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AVEVA™ Process Simulation

Fluid Flow mode results for the F4 example simulation

Fluid Flow mode results for the F4 example simulation

  • Last UpdatedOct 04, 2024
  • 3 minute read

The following table shows the relief valve back pressures for the case in which all valves are relieving (FF 1) at the rated flow conditions. We can see that all the downstream piping has been adequately sized since the back pressure is low for all relief valves.

Name

Variable

UOM

RV1

RV2

RV3

RV4

Model

PSV

PRV

PRV

PRV

Relief Valve Type

Type

Conventional

Conventional

Conventional

Conventional

Orifice Letter

Size

N

J

G

D

Mass flow

W

kg/h

18,000

6,000

10,000

2,000

Set pressure

SP

kPa

844

1,726

1,272

3,544

Area

A

mm2

2,800

830

324

71

Capacity

Capacity

%

82

51

37

16

Molar Vapor Fraction

OutState.VF

%

100

100

17

0

Inlet pressure

P1

kPa

1,030

2,000

1,499

4,000

Back pressure

Pb

kPa

154

152

195

136

Back pressure fraction

BPf

%

6

3

7

1

The following table shows the relief valve back pressures for the case in which total power failure (FF2) occurs at the rated flow conditions. We see that during a total power failure, the relief valves are still appropriately sized, with all back pressure fractions being less than 10%.

Name

Variable

UOM

RV1

RV2

RV3

RV4

Model

PSV

PRV

PRV

PRV

Relief Valve Type

Type

Conventional

Conventional

Conventional

Conventional

Orifice Letter

Size

N

J

G

D

Mass flow

W

kg/h

18,000

6,000

10,000

0

Set pressure

SP

kPa

844

1,726

1,272

3,544

Area

A

mm2

2,800

830

324

71

Capacity

Capacity

%

82

51

37

81

Vapor Fraction

OutState.VF

%

100

100

17

0

Inlet pressure

P1

kPa

1,030

2,000

1,499

4,000

Back pressure

Pb

kPa

153

151

194

132

Back pressure fraction

BPf

%

6

3

7

1

The following table shows the relief valve back pressures for the case in which cooling water failure (FF3) occurs. In this case as well, no back pressure fraction exceeds 6% and the relief valves are still appropriately sized.

Name

Variable

UOM

RV1

RV2

RV3

RV4

Model

PSV

PRV

PRV

PRV

Relief Valve Type

Type

Conventional

Conventional

Conventional

Conventional

Orifice Letter

Size

N

J

G

D

Mass flow

W

kg/h

18,000

6,000

0

0

Set pressure

SP

kPa

844

1,726

1,272

3,544

Area

A

mm2

2,800

830

324

71

Capacity

Capacity

%

82

51

59

81

Vapor Fraction

OutState.VF

%

100

100

4

0

Inlet pressure

P1

kPa

1,030

2,000

1,499

4,000

Back pressure

Pb

kPa

138

133

129

123

Back pressure fraction

BPf

%

4

2

2

1

Additionally, we can observe the heat loss across specified inlet and tail pipes only looking at the temperature difference (DT). The heat transfer across each pipe, including the heat loss method is shown in the following table for the case where all valves are relieving.

Case – All Valves Relieving

Model

Pipe Service

Heat Loss Method

Temperature Difference (°C)

PI1

Inlet

PipeInAir

0.4

PIR1

Tail

PipeInAir

6.2

PIR2

Inlet

PipeInAir

0.0

PIR3

Tail

PipeInAir

2.2

PIR4

Inlet

PipeInAir

0.0

PIR5

Tail

PipeInAir

8.2

PIR6

Inlet

PipeInAir

0.8

PIR7

Tail

PipeInAir

4.1

PIR8

Other

PipeInAir

1.5

PIR9

Other

PipeInAir

2.7

PIR10

Other

PipeInAir

6.6

After all the fluid has been collected by the common headers, the fluid is sent to the knockout drum where the phases are separated. For each case, the amount of fluid fed to the drum changes, which results in differing vapor and liquid product that is sent to the stack and downstream pump, respectively. The following table shows the mass balance around the drum for each case.

Variable

Model

Variable

UOM

Case – All Valves Relieving

Case – Total Power Failure

Case – Cooling Water Failure

Drum Feed

S28

W

kg/h

36,000.00

36,000.00

36,000.00

Vapor Product to Stack

S17

W

kg/h

26,824.46

26,824.46

26,824.46

Liquid Product to Pump

S19

W

kg/h

9,175.54

9,175.54

9,175.54

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