Evaporator water temperature control for a chiller system

• US 5,419,146 A
• Filed: 04/28/1994
• Issued: 05/30/1995
• Est. Priority Date: 04/28/1994
• Status: Expired due to Term

• Current Assignee: Trane International Inc. (Trane Technologies plc)
• Original Assignee: American Standard Companies Incorporated (Ideal Standard International Topco SCA)
• Inventors: Leaver, Daniel C., Glamm, Paul R., Sibik, Lee L.
• Primary Examiner(s): Wayner, William E.
• Application Number:
  US08/234,091
• Time in Patent Office: 397 Days
• Field of Search: 62/201, 62/228.5, 62/204-223, 62/115, 62/196.1
• US Class Current: 62/115
• CPC Class Codes: F04C 2270/19 Temperature
• CPC Class Codes: F04C 2270/22 Temperature difference
• CPC Class Codes: F04C 28/00 Control of, monitoring of, or safety arrangements for, pumps or pumping installations specially adapted for elastic fluids
• CPC Class Codes: F04C 28/12 using sliding valves
• CPC Class Codes: F05B 2270/303 Temperature
• CPC Class Codes: F25B 2341/063 Feed forward expansion valves
• CPC Class Codes: F25B 2600/21 Refrigerant outlet evaporator temperature
• CPC Class Codes: F25B 41/34 with the valve member being actuated by electric means, e.g. by piezoelectric actuators
• CPC Class Codes: F25B 49/022 Compressor control arrangements
• CPC Class Codes: F25D 17/02 for circulating liquids, e.g. brine
• 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 controlling the capacity of a chiller system, the chiller system including a circularly linked compressor, condenser, expansion device, and evaporator. The method comprises the steps of: measuring a first chiller system parameter; determining a first parameter error as a function of the difference between the first parameter and a first setpoint; measuring a second chiller system parameter; determining a second parameter error as a function of the difference between the second parameter and a second setpoint; providing a first mode of capacity control where the compressor is modulated in response to the first parameter error and the expansion valve is modulated in response to the second parameter error; and providing a second mode of capacity control where the compressor is maintained at a minimum capacity and the expansion valve is modulated in response to the first parameter error.

Claims

1. A method of controlling the capacity of a chiller system, the chiller system including a circularly linked compressor, condenser, expansion device, and evaporator, the method comprising the steps of:

measuring a first chiller system parameter;

determining a first parameter error as a function of the difference between the first parameter and a first setpoint;

measuring a second chiller system parameter;

determining a second parameter error as a function of the difference between the second parameter and a second setpoint;

providing a first mode of capacity control where the compressor is modulated in response to the first parameter error and the expansion valve is modulated in response to the second parameter error; and

providing a second mode of capacity control where the compressor is maintained at a minimum capacity and the expansion valve is modulated in response to the first parameter error.

2. The method of claim 1 including the further step of providing, from the evaporator, a leaving fluid having a leaving fluid temperature, wherein the first parameter is the leaving fluid temperature as measured by a first sensor and the second parameter is refrigerant superheat as measured by a second sensor.

3. The method of claim 2 wherein the leaving fluid is water.

4. The method of claim 3 including the further steps of:

measuring the temperature of water entering the evaporator;

determining an evaporator temperature differential as a function of the difference between entering water temperature and leaving water temperature; and

selecting either the first or the second mode of capacity control as a function of the evaporator temperature differential.

5. The method of claim 4 wherein the selecting step includes the use of fuzzy logic.

6. A method of controlling the capacity of a chiller system, the chiller system including a circularly linked compressor, condenser, expansion device, and evaporator, where the evaporator receives entering water having an entering water temperature and provides leaving water having a leaving water temperature and where the compressor compresses refrigerant having a measured superheat, the method comprising the steps of:

measuring the leaving water temperature and the refrigerant superheat;

determining a leaving water temperature error as a function of the difference between the leaving water temperature and a setpoint;

providing a first mode of capacity control wherein the compressor is modulated in response to the leaving water temperature error and the expansion valve is modulated in response to the measured superheat; and

providing a second mode of capacity control where the compressor is maintained at its minimum capacity and the expansion valve is modulated in response to the leaving water temperature error.

