Torque controlled pump protection with mechanical loss compensation

• US 7,080,508 B2
• Filed: 05/13/2004
• Issued: 07/25/2006
• Est. Priority Date: 05/13/2004
• Status: Active Grant

• Current Assignee: ITT Manufacturing Enterprises, Inc. (ITT, Inc.)
• Original Assignee: ITT Manufacturing Enterprises, Inc. (ITT, Inc.)
• Inventors: Kernan, Daniel J., Ganzon, Nicolas W., Stavale, Anthony E.
• Primary Examiner(s): Look, Edward K.
• Assistant Examiner(s): Leslie, Michael
• Application Number:
  US10/846,946
• Publication Number:
  US 20050252205A1
• Time in Patent Office: 803 Days
• Field of Search: 604/31, 604/45, 604/52, 415/30, 417/42, 417/44.1, 417/53, 417/63
• US Class Current: 60/431
• CPC Class Codes: F04B 2201/1202 Torque on the axis
• CPC Class Codes: F04D 15/0066 by changing the speed, e.g. of the driving engine
• CPC Class Codes: F04D 15/0254 the condition being speed or load

Abstract

A method and apparatus are provided for controlling the operation of a pump, such as a centrifugal pump, featuring steps of either adjusting the operation of the pump, or issues a warning to a user of the pump of an undesirable operating condition, or both, based on a comparison of an actual torque value and a corrected torque value either alone or in combination with a further step of compensating the corrected torque value based on a mechanical power offset correction. The corrected torque value may include a Best Efficiency Point (BEP) torque value and may also be compensated for based on at least the current operating speed of the pump. The pump has a controller for performing the steps of the method. The controller can compensate the corrected torque value based on the square of the speed change of the pump. The comparison may include a ratio of the actual torque value to the corrected torque value.

Claims

1. A method for controlling the operation of a centrifugal pump, centrifugal blower, centrifugal mixer or centrifugal compressor characterized in that the method includes the steps of:

adjusting either the operation of the pump, or issuing a warning to a user of the pump of an undesirable operating condition, or both, based on a comparison of an actual torque value and a corrected torque value; and

compensating the corrected torque value based on a mechanical power offset correction.

2. A method according to claim 1, wherein the corrected torque value is a best efficiency point (BEP) torque value.

3. A method according to claim 1, wherein the corrected torque value is compensated for based on at least the current operating speed of the pump.

4. A method according to claim 3, wherein the method includes the step of compensating the corrected torque value based on the square of the speed change of the pump.

5. A method according to claim 1, wherein the comparison includes a ratio of the actual torque value to the corrected torque value.

6. A method according to claim 5, wherein the ratio of the actual torque value to the corrected torque value is compared to ratios corresponding to either a dry run condition, a minimum flow condition, a runout condition, or some combination thereof.

7. A method according to claim 1, wherein the method includes the steps of detecting and differentiating between different undesirable operating conditions, including either a dry run condition, a minimum flow condition, a runout condition, or some combination thereof, and controlling the pump accordingly by either slowing the pump to a safe operating speed, shutting down the pump, re-starting the pump after a time delay, or some combination thereof.

8. A method according to claim 1, wherein the method includes the step of setting a protection delay to avoid nuisance trips caused by system transients.

9. A method according to claim 1, wherein the method includes performing the steps of the method with a controller that is either a variable frequency drive (VFD) or a programmable logic controller (PLC).

10. A centrifugal pump, centrifugal blower, centrifugal mixer or centrifugal compressor pump having a controller for controlling the operation of the pump characterized in that

the controller either adjusts the operation of the pump, or issues a warning to a user of the pump of an undesirable operating condition, or both, based on a comparison of an actual torque value and a corrected torque value;

and compensates the corrected torque value based on a mechanical power offset correction.

11. A pump according to claim 10, wherein the corrected torque value is a best efficiency point (BEP) torque value.

12. A pump according to claim 10, wherein the corrected torque value is compensated for based on at least the current operating speed of the pump.

