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A system for controlling a centrifugal gas compressor (108) in an HVAC, refrigeration or liquid chiller system (100) in which flow of gas through the compressor is automatically controlled to maintain desired parameters within predetermined ranges so as to prevent stall and surge conditions within t

A system for controlling a centrifugal gas compressor (108) in an HVAC, refrigeration or liquid chiller system (100) in which flow of gas through the compressor is automatically controlled to maintain desired parameters within predetermined ranges so as to prevent stall and surge conditions within the system. A variable geometry diffuser (119) in the compressor controls the refrigerant gas flow at the discharge of the compressor impeller wheel (201). This arrangement reduces mass flow, decrease/eliminate flow-reducing stall, and increases the operating efficiency of the compressor at partial load conditions. The variable geometry diffuser control in combination with a variable speed drive (VSD) (120) increases the efficiency of the compressor at partial system loads, and eliminates the need for pre-rotation vanes at the inlet of the centrifugal compressor.

대표청구항 ▼

1. A method of controlling the capacity of a gas compression system having a compressor, a refrigerant condenser, and an evaporator connected in a refrigerant loop, the method comprising the steps of: providing a variable geometry diffuser at a compressor discharge;sensing a value representative of

1. A method of controlling the capacity of a gas compression system having a compressor, a refrigerant condenser, and an evaporator connected in a refrigerant loop, the method comprising the steps of: providing a variable geometry diffuser at a compressor discharge;sensing a value representative of a load of the gas compression system;determining a system pressure differential of the gas compression system;controlling a position of the variable geometry diffuser in response to the sensed load value and the determined system pressure differential to control a capacity of the gas compression system; wherein the gas compression system has no controllable vanes disposed at an inlet of the compressor. 2. The method of claim 1 further comprising the steps of: providing a prime mover controllably operable at a variable speed for driving the compressor,controlling a speed of the prime mover in response to the sensed load value and the determined system pressure differential. 3. The method of claim 2 further comprising the steps of: providing a hot gas bypass valve to regulate flow of refrigerant between a high pressure side of the gas compression system and a low pressure side of the gas compression system; andcontrolling the hot gas bypass valve in response to the sensed load value and the determined system pressure differential to control the capacity of the gas compression system. 4. The method of claim 3 wherein: the step of controlling a speed of the prime mover includes adjusting a speed of the compressor to maintain a desired system load condition; the step of controlling a position of the diffuser includes positioning the diffuser in a predetermined minimum position, wherein the predetermined minimum position is based on the system pressure differential; andthe step of controlling the hot gas bypass valve includes positioning the hot gas bypass valve in a closed position. 5. The method of claim 3, further comprising: sensing a plurality of gas compression system operating parameters indicative of a surge condition or an incipient stall condition;detecting an onset of a surge condition or an incipient stall condition; andoverriding the response to the sensed load value and the determined system pressure differential in response to the detecting an onset of a surge condition or an incipient stall condition. 6. The method of claim 4, wherein the predetermined minimum position for the diffuser prevents the compressor from operating in a surge condition 7. The method of claim 3 wherein: the step of controlling a speed of the prime mover includes operating the compressor at a predetermined minimum speed, wherein the predetermined minimum speed is based on the system pressure differential;the step of controlling a position of the diffuser includes adjusting a position of the diffuser to maintain a desired system load condition; andthe step of controlling the hot gas bypass valve includes positioning the hot gas bypass valve in a closed position. 8. The method of claim 4 wherein the predetermined minimum speed for the prime mover prevents the compressor from operating in a surge condition. 9. The method of claim 3 wherein: the step of controlling the speed of the prime mover includes operating the compressor at a predetermined minimum speed, wherein the predetermined minimum speed is based on the system pressure differential;the step of controlling a position of the diffuser includes positioning the diffuser in a predetermined minimum position, wherein the predetermined minimum position is based on the system pressure differential; andthe step of controlling the hot gas bypass valve includes adjusting a position of the hot gas bypass valve to maintain a desired system load condition. 