Heating, ventilation and air conditioning (HVAC) system and method using feedback linearization

• US 7,076,962 B2
• Filed: 11/05/2003
• Issued: 07/18/2006
• Est. Priority Date: 01/23/2003
• Status: Expired due to Fees

• Current Assignee: Massachusetts Institute of Technology
• Original Assignee: Massachusetts Institute of Technology
• Inventors: He, Xiang-Dong, Asada, H. Harry
• Primary Examiner(s): Norman, Marc
• Application Number:
  US10/701,799
• Publication Number:
  US 20040144112A1
• Time in Patent Office: 986 Days
• Field of Search: 621/15, 622/16, 622/24, 622/25, 624/98
• US Class Current: 62/225
• CPC Class Codes: F24F 11/30 for purposes related to the operation of the system, e.g. for safety or monitoring
• CPC Class Codes: F24F 11/62 characterised by the type of control or by internal processing, e.g. using fuzzy logic, adaptive control or estimation of values
• CPC Class Codes: F25B 2600/0253 with variable speed
• CPC Class Codes: F25B 2600/21 Refrigerant outlet evaporator temperature
• CPC Class Codes: F25B 49/02 for compression type machines, plants or systems
• CPC Class Codes: G05B 11/42 for obtaining a characteristic which is both proportional and time-dependent, e.g. P. I., P. I. D.
• CPC Class Codes: G05B 17/02 electric
• CPC Class Codes: G05D 23/1917 using digital means
• CPC Class Codes: Y02B 30/70 Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

Abstract

A new feedback linearization approach to advanced control of single-unit and multi-unit HVAC systems is described. In accordance with the approach of the invention, this new nonlinear control includes a model-based feedback linearization part to compensate for the nonlinearity in the system dynamics. Therefore, the evaporating temperature and superheat values can be controlled by linear PI control designs to achieve desired system performance and reliability. The main advantages of the new nonlinear control approach include (1) better performance even with large model errors, (2) being able to adapt to indoor unit turn on/off operation, (3) much smaller PI control gains compared to that of current feedback PI controls, (4) much easier design procedures since there is no need for tuning the PI control gains over wide range operation.

Claims

1. A heat transfer system, comprising:

a first heat exchanger;

a second heat exchanger in thermal communication with a space; and

a processor for estimating an amount of heat transferred between the second heat exchanger and the space and altering a control parameter of the heat transfer system based on the estimated amount of heat transferred to control the heat transfer system;

wherein;

the processor controls a temperature of refrigerant in the second heat exchanger; and

the processor comprises;

a non-linear observer for estimating a plurality of state variables which define a state of the second heat exchanger, the non-linear observer estimating the state variables based on a non-linear model which describes dynamic behavior of the second heat exchanger, the non-linear observer using the estimates of the state variables to compute an estimate of the amount of heat transferred between the second heat exchanger and the space.

2. The heat transfer system of claim 1, wherein the first heat exchanger is a condenser.

3. The heat transfer system of claim 1, wherein the first heat exchanger is an evaporator.

4. The heat transfer system of claim 1, wherein the second heat exchanger is a condenser.

5. The heat transfer system of claim 1, wherein the second heat exchanger is an evaporator.

6. The heat transfer system of claim 5, wherein the processor controls a temperature of refrigerant in the first heat exchanger.

7. The heat transfer system of claim 5, wherein the processor controls a degree of superheat in the evaporator.

8. The heat transfer system of claim 7, wherein the parameter altered by the processor is an expansion valve opening.

9. The heat transfer system of claim 5, wherein the processor controls a discharge pressure of refrigerant in a compressor of the heat transfer system.

10. The heat transfer system of claim 5, wherein the processor controls a discharge temperature of refrigerant in a compressor of the heat transfer system.

11. The heat transfer system of claim 5, further comprising a plurality of evaporators in thermal communication with a respective plurality of spaces.

12. The heat transfer system of claim 5, further comprising a plurality of evaporators in thermal communication with the space.

13. The heat transfer system of claim 1, further comprising a compressor for increasing pressure of a refrigerant flowing between the first and second heat exchangers.

