3.14

2.00E+11 2.00E+11

14 14

355.6 355.6

12.7 12.7

11.1252 11.12

1537.8 220

250 220

1249 1249

2.15E+06 3.90E+06

183.8 333.6

2.5 0.4

13.5 13.5

-0.36489 -0.45593 -0.48811 -0.48785 -0.56759 -0.48785 -0.36489 -0.45593 -0.48811 -0.48785 -0.56759 -0.48785

-5.68E-02 -9.07E-02

2.16E+05 3.50E+05

18.5 30.0

4 4

1.1 1.1

79 79

IP-P-010/211-0010 IP-P-211/203-0722

AVU AVU AVU

Kerosene product to storage

759.3 759.3 759.3

9.97E+08 9.97E+08 9.97E+08

2.16E+06 2.16E+06 2.16E+06

1.47 2.55 1.88

2.00E+11 2.00E+11 2.00E+11

8.625 6.625 18

219.075 168.275 457.2

8.13 7.11 12.7

8.13 7.11 14.27

2233 342.1 220

250 250 220

1146 1146 1146

1.28E+06 2.22E+06 1.64E+06

41.3 41.4 239.5

3.9 0.6 0.4

20 20 20

-0.33405 -0.33405 -0.33405

-0.4333 -0.4333 -0.4333

-5.60E-02 -9.71E-02 -6.30E-02

1.24E+05 2.20E+05 1.40E+05

4.0 4.1 20.6

4 4 4

1.0 1.0 0.9

16 7 135

IP-P-010/211-0009 IP-P-211/013-0102

AVU

AGO/Kerosene product to DHDT

778.9

9.97E+08

2.74E+06

2.23

2.00E+11

12.75

323.85

10.41

10.41

550

250

1131

1.96E+06

141.7

1.0

9

-0.41233 -0.50289 -0.59467 -0.57178 -0.69389 -0.57178

-9.05E-02

2.60E+05

18.7

4

1.0

53

IP-P-010/211-0008 IP-P-203/211-0725

AVU AVU

AGO/Kerosene product to storage

792.8 792.8

1.55E+09 1.55E+09

2.74E+06 2.74E+06

2.55 1.88

2.00E+11 2.00E+11

10.75 18

273.05 457.2

9.4 12.7

9.27 14.27

2255 220

250 220

1398 1398

2.83E+06 2.08E+06

143.5 305.1

3.2 0.3

41.25 41.25

-0.30105 -0.39274 -0.34475 -0.37493 -0.39767 -0.37493 -0.30105 -0.39274 -0.34475 -0.37493 -0.39767 -0.37493

-6.91E-02 -4.48E-02

1.96E+05 1.26E+05

10.0 18.4

4 4

1.0 0.9

32 135

IP-P-010/211-0012 IP-P-205T/211-0778

AVU AVU

Stabilised naphtha from AVU to naphtha export tank

692.3 692.3

9.77E+08 9.77E+08

1.34E+06 1.34E+06

1.80 0.86

2.00E+11 2.00E+11

12.75 28

323.85 711.2

9.65 16

10.41 17.48

3410 220

250 220

1188 1188

1.48E+06 7.07E+05

107.8 256.2

5.7 0.4

45 45

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036 -0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036

-8.64E-02 -3.63E-02

1.20E+05 4.94E+04

8.8 17.9

4 4

0.9 0.9

49 533

-0.4408 -0.4408

Valve characteristic φ φ -0.53107 -0.6586 -0.62213 -0.76967 -0.62213 -0.53107 -0.6586 -0.62213 -0.76967 -0.62213

Ω -4.32E-02 -6.17E-02

Pa Psurge 1.90E+05 2.74E+05

kN Fmax 79.7 40.1

-0.53107

-0.4254 -0.4254 -0.4254

-0.6586

-0.41885 -0.41885 -0.41885

-0.4333 -0.4333 -0.4333

-0.4855 -0.4855 -0.4855

4 4

ψ 0.9 0.9

kN Flim 660 135

Line number

IP-P-010/211-0014/ IPP-024/211-0227

Area

AVU

System

Fluid density

Fluid properties Fluid bulk Upstream Steady modulus static state fluid pressure velocity

Young's modulus of main pipe

Main pipe properties Outside diameter of Pipe wall Schedule pipe thickness 40 pipe (actual) wall thickness inch mm mm mm Dext Dext T T40

Actual length of pipeline

Sonic velocity

m L

Length of pipeline between changes in m Lup

m/s C

Maximum Maximum surge out-ofpressure balance force Pa kN Pmax Fmax

Valve type and characteristic Full bore Reduced Butterfly Globe ball bore ball

sec Tsud

6.2

1.7

0.5

3.21E+05

6.0

4

1.0

7

6.2 235.4

2.1 0.3

4.5 4.5

-0.55467 -0.64378 -0.91433 -0.82356 -1.07278 -0.82356 -0.55467 -0.64378 -0.91433 -0.82356 -1.07278 -0.82356

