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Compressor Sizing Cal

This document provides calculations for selecting and sizing a booster compressor with two stages. It includes process parameters like flow rates, pressures, temperatures. It then calculates the compressor power required, number of impellers, stage ratios, and determines that one stage is sufficient based on the overall and maximum stage pressure ratios. The power required for the gas engine and deratings due to altitude and temperature are also calculated.
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100% found this document useful (1 vote)
553 views2 pages

Compressor Sizing Cal

This document provides calculations for selecting and sizing a booster compressor with two stages. It includes process parameters like flow rates, pressures, temperatures. It then calculates the compressor power required, number of impellers, stage ratios, and determines that one stage is sufficient based on the overall and maximum stage pressure ratios. The power required for the gas engine and deratings due to altitude and temperature are also calculated.
Copyright
© Attribution Non-Commercial (BY-NC)
We take content rights seriously. If you suspect this is your content, claim it here.
Available Formats
Download as XLS, PDF, TXT or read online on Scribd
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UMUECHEM BOOSTER COMPRESSOR SELECTION AND SIZING - BASE CASE - FIRST STAGE

A. PROCESS PARAMETERS: STAGE CALCULATIONS

Discharge Pressure Stage Specific Power


DESCRIPTION SUCTION DISCHARGE Stage Suction Pressure (ps) Suction Pressure (ps)- Discharge Pressure
Pressure Ratio - r Disch. Temp (Td) Absorbed (from chart
Stage Shaft Absorbed
2nd formular (pd) (pd)-2nd formular Power (KW)
1.2.3-4b)

1 Flow Rates 1 3.300 3.431 11.942 11.998 3.636 348.442 0.700 494.768

SYMBOL VALUE SYMBOL VALUE

Standard MMscf/d 6.9 6.9

Standard m3/h 8139.86 8139.86

Standard m3/s qs(st) 2.26 qd(st) 2.26

COMPRESSOR POWER [kW]

2 Pressures (Bar) Total Shaft Power (Including 5% for data inacuracies) 519.51

Gauge 2.5 10.2 Total Driver Power (Including 4% for transmission losses) 540.29

Absolute Ps 3.5 Pd 11.2

GAS ENGINE DERATING

3 Temperatures Altitude (-3.5% ISO for every 300 m above 150 m) Sea Level 0.00

Shell Petroleum Development Company of Nigeria


C
o
39.6 137.8 Temperature (-1.8% ISO for every 50C above 300C) 4.68% 565.57

K Ts 312.6 Td 410.8

4 Compressibility Factor Stage Polytropic Head [Hp] 214.29

Z Zs 0.9892 Zd 0.9871 No. of Impellers 7.14

Av. Comp. Fac Zav 0.9521

Polytropic Eff. (table


5 1.2.3-1)

Minimum np 0.800 NOTES

Maximum np 1.000 1 The calculations here presented are done in line with procedure outlined
Average np 0.900 in Production Handbook Vol. 9, Chapter 1, Section 1.2.3,

pages1-89 to 1-107.

Adiabatic exponent
6 for gas (Cp/Cv)

Minimum Cp/Cv 1.220 2 Indicates selected option in line with guidelines as stated

Maximun Cp/Cv 1.250 in Production Handbook.

Average k 1.235 3 Indicates Manual data input.

Polytropic exponent
7 for gas n 1.268

n-1 0.268

n/(n-1) 4.730

(n-1)/n 0.211

B. GENERAL CALCULATIONS

1 Actual Vol. [m3/s] qs 0.702 qd 0.288

2 Actual press. (bar)

ps1(large) 3.431 pdN (large) 11.592


ps1(small) 3.300 pdN (small) 11.550

Calculation Spreadsheet
Overall pressure ratio
3 (pdN/ps1) ro 3.51

4 Max. Stage Ratio rs 3.64

No. of Stages
5 (Logro/Logrs) Q 0.97 Nearest Whole No. 1

Theoretical Stage
6 Press. Ratio rQ 3.51

AGS-TEF-OTU-M14-00001-000 1 of 2 Mechanical Datasheet Otumara Main Compressor Package


UMUECHEM BOOSTER COMPRESSOR SELECTION AND SIZING - BASE CASE - SECOND STAGE
A. PROCESS PARAMETERS: STAGE CALCULATIONS

Discharge Pressure Stage Specific Power


DESCRIPTION SUCTION DISCHARGE Stage Suction Pressure (ps) Suction Pressure (ps)- Discharge Pressure
Pressure Ratio - r Disch. Temp (Td) Absorbed (from Chart
Stage Shaft Absorbed
2nd formular (pd) (pd)-2nd formular Power (KW)
1.2.3-4a)

1 Flow Rates: 1 10.800 10.784 18.126 18.398 1.706 286.969 0.255 525.301

SYMBOL VALUE SYMBOL VALUE

Standard MMscf/d 19.9 19.9

Standard m3/h 23475.84 23475.84

Standard m3/s qs(st) 6.52 qd(st) 6.52

COMPRESSOR POWER [kW]

2 Pressures (Bar) Total Shaft Power (Including 5% for data inacuracies) 551.57

Gauge 10 16.2 Total Driver Power (Including 4% for transmission losses) 573.63

Absolute Ps 11 Pd 17.2

GAS ENGINE DERATING

3 Temperatures Altitude (-3.5% ISO for every 300 m above 150 m) Sea Level 0.00

C
o
42.9 81.6 Temperature (-1.8% ISO for every 50C above 300C) 4.68% 600.47

Shell Petroleum Development Company of Nigeria


K Ts 315.9 Td 354.6

Compressibility
4 Factors

Z Zs 0.9705 Zd 0.9694

Av. Comp. Fac Zav 0.9400

Polytropic Efficiency
5 (table 1.2.3-1)

Minimum np 0.50 NOTES

Maximum np 1.00 1 The calculations here presented are done in line with procedure outlined
Average np 0.75 in Production Handbook Vol. 9, Chapter 1, Section 1.2.3,

pages1-89 to 1-107.

Adiabatic exponent Indicates Manual data input.


6 for gas (Cp/Cv) 2

Minimum Cp/Cv 1.270 3 Indicates selected option in line with guidelines as stated

Maximun Cp/Cv 1.280 in Production Handbook.

Average k 1.275

Polytropic exponent
7 for gas n 1.40

n-1 0.40

n/(n-1) 3.48

(n-1)/n 0.29

B. GENERAL CALCULATIONS

1 Actual Vol. [m3/s] qs 0.639 qd 0.458

2 Actual press. (bar)


ps1(small) 10.784 pdN (large) 17.802
ps1(large) 10.800 pdN (small) 17.550

Calculation Spreadsheet
Overall pressure ratio
3 (pdN/ps1) ro 1.65

4 Max. Stage Ratio rs 1.71

Number of Stages
5 (Logro/Logrs) Q 0.93 Nearest Whole No. 1

Theoretical Stage
6 Press. Ratio rQ 1.65

AGS-TEF-OTU-M14-00001-000 2 of 2 Mechanical Datasheet Otumara Main Compressor Package

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