Default Separator Calculation

SEPARATOR SIZING

Design Condition :

Gas flow rate = 25 MMSCFD

Oil flow rate = 3000 BPD

Operating pressure = 800 psig

Operating temperature = 80

Gas density = 3.4

Oil density = 51.5

API gravity = 35 Refer to Hysis

Separator type = Vertical

Assume :

Shell height = 10 ft See Table C.1

Liquid volume = 30 %

Liquid height = 3 ft

for K = 0.18 See Table C.1

Va = 0.68 ft/s

Actual gas flow rate = 4.552 Refer to Hysis

Minimum gas flow area = 6.72

Minimum ID of separator = 2.93 ft = 35.1 inches

Use = 40 inches = 3.3 ft

Retention time = 1 minute See Table C.1.7

26.17 4.66 barrel

6711.09 BPD

ID = 3.3 ft OKE

H = 10 ft OKE

(H/D) = 3

Shell height = 10 ft See Table C.1

Liquid volume = 30 %

Liquid height = 3 ft

for K = 0.35 See Table C.1

Va = 1.32 ft/s

Actual gas flow rate = 4.552 Refer to Hysis

Minimum gas flow area = 3.46

Minimum ID of separator = 2.10 ft = 25.2 inches

Use = 30 inches = 2.5 ft

Retention time = 1 minute See Table C.1.7

14.72 2.62 barrel

oF

lb/ft3

lb/ft3

ft3/s

ft2

Liquid volume (excluding bottom head) = ft3 =

Liquid capacity of the separator =

[Range 2.5~6 refer to Shell Standard - Kepatutan Bentuk]

ft3/s

ft2

Liquid volume (excluding bottom head) = ft3 =

3774.99 BPD

ID = 2.5 ft OKE

H = 10 ft OKE

(H/D) = 4

0.35

Liquid capacity of the separator =

[Range 2.5~6 refer to Shell Standard - Kepatutan Bentuk]

In case there is no data due to absences of vendor recommendation

use K =

Refer to page 97 Oilfield processing Volume 2 : Crude Oil, Francis S. Manning

SEPARATOR SIZING

Example case GPSA

Design Condition :


Gas mass flow = 39.8 lb/s Refer to Hysis

Gas viscosity = 0.012 cP



Gas density = 2.07

Oil density = 31.2

Separator type = Horizontal

Demister = No

Gravitational acceleration = 32.2 ft/s

Dp = (particle diameter) 150 micron = 0.000492125 ft

4741.31 Formula 7-3

C = 1.4 Fiq 7-3

Vt = (terminal velocity) 0.461 ft/s Formula 7-1

Gas flow = 19.23

Assume diameter : ID = 3.50 ft = 42 inch

Vessel length : H = 15.19 ft Formula 7-12

(H/ID) = 4.34 Normally 2 < (H/ID) < 4

Assume diameter : ID = 4.00 ft 48 inch


(H/ID) = 3.32 Normally 2 < (H/ID) < 4



(H/ID) = 2.62 Normally 2 < (H/ID) < 4



(H/ID) = 2.13 Normally 2 < (H/ID) < 4

Design Condition :






Gas density = 2.07

Oil density = 31.2


Demister = No


Vt = (terminal velocity) 0.461 ft/s Formula 7-1

Gas flow = 19.23

oF

lb/ft3

lb/ft3

C.Re2 =

ft3/s

oF

lb/ft3

lb/ft3

ft3/s

A = 41.72

ID = 7.3 ft = 87 inch

Select ID = 90 inch

H = 180 inch 15 ft for (H/ID) = 2H = 270 inch 23 ft for (H/ID) = 3H = 360 inch 30 ft for (H/ID) = 4

Design Condition :






Gas density = 2.07

Oil density = 31.2


Demister = Yes


K1 = 0.18 refer to Fig 7-9

0.144 for 500 psig

K2 = 0.35 refer to Fig 7-9

0.28 for 500 psig

Vt = (terminal velocity) 0.540 ft/s for K1

Vt = (terminal velocity) 1.050 ft/s for K2

A = 35.59

ID = 6.73 ft = 81 inch

Select ID = 90 inch

H = 180 inch for (H/ID) = 2H = 270 inch for (H/ID) = 3H = 360 inch for (H/ID) = 4

A = 18.30

ID = 4.83 ft = 58 inch

Select ID = 60 inch

H = 120 inch 10 ft for (H/ID) = 2H = 180 inch 15 ft for (H/ID) = 3H = 240 inch 20 ft for (H/ID) = 4

0.35

ft2

oF

lb/ft3

lb/ft3

ft2 for K1

ft2 for K2

In case there is no data due to absences of vendor recommendation use K =

Refer to page 97 Oilfield processing Volume 2 : Crude Oil, Francis S.

Manning

SEPARATOR SIZING

Design Condition :


Oil flow rate = 3000 BPD = 0.331



Gas density = 3.4 54.5

Oil density = 51.5 825.0

API gravity = 35 Refer to Hysis


Kc1 = 0.8 Without demisterRefer to Ap Greid Manual Training

Kc2 = 1.7 With demister

Va = 0.18 m/s Critical velocity

Vg1 = 0.14 m/s Gas velocity without demister

Vg2 = 0.31 m/s Gas velocity with demister

Actual gas flow rate = 4.552 0.129

Minimum gas flow area = 0.89 Without demister

Minimum gas flow area = 0.42 With demister

Minimum ID of separator = 1.07 m = 42.0 inches =

Minimum ID of separator = 0.75 m = 29.5 inches =

Use = 43.3 inches = 1100.0 mm

Use = 31.50 inches = 800 mm

h1 = 400 mm 0.6 minute residence time



ID nozzle inlet = 304.8 mm

h3 = 400 mm or h3 = 602.4 mm

selected h3 = 602.4 mm 0.9 minute residence time

h1 + h2 + h3 = 825 mm 2.4 minute residence time

h1 + h2 + h3 = 900 minimum mm 2.4 minute residence time

h1 + h2 + h3 = 1800 minimum mm 5.2 minute residence time

selected h1 + h2 + h3 = 900 mm 2.6 minute residence time

h4a = 457.2 mm 1.3 minute residence time

h4b = 457.2 mm 0.7 minute residence time

h4a = 552.4 mm 1.6 minute residence time

h4b = 552.4 mm 0.8 minute residence time



h5 = minimum 200 mm

V5 = 331223531 1 minute residence time

A5 = 949850

h5 = 349 mm


A5 = 949850

h5 = 697 mm


A5 = 502400

h5 = 659 mm


m3/min =

oF

lb/ft3 = kg/m3

lb/ft3 = kg/m3

ft3/s = m3/s

m2

m2

mm3

mm2

mm3

mm2

mm3

mm2

mm3

A5 = 502400

h5 = 1319 mm

h6 = minimum 300 mm


A6 = 949850

h6 = 1046 mm


A6 = 502400

h6 = 1978 mm

h7 = minimum 150 mm


A7 = 949850

h7 = 349 mm


A7 = 949850

h7 = 697 mm


A7 = 502400

h7 = 659 mm


A7 = 502400

h7 = 1319 mm

h8a = 150 mm 0.4 minute residence time

h8b = 150 mm 0.2 minute residence time

h8a = 300 mm 0.9 minute residence time

h8b = 300 mm 0.5 minute residence time

SUMMARY :

ID = 800 mm = 2.62 ft

H = 5301 mm

Choosen H = 5350 mm 17.55 ft

(H/ID) = 6.69

Total liquid residence time = 8.0 minute

ID = 1100.0 mm = 3.61 ft

H = 2944 mm

Choosen H = 3000 mm 9.84 ft

(H/ID) = 2.73

Total liquid residence time = 10.0 minute

Normal level = 1948.21 mm

% liquid level at normal = 37 %

h1 =

h2 =

h3 =

mm2

mm3

mm2

mm3

mm2

mm3

mm2

mm3

mm2

mm3

mm2

mm3

mm2

WITH DEMISTER

WITHOUT DEMISTER

h3 =

h4 =

d

H = 5301.2 mm

(H/ID) = 6.63

HHLA

h5 =HLA

h6 =NL

LLA

h7 =LLLA

h8 =

ID= 800.0 mm

Separator type = Horizontal without demister

[1] Vapor liquid settling velocity

Va = 0.18 m/s Critical velocity

K = 1.7 Assume production separator Refer to Ap Greid Manual Training

Vg = 0.31 m/s Gas velocity

[2] Vapor area :