-4.87E-02 -7.15E-01

1.20E+05 2.44E+06

1.0 45.5

4 4

1.0 1.0

2 7

9.39E+05

7.7

3.3

7.5

-0.4408

-0.53107

-0.6586

-0.62213 -0.76967 -0.62213

-4.07E-02

1.03E+05

0.8

4

1.0

2

3.09E+06

274.8

0.3

7.5

-0.4408

-0.53107

-0.6586

-0.62213 -0.76967 -0.62213

-1.18E-01

3.11E+05

27.6

4

1.0

72

kg/m3 ρ

N/m2 K

Pa P1

m/s v

N/m2 Eml

C4 from AVU to alkylation unit

552.3

9.77E+08

2.41E+06

0.45

2.00E+11

6.625

168.275

7.11

7.11

1100

250

1330

3.31E+05

553 553

9.77E+08 9.77E+08

2.41E+06 2.41E+06

1.03 17.18

2.00E+11 2.00E+11

4.5 6.625

114.3 168.275

6.1 7.11

6.1 7.11

1386 220

250 220

1329 1329

7.57E+05 1.26E+07

467

9.77E+08

2.48E+06

1.39

2.00E+11

4.5

114.3

6.1

6.1

2394

250

1446

467

9.77E+08

2.48E+06

4.58

2.00E+11

14

355.6

9.65

9.525

220

220

1446

Gate

Selected valve characteri stic φ

Ω

-7.135

-4.852

-1.25E-01

Valve characteristic φ -2.832

-2.898

-6.029

-4.852

Valve factor

Peak Maximum outsurge of-balance pressure force (inc valve characteristic) Pa kN Psurge Fmax

Calculation of limit force Selected Wall Limit support thickness/ force stiffness schedule 40 wall kN ψ Flim

Actual valve closure time sec Tclose

IP-P-010/211-0014/ IPP-024/211-0227

AVU

C4 from AVU to blending

IP-P-010/211-0016/ IPP-204/211-0734 or IPP-205/211-0757

AVU

C4 from AVU to LPG bullets/ LPG STG (U205)

IP-P-010/211-0017/ IPP-204/211-xxxx

AVU

C3 LPG from AVU to blending

466 466

9.77E+08 9.77E+08

2.48E+06 2.48E+06

0.64 17.18

2.00E+11 2.00E+11

3.5 6.625

88.9 168.275

5.59 7.11

5.74 7.11

1617 220

250 220

1448 1448

4.32E+05 1.16E+07

2.0 216.1

2.2 0.3

1.5 1.5

-1.124 -1.124

-1.20733 -1.20733

-2.193 -2.193

-1.83067 -2.58833 -1.83067 -1.83067 -2.58833 -1.83067

-5.50E-02 -1.30E+00

1.40E+05 5.94E+06

0.7 110.7

4 4

1.0 1.0

1 7

IP-P-010/211-0018 IP-P-080/211-0508

AVU AVU AVU

Sour water from AVU to SWS

988.3 988.3 988.3

9.77E+08 9.77E+08 9.77E+08

1.51E+06 1.51E+06 1.51E+06

1.70 1.97 1.73

2.00E+11 2.00E+11 2.00E+11

12.75 10.75 12.75

323.85 273.05 323.85

17.526 15 17.526

10.41 9.27 10.41

649 363 209

250 250 209

994 994 994

1.67E+06 1.94E+06 1.70E+06

109.4 89.8 111.4

1.3 0.7 0.4

7.5 7.5 7.5

-0.4408 -0.4408 -0.4408

-0.53107 -0.53107 -0.53107

-0.6586 -0.6586 -0.6586

-0.62213 -0.76967 -0.62213 -0.62213 -0.76967 -0.62213 -0.62213 -0.76967 -0.62213

-1.73E-01 -2.01E-01 -1.47E-01

2.85E+05 3.35E+05 2.39E+05

18.7 15.5 15.7

4 4 4

1.7 1.6 1.7

84 48 84

IP-P-010/211-0020 IP-P-020/211-0665

AVU AVU

VGO from AVU to VGO HDT storage

868.4 868.4

1.55E+09 1.55E+09

2.84E+06 2.84E+06

2.39 2.04

2.00E+11 2.00E+11

12.75 20

323.85 508

10.41 14.97

10.41 10.41

1958 220

250 220

1336 1336

2.77E+06 2.37E+06

200.0 424.8

2.9 0.3

33.75 33.75

-0.30796 -0.39957 -0.36024 -0.38714 -0.41604 -0.38714 -0.30796 -0.39957 -0.36024 -0.38714 -0.41604 -0.38714

-7.08E-02 -5.32E-02

2.08E+05 1.55E+05

15.0 27.8

4 4

1.0 1.4

53 301

IP-P-010/211-0021 IP-P-203/211-0723

AVU AVU

VAC diesel from AVU to DHDT feed tank

810.7 810.7

1.55E+09 1.55E+09

2.43E+06 2.43E+06

1.09 1.88

2.00E+11 2.00E+11

6.625 18

168.275 457.2

7.11 12.7

7.11 14.27

2240 220

250 220

1383 1383

1.22E+06 2.11E+06

22.8 308.6

3.2 0.3

15 15

-0.3554 -0.3554

-4.28E-02 -6.50E-02

1.06E+05 1.63E+05

2.0 23.9

4 4

1.0 0.9

7 135

-0.44653 -0.44653

-0.4668 -0.4668

-0.47107 -0.54233 -0.47107 -0.47107 -0.54233 -0.47107

Line number

IP-P-203/211-0658/ IPP-040/211-0362 IP-P-030/211-0323/ IPP-040/211-0356 IP-P-040/211-0368 IP-P-081/211-0541

Area

System

Fluid density

Fluid properties Fluid bulk Upstream Steady modulus static state fluid pressure velocity

Young's modulus of main pipe

kg/m3 ρ

N/m2 K

Pa P1

m/s v

N/m2 Eml

Main pipe properties Outside diameter of Pipe wall Schedule pipe thickness 40 pipe (actual) wall thickness inch mm mm mm Dext Dext T T40

