Method and apparatus for controlling a multicompressor station

• US 4,494,006 A
• Filed: 09/15/1982
• Issued: 01/15/1985
• Est. Priority Date: 09/15/1982
• Status: Expired due to Term

• Current Assignee: Ropintassco Holdings, L.P. (Roper Technologies, Inc.)
• Original Assignee: Compressor Controls Corporation (Roper Technologies, Inc.)
• Inventors: Staroselsky, Naum, Mirsky, Saul
• Primary Examiner(s): Witkowski, Stanley J.
• Assistant Examiner(s): Wade, Shelley
• Application Number:
  US06/418,224
• Time in Patent Office: 853 Days
• Field of Search: 417/2-5, 290/4, 290/40 R
• US Class Current: 290/4.00R
• CPC Class Codes: F02C 6/00 Plural gas-turbine plants; Combinations of gas-turbine plants with other apparatus; Adaptations of gas-turbine plants for special use
• CPC Class Codes: F04D 27/0261 by varying driving speed
• CPC Class Codes: F04D 27/0284 Conjoint control of two or more different functions
• CPC Class Codes: Y02B 30/70 Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

Abstract

A method of control and control apparatus for load sharing between multiple compressors working in parallel and/or in series which enables all of the load-sharing compressors to carry their optimum share of the load. This load-sharing scheme follows the safest load-sharing formula and also provides for substantial energy savings. It automatically divides the load whenever a strong decoupling between process control and compressors after the compressors'"'"' operating points cross their Surge Control lines.

Claims

1. A method of controlling a compressor station receiving gas from an upstream process, compressing the gas and delivering it to a process downstream thereof, said compressor station having a station control means to adjust the station performance to the demand of a process located upstream or downstream, said compressor station including also a plurality of dynamic compressors driven by a plurality of respective prime movers, each of said dynamic compressors having a variable performance, a main control means associated with each of said compressors for changing its performance and a surge control means associated with each respective compressor for maintaining said respective compressor along a surge control line having a predetermined equation and located a predetermined distance from the respective surge limit of each respective compressor;

said method comprising;

transforming said predetermined equation of each respective surge control line into a variable criterion representing a relative distance between each respective compressor'"'"'s operating point and its surge control line, said variable criterion reaching a predetermined value when said relative distance reaches zero value;

simultaneously changing the set points for all of said respective criterions representing the relative distance between each respective compressor'"'"'s operating point and its surge control line by changing an output of said station control means to control the performance of said compressor station; and

keeping said set points equal and maintaining said criterion substantially equal at substantially all times for each of said respective compressors.

2. The method of claim 1 further comprising limiting said respective set points and providing for a decoupling between each respective compressor and said station control means to avoid a dangerous approaching of said respective surge limit line after the compressor'"'"'s operating point crosses its surge control line and reaches some predetermined deviation from said control line.

3. The method of claim 1 wherein said equation is kf(Z)Y+b=X, where Kf(Z) is the variable slope of the surge control line and b is the bias representing the respective distance between the surge control line and the surge limit line, said criterion equaling ##EQU2## where X, Y and Z are the compressor variables representing the respective compressor performance and are used to build the respective compressor maps.

4. The method of claim 3 wherein X is a parameter related to flow through each respective compressor, Y is a parameter related to the pressure differential across each respective compressor, and Z is a parameter related to the speed of rotation of each respective compressor.

5. The method of claim 3 wherein X is a parameter related to flow through each respective compressor, Y is a parameter related to the pressure differential across each respective compressor, and Z represents the position of guide vanes of each respective compressor.

6. The method of claim 3 wherein X is a parameter related to flow through each respective compressor, Y is a parameter related to the pressure differential across each respective compressor, and Z represents a parameter related to the inlet density of the fluid entering each respective compressor.

7. Apparatus for controlling a compressor station receiving a gas from upstream of a process, compressing the gas and delivering it to the process downstream thereof, said compressor station including a plurality of respective prime movers, each of said dynamic compressors having a variable performance defined by three variable parameters, a main control means associated with each of said compressors for changing the performance of each respective compressor, a surge control means associated with each respective compressor for maintaining each respective compressor along a predetermined surge control line and located a predetermined distance from the respective surge limit of each respective compressor;

the improvement comprising;

means for maintaining one of the gas parameters constant for each respective compressor;

means for computing a criterion respresenting a relative distance between each respective compressor'"'"'s operating point from the respective surge control line;

set point control means for controlling one of said gas parameters by simultaneously changing the set points of each respective compressor for said criterion, representing the relative distance between each respective compressor'"'"'s operating point and its surge control line; and

means for maintaining said criterion substantially equal at substantially all times for each of said compressors.

8. The apparatus of claim 7 wherein said means for maintaining one of the gas parameters constant includes a primary closed loop controller having an output.

9. The apparatus of claim 8 wherein said set point control means comprises a secondary closed loop controller means for each of said compressors for receiving the output of said primary controller as its set point and changing the performance of each respective compressor by opening its main control means, each of said secondary closed loop controller means further maintaining said criterion representing the relative distance between each compressor'"'"'s operating point and each respective surge control line at the required level corresponding to the set point developed by said primary controller means.