Av = 0.42

ID = 0.60 m = 600.00 mm

Use ID = 600.00 mm

[3] Required liquid hold up times :

h4 = minimum 100 mm


A4 = 282600

h4 = 1172 mm


A4 = 282600

h4 = 2344 mm

h5 = minimum 300 mm

m2

mm3

mm2

mm3

mm2


A5 = 282600

h5 = 3516 mm

h6 = minimum 100 mm


A4 = 282600

h4 = 1172 mm


A4 = 282600

h4 = 2344 mm

Vtotal = 1656117656

hut = 5 minutes

[4] Drum sizing :

Preliminary sizing

Trial 1 2

Selected (L/ID) normally 3 <(L/ID) <4 3.5

Selected (h/ID) 0.5

Calculated vapor area Av =

mm3

mm2

mm3

mm2

mm3

mm2

mm3

SEPARATOR SIZING

331223531

Refer to Ap Greid Manual Training

Refer to Hysis

1066 mm

748 mm

Without demister

With demister

for ID < 1200 mm height from bottom of head to mesh pad

for no carbon deposite service height of mesh pad

for carbon deposite service

Refer to line sizing

Greater value is selected height from mesh pad to half of inlet nozzle

Without demister

With demister

Without demister height from half of inlet nozzle to high high level alarm

With demister

Without demister

With demister

height from high high alarm to high level alarm

mm3/min

WITH DEMISTER

WITHOUT DEMISTER

WITHOUT DEMISTER

WITH DEMISTER

normal level from high level alarm to low level alarm

height from low level to low low level alarm

Without demister for bottom connected to level transmitter

With demister for bottom connected to level transmitter height from low low level alarm to bottom head

Without demister for side connected to level transmitter

With demister for side connected to level transmitter

400.0 mm

150.0 mm

602.4 mm

WITHOUT DEMISTER

WITH DEMISTER

WITHOUT DEMISTER

WITH DEMISTER

WITH DEMISTER

WITHOUT DEMISTER

602.4 mm

552.4 mm

659.3 mm

1977.8 mm

659.3 mm

300.0 mm

Refer to Ap Greid Manual Training

3 4

WITH DEMISTER

height from low low level alarm to bottom head

PROJECT : TAG NO.

CLIENT : PETRONAS CARIGALI PAKISTAN TYPE

SERVICE : DEETHANIZER REFLUX DRUM CASE

PT.ISTANA KARANG LAUTVERTICAL SEPARATOR

DESIGN BASIS

BASED ON PROCESS FLOW DIAGRAM

GAS RATE 150

GAS RATE FOR DESIGN 165LIQUID RATE 5

LIQUID RATE FOR DESIGN 5.5

AQUEOUS RATE 5

AQUEOUS RATE FOR DESIGN 5.5

OPERATING PRESSURE 964.7

TEMPERATURE 120

LIQUID DENSITY 49.94

AQUEOUS DENSITY 62.42

MW GAS 16.49

GAS COMP. FACTOR 0.9

WITH MIST ELIMINATOR ( YES/NO ) YES

K FACTOR 0.2719

CALCULATION

GAS DENSITY 2.840

GAS DENSITY REFER TO DESIGN FOR CHECK

MIXED LIQUID DENSITY 56.181

MIXED LIQUID DENSITY REFER TO DESIGN FOR CHECK

ACTUAL GAS RATE 29.212

ACTUAL GAS RATE REFER TO HYSIS FOR CHECK

LIQUID RATE 0.043

LIQUID RATE REFER TO HYSIS FOR CHECK

GAS VELOCITY 1.179

MINIMUM GAS AREA 24.787

MINIMUM DIAMETER 5.618

DEMISTER CLEARANCE 3.000

DIAMETER 6.1

1865

PROPOSED DIAMETER 6.2

74.80

1900.00

LLLA

SETTING LIQUID HEIGHT, INCH (T/T) 6

SETTING LIQUID HEIGHT, FT 0.500

LIQUID VOLUME, CUFT 46.97

RETENTION TIME, MIN (Bottom Base) 1095.96

RETENTION TIME, MIN (Level Base) 1096.0

GUESSING GAS HEIGHT

- BOTTOM TO HHLL 36.000

- DIVERTER 28.000

- DIVERTER TO MIST ELIMINATOR 74.803

- MIST ELIMINATOR THICKNESS 6.000

- MIST ELIMINATOR TO TOP 30.402

MINIMUM VESSEL HEIGHT S/S 14.60

4450.20

PROPOSED VESSEL HEIGHT S/S 14.76

177.17

4500

NOZZLE SIZING

A) INLET NOZZLE

INLET NOZZLE DIAMETER VELOCITY DENSITY

IN FPS LB/CUFT

14 27.341 2.839

14 27.341 2.839

14 27.341 2.839

Use = 14 Inch

B) OUTLET NOZZLE

VAPOR NOZZLE

OUTLET NOZZLE DIAMETER VELOCITY DENSITY

IN FPS LB/CUFT

14 27.340 2.840

14 27.340 2.840

14 27.340 2.840

Use = 14 Inch

C) LIQUID NOZZLE


IN FPS LB/CUFT

2 0.033 56.181

2 0.033 56.181

2 0.033 56.181

Use = 2 Inch

DIAMETER 74.803

HEIGHT 14.764

H/D 2.368

LIQUID RETENTION TIME AT NLL 1570.73

NOTE* INPUT DATA Note 3 GPSA Eq. 7-7Note 1 ASSUMED SINCE NO LIQUID AVAILABL Note 4 Gas Conditioning & Processing - Campbell Eq. 11.21, Eq. 11.22, Eq. 11.23Note 2 GPSA Fig. 7-9 and Chemical Engineering Progrees. Design Two-Phase Separator Within the Right Limits W.Y.Svrcek, W.D. Monnery

Own Calculations :

h7 = 304.80 mm 12 inch minimum 1.0 fth6 = 304.80 mm 12 inch minimum 1.0 fth5 = 304.80 mm 12 inch minimum 1.0 fth4 = 711.20 mm 28 inch 2.3 fth3 = 1900.00 mm 24 inch min or ID 6.2 fth2 = 152.40 mm 6 inch 0.5 fth1 = 772.20 mm 30 inch 2.5 fthT = 4450.20 mm 14.6 inch 14.6 ft

Selected H = 4500.00 mm 177 inch 14.8 ftID = 1900.00 mm 74.8 inch 6.2 ft

(H/ID) = 2.37

h1 = 772.2 mm

h2 = 152.4 mm

h3 = 1900.0 mm

h4 = 711.2 mmHHLA

h5 = 304.8 mmH = 4500.0 mm(H/ID) = 2.37

HLA

h6 = 304.8 mmNL

LLA

h7 = 304.8 mmLLLA

ID = 1900.0 mm

: V-2701

: VERTICAL, 2-PHASE

: MAXIMUM FLOW RATE


MMSCFD 1.5

MMSCFD 10 % tolerance for design BLPD Note 1

BLPD 10 % tolerance for design BAPD Note 1

BAPD 10 % tolerance for design PSIA *

F *

LB/CUFT * Refer to Hysis Simulation


* Refer to Hysis Simulation


(Vane Pack Mist Elim.)