Actual length of pipeline

Sonic velocity

m L

Length of pipeline between changes in m Lup

m/s C

Maximum Maximum surge out-ofpressure balance force Pa kN Pmax Fmax

sec Tsud

Actual valve closure time sec Tclose

Valve type and characteristic Full bore Reduced Butterfly Globe ball bore ball

Gate

Valve characteristic φ

NHT

Naphtha from storage to NHT unit

712

9.97E+08

1.81E+06

2.09

2.00E+11

14

355.6

9.65

9.525

1387

250

1183

1.76E+06

156.4

2.3

3

-0.697

-0.78467

-1.234

NHT

Naphtha feed line from DCU to NHT unit

623

9.77E+08

1.85E+06

1.22

2.00E+11

4.5

114.3

6.1

6.1

1004

250

1252

9.52E+05

7.8

1.6

1

-1.551

-1.63

-3.152

NHT

Sour water from NHT unit to SWS

985.7 985.7 985.7

9.77E+08 9.77E+08 9.77E+08

4.58E+06 4.58E+06 4.58E+06

0.98 0.88 1.39

2.00E+11 2.00E+11 2.00E+11

12.75 12.75 3.5

323.85 323.85 88.9

17.526 17.526 7.62

10.41 10.41 5.74

847 748 132

250 250 132

996 996 996

9.62E+05 8.64E+05 1.36E+06

63.0 56.6 5.8

1.7 1.5 0.3

0.6 0.6 0.6

-2.405 -2.405 -2.405

-2.47533 -2.47533 -2.47533

-5.07 -5.07 -5.07

Selected valve characteri stic φ

-1.07533 -1.45167 -1.07533 -2.586

-3.725

-2.586

-4.09667 -5.99833 -4.09667 -4.09667 -5.99833 -4.09667 -4.09667 -5.99833 -4.09667

Valve factor

Ω

Peak Maximum outsurge of-balance pressure force (inc valve characteristic) Pa kN Psurge Fmax

Calculation of limit force Selected Wall Limit support thickness/ force stiffness schedule 40 wall kN ψ Flim

-2.21E-01

4.47E+05

39.7

4

1.0

72

-2.66E-01

5.61E+05

4.6

4

1.0

2

-2.16E-01 -1.94E-01 -1.62E-01

1.10E+06 9.79E+05 8.03E+05

72.2 64.1 3.4

4 4 4

1.7 1.7 1.3

84 84 1

NFU Line number

Area

System

Fluid density

Fluid properties Fluid bulk Upstream Steady modulus static state fluid pressure velocity N/m2 K 9.77E+08 9.77E+08

Pa P1 1.71E+06 1.71E+06

m/s v 1.89 3.62

N/m2 Eml 2.00E+11 2.00E+11

Young's modulus of main pipe

Main pipe properties Outside diameter of Pipe wall Schedule pipe thickness 40 pipe (actual) wall thickness inch mm mm mm Dext Dext T T40 6.625 168.275 7.11 7.11 6.625 168.275 7.11 7.11

Actual length of pipeline

Sonic velocity

m L 2128 220

Length of pipeline between changes in m Lup 250 220

m/s C 1226 1226

Maximum Maximum surge out-ofpressure balance force Pa kN Pmax Fmax 1.51E+06 28.1 2.88E+06 53.8

sec Tsud 3.5 0.4

Actual valve closure time sec Tclose 36.25 36.25

Valve type and characteristic Full bore Reduced Butterfly Globe ball bore ball

Valve characteristic φ φ -0.30534 -0.39698 -0.35437 -0.38251 -0.40907 -0.38251 -0.30534 -0.39698 -0.35437 -0.38251 -0.40907 -0.38251

Ω -6.89E-02 -1.16E-01

-0.30796 -0.39957 -0.36024 -0.38714 -0.41604 -0.38714 -0.30796 -0.39957 -0.36024 -0.38714 -0.41604 -0.38714

-5.25E-02 -3.15E-02

7.88E+04 4.68E+04

1.5 17.0

4 4

1.0 0.9

7 534

-2.74E-01 -6.91E-01

6.07E+05 1.88E+06

19.6 95.5

4 4

1.0 1.0

16 32

-1.40E-01 -7.02E-02

1.70E+05 8.28E+04

8.7 7.4

4 4

1.0 0.9

31 62

-1.83067 -2.58833 -1.83067

-1.05E-01

2.68E+05

2.2

4

1.0

2

IP-P-041/211-0397/ IPP-203/211-0670

NFU

Hydrotreated light naphtha to HGU

IP-P-041/211-2907/ IPP-203/211-0764

NFU

HDT HVY naphtha from NFU to naphtha export storage

629.3 629.3

9.77E+08 9.77E+08

1.46E+06 1.46E+06

1.26 0.86

2.00E+11 2.00E+11

6.625 28

168.275 711.2

7.11 16

7.11 17.45

3531 220

250 220

1246 1246

9.88E+05 6.74E+05

18.4 244.3

5.7 0.4

33.75 33.75

IP-P-041/211-0399/ IPP-203/211-0700

NFU

Hydrotreated naphtha from NFU to CCR feed tank

632.1 632.1

9.77E+08 9.77E+08

1.94E+06 1.94E+06

0.47 1.35

2.00E+11 2.00E+11

8.625 10.75

219.075 273.05

8.13 9.4

8.18 9.27

1192 220

250 220

1243 1243

3.69E+05 1.06E+06

11.9 53.9

1.9 0.4

0.5 0.5

CCR

Offspec reformate from CCR unit to reformate tank

817.6 817.6

9.77E+08 9.77E+08

1.14E+06 1.14E+06

2.10 1.20

2.00E+11 2.00E+11

10.75 14

273.05 355.6

9.4 9.65

9.4 11.1

3145 220

250 220

1093 1093

1.88E+06 1.07E+06

95.3 95.3

5.8 0.4

45 45

6.1

6.1

825

250

1370

7.63E+05

6.2

1.2

1.5

-1.124

-1.20733

-2.193

-2.832 -2.832

-2.898 -2.898

-6.029 -6.029

-4.852 -4.852

-7.135 -7.135

Selected valve characteri stic

-7.135 -7.135

Valve factor

Calculation of limit force Selected Wall Limit support thickness/ force stiffness schedule 40 wall kN ψ Flim 4 1.0 7 4 1.0 7