10. The method of claim 2 wherein the step of controlling a position of the diffuser includes: determining a minimum position for the diffuser in response to the determined system pressure differential, wherein the determined minimum position for the diffuser prevents the compressor from operating in a surge condition; andsending a control signal to the diffuser to set a position of the variable geometry diffuser to the determined minimum position. 11. The method of claim 1 wherein the step of controlling a speed of the compressor includes: determining a minimum speed for the compressor in response to the determined system pressure differential, wherein the determined minimum speed for the compressor prevents the compressor from operating in a surge condition; andsending a control signal to the compressor to set a speed of the compressor to the determined minimum speed. 12. The method of claim 1 wherein the step of sensing a value representative of a load of the gas compression system includes determining a leaving chilled liquid temperature from the evaporator. 13. The method of claim 1 wherein the step of determining a system pressure differential includes: measuring a condenser pressure;measuring an evaporator pressure;and subtracting the measured evaporator pressure from the measured condenser pressure to determine the system pressure differential. 14. The method of claim 2 wherein the prime mover is a steam turbine. 15. The method of claim 2, wherein the prime mover is a motor powered by a variable speed drive. 16. A gas compression system having a compressor, a refrigerant condenser, and an evaporator connected in a refrigerant loop, the gas compression system comprising: a diffuser disposed at a discharge of the compressor, the diffuser configured to regulate flow of refrigerant from the compressor; the gas compression system having no controllable vanes disposed at an inlet of the compressor; anda central control panel gas compression system comprising a capacity control system, the capacity control system being configured to adjust a position of the diffuser to control the capacity of the gas compression system in response to a leaving chilled liquid temperature and a system pressure differential. 17. The gas compression system of claim 16 wherein: the gas compression system further comprises the capacity control system being configured to adjust a speed of the compressor in response to a leaving chilled liquid temperature and a system differential pressure. 18. The gas compression system of claim 17 wherein: the gas compression system further comprises a hot gas bypass valve to regulate flow of refrigerant between a high pressure side of the gas compression system and a low pressure side of the gas compression system; andthe capacity control system being configured to adjust a position of the hot gas bypass valve to control the capacity of the gas compression system in response to a leaving chilled liquid temperature and a system pressure differential. 19. The gas compression system of claim 18, wherein the control system is further configured to: detect an onset of a surge condition or an incipient stall condition; andoverride the response to the chilled liquid temperature and the determined system pressure differential in response to detecting an onset of a surge condition or an incipient stall condition. 20. The gas compression system of claim 18 wherein the capacity control system is configured to control the diffuser, the hot gas bypass valve and the speed of the compressor to prevent the compressor from operating in a surge condition. 21. The gas compression system of claim 18 wherein the capacity control system is configured to operate in one of a hot gas bypass control mode, a diffuser control mode, or a turbine speed control mode to control the capacity of the gas compression system. 22. The gas compression system of claim 21 wherein: the hot gas bypass control mode includes operation at a predetermined minimum turbine speed and a predetermined minimum diffuser position;the diffuser control mode includes operation with a closed hot gas bypass valve and at a predetermined minimum turbine speed; andthe turbine speed control mode includes operation with a closed hot gas bypass valve and at a predetermined minimum diffuser position. 23. The gas compression system of claim 16, wherein the diffuser further comprises vanes. 24. The gas compression system of claim 23, wherein the vanes are selected from one of low solidity and high solidity vanes. 25. The gas compression system of claim 17, further comprising a steam turbine and a steam condenser connected in a steam loop, wherein the compressor is driven by the steam turbine. 26. The gas compression system of claim 16, further comprising a variable speed drive controllable to vary the speed of the compressor. 27. The gas compression system of claim 16, wherein the compressor comprises multiple stages, each stage of the multiple stage compressor having a discharge diffuser disposed therein.