Note 2

LB/CUFT


LB/CUFT


CUFT/SEC

CUFT/SEC * Refer to Hysis Simulation

CUFT/MIN

CUFT/MIN * Refer to Hysis Simulation

FPS Note 3

SQFT

FT

INCH 3"~6" for ring support of mist eliminator

FT

mm

FT

INCH

mm * (SELECTED)

LLA NLA HLA HHLA

12 14 24 36

1.000 1.167 2.000 3.000

62.23 67.31 92.74 123.26

1452.03 1570.73 2164.19 2876.34

356.1 118.7 593.5 712.2

IN

IN (2 x D inlet Nozzle) Fig 7-6. GPSA

IN (Minimum 24" or ID) Fig 7-6. GPSA

IN * (Minimum Recommended 4" at E-7 GPSA)

IN Fig 7-10. GPSA

FT

mm

FT

INCH

mm * (SELECTED)

Note 4

REMARK

LB/SQFT

2121.960 OK

2121.960 OK

2121.960 OK

Note 4

REMARK

LB/SQFT

2122.956 OK

2122.956 OK

2122.956 OK

Note 4

REMARK

VELOCITY =< 3.3

OK

OK

OK

INCH

FT

MINUTES

Gas Conditioning & Processing - Campbell Eq. 11.21, Eq. 11.22, Eq. 11.23Note 2 GPSA Fig. 7-9 and Chemical Engineering Progrees. Design Two-Phase Separator Within the Right Limits W.Y.Svrcek, W.D. Monnery

Fig 7-9. API Sect 7 712 minutesFig 7-9. API Sect 7 712 minutesFig 7-9. API Sect 7 712 minutesFig 7-9. API Sect 7 1661 minutesFig 7-9. API Sect 7 4437 minutesFig 7-9. API Sect 7 356 minutesFig 7-10. API Sect 7 1803 minutes

r X V2

r X V2

PROJECT : TAG NO.

CLIENT : PETRONAS CARIGALI PAKISTAN TYPE

SERVICE : DEETHANIZER REFLUX DRUM CASE


Refer to : W.Y. Svrcek, W.D. Monnery," Design Two-Phase Separators Within the Right Limits

DESIGN BASIS


GAS RATE 150

GAS RATE FOR DESIGN 165LIQUID RATE 5

LIQUID RATE FOR DESIGN 5.5

AQUEOUS RATE 5

AQUEOUS RATE FOR DESIGN 5.5

OPERATING PRESSURE 964.7

66.53

TEMPERATURE 120

LIQUID DENSITY 49.94

AQUEOUS DENSITY 62.42

MW GAS 16.49

GAS COMP. FACTOR 0.9

WITH MIST ELIMINATOR ( YES/NO ) YES

K FACTOR 0.2719

CALCULATION

GAS DENSITY 2.840


MIXED LIQUID DENSITY 56.181


ACTUAL GAS RATE 29.212


LIQUID RATE 0.043


GAS VELOCITY 1.179

GAS VELOCITY FOR CONCERVATIVE DESIGN 1.179

MINIMUM GAS AREA 24.787

MINIMUM DIAMETER 5.618

DEMISTER CLEARANCE 3.000

DIAMETER 6.118

1865

PROPOSED DIAMETER 6.2

74.80

1900.0

LLLA

SETTING LIQUID HEIGHT, INCH (T/T) 3

SETTING LIQUID HEIGHT, FT 0.250

LIQUID VOLUME, CUFT 39.34

RETENTION TIME, MIN (Bottom Base) 917.92

RETENTION TIME, MIN (Level Base) 917.9

GUESSING GAS HEIGHT

- BOTTOM TO HHLL 49

- HHLA to BOTTOM OF MIST ELIMINATOR 37.40

- MIST ELIMINATOR THICKNESS 6

- MIST ELIMINATOR TO TOP 12

MINIMUM VESSEL HEIGHT S/S 8.70

2652

PROPOSED VESSEL HEIGHT S/S 13.94

167.32

4250

DIAMETER 1900

HEIGHT 4250

H/D 2.237

LIQUID RETENTION TIME AT NLL 1808.11

NOZZLE SIZING

A) INLET NOZZLE

INLET NOZZLE DIAMETER VELOCITY DENSITY

IN FPS LB/CUFT

14 27.341 2.839

14 27.341 2.839

14 27.341 2.839

Use = 14 Inch

B) OUTLET NOZZLE

VAPOR NOZZLE


IN FPS LB/CUFT

14 27.340 2.840

14 27.340 2.840

14 27.340 2.840

Use = 14 Inch

C) LIQUID NOZZLE


IN FPS LB/CUFT

2 0.033 56.181

2 0.033 56.181

2 0.033 56.181

Use = 2 Inch

NOTE* INPUT DATA Note 3 GPSA Eq. 7-7 then 0.75 x gas velocity for conservative designNote 1 ASSUMED SINCE NO LIQUID AVAILABL Note 4 Gas Conditioning & Processing - Campbell Eq. 11.21, Eq. 11.22, Eq. 11.23Note 2 GPSA Fig. 7-9 and Chemical Engineering Progrees. Design Two-Phase Separator Within the Right Limits W.Y.Svrcek, W.D. Monnery

h7 = 152.40 mm 6 inch 0.5 fth6 = 2.14 mm 0.084 inch 0.01 ft

h6 selected = 304.80 mm 12 inch 1.0 ft minimumh5 = 1.28 mm 0.051 inch 0.004 ft

h5 selected = 304.80 mm 12 inch 1.0000 fth4 = 482.60 mm 19 inch 1.6 ft

h3 = 950.00 mm 37 inch 3.1 fth3 = 787.40 mm 31 inch 2.6 fth3 = 2077.80 mm 82 inch 6.8 ft

h3 selected = 2077.80 mm 82 inch 6.8 fth2 = 152.40 mm 6 inch 0.5 fth1 = 304.80 mm 12 inch 1.0 fth1 = 772.20 mm 30 inch 2.5 ft

Selected h1 = 772.20 mm 30 inch 2.5 fthT = 4247.00 mm 167.2 inch 13.9 ft

Selected H = 4250.00 mm 167 inch 13.9 ftID = 1900.00 mm 74.8 inch 6.2 ft

(H/ID) = 2.24

h1 = 772.2 mm

h2 = 152.4 mm

h3 = 2077.8 mmHHLA

h4 = 482.6 mmH = 4250.0 mm(H/ID) = 2.24

HLA

h5 = 304.8 mm

NLh6 = 304.8 mm

LLAh7 = 152.4 mm

ID = 1900.0 mm

: V-2701

: VERTICAL, 2-PHASE

: MAXIMUM FLOW RATE


Refer to : W.Y. Svrcek, W.D. Monnery," Design Two-Phase Separators Within the Right Limits

MMSCFD 1.5

MMSCFD 10 % tolerance for design BLPD Note 1

BLPD 10 % tolerance for design BAPD Note 1

BAPD 10 % tolerance for design PSIA *

BARA

F *





(Vane Pack Mist Elim.)

Note 2

LB/CUFT


LB/CUFT


CUFT/SEC

CUFT/SEC * Refer to Hysis Simulation

CUFT/MIN

CUFT/MIN * Refer to Hysis Simulation

FPS Note 3

FPS * Take 75%~100% from gas velocity

SQFT

FT

INCH

FT

mm

FT

INCH

mm * (SELECTED)

LLA NLA HLA HHLA

6 18 30 49

0.500 1.500 2.500 4.083

46.97 77.49 108.00 156.33

1095.96 1808.11 2520.27 3647.84

178.0 712.2 712.2 1127.6

IN

IN

IN

IN

FT

MM

FT

INCH

MM * (SELECTED)

MM

MM

* The ratio (H/D) should be in 1.5~6

MINUTES

Note 4

REMARK

LB/SQFT

2121.960 OK

2121.960 OK

2121.960 OK

Note 4

REMARK

LB/SQFT

2122.956 OK

2122.956 OK

2122.956 OK

Note 4

REMARK

VELOCITY =< 3.3

OK

OK

OK

GPSA Eq. 7-7 then 0.75 x gas velocity for conservative design

Gas Conditioning & Processing - Campbell Eq. 11.21, Eq. 11.22, Eq. 11.23Note 2 GPSA Fig. 7-9 and Chemical Engineering Progrees. Design Two-Phase Separator Within the Right Limits W.Y.Svrcek, W.D. Monnery

Refer to Table 3. Low liquid level heightv6 = 0.2143 CUFT Refer to Table.2 Liquid holdup and surge times

v6 selected = 30.5033 CUFT 1.0 ft minimum holding time= 711.8 minutesv5 = 0.1286 CUFT Refer to Table.2 Liquid holdup and surge times

v5 selected = 30.5033 CUFT 1.0 feet minimum holding time= 711.8 minutes

r X V2

r X V2

Surge volume

Holding volume

M120

Holding volume

M122

Surge volume

Refer to Fig. 1 Svrcek and Monnery

Refer to Fig 7-6. GPSA sec. 7

Refer to Fig. 1 Vertical 2 phase separator Svrcek & MonneryRefer to Fig 24 Amistco Mest and Vane Mist Eliminator/Fig 6 The engineered mist eliminator/Fig. 7-10 GPSA sec. 7