Peak Maximum outsurge of-balance pressure force (inc valve characteristic) Pa kN Psurge Fmax 1.22E+05 2.3 2.10E+05 3.9

kg/m3 ρ 649.8 649.8

Gate

CCR IP-P-042/211-0404/ IPP-203/211-0683

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036 -0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036

IP-P-042/211-0408/ IPP-024/211-0226

CCR

Unstabilised LPG from CCR unit to alkylation unit

520.3

9.77E+08

2.43E+06

1.07

2.00E+11

4.5

114.3

IP-P-042/211-0407/ IPP-024/211-1883

CCR

Unstabilised LPG from CCR unit to LPG storage

520.3

9.77E+08

2.43E+06

1.07

2.00E+11

4.5

114.3

6.1

6.1

1943

250

1370

7.63E+05

6.2

2.8

7.5

-0.4408

-0.53107

-0.6586

-0.62213 -0.76967 -0.62213

-3.56E-02

8.81E+04

0.7

4

1.0

2

520.3 520.3

9.77E+08 9.77E+08

2.43E+06 2.43E+06

3.60 8.01

2.00E+11 2.00E+11

14 10.75

355.6 273.05

9.65 9.4

11.1 9.27

1078 220

250 220

1370 1370

2.57E+06 5.71E+06

228.0 289.9

1.6 0.3

7.5 7.5

-0.4408 -0.4408

-0.53107 -0.53107

-0.6586 -0.6586

-0.62213 -0.76967 -0.62213 -0.62213 -0.76967 -0.62213

-1.20E-01 -2.35E-01

3.09E+05 6.41E+05

27.5 32.6

4 4

0.9 1.0

62 32

Line number

Area

System

Fluid density

Fluid properties Fluid bulk Upstream Steady modulus static state fluid pressure velocity

kg/m3 ρ

N/m2 K

Pa P1

m/s v

Young's modulus of main pipe N/m2 Eml

Main pipe properties Outside diameter of Pipe wall Schedule pipe thickness 40 pipe (actual) wall thickness inch mm mm mm Dext Dext T T40

Actual length of pipeline

Sonic velocity

m L

Length of pipeline between changes in m Lup

m/s C

Maximum Maximum surge out-ofpressure balance force Pa kN Pmax Fmax

sec Tsud

Actual valve closure time sec Tclose

Valve type and characteristic Full bore Reduced Butterfly Globe ball bore ball

Gate

Valve characteristic φ

Selected valve character istic

Valve factor

φ

Ω

Peak Maximum outsurge of-balance pressure force (inc valve characteristic) Pa kN Psurge Fmax

Calculation of limit force Selected Wall Limit support thickness/ force stiffness schedule 40 wall kN ψ Flim

MISC 1 IP-P-205T/211-0761/ IP-P-055/211-0412

BOO

Offspec LPG line from LPG storage to HGU

468

9.77E+08

3.62E+06

1.11

2.00E+11

6.625

168.275

7.11

7.11

3545

250

1445

7.51E+05

14.0

4.9

0.75

-3.34133 -4.86167 -3.34133

-1.20E-01

4.61E+05

8.6

4

1.0

IP-P-203/211-0697/ IPP-030/211-0315

BOO

HVY Slop oil from SLOP tank to DCU

970

1.55E+09

2.28E+06

0.42

2.00E+11

4.5

114.3

6.1

6.1

2552

250

1264

5.15E+05

4.2

4.0

2.25

-0.83933 -0.92556 -1.55367 -1.32711 -1.83056 -1.32711

-5.94E-02

1.39E+05

1.1

4

1.0

2

HVY Slop oil from SLOP tank to crude tank

970 970

1.50E+09 1.50E+09

2.28E+06 2.28E+06

0.66 3.11

2.00E+11 2.00E+11

8.625 16

219.075 406.4

8.13 9.4

8.13 12.7

3525 220

250 220

1243 1243

7.96E+05 3.75E+06

25.7 442.6

5.7 0.4

45 45

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036 -0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036

-2.60E-02 -1.08E-01

6.01E+04 2.59E+05

1.9 30.6

4 4

1.0 0.7

16 81 7 81

-1.978

-2.05267

-4.111

7

IP-P-203/211-0695/ IPP-201/211-0644

BOO

IP-P-203/211-0692/ IPP-201/211-0643

BOO

LT DRY SLOP from SLOP tank to crude tank

740 740

9.77E+08 9.77E+08

1.34E+06 1.34E+06

1.51 3.11

2.00E+11 2.00E+11

6.625 16

168.275 406.4

7.11 9.4

7.11 12.7

3525 220

250 220

1149 1149

1.28E+06 2.64E+06

23.9 312.0

6.1 0.4

8 8

-0.43013 -0.43013

-0.63463 -0.60325 -0.74125 -0.74125 -0.63463 -0.60325 -0.74125 -0.74125

-1.55E-01 -2.81E-01

2.24E+05 4.32E+05

4.2 50.9

4 4

1.0 0.7

IP-P-203/211-0714/ IPP-201/211-0642

BOO

WET SLOP from SLOP tank to crude tank

900 740

1.50E+09 9.77E+08

1.03E+06 1.03E+06

3.58 3.11

2.00E+11 2.00E+11

6.625 16

168.275 406.4

7.11 9.4

7.11 12.7

3525 220

250 220

1291 1149

4.16E+06 2.64E+06

77.5 312.0

5.5 0.4

45 45

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.39078 -0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.39078

-3.05E-01 -1.92E-01

3.66E+05 2.18E+05

6.8 25.7

4 4

1.0 0.7

7 81

IP-P-010/211-0002/ IPP-201/211-0639

AVU

Startup recycle from AVU to crude tank

892 892

1.50E+09 1.50E+09

3.73E+06 3.73E+06

3.89 0.00

2.00E+11 2.00E+11

18 42

457.2 1066.8

14.22 0

14.22 0

2338 220

250 #DIV/0!

