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Gas Compression Part II

Gas Compression Part II. Ref.1: Kumar, Gas Production Engineering, Gulf Publishing Com ., 1987, Chapter 9. Ref.2: GPSA Electronic Data Book, Gas Processors Association , 1998, Chapter 13.

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Gas Compression Part II

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  1. Gas CompressionPart II Ref.1: Kumar, Gas Production Engineering, Gulf Publishing Com., 1987, Chapter 9. Ref.2: GPSA Electronic Data Book, Gas Processors Association, 1998, Chapter 13. Ref.3: Mokhatab et al, Handbook of Natural Gas Transmission and Processing, Gulf Publishing Com., 2006, Chapter 8.

  2. Gas CompressionReciprocating Compressors Number of Stages: Calculate the overall compression ratio (rt). If the compression ratio is under 4, consider using one stage. If it is not, select an initial number of stages (ns) based on the following equation (3% pressure drop was assumed in each coolers): Calculate the discharge gas temperature for the first stage. If the discharge temperature is too high (more than 300 oF), either increase the number of stages or reduce the suction temperature through precooling.

  3. Gas CompressionReciprocating Compressors BHP of each stage: Calculate the ideal head of each stage based on the Isentropic assumption, then calculate the GHP and BHP with using isentropic and mechanical efficiency: Gas flow rate at suction conditions: Gas flow rate at suction conditions is required for capacity calculation of each stage.

  4. Gas CompressionReciprocating Compressors Capacity (or speed) of each stage: For single acting: For double acting: Stroke length Piston diameter Rod diameter

  5. Gas CompressionReciprocating Compressors Volumetric efficiency: The term “volumetric efficiency” refers to the actual pumping capacity of a cylinder compared to the piston displacement. Where: Subtract about 0.05 from volumetric efficiency when a non-lubricated compressor is used.

  6. Gas CompressionCentrifugal Compressors Number of Stages: The total polytropic head (Hpt) is an indication of the number of stages required for centrifugal compression: Or from Fig 13-39: The discharge temperature must be less than 350 oF

  7. Gas CompressionCentrifugal Compressors BHP of all stages (one unit): Calculate the ideal head of all stages based on the polytropic assumption, then: 1- Calculate the GHP with using polytropic efficiency: 2- Calculate the BHP with using mechanical losses:

  8. Gas Compression Centrifugal Compressors Capacity (or speed):

  9. Gas CompressionCentrifugal Compressors Performance Curves: Generally, the performance of a centrifugal compressor follows the “affinity laws.”According to the affinity laws, as the rotational speed of the centrifugal compressor is changed, the inlet flow and head vary as the speed and the square of the speed, respectively As the speed deviates from the design speed, the error of “affinity laws” will increase.

  10. Gas Compression Centrifugal Compressors Stone wall Limit

  11. Gas Compression Centrifugal Compressors Surge Line Control: In all modern centrifugal compressors, a recycle line with a control valve that allows the flow to increase through the compressor is used for surge control. The flow through the compressor must be 10-20% greater than surge limit. SC

  12. Gas Compression Example • Pressure of a gas stream (30 oC, 200 MMscfd, 90% C1, 10% C2) must increase from 600 psia to 1100 psia. • Design a reciprocating compressor (dp= 25 cm, Ls=1.2 m, dr=3 cm, single acting, Clearance fraction = 0.15) • Design a Centrifugal compressor Solution:

  13. Gas Compression Example: Solution a) Reciprocating: The values in the parenthesis are calculated by HYSYS b) Centrifugal:

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