Surge volume

Refer to Fig 24 Amistco Mest and Vane Mist Eliminator/Fig 6 The engineered mist eliminator/Fig. 7-10 GPSA sec. 7

PROJECT :

CLIENT : PETRONAS CARIGALI PAKISTAN

SERVICE : DEETHANIZER REFLUX DRUM


Refer to : W.Y. Svrcek, W.D. Monnery,"Design Two-Phase Separators Within the Right Limits"

DESIGN BASIS


GAS RATE

GAS RATE FOR DESIGNLIQUID RATE

LIQUID RATE FOR DESIGN

AQUEOUS RATE

AQUEOUS RATE FOR DESIGN

OPERATING PRESSURE

TEMPERATURE

LIQUID DENSITY

AQUEOUS DENSITY

MW GAS

GAS COMP. FACTOR

WITH MIST ELIMINATOR ( YES/NO )

K FACTOR

K FACTOR WIT/WITHOUT MIST ELIMINATOR

CALCULATION

GAS DENSITY


MIXED LIQUID DENSITY


ACTUAL GAS RATE


LIQUID RATE


GAS VELOCITY

GAS VELOCITY FOR CONCERVATIVE DESIGN

HOLD UP VOLUME

SURGE VOLUME

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

LOW LIQUID LEVEL HEIGHT (LLA)


SELECTED LLA

(LLA/ID)

1ST ITERATION :

TOTAL CROSS SECTIONAL AREA (AT)

(ALLA/AT)

SELECTED LENGTH OF SEPARATOR L

SUMMARY

PROPOSED DIAMETER (ID)

PROPOSED LENGTH (L)

(L/ID)

ASSUME 2:1 ELLIPTICAL DISH HEAD

USE SA-516 70 CARBON STEEL

S

CORROSION ALLOWANCE

ASSUME WELDING JOINT EFFICIENCY

P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME



SELECTED LLA

(LLA/ID)

ALLA

HV =

HV =

SELECTED HV =

(HV/ID)

(AV/AT)

AV

MINIMUM LENGTH FOR ACCOMODATING HOLD UP/SURGE (LHOLDUP-SURGE)

SELECTED LHOLDUP-SURGE

LIQUID DROP OUT TIME (TDROP)

ACTUAL VAPOR VELOCITY (UVA)

MINIMUM LENGTH FOR VAPOR LIQUID SEPARATION (LMIN)

HH

AH

HS

AS

tS

SELECTED tS

tH

SELECTED tH

AS

AH

2ND ITERATION :


(ALLA/AT)


SUMMARY


PROPOSED LENGTH (L)

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME



SELECTED LLA

(LLA/ID)

ALLA

HV =

HV =

SELECTED HV =

(HV/ID)

(AV/AT)

AV






HH

AH

HS

AS

tS

SELECTED tS

tH

SELECTED tH

AS

AH

3RD ITERATION :


(ALLA/AT)


SUMMARY


PROPOSED LENGTH (L)

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ITERASI ID L1 2150.0 MM 3650.0 MM

2 1900.0 MM 5100.0 MM

3 1700.0 MM 7000.0 MM

ALLA

HV =

HV =

SELECTED HV =

(HV/ID)

(AV/AT)

AV






HH

AH

HS

AS

tS

SELECTED tS

tH

SELECTED tH

AS

AH

Min 12.0 Inch

HLA

ID = 1900 MM

NLA

LLA

L = 3650 MM

TAG NO. : V-2701

TYPE : VERTICAL, 2-PHASE

CASE : MAXIMUM FLOW RATE


Refer to : W.Y. Svrcek, W.D. Monnery,"Design Two-Phase Separators Within the Right Limits"

145600 LB/HR

160160 LB/HR 10 % tolerance for design46100 LB/HR Note 1


0 LB/HR 10 % tolerance for design989.70 PSIA *

68.25 BARA

650 F *

343.3 C

38.83 LB/CUFT * Refer to Hysis Simulation

0 LB/CUFT * Refer to Hysis Simulation

16.49 * Refer to Hysis Simulation


YES

0.2714 Note 2

0.2714 Note 2

LB/CUFT


LB/CUFT


CUFT/SEC

11.094 CUFT/SEC * Refer to Hysis Simulation

CUFT/MIN

21.766 CUFT/MIN * Refer to Hysis Simulation

0.800 FPS Note 3

0.800 FPS * Take 75%~100% from gas velocity

217.658 CUFT * Table 2. Liquid holdup and surge times

108.829 CUFT * Table 2. Liquid holdup and surge times

2.000 * Table 5. (L/D) Ratio Guidelines

7.024 FT 2141.0 MM

7.054 FT 2150.0 MM

39.059 SQFT

467.729 CUFT

10.000 INCH 254.0 MM Tabel 3. Low Liquid Level Height

10.527 INCH 267.4 MM

10.527 INCH 254.0 MM

0.118

0.066 Tabel 6. Cylindrical height and area conversion

2.593 SQFT

1.411 FT 430.0 MM

Min 2.0 FT 609.6 MM Fig 2. Horizontal 2 phase separator

2.000 FT 609.6 MM

0.284

0.233

9.115 SQFT

11.937 FT 3638.4 MM

11.975 FT 3650.0 MM

2.501 SEC

1.217 FT/SEC

3.044 FT

11.975 FT

3.282 FT 1000.5 MM

18.176 SQFT

0.938 FT 285.9 MM

9.175 SQFT

7.054 FT 2150 MM

11.975 FT 3650 MM

1.698

* Table 7

17500 PSI

1/16 INCH 1.6 MM

0.850

1019.696 PSI * Design pressure

3.09 INCH 78.4 MM * Table 7

3.15 INCH 80.0 MM

2.984 INCH 75.8 MM * Design pressure


265.235 SQFT * Table 7


490.000 LB/CUFT * Table 3

47364.117 LB 21.5 TONNES


6.136 FT 1870.4 MM

6.234 FT 1900.0 MM

30.503 SQFT

510.390 CUFT


10.117 INCH 257.0 MM

10.117 INCH 254.0 MM

0.134


IF LHOLDUP-SURGE > LMIN THEN USE LHOLDUP-SURGE, IF LHOLDUP-SURGE < LMIN THEN INCREASE HV

2.426 SQFT

1.247 FT 380.0 MM


2.000 FT 609.6 MM

0.321

0.277

8.448 SQFT

16.633 FT 5069.6 MM

16.732 FT 5100.0 MM

2.501 SEC

0.354 FT/SEC

0.886 FT

16.732 FT

2.658 FT 810.3 MM

13.008 SQFT

0.742 FT 226.1 MM

6.621 SQFT

6.234 FT 1900 MM

16.732 FT 5100 MM

2.684

* Table 7

17500 PSI

1/16 INCH 1.6 MM

0.850



2.83 INCH 72.0 MM






47168.818 LB 21.4 TONNES


5.575 FT 1699.3 MM

5.577 FT 1700.0 MM

24.420 SQFT

560.816 CUFT


9.789 INCH 248.6 MM

9.789 INCH 254.0 MM

0.149



2.284 SQFT

1.115 FT 340.0 MM


2.000 FT 609.6 MM

0.359

0.322

7.873 SQFT

22.892 FT 6977.3 MM

22.966 FT 7000.0 MM

2.501 SEC

0.340 FT/SEC

0.850 FT

22.966 FT

2.165 FT 659.8 MM

9.477 SQFT

0.579 FT 176.6 MM

4.785 SQFT

5.577 FT 1700 MM

22.966 FT 7000 MM

4.118

* Table 7

17500 PSI

1/16 INCH 1.6 MM

0.850



2.52 INCH 64.0 MM






48358.917 LB 21.9 TONNES

(L/ID) W1.70 21.5 TONNES

2.68 21.4 TONNES

4.12 21.9 TONNES


HV = 609.6 MM

Min 12.0 Inch

HLA

Surge = 226.1 MM

NLA

Hold up = 810.3 MMLLA

HLL = 254.0 MM

L = 3650 MM


1456

THEN INCREASE HV

THEN INCREASE HV

THEN INCREASE HV

8.4 SQFT

HLA

6.6 SQFT

NLA

13.0 SQFTLLA

2.4 SQFT

AV =

AS =

AH =

ALL =

AV

ALL

AH

AS

PROJECT :