1297 #DIV/0!

4.50E+06 #DIV/0!

649.6 #DIV/0!

3.6 #DIV/0!

10.5 10.5

-0.392 -0.392

-0.48276 -0.48276

-0.549 -0.549

-0.53581 -0.63976 -0.63976 -0.53581 -0.63976 -0.63976

-1.49E-01 #DIV/0!

5.98E+05 #DIV/0!

86.3 #DIV/0!

4 4

1.0 #DIV/0!

149 #DIV/0!

IP-P-030/211-0321/ IPP-026/211-0268

DCU

Sweet LPG from DCU to FCC LPG treater

550 550

9.77E+08 9.77E+08

2.11E+06 2.11E+06

1.12 2.52

2.00E+11 2.00E+11

4.5 10.75

114.3 273.05

6.1 12.7

6.1 9.27

1332 220

250 220

1333 1333

8.21E+05 1.85E+06

6.7 89.0

2.0 0.3

2.5 2.5

-0.7824 -0.7824

-0.8692 -0.8692

-1.4258 -1.4258

-1.2264 -1.2264

-1.679 -1.679

-1.679 -1.679

-1.23E-01 -2.43E-01

2.75E+05 5.78E+05

2.3 27.8

4 4

1.0 1.4

2 41

IP-P-023/211-0188/ IPP-026/211-0269

FCC

LPG from FCC unit to FCC LPG treater

550 550

9.77E+08 9.77E+08

2.11E+06 2.11E+06

2.20 2.52

2.00E+11 2.00E+11

10.75 10.75

273.05 273.05

9.4 12.7

9.27 9.27

484 220

250 220

1333 1333

1.61E+06 1.85E+06

81.9 89.0

0.7 0.3

2.5 2.5

-0.7824 -0.7824

-0.8692 -0.8692

-1.4258 -1.4258

-1.2264 -1.2264

-1.679 -1.679

-1.679 -1.679

-2.41E-01 -2.43E-01

5.73E+05 5.78E+05

29.1 27.8

4 4

1.0 1.4

32 41

IP-P-026/211-0270/ IP-P- TREATER Treated LPG from FCC LPG 204/211-xxxxx or IP-Ptreater to LPG blending/ LPG 205T/211-0756 bullet (U205)

511 511 511

9.77E+08 9.77E+08 9.77E+08

1.99E+06 1.99E+06 1.99E+06

2.75 6.65 4.76

2.00E+11 2.00E+11 2.00E+11

10.75 10.75 14

273.05 273.05 355.6

12.7 12.7 12.7

9.27 9.27 11.1

2566 1078 220

250 250 220

1383 1383 1383

1.94E+06 4.70E+06 3.36E+06

93.6 226.3 288.0

3.7 1.6 0.3

45 45 45

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.39078 -0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.39078 -0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.39078

-6.89E-02 -1.67E-01 -1.05E-01

1.42E+05 3.61E+05 2.20E+05

6.8 17.4 18.9

4 4 4

1.4 1.4 1.1

41 41 79

HDT LT naphtha from NFU to Naphtha export tank

649.8 649.8

9.77E+08 9.77E+08

1.71E+06 1.71E+06

1.34 0.86

2.00E+11 2.00E+11

6.625 28

168.275 711.2

7.11 16

7.11 17.45

3155 220

250 220

1226 1226

1.07E+06 6.85E+05

19.9 248.2

5.1 0.4

28 28

-0.31575 -0.40729 -0.37775 -0.40093 -0.43679 -0.40093 -0.31575 -0.40729 -0.37775 -0.40093 -0.43679 -0.40093

-5.12E-02 -2.89E-02

8.95E+04 5.00E+04

1.7 18.1

4 4

1.0 0.9

7 534

Sweet Naphtha from CCR feed to NHT unit

726

9.77E+08

1.97E+06

1.51

2.00E+11

10.75

273.05

9.4

9.27

1969

250

1160

1.27E+06

64.6

3.4

3

-1.07533 -1.45167 -1.07533

-1.49E-01

3.18E+05

16.1

4

1.0

32

629.3

9.77E+08

1.70E+06

1.26

2.00E+11

6.625

168.275

7.11

7.11

3210

250

1246

9.88E+05

18.4

5.2

31.25

-0.31099 -0.40258 -0.36706 -0.39251 -0.42412 -0.39251

-4.57E-02

7.96E+04

1.5

4

1.0

7

629.3 629.3

9.77E+08 9.77E+08

1.70E+06 1.70E+06

1.35 3.54

2.00E+11 2.00E+11

26 18

660.4 457.2

9.4 9.65

17.45 14.27

1324 220

250 220

1246 1246

1.06E+06 2.78E+06

342.2 418.0

2.1 0.4

31.25 31.25

-0.31099 -0.40258 -0.36706 -0.39251 -0.42412 -0.39251 -0.31099 -0.40258 -0.36706 -0.39251 -0.42412 -0.39251