14. The heat transfer system of claim 13, wherein the parameter altered by the processor is a speed of the compressor.

15. The heat transfer system of claim 1, wherein the processor controls a temperature of refrigerant in the first heat exchanger.

16. The heat transfer system of claim 1, wherein the processor controls a degree of superheat in the second heat exchanger.

17. The heat transfer system of claim 16, wherein the parameter altered by the processor is an expansion valve opening.

18. The heat transfer system of claim 1, wherein the processor controls a discharge pressure of refrigerant in a compressor of the heat transfer system.

19. The heat transfer system of claim 1, wherein the processor controls a discharge temperature of refrigerant in a compressor of the heat transfer system.

20. The heat transfer system of claim 1, wherein the processor controls the parameter using a feedback linearization approach.

21. The heat transfer system of claim 1, further comprising a plurality of second heat exchangers in thermal communication with a respective plurality of spaces.

22. The heat transfer system of claim 1, further comprising a plurality of second heat exchangers in thermal communication with the space.

23. The heat transfer system of claim 1, wherein the heat transfer system is controlled to protect a component of the heat transfer system from damage.

24. The heat transfer system of claim 23, wherein the component is a compressor.

25. A method of heat transfer, comprising:

providing a first heat exchanger;

providing a second heat exchanger in thermal communication with a space;

estimating an amount of heat transferred between the second heat exchanger and the space, estimating the amount of heat transferred between the second heat exchanger and the space comprising using a non-linear observer to estimate a plurality of state variables which define a state of the second heat exchanger, the non-linear observer estimating the state variables based on a non-linear model which describes dynamic behavior of the second heat exchanger, the non-linear observer using the estimates of the state variables to compute an estimate of the amount of heat transferred between the second heat exchanger and the space;

altering a control parameter based on the estimated amount of heat transferred to control the heat transfer system; and

controlling a temperature of refrigerant in the second heat exchanger.

26. The method of claim 25, wherein the first heat exchanger is a condenser.

27. The method of claim 25, wherein the first heat exchanger is an evaporator.

28. The method of claim 25, wherein the second heat exchanger is a condenser.

29. The method of claim 25, wherein the second heat exchanger is an evaporator.

30. The method of claim 29, further comprising controlling a temperature of refrigerant in the first heat exchanger.

31. The method of claim 29, further comprising controlling a degree of superheat in the evaporator.

32. The method of claim 31, wherein the parameter altered by the processor is an expansion valve opening.

33. The method of claim 29, further comprising controlling a discharge pressure of refrigerant in a compressor of the heat transfer system.

34. The method of claim 29, further comprising controlling a discharge temperature of refrigerant in a compressor of the heat transfer system.

35. The method of claim 29, further comprising providing a plurality of evaporators in thermal communication with a respective plurality of spaces.

36. The method of claim 29, further comprising providing a plurality of evaporators in thermal communication with the space.

37. The method of claim 25, further comprising providing a compressor for increasing pressure of a refrigerant flowing between the first and second heat exchangers.

38. The method of claim 37, wherein the altered parameter is a speed of the compressor.

39. The method of claim 25, further comprising controlling a temperature of refrigerant in the first heat exchanger.

40. The method of claim 25, further comprising controlling a degree of superheat in the second heat exchanger.

41. The method of claim 40, wherein the parameter altered by the processor is an expansion valve opening.

42. The method of claim 25, further comprising controlling a discharge pressure of refrigerant in a compressor of the heat transfer system.

43. The method of claim 25, further comprising controlling a discharge temperature of refrigerant in a compressor of the heat transfer system.

44. The method of claim 25, altering the parameter comprises using a feedback linearization approach.

45. The method of claim 25, further comprising providing a plurality of second heat exchangers in thermal communication with a respective plurality of spaces.

46. The method of claim 25, further comprising providing a plurality of second heat exchangers in thermal communication with the space.

47. The method of claim 25, wherein the control parameter is altered to protect a component of the heat transfer system from damage.

48. The method of claim 47, wherein the component is a compressor.