Refer to : W.Y. Svrcek, W.D. Monnery,"Successfully Specify Three-Phase Separators"

DESIGN BASIS


GAS RATE



AQUEOUS RATE


OPERATING PRESSURE

TEMPERATURE

LIQUID DENSITY

LIQUID VISCOSITY

AQUEOUS DENSITY

AQUEOUS VISCOSITY

MW GAS

GAS COMP. FACTOR


K FACTOR


CALCULATION

GAS DENSITY


ACTUAL GAS RATE

QV = ACTUAL GAS RATE REFER TO HYSIS FOR CHECK

LIQUID RATE

QLL =LIQUID RATE REFER TO HYSIS FOR CHECK

AQUEOUS RATE

QHV =AQUEOUS RATE REFER TO HYSIS FOR CHECK

GAS VELOCITY


TIME FOR HOLD UP

TIME FOR SURGE

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VH

VS

VH + VS

1 ST ITERATION :


ASSUME HV = 0.2 ID

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.4 ID

KS

SELECTED U

tS

SELECTED tS

tH

SELECTED tH

AS

AH

2 ND ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.5 ID

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

3 RD ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

4 TH ITERATION :


ASSUME HV = 0.6 ID

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.7 ID

KS

SELECTED U

tS

SELECTED tS

tH

SELECTED tH

AS

AH

5 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.7 ID

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

6 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

7 TH ITERATION :

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.2 ID

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)




HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.4 ID

KS

SELECTED U

tS

SELECTED tS

tH

SELECTED tH

AS

AH

8 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.6 ID

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

9 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

10 TH ITERATION :

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.7 ID

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN


S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.2 ID

KS

SELECTED U

tS

SELECTED tS

tH

SELECTED tH

AS

AH

11 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.4 ID

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

12 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

13 TH ITERATION :

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.6 ID

KS

SELECTED U

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VESSEL VOLUME

ASSUME HV = 0.7 ID

KS

SELECTED U

tS

SELECTED tS

tH

SELECTED tH

AS

AH

14 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLL

HLLL

SELECTED HLLL

(HLLL/ID)

(ALLL/AT)

ALLL

HW

L2

HHL = HLL

(HHL/ID)

(AHL/AT)

AHL

ALL

UHL

ULH

L = L1 + L2

USE L

f

NOTE :

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

SUMMARY :

ITERASI Hv Hv ID L

1 2 ASSUME HV = 0.20 ID 650.0 MM 3250.0 MM 3500.0 MM














tHL = tLH

L1

L1

SELECTED L1

UVA

LMIN

USE LMIN

L << LMIN

tS

SELECTED tS

tH

SELECTED tH

AS

AH

(L/ID) Assumption

then (L/ID) is set to value minimum 2

SUMMARY


PROPOSED LENGTH (L)

(L/ID)