-4.90E-02 -1.13E-01

8.54E+04 2.04E+05

27.6 30.7

4 4

0.5 0.7

265 106

902

1.55E+09

3.64E+06

0.89

2.00E+11

4.5

114.3

6.1

6.1

2751

250

1311

1.05E+06

8.6

4.2

0.5

-2.832

-2.898

-6.029

-4.852

-7.135

-7.135

-3.93E-01

1.74E+06

14.3

4

1.0

2

962

1.55E+09

3.64E+06

1.09

2.00E+11

10.75

273.05

9.4

9.27

220

220

1269

1.33E+06

67.6

0.3

0.5

-2.832

-2.898

-6.029

-4.852

-7.135

-7.135

-4.52E-01

2.06E+06

104.6

4

1.0

32

962

1.55E+09

1.13E+06

1.77

2.00E+11

12.75

323.85

10.41

10.41

2959

250

1269

2.16E+06

155.9

4.7

35

-0.3066

-0.39823

-0.3572

-0.38474 -0.41243 -0.38474

-1.45E-01

1.76E+05

12.7

4

1.0

53

962

1.55E+09

1.13E+06

2.51

2.00E+11

10.75

273.05

9.4

9.27

11

11

1269

3.06E+06

155.6

0.0

35

-0.3066

-0.39823

-0.3572

-0.38474 -0.41243 -0.38474

-9.05E-03

1.03E+04

0.5

4

1.0

32

-0.5205 -0.5205

MISC 2 IP-P-041/211-0396/ IPP-205T/211-0763 IP-P-203/211-0698/ IPP-040/211-0369 IP-P-041/211-0398/ IPP-0205T/211-0775

IP-P-023/211-0174/ IPP-105/211-xxxx & IP-P124/211-xxxx IP-P-201/211-0648/ IPP-105/211-xxxx & IP-P124/211-xxxx

NFU

NHT BOO

FCC

U124

HDT heavy naphtha from gasolene blending extended upto storage (MS PREM)

CLO from FCC to RFO

LSFO from crude tank to U105 & U124

-0.697

-0.78467

-1.234

MISC 4 - SLOPS IP-P-010/211-2654/ IPP-203/211-0694 IP-P-010/211-xxxx/ IPP-203/211-0691 IP-P-010/211-0029/ IPP-203/211-0715 IP-P-040/211-0372/ IPP-203/211-0715