7. The method of claim 6 including the further steps of:

determining an evaporator temperature differential as a function of the difference between the entering water temperature and the leaving water temperature; and

selecting and implementing a mode of capacity control as a function of evaporator differential temperature and leaving water temperature error.

8. The method of claim 7 wherein the selecting and implementing step includes the further step of using fuzzy logic to select the mode of capacity control.

9. The method of claim 8 wherein the fuzzy logic includes membership rules which are functions of the evaporator differential temperature and the leaving water temperature error.

10. A method of controlling the capacity of a chiller system comprising the steps of:

determining a needed capacity for the chiller system;

adjusting a compressor flow control means to meet the needed capacity;

repositioning an expansion valve in response to the adjusting step;

determining if the compressor flow control means is at an end of range capacity; and

modulating the position of the expansion valve to control chiller system capacity whenever the flow control means has been determined to be at an end of capacity range.

11. The method of claim 10 including the further step of determining a mode of capacity control as a function of an evaporator water temperature differential and a leaving water temperature error.

12. A method of controlling the capacity of a water chiller system having a variable capacity compressor, a variable capacity expansion device, and an evaporator having a leaving water temperature, the method comprising the steps of:

measuring the leaving water temperature;

comparing the leaving water temperature to a setpoint so as to determine an error;

modulating the compressor capacity to minimize the error unless the compressor capacity is at a minimum capacity position;

maintaining the compressor at the minimum capacity position; and

modulating the expansion device to minimize the error.

13. A method of selecting between first and second modes of capacity control for a water chiller system including an evaporator having an entering fluid temperature and a leaving fluid temperature, the method comprising the steps of:

determining the leaving fluid temperature;

determining the entering fluid temperature;

determining a differential temperature as a function of the difference between the leaving fluid temperature and the entering fluid temperature;

determining a temperature error as a function of the difference between the leaving fluid temperature and a setpoint; and

selecting either the first or second mode of capacity control as a function of the temperature differential and the temperature error.

14. The method of claim 13 wherein the fluid is water.

15. The method of claim 13 wherein the selecting step includes the further steps of:

defining a first fuzzy logic membership as a function of the temperature error;

defining a second fuzzy logic membership as a function of the differential temperature;

applying at least one predetermined set of fuzzy logic rules to the first and second fuzzy logic memberships to obtain at least one result;

converting the at least one result to one or more commands indicative of either the first or second mode of capacity control; and

commanding said mode of capacity control.

16. The method of claim 15 wherein the water chiller system includes an expansion device and an unloader and wherein the converting step includes the further steps of:

establishing a first mode of operation for the expansion device if the at least one result exceeds a first empirically determined value;

establishing a second mode of operation for the expansion device if the at least one result is less than a second empirically determined value;

establishing a first mode of operation for the unloader if the at least one result if greater than a third empirically determined value; and

establishing a second mode of operation for the unloader if the at least one result is less than a fourth empirically determined value.

17. The method of claim 16 wherein the first and third empirically determined values are 0.4 and the second and fourth empirically determined values are -0.4.

18. The method of claim 15 wherein the step of defining a first fuzzy logic membership includes the further step of defining the temperature error (Te) as low, high, or normal;

where the low definition is a function of (Te-C1)/C2;

where the high definition is a function of (Te+C3)/C4;

where the normal definition is a function of (C5±

Te)/C6; and

where C1 through C6 are constants.

19. The method of claim 15 wherein the step of defining a second fuzzy logic membership includes the further step of defining the differential temperature (evapdt) as unload, load, or trans;

where the unload definition is a function of (C7 -evapdt)/C8;

where the load definition is a function of (evapdt -C9);

where the trans definition is a function of either (evapdt -C10) or (C11 -evapdt); and

where C7 through C11 are constants.