L2

L1

304.8 MM OR 12 INCH

HV = 1625 MM

1320.2 MM

ID = 3250 MM HLL = 813 MM

(L/ID) = 2

HHL = 813 MM

L1 = 4377 MM

L = 6500 MM

3RD ITERATION IS SELECTED

HHLL = HW

ANLL

ANLL/AT

HNLL/ID

HNLL

HV

HLLL

HNLL

HHLL

HW

HHL

HLL

INTERFACE

HEAVY LIQUID

LIGHT LIQUID

GAS

TAG NO. : V-2701





235000 LB/HR 2350




2.74 BARA

100 F *

37.8 C


0.24 cP


0.682 cP



YES

0.3453 Note 2

0.3453 Note 2

LB/CUFT


CUFT/SEC


CUFT/MIN


CUFT/MIN


5.030 FPS Note 3


10.000 MIN * Refer to Tabel 6

5.000 * Refer to Tabel 6

185.185 CUFT

92.593 CUFT

277.778 CUFT


10.566 FT 3220.5 MM

10.663 FT 3250.0 MM

89.250 SQFT

2.133 FT 650.0 MM

2.000 FT 609.6 MM *Minimum

2.133 FT 650.0 MM

0.200

0.142

12.710 SQFT

12.331 INCH 313.2 MM

13.000 INCH 330.2 MM * Table 9

13.000 INCH 330.2 MM

0.102

0.053

4.744 SQFT

8.530 FT 2600.0 MM

3.869 FT 1179.3 MM

4.265 FT 1300.0 MM

0.400

0.373

4.855 SQFT

71.684 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

4.875 MIN

2.024 FT 617.1 MM

1.259 FT 383.9 MM

2.024 FT 617.1 MM

5.893 FT 1796.3 MM

5.906 FT 1800.0 MM

0.424 SEC

27.031 FT/SEC

11.460 FT 3493.1 MM

11.483 FT 3500.0 MM

11.483 FT 3500.0 MM

1.077

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

384.460 SQFT

123.926 SQFT

490.000 LB/CUFT

10165.128 LB 4.6 TONNES


10.566 FT 3220.5 MM

10.663 FT 3250.0 MM

89.250 SQFT

4.265 FT 1300.0 MM


4.265 FT 1300.0 MM

0.400

0.373

33.334 SQFT

12.331 INCH 313.2 MM

13.000 INCH 330.2 MM * Table 9

13.000 INCH 330.2 MM

0.102

0.053

4.744 SQFT

6.398 FT 1950.0 MM

5.428 FT 1654.5 MM

3.199 FT 975.0 MM

0.300

0.252

3.281 SQFT

52.635 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

3.657 MIN

30.129 FT 9183.4 MM

0.029 FT 9.0 MM

30.129 FT 9183.4 MM

35.558 FT 10837.9 MM

35.597 FT 10850.0 MM

0.848 SEC

10.307 FT/SEC

8.740 FT 2663.8 MM

8.858 FT 2700.0 MM

35.597 FT 10850.0 MM

3.338

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

1191.826 SQFT

123.926 SQFT

490.000 LB/CUFT

23144.436 LB 10.5 TONNES


10.566 FT 3220.5 MM

10.663 FT 3250.0 MM

89.250 SQFT

5.331 FT 1625.0 MM


5.331 FT 1625.0 MM

0.500

0.500

44.624 SQFT

12.331 INCH 313.2 MM

13.000 INCH 330.2 MM * Table 9

13.000 INCH 330.2 MM

0.102

0.053

4.744 SQFT

5.331 FT 1625.0 MM

6.965 FT 2122.9 MM

2.666 FT 812.5 MM

0.250

0.196

2.542 SQFT

42.084 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

3.047 MIN

12.353 FT 3765.3 MM

0.061 FT 18.7 MM

12.353 FT 3765.3 MM

19.318 FT 5888.3 MM

19.357 FT 5900.0 MM

1.060 SEC

7.699 FT/SEC

8.161 FT 2487.4 MM

8.202 FT 2500.0 MM

21.325 FT 6500.0 MM

2.000

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

713.997 SQFT

123.926 SQFT

490.000 LB/CUFT

15462.805 LB 7.0 TONNES


10.566 FT 3220.5 MM

10.663 FT 3250.0 MM

89.250 SQFT

0.000 CUFT

6.398 FT 1950.0 MM


6.398 FT 1950.0 MM

0.600

0.627

55.916 SQFT

12.331 INCH 313.2 MM

13.000 INCH 330.2 MM * Table 9

13.000 INCH 330.2 MM

0.102

0.053

4.744 SQFT

4.265 FT 1300.0 MM

9.716 FT 2961.4 MM

2.133 FT 650.0 MM

0.200

0.142

1.851 SQFT

31.482 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

2.438 MIN

10.138 FT 3090.0 MM

0.082 FT 25.0 MM

10.138 FT 3090.0 MM

19.854 FT 6051.4 MM

20.013 FT 6100.0 MM

1.272 SEC

6.144 FT/SEC

7.815 FT 2382.0 MM

7.874 FT 2400.0 MM

20.013 FT 6100.0 MM

1.877

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

670.059 SQFT

123.926 SQFT

490.000 LB/CUFT

14756.448 LB 6.7 TONNES


10.566 FT 3220.5 MM

10.663 FT 3250.0 MM

89.250 SQFT

0.000 CUFT

7.464 FT 2275.0 MM


7.464 FT 2275.0 MM

0.700

0.748

66.730 SQFT

12.331 INCH 313.2 MM

13.000 INCH 330.2 MM * Table 9

13.000 INCH 330.2 MM

0.102

0.053

4.744 SQFT

3.199 FT 975.0 MM

15.627 FT 4763.1 MM

1.599 FT 487.5 MM

0.150

0.094

1.222 SQFT

21.297 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

1.828 MIN

9.193 FT 2802.0 MM

0.109 FT 33.3 MM

9.193 FT 2802.0 MM

24.820 FT 7565.0 MM

24.934 FT 7600.0 MM

1.484 SEC

5.149 FT/SEC

7.640 FT 2328.7 MM

7.710 FT 2350.0 MM

24.934 FT 7600.0 MM

2.338

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

834.827 SQFT

123.926 SQFT

490.000 LB/CUFT

17405.286 LB 7.9 TONNES


10.566 FT 3220.5 MM

10.663 FT 3250.0 MM

89.250 SQFT

0.000 CUFT

6.931 FT 2112.5 MM


6.931 FT 2112.5 MM

0.650

0.688

61.414 SQFT

12.331 INCH 313.2 MM

13.000 INCH 330.2 MM * Table 9

13.000 INCH 330.2 MM

0.102

0.053

4.744 SQFT

3.732 FT 1137.5 MM

12.029 FT 3666.5 MM

1.866 FT 568.7 MM

0.175

0.118

1.528 SQFT

26.308 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

2.133 MIN

7.188 FT 2190.8 MM

0.120 FT 36.7 MM

7.188 FT 2190.8 MM

19.217 FT 5857.3 MM

19.357 FT 5900.0 MM

1.378 SEC

5.594 FT/SEC

7.708 FT 2349.5 MM

7.710 FT 2350.0 MM

19.357 FT 5900.0 MM

1.815

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

648.090 SQFT

123.926 SQFT

490.000 LB/CUFT

14403.270 LB 6.5 TONNES


9.230 FT 2813.3 MM

9.350 FT 2850.0 MM

68.632 SQFT

0.000 CUFT

1.870 FT 570.0 MM


2.000 FT 609.6 MM

0.214

0.157

10.759 SQFT

11.675 INCH 296.5 MM

12.000 INCH 304.8 MM * Table 9

12.000 INCH 304.8 MM

0.107

0.057

3.933 SQFT

7.350 FT 2240.4 MM

5.150 FT 1569.6 MM

3.675 FT 1120.2 MM

0.393

0.365

4.378 SQFT

53.496 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

4.201 MIN

5.896 FT 1797.1 MM

0.100 FT 30.4 MM

5.896 FT 1797.1 MM

11.046 FT 3366.7 MM

11.155 FT 3400.0 MM

0.398 SEC

31.934 FT/SEC

12.697 FT 3870.2 MM

12.795 FT 3900.0 MM

12.795 FT 3900.0 MM

1.368

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

375.672 SQFT

95.299 SQFT

490.000 LB/CUFT

9103.412 LB 4.1 TONNES


9.230 FT 2813.3 MM

9.350 FT 2850.0 MM

68.632 SQFT

0.000 CUFT

3.740 FT 1140.0 MM


3.740 FT 1140.0 MM

0.400

0.373

25.633 SQFT

11.675 INCH 296.5 MM

12.000 INCH 304.8 MM * Table 9

12.000 INCH 304.8 MM

0.107

0.057

3.933 SQFT

5.610 FT 1710.0 MM

7.111 FT 2167.3 MM

2.805 FT 855.0 MM

0.300

0.252

3.028 SQFT

39.971 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

3.207 MIN

5.452 FT 1661.7 MM

0.119 FT 36.3 MM

5.452 FT 1661.7 MM

12.562 FT 3829.0 MM

12.795 FT 3900.0 MM

0.744 SEC

13.403 FT/SEC

9.966 FT 3037.7 MM

10.007 FT 3050.0 MM

12.795 FT 3900.0 MM

1.368

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

375.672 SQFT

95.299 SQFT

490.000 LB/CUFT

9103.412 LB 4.1 TONNES


9.230 FT 2813.3 MM

9.350 FT 2850.0 MM

68.632 SQFT

0.000 CUFT

5.610 FT 1710.0 MM


5.610 FT 1710.0 MM

0.600

0.627

42.999 SQFT

11.675 INCH 296.5 MM

12.000 INCH 304.8 MM * Table 9

12.000 INCH 304.8 MM

0.107

0.057

3.933 SQFT

3.740 FT 1140.0 MM

12.801 FT 3901.7 MM

1.870 FT 570.0 MM

0.200

0.142

1.709 SQFT

23.924 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

2.138 MIN

39.945 FT 12175.4 MM

0.036 FT 10.8 MM

39.945 FT 12175.4 MM

52.746 FT 16077.1 MM

52.822 FT 16100.0 MM

1.115 SEC

7.990 FT/SEC

8.912 FT 2716.4 MM

9.022 FT 2750.0 MM

52.822 FT 16100.0 MM

5.649

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

1550.852 SQFT

95.299 SQFT

490.000 LB/CUFT

27995.743 LB 12.7 TONNES


9.230 FT 2813.3 MM

9.350 FT 2850.0 MM

68.632 SQFT

0.000 CUFT

6.545 FT 1995.0 MM


6.545 FT 1995.0 MM

0.700

0.748

51.315 SQFT

11.675 INCH 296.5 MM

12.000 INCH 304.8 MM * Table 9

12.000 INCH 304.8 MM

0.107

0.057

3.933 SQFT

2.805 FT 855.0 MM

20.755 FT 6326.0 MM

1.403 FT 427.5 MM

0.150

0.094

1.128 SQFT

16.189 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

1.603 MIN