SLOP

Heavy SLOP collection system to SLOP tank

855

1.55E+09

3.14E+06

1.54

2.00E+11

16

406.4

12.7

12.7

2021

250

1346

1.77E+06

202.1

3.0

11.25

-0.38387 -0.47471 -0.53073 -0.52142 -0.61811 -0.52142

-5.47E-02

1.76E+05

20.1

4

1.0

105

SLOP

Lt dry SLOP collection system to SLOP tank

736

1.55E+09

2.75E+06

1.65

2.00E+11

14

355.6

9.65

11.1

1956

250

1451

1.76E+06

156.5

2.7

12.5

-0.37248 -0.46344 -0.50516 -0.50128

-0.50128

-5.54E-02

1.56E+05

13.9

4

0.9

62

SLOP

Wet SLOP collection system to SLOP tank

675

1.55E+09

1.20E+06

1.53

2.00E+11

8.625

219.075

8.13

8.18

2005

250

1515

1.56E+06

50.6

2.6

11.25

-0.38387 -0.47471 -0.53073 -0.52142 -0.61811 -0.52142

-1.12E-01

1.42E+05

4.6

4

1.0

16

675

1.55E+09

1.20E+06

1.93

2.00E+11

6.625

168.275

7.11

7.11

16.5

16.5

1515

1.97E+06

36.8

0.0

11.25

-0.38387 -0.47471 -0.53073 -0.52142 -0.61811 -0.52142

-9.33E-03

1.13E+04

0.2

4

1.0

7

119.3

2.6

25.75

-0.31975 -0.41124 -0.38673

-1.21E-01

2.12E+05

8.7

4

1.0

22

-0.5878

SLOP

Wet SLOP collection system to SLOP tank

700

1.55E+09

1.65E+06

2.80

2.00E+11

9.625

244.475

8.13

8.18

1960

250

1488

2.92E+06

DCU

HVY naphtha from coker to NHT feed tank

730

1.55E+09

1.85E+06

0.58

2.00E+11

8.625

219.075

8.13

8.18

2691

250

1457

6.17E+05

19.9

3.7

10.5

-0.392

-0.48276

-0.549

-0.53581 -0.63976 -0.53581

-3.07E-02

5.76E+04

1.9

4

1.0

16

730

1.55E+09

1.85E+06

5.25

2.00E+11

14

355.6

9.65

11.1

220

220

1457

5.58E+06

496.0

0.3

10.5

-0.392

-0.48276

-0.549

-0.53581 -0.63976 -0.53581

-2.44E-01

5.10E+05

45.3

4

0.9

62

792.8

1.55E+09

2.74E+06

2.55

2.00E+11

10.75

273.05

9.4

9.27

1678

250

1398

2.83E+06

143.5

2.4

32.5

-0.30942 -0.40102 -0.36352 -0.38972 -0.41992 -0.38972

-7.18E-02

2.04E+05

10.4

4

1.0

32

792.8

1.55E+09

2.74E+06

4.68

2.00E+11

12.75

323.85

10.41

10.41

220

220

1398

5.19E+06

374.1

0.3

32.5

-0.30942 -0.40102 -0.36352 -0.38972 -0.41992 -0.38972

-1.16E-01

3.37E+05

24.3

4

1.0

53

-0.408

-0.44743

-0.408

MISC 5 IP-P-030/211-0324/ IPP-203/211-0652 IP-P-010/211-0008/ IPP-105/211-xxxx

AVU

AGO line to HSFO tank

IP-P-010/211-0008/ IPP-124/211-xxxx

AVU

AGO line to fuel oil tank

792.8

1.55E+09

2.74E+06

2.55

2.00E+11

10.75

273.05

9.4

9.27

2596

250

1398

2.83E+06

143.5

3.7

43.75

-0.29928 -0.39098 -0.34076 -0.37179 -0.39294 -0.37179

-6.85E-02

1.94E+05

9.9

4

1.0

32

IP-P-010/211-0022/ IPP-105/211-xxxx

BOO

VR (hot) from AVU to HSFO tank

993.3

1.55E+09

3.69E+06

1.73

2.00E+11

14

355.6

12.7

11.1

1678

250

1249

2.15E+06

183.8

2.7

13.75

-0.36316 -0.45422 -0.48424

-0.4848

-0.563

-0.4848

-5.64E-02

2.14E+05

18.3

4

1.1

79

993.3

1.55E+09

3.69E+06

4.83

2.00E+11

12.75

323.85

12.7

10.41

220

220

1249

5.99E+06

419.2

0.4

13.75

-0.36316 -0.45422 -0.48424

-0.4848

-0.563

-0.4848

-1.39E-01

5.48E+05

38.4

4

1.2

63

-0.4408

-0.62213 -0.76967 -0.62213

-1.27E-01

2.30E+05

26.2

4

1.0

105

IP-P-203/211-0668/ IPP-030/211-0305

DCU

Cold feed storage from alkylate bullet to DCU

888

1.55E+09

1.70E+06

1.56

2.00E+11

16

406.4

12.7

12.7

3974

250

1321

1.83E+06

208.6

6.0

7.5

NFU

HDT LT naphtha from NFU to CCR feed tank

649.8

9.77E+08

1.71E+06

1.89

2.00E+11

6.625

168.275

7.11

7.11

1995

250

1226

1.51E+06

28.1

3.3

33.75

-0.30796 -0.39957 -0.36024 -0.38714 -0.41604 -0.38714

-6.97E-02

1.23E+05

2.3

4

1.0

7

649.8

9.77E+08

1.71E+06

0.69

2.00E+11

10.75

273.05

9.4

9.27

220

220

1226

5.50E+05

27.9

0.4

33.75

-0.30796 -0.39957 -0.36024 -0.38714 -0.41604 -0.38714

-2.24E-02

3.86E+04

2.0

4

1.0

32

692.3

9.77E+08

1.34E+06

1.80

2.00E+11

12.75

323.85

9.65

10.41

2189

250

1188

1.48E+06

107.8

3.7

45

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036

-8.64E-02

1.20E+05

8.8

4

0.9

49

692.3

9.77E+08

1.34E+06

5.25

2.00E+11

14

355.6

9.65

11.1

220

220

1188

4.32E+06

383.5

0.4

45

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036

-2.22E-01

3.31E+05

29.4

4

0.9

62

692.3

9.77E+08

1.34E+06

1.01

2.00E+11

6.625

168.275

7.11

7.11

2452

250

1188

8.31E+05

15.5

4.1

22.5

-0.32693 -0.41836 -0.40287 -0.42071 -0.46656 -0.42071

-5.51E-02

7.56E+04

1.4

4

1.0

7

692.3

9.77E+08

1.34E+06

3.62

2.00E+11

6.625

168.275

7.11

7.11

220

220

1188

2.98E+06

55.5

0.4

22.5

-0.32693 -0.41836 -0.40287 -0.42071 -0.46656 -0.42071

-1.74E-01

2.53E+05

4.7

4

1.0

7

692.3

9.77E+08

1.34E+06

1.30

2.00E+11

6.625

168.275

7.11

7.11

1695

250

1188

1.07E+06

19.9

2.9

26.25

-0.3188

-0.4103

-0.3846

-0.40632

-0.4449

-0.40632

-6.84E-02

9.46E+04

1.8

4

1.0

7

692.3

9.77E+08

1.34E+06

1.56

2.00E+11

6.625

168.275

7.11

7.11

220

220

1188

1.28E+06

23.9

0.4