19.050 FT 5806.5 MM

0.074 FT 22.4 MM

19.050 FT 5806.5 MM

39.805 FT 12132.6 MM

39.862 FT 12150.0 MM

1.301 SEC

6.695 FT/SEC

8.712 FT 2655.5 MM

8.858 FT 2700.0 MM

39.862 FT 12150.0 MM

4.263

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.394 INCH 10.0 MM


0.394 INCH 10.0 MM * Table 8

1170.364 SQFT

95.299 SQFT

490.000 LB/CUFT

21878.964 LB 9.9 TONNES


8.386 FT 2556.1 MM

8.530 FT 2600.0 MM

57.120 SQFT

0.000 CUFT

1.706 FT 520.0 MM


2.000 FT 609.6 MM

0.234

0.179

10.202 SQFT

11.265 INCH 286.1 MM

12.000 INCH 304.8 MM * Table 9

12.000 INCH 304.8 MM

0.117

0.066

3.746 SQFT

6.530 FT 1990.4 MM

6.434 FT 1961.2 MM

3.265 FT 995.2 MM

0.383

0.352

4.225 SQFT

42.693 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

3.732 MIN

7.058 FT 2151.4 MM

0.098 FT 29.7 MM

7.058 FT 2151.4 MM

13.493 FT 4112.5 MM

13.615 FT 4150.0 MM

0.398 SEC

33.676 FT/SEC

13.390 FT 4081.3 MM

13.451 FT 4100.0 MM

13.615 FT 4150.0 MM

1.596

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.315 INCH 8.0 MM


0.394 INCH 10.0 MM * Table 8

364.688 SQFT

79.313 SQFT

490.000 LB/CUFT

7240.293 LB 3.3 TONNES


8.386 FT 2556.1 MM

8.530 FT 2600.0 MM

57.120 SQFT

0.000 CUFT

3.412 FT 1040.0 MM


3.412 FT 1040.0 MM

0.400

0.373

21.334 SQFT

11.265 INCH 286.1 MM

12.000 INCH 304.8 MM * Table 9

12.000 INCH 304.8 MM

0.117

0.066

3.746 SQFT

5.118 FT 1560.0 MM

8.670 FT 2642.5 MM

2.559 FT 780.0 MM

0.300

0.252

3.028 SQFT

32.758 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

2.925 MIN

6.468 FT 1971.3 MM

0.116 FT 35.4 MM

6.468 FT 1971.3 MM

15.137 FT 4613.8 MM

15.256 FT 4650.0 MM

0.678 SEC

16.105 FT/SEC

10.925 FT 3329.8 MM

10.991 FT 3350.0 MM

15.256 FT 4650.0 MM

1.788

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.315 INCH 8.0 MM



408.626 SQFT

79.313 SQFT

490.000 LB/CUFT

10113.204 LB 4.6 TONNES


8.386 FT 2556.1 MM

8.530 FT 2600.0 MM

57.120 SQFT

0.000 CUFT

5.118 FT 1560.0 MM


5.118 FT 1560.0 MM

0.600

0.627

35.786 SQFT

11.265 INCH 286.1 MM

12.000 INCH 304.8 MM * Table 9

12.000 INCH 304.8 MM

0.117

0.066

3.746 SQFT

3.412 FT 1040.0 MM

15.794 FT 4813.9 MM

1.706 FT 520.0 MM

0.200

0.142

1.709 SQFT

19.625 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

1.950 MIN

38.430 FT 11713.4 MM

0.040 FT 12.0 MM

38.430 FT 11713.4 MM

54.223 FT 16527.3 MM

54.298 FT 16550.0 MM

1.018 SEC

9.601 FT/SEC

9.769 FT 2977.5 MM

9.843 FT 3000.0 MM

54.298 FT 16550.0 MM

6.365

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.315 INCH 8.0 MM



1454.357 SQFT

79.313 SQFT

490.000 LB/CUFT

20744.397 LB 9.4 TONNES


8.386 FT 2556.1 MM

8.530 FT 2600.0 MM

57.120 SQFT

0.000 CUFT

5.971 FT 1820.0 MM


5.971 FT 1820.0 MM

0.700

0.748

42.707 SQFT

11.265 INCH 286.1 MM

12.000 INCH 304.8 MM * Table 9

12.000 INCH 304.8 MM

0.117

0.066

3.746 SQFT

2.559 FT 780.0 MM

26.042 FT 7937.5 MM

1.280 FT 390.0 MM

0.150

0.094

1.128 SQFT

13.284 SQFT

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

10.498 INCH/MIN

1.463 MIN

20.882 FT 6364.9 MM

0.075 FT 22.8 MM

20.882 FT 6364.9 MM

46.924 FT 14302.3 MM

46.916 FT 14300.0 MM

1.187 SEC

8.045 FT/SEC

9.550 FT 2910.8 MM

9.678 FT 2950.0 MM

46.916 FT 14300.0 MM

5.500

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.315 INCH 8.0 MM



1256.635 SQFT

79.313 SQFT

490.000 LB/CUFT

18201.513 LB 8.3 TONNES

(L/ID) W

1.08 4.61 TONNES 1800.0 MM 3500.0 MM NOT OKE OKE NOT OKE

3.34 10.50 TONNES 10850.0 MM 2700.0 MM OKE NOT OKE NOT OKE

2.00 7.01 TONNES 5900.0 MM 2500.0 MM OKE OKE OKE




1.37 4.13 TONNES 3400.0 MM 3900.0 MM NOT OKE OKE NOT OKE

1.37 4.13 TONNES 3900.0 MM 3050.0 MM OKE OKE NOT OKE







L for Hold up and surge

L for vapor liquid

separation

5.331 FT 1625.0 MM

31.332 SQFT

0.351

0.382

4.073 FT 1241.4 MM

10.663 FT 3250 MM

21.325 FT 6500 MM

2.000

5.331 FT 1625 MM

1.083 FT 330 MM

4.073 FT 1241 MM

5.331 FT 1625 MM

5.331 FT 1625 MM

2.666 FT 813 MM

2.666 FT 813 MM

6.965 FT 2123 MM

14.361 FT 4377 MM

304.8 MM OR 12 INCH

1320.2 MM

HHLL = 384 MM

1ST HIGH ALARM

HNLL = 911 MM NORMAL LEVELFOR LIGHT LIQUID HOLD UP AND SURGE

1ST LOW ALARM

HLLL = 330 MM

L1 = 4377 MM

L2 = 2123 MM

L = 6500 MM

LIGHT LIQUID

PROJECT :





DESIGN BASIS


GAS RATE



AQUEOUS RATE


OPERATING PRESSURE

TEMPERATURE

LIQUID DENSITY

LIQUID VISCOSITY

AQUEOUS DENSITY

AQUEOUS VISCOSITY

MW GAS

GAS COMP. FACTOR


K FACTOR


CALCULATION

GAS DENSITY


ACTUAL GAS RATE

QV = ACTUAL GAS RATE REFER TO HYSIS FOR CHECK

LIQUID RATE

QLL =LIQUID RATE REFER TO HYSIS FOR CHECK

AQUEOUS RATE

QHV =AQUEOUS RATE REFER TO HYSIS FOR CHECK

GAS VELOCITY


TIME FOR HOLD UP

TIME FOR SURGE

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

VH

VS

VH + VS

1 ST ITERATION :


ASSUME HV = 0.2 ID

L

SELECTED L

f

SELECTED L

SELECTED L

KS

SELECTED U

L

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

UVA

LMIN

UHL

ULH

tHL

fLL

tS

SELECTED tS

tH

SELECTED tH

AS

AH

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.5 ID

L

SELECTED L

f

SELECTED L

SELECTED L

KS

SELECTED U

L

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

2 ND ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

UVA

LMIN

UHL

ULH

tHL

fLL

tS

SELECTED tS

tH

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.7 ID

L

SELECTED L

f

SELECTED L

SELECTED L

KS

SELECTED U

L

SELECTED L

(L/ID)



SELECTED tH

AS

AH

3 RD ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

UVA

LMIN

UHL

ULH

tHL

fLL

S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.2 ID

L

SELECTED L

f

SELECTED L

SELECTED L

KS

SELECTED U

tS

SELECTED tS

tH

SELECTED tH

AS

AH

4 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

UVA

LMIN

UHL

ULH

tHL

fLL

L

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.5 ID

L

SELECTED L

f

SELECTED L

SELECTED L

KS

tS

SELECTED tS

tH

SELECTED tH

AS

AH

5 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

UVA

LMIN

UHL

SELECTED U

L

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.7 ID

L

SELECTED L

f

ULH

tHL

fLL

tS

SELECTED tS

tH

SELECTED tH

AS

AH

6 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

UVA

SELECTED L

SELECTED L

KS

SELECTED U

L

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.2 ID

LMIN

UHL

ULH

tHL

fLL

tS

SELECTED tS

tH

SELECTED tH

AS

AH

7 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

L

SELECTED L

f

SELECTED L

SELECTED L

KS

SELECTED U

L

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.5 ID

UVA

LMIN

UHL

ULH

tHL

fLL

tS

SELECTED tS

tH

SELECTED tH

AS

AH

8 TH ITERATION :


HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

L

SELECTED L

f

SELECTED L

SELECTED L

KS

SELECTED U

L

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

ASSUME (L/ID)

DIAMETER (ID)

SELECTED ID

ASSUME HV = 0.7 ID

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

UVA

LMIN

UHL

ULH

tHL

fLL

tS

SELECTED tS

tH

SELECTED tH

AS

AH

9 TH ITERATION :


L

SELECTED L

f

SELECTED L

SELECTED L

KS

SELECTED U

L

SELECTED L

(L/ID)



S

CORROSION ALLOWANCE


P

r

W

HV

HV

SELECTED HV =

(HV/ID)

(AV/AT)

AV

HLLV

HLLB

(HLLV/ID)

(ALLV/AT)

ALLV

UVA

LMIN

UHL

ULH

tHL

fLL

tS

SELECTED tS

tH

SELECTED tH

AS

AH

SUMMARY :

ITERASI Hv Hv ID L










then (L/ID) is set to value minimum 3

ASSUME HHL = 12 INCH

SUMMARY


PROPOSED LENGTH (L)

(L/ID)

MINIMUM 12 INCH OR = 304.8 MM

HV = 609.6 MM

304.8 MM

ID = 1800 MM HNLL = 886 MM

FOR LIGHT LIQUID HOLD UP AND SURGEHHLL = 1190.4 MM

(L/ID) = 3

(L/ID) Assumption

4TH ITERATION IS SELECTED

HHLL

HNLL

ULH

DB

tLH

fHL

HV

HHLL

HNLL

HLLV

HLLB

HHL

DB

GAS

HLLV = 304.8 MM

HLLB = 152.4 MM

HHL = 304.8 MM

L = 5400.0 MM

TAG NO. : V-2701





235000 LB/HR 2350




2.74 BARA

100 F *

37.8 C


0.24 cP


0.682 cP



YES

0.3453 Note 2

0.3453 Note 2

LB/CUFT


CUFT/SEC


CUFT/MIN


CUFT/MIN


5.030 FPS Note 3


10.000 MIN * Refer to Tabel 6

5.000 * Refer to Tabel 6

185.185 CUFT

92.593 CUFT

277.778 CUFT


6.656 FT 2028.8 MM

6.726 FT 2050.0 MM

35.510 SQFT

1.345 FT 410.0 MM


2.000 FT 609.6 MM

0.297

0.249

8.852 SQFT

12.000 INCH 304.8 MM * Minimum


0.149

0.093

3.295 SQFT

11.890 FT 3624.1 MM

11.975 FT 3650.0 MM

0.398 SEC

38.813 FT/SEC

15.433 FT 4703.9 MM

15.420 FT 4700.0 MM

15.420 FT 4700.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

4.315 MIN

22.197 MIN OKE

15.420 FT 4700.0 MM

15.420 FT 4700.0 MM

2.293

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.315 INCH 8.0 MM






5456.405 LB 2.5 TONNES


6.656 FT 2028.8 MM

6.726 FT 2050.0 MM

35.510 SQFT

3.363 FT 1025.0 MM


3.363 FT 1025.0 MM

0.500

0.500

17.754 SQFT



0.149

0.093

3.295 SQFT

19.210 FT 5855.2 MM

11.975 FT 3650.0 MM

0.669 SEC

19.351 FT/SEC

12.938 FT 3943.4 MM

12.959 FT 3950.0 MM

12.959 FT 3950.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

3.766 MIN

12.425 MIN OKE

12.959 FT 3950.0 MM

12.959 FT 3950.0 MM

1.927

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.315 INCH 8.0 MM






4788.082 LB 2.2 TONNES


6.656 FT 2028.8 MM

6.726 FT 2050.0 MM

35.510 SQFT

4.708 FT 1435.0 MM


4.708 FT 1435.0 MM

0.700

0.748

26.550 SQFT



0.149

0.093

3.295 SQFT

49.039 FT 14947.1 MM

49.049 FT 14950.0 MM

0.936 SEC

12.940 FT/SEC

12.112 FT 3691.8 MM

12.139 FT 3700.0 MM

49.049 FT 14950.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

3.225 MIN

23.731 MIN OKE

49.049 FT 14950.0 MM

49.049 FT 14950.0 MM

7.293

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.315 INCH 8.0 MM



1035.845 SQFT * Table 8



14590.143 LB 6.6 TONNES


5.815 FT 1772.3 MM

5.906 FT 1800.0 MM

27.377 SQFT

1.181 FT 360.0 MM


2.000 FT 609.6 MM

0.339

0.298

8.164 SQFT



0.169

0.112

3.068 SQFT

17.205 FT 5244.2 MM

17.224 FT 5250.0 MM

0.398 SEC

42.084 FT/SEC

16.733 FT 5100.3 MM

16.732 FT 5100.0 MM

17.224 FT 5250.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

3.985 MIN

17.870 MIN OKE

17.224 FT 5250.0 MM

17.717 FT 5400.0 MM

3.000

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.236 INCH 6.0 MM






3814.140 LB 1.7 TONNES


5.815 FT 1772.3 MM

5.906 FT 1800.0 MM

27.377 SQFT

2.953 FT 900.0 MM


2.953 FT 900.0 MM

0.500

0.500

13.688 SQFT



0.169

0.112

3.068 SQFT

26.154 FT 7971.8 MM

26.247 FT 8000.0 MM

0.587 SEC

25.100 FT/SEC

14.734 FT 4491.1 MM

14.764 FT 4500.0 MM

26.247 FT 8000.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

3.601 MIN

19.402 MIN OKE

26.247 FT 8000.0 MM

26.247 FT 8000.0 MM

4.444

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.236 INCH 6.0 MM






5427.894 LB 2.5 TONNES


5.815 FT 1772.3 MM

5.906 FT 1800.0 MM

27.377 SQFT

4.134 FT 1260.0 MM


4.134 FT 1260.0 MM

0.700

0.748

20.469 SQFT



0.169

0.112

3.068 SQFT

72.346 FT 22051.0 MM

72.343 FT 22050.0 MM

0.822 SEC

16.785 FT/SEC

13.794 FT 4204.5 MM

13.780 FT 4200.0 MM

72.343 FT 22050.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

3.126 MIN

26.985 MIN OKE

72.343 FT 22050.0 MM

72.343 FT 22050.0 MM

12.250

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.236 INCH 6.0 MM



1341.470 SQFT * Table 8



13672.709 LB 6.2 TONNES


5.283 FT 1610.2 MM

5.413 FT 1650.0 MM

23.004 SQFT

1.083 FT 330.0 MM


2.000 FT 609.6 MM

0.369

0.336

7.722 SQFT



0.185

0.127

2.923 SQFT

22.475 FT 6850.3 MM

22.474 FT 6850.0 MM

0.398 SEC

44.493 FT/SEC

17.691 FT 5392.4 MM

17.717 FT 5400.0 MM

22.474 FT 6850.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

3.787 MIN

18.547 MIN OKE

22.474 FT 6850.0 MM

22.474 FT 6850.0 MM

4.152

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.236 INCH 6.0 MM






4300.945 LB 2.0 TONNES


5.283 FT 1610.2 MM

5.413 FT 1650.0 MM

23.004 SQFT

2.707 FT 825.0 MM


2.707 FT 825.0 MM

0.500

0.500

11.502 SQFT



0.185

0.127

2.923 SQFT

32.377 FT 9868.5 MM

32.480 FT 9900.0 MM

0.538 SEC

29.871 FT/SEC

16.074 FT 4899.3 MM

16.076 FT 4900.0 MM

32.480 FT 9900.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

3.502 MIN

20.175 MIN OKE

32.480 FT 9900.0 MM

32.480 FT 9900.0 MM

6.000

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.236 INCH 6.0 MM






5941.595 LB 2.7 TONNES


5.283 FT 1610.2 MM

5.413 FT 1650.0 MM

23.004 SQFT

3.789 FT 1155.0 MM


3.789 FT 1155.0 MM

0.700

0.748

17.200 SQFT



0.185

0.127

2.923 SQFT

96.401 FT 29383.0 MM

96.457 FT 29400.0 MM

0.753 SEC

19.975 FT/SEC

15.048 FT 4586.8 MM

15.092 FT 4600.0 MM

96.457 FT 29400.0 MM

0.333 * Table 1

29.831 INCH/MIN

10.498 INCH/MIN

29.831 INCH/MIN

3.067 MIN

30.233 MIN OKE

96.457 FT 29400.0 MM

96.457 FT 29400.0 MM

17.818

* Table 8

17500 PSI

1/16 INCH 1.6 MM

0.850



0.236 INCH 6.0 MM



1639.574 SQFT * Table 8



16430.995 LB 7.5 TONNES

(L/ID) W

2.29 2.47 TONNES 3650.0 MM 4700.0 MM NOT OKE NOT OKE NOT OKE

1.93 2.17 TONNES 3650.0 MM 3950.0 MM NOT OKE OKE OKE








3.906 FT 1190.4 MM

2.906 FT 885.6 MM

10.498 INCH/MIN

1.713 FT 522.3 MM

1.143 MIN

18.290 MIN OKE

5.906 FT 1800.0 MM

17.717 FT 5400.0 MM

3.000

2.000 FT 609.6 MM

3.906 FT 1190.4 MM

2.906 FT 885.6 MM

1.000 FT 304.8 MM

0.500 FT 152.4 MM

1.000 FT 304.8 MM

1.713 FT 522.3 MM

MINIMUM 12 INCH OR = 304.8 MM

304.8 MM

NORMAL LEVEL

L for Hold up and surge

L for vapor liquid

separation

LIGHT LIQUID

DB = 522.3 MM

L = 5400.0 MM

HEAVY LIQUID

INTERFACE

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Default Separator Calculation