26.25

-0.3188

-0.4103

-0.3846

-0.40632

-0.4449

-0.40632

-7.23E-02

1.00E+05

1.9

4

1.0

7

649.8

9.77E+08

1.71E+06

1.89

2.00E+11

6.625

168.275

7.11

7.11

1238

250

1226

1.51E+06

28.1

2.0

22.5

-0.32693 -0.41836 -0.40287 -0.42071 -0.46656 -0.42071

-7.57E-02

1.34E+05

2.5

4

1.0

7

649.8

9.77E+08

1.71E+06

2.27

2.00E+11

6.625

168.275

7.11

7.11

220

220

1226

1.81E+06

33.7

0.4

22.5

-0.32693 -0.41836 -0.40287 -0.42071 -0.46656 -0.42071

-8.00E-02

1.42E+05

2.6

4

1.0

7

792.8

1.55E+09

2.74E+06

2.55

2.00E+11

10.75

273.05

9.4

9.27

1326

250

1398

2.83E+06

143.5

1.9

26.25

-0.3188

-0.4103

-0.3846

-0.40632

-0.4449

-0.40632

-7.49E-02

2.13E+05

10.8

4

1.0

32

792.8

1.55E+09

2.74E+06

3.79

2.00E+11

14

355.6

9.65

11.1

220

220

1398

4.20E+06

373.1

0.3

26.25

-0.3188

-0.4103

-0.3846

-0.40632

-0.4449

-0.40632

-9.79E-02

2.82E+05

25.1

4

0.9

62

792.8

1.55E+09

2.74E+06

2.55

2.00E+11

10.75

273.05

9.4

9.27

1744

250

1398

2.83E+06

143.5

2.5

32.5

-0.30942 -0.40102 -0.36352 -0.38972 -0.41992 -0.38972

-7.18E-02

2.04E+05

10.4

4

1.0

32

792.8

1.55E+09

2.74E+06

2.16

2.00E+11

12.75

323.85

10.41

10.41

220

220

1398

2.39E+06

172.7

0.3

32.5

-0.30942 -0.40102 -0.36352 -0.38972 -0.41992 -0.38972

-5.35E-02

1.51E+05

10.9

4

1.0

53

921.8

1.55E+09

2.22E+06

1.34

2.00E+11

6.625

168.275

7.11

7.11

1833

250

1297

1.60E+06

29.9

2.8

20

-0.33405

-0.4254

-0.41885

-0.4333

-0.4855

-0.4333

-6.02E-02

1.38E+05

2.6

4

1.0

7

921.8

1.55E+09

2.22E+06

4.83

2.00E+11

12.75

323.85

12.7

10.41

220

220

1297

5.77E+06

403.9

0.3

20

-0.33405

-0.4254

-0.41885

-0.4333

-0.4855

-0.4333

-1.91E-01

4.67E+05

32.7

4

1.2

63

858

1.55E+09

2.37E+06

1.43

2.00E+11

8.625

219.075

8.13

8.18

2239

250

1344

1.65E+06

53.3

3.3

20

-0.33405

-0.4254

-0.41885

-0.4333

-0.4855

-0.4333

-5.60E-02

1.37E+05

4.4

4

1.0

16

858

1.55E+09

2.37E+06

4.83

2.00E+11

12.75

323.85

12.7

10.41

220

220

1344

5.57E+06

389.6

0.3

20

-0.33405

-0.4254

-0.41885

-0.4333

-0.4855

-0.4333

-1.66E-01

4.29E+05

30.0

4

1.2

63

559

9.77E+08

2.24E+06

0.90

2.00E+11

8.625

219.075

8.13

8.13

215

215

1322

6.65E+05

21.5

0.3

1

-1.551

-1.63

-3.152

-2.586

-3.725

-2.586

-1.25E-01

2.98E+05

9.6

4

1.0

16

550

9.77E+08

1.67E+06

2.09

2.00E+11

6.625

168.275

7.11

7.11

1895

250

1333

1.53E+06

28.6

2.8

1.2

-1.3375

-1.41867

-2.6725

-2.20833 -3.15667 -2.20833

-3.81E-01

7.67E+05

14.3

4

1.0

7

550

9.77E+08

1.67E+06

8.15

2.00E+11

3.5

88.9

5.59

5.74

220

220

1333

5.97E+06

28.3

0.3

1.2

-1.3375

-1.41867

-2.6725

-2.20833 -3.15667 -2.20833

-1.31E+00

4.03E+06

19.1

4

1.0

1

629.3

9.77E+08

1.46E+06

1.26

2.00E+11

6.625

168.275

7.11

7.11

1238

250

1246

9.88E+05

18.4

2.0

13.75

-0.36316 -0.45422 -0.48424

-0.4848

-0.563

-0.4848

-6.57E-02

9.93E+04

1.9

4

1.0

7

629.3

9.77E+08

1.46E+06

1.51

2.00E+11

6.625

168.275

7.11

7.11

220

220

1246

1.18E+06

22.1

0.4

13.75

-0.36316 -0.45422 -0.48424

-0.4848

-0.563

-0.4848

-6.93E-02

1.05E+05

2.0

4

1.0

7

692.3

9.77E+08

1.34E+06

1.82

2.00E+11

12.75

323.85

10.41

10.41

1627

250

1188

1.50E+06

107.9

2.7

45

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036

-8.73E-02

1.22E+05

8.8

4

1.0

53

692.3 692.3

9.77E+08 9.77E+08

1.34E+06 1.34E+06

1.35 3.54

2.00E+11 2.00E+11

26 18

660.4 457.2

9.4 9.65

17.4 14.3

1202 220

250 220

1188 1188

1.11E+06 2.91E+06

358.9 438.4

2.0 0.4

45 45

-0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036 -0.29847 -0.39018 -0.33893 -0.37036 -0.39078 -0.37036

-6.48E-02 -1.50E-01

8.94E+04 2.15E+05

28.9 32.4

4 4

0.5 0.7

266 106

-0.53107

-0.6586

MISC 7 IP-P-041/211-0397/ IPP-203/211-0699 IP-P-010/211-0012/ IPP-203/211-0655 IP-P-010/211-0012/ IPP-203/211-0669 IP-P-010/211-0012/ IPP-203/211-0669

AVU

AVU

AVU

SR naphtha from AVU to NHT feed tank SR naphtha from AVU to HGU feed tank SR naphtha from AVU to GT distillate tank

MISC 8 IP-P-041/211-0397/ IPP-110/211-xxxx

NFU

HDT LT naphtha from NFU to GT distillate tank

IP-P-010/211-0008/ IPP-203/211-0660

AVU

AGO line from AVU to VR storage tank

IP-P-010/211-0008/ IPP-126/211-1541

AVU

AGO line from AVU to flushing tank

IP-P-023/211-0177/ IPP-105/211-xxxx IP-P-030/211-0307/ IPP-105/211-xxxx

FCC

DCU

LCO from FCC to HSFO tank

LCGO from DCU to HSFO tank

MISC 8 IP-P-070/211-0459/ IPP-024/211-0217

PRU

IP-P-203/211-0704/ IPP-024/211-0220

BOO

IP-P-041/211-2907/ IPP-110/211-xxxx IP-P-010/211-0012/ IPP-205T/211-xxxx

NFU

AVU

LPG from PRU to alkylation unit pure isobutane from alkylate storage bullet to alkylation unit HDT HVY naphtha from NFU to GT distillate tank SR naphtha from AVU to MS blending/ MS regular tanks