13. A pump according to claim 12, wherein the controller compensates the corrected torque value based on the square of the speed change of the pump.

14. A pump according to claim 10, wherein the comparison includes a ratio of the actual torque value to the corrected torque value.

15. A pump according to claim 14, wherein the ratio of the actual torque value to the corrected torque value is compared to ratios corresponding to either a dry run condition, a minimum flow condition, a runout condition, or some combination thereof.

16. A pump according to claim 10, wherein the controller detects and differentiates between different undesirable operating conditions, including either a dry run condition, a minimum flow condition, a runout condition, or some combination thereof, and controls the pump accordingly by either slowing the pump to a safe operating speed, shutting down the pump, re-starting the pump after a time delay, or some combination thereof.

17. A pump according to claim 10, wherein a protection delay can be set to avoid nuisance trips caused by system transients.

18. A pump according to claim 10, wherein the controller is a variable frequency drive (VFD) or a programmable logic controller (PLC).

19. A controller for controlling the operation of a centrifugal pump, centrifugal blower, centrifugal mixer or centrifugal compressor, characterized in that

the controller either adjusts the operation of the pump, or issues a warning to a user of the pump of an undesirable operating condition, or both, based on a comparison of an actual torque value and a corrected torque value;

and compensates the corrected torque value based on a mechanical power offset correction.

20. A controller according to claim 19, wherein the corrected torque value is a best efficiency point (BEP) torque value.

21. A controller according to claim 19, wherein the corrected torque value is compensated for based on at least the current operating speed of the pump.

22. A controller according to claim 21, wherein the controller compensates the corrected torque value based on the square of the speed change of the pump.

23. A controller according to claim 19, wherein the comparison includes a ratio of the actual torque value to the corrected torque value.

24. A controller according to claim 23, wherein the ratio of the actual torque value to the corrected torque value is compared to ratios corresponding to either a dry run condition, a minimum flow condition, a runout condition, or some combination thereof.

25. A controller according to claim 19, wherein the controller detects and differentiates between different undesirable operating conditions, including either a dry run condition, a minimum flow condition, a runout condition, or some combination thereof, and controls the pump accordingly by either slowing the pump to a safe operating speed, shutting down the pump, re-starting the pump after a time delay, or some combination thereof.

26. A controller according to claim 19, wherein the controller sets a protection delay to avoid nuisance trips caused by system transients.

27. A controller according to claim 19, wherein the controller is a variable frequency drive (VFD) or a programmable logic controller (PLC).

28. A controller according to claim 19, wherein the controller includes an enter data application module for receiving default values for best efficiency point speed and power, as well as a default value for a power offset, and for calculating torque at a best efficiency point and a torque offset.

29. A controller according to claim 19, wherein the controller includes a correct for speed module for determining a correction of best efficiency point torque (T_BEP) for the current motor speed.

30. A controller according to claim 19, wherein the controller includes an evaluate module for comparing the actual torque value to the corrected torque value.

31. A controller according to claim 30, wherein the corrected torque value is a target BEP torque as a percentage of a best efficiency point torque (T_BEP(C)).

32. A controller according to claim 19, wherein the controller includes a determining status module that determines the undesirable operating condition based upon the comparison, including either a running dry condition, a minimum flow or shutoff operation condition, a runout flow condition, or some combination thereof.

33. A controller according to claim 32, wherein the determining status module determines the status of the pump to be O.K. and returns the controller to the step for correcting for speed if the comparison is greater than a second percentage (B %) and less than a third percentage (C %).

34. A controller according to claim 32, wherein the determine status module determines the status of the pump condition to be not O.K. if the comparison is less than a second percentage (B %) or greater than a third percentage (C %), then either in one case if the comparison is less than the second percentage (B %) passed the controller to a step for determining whether the pump condition is a MIN FLOW or DRY RUN condition, or in the other case if the comparison is greater than the third percentage (C %) passes the controller to a step for controlling the operation of the pump based on a RUN OUT condition.

35. A controller according to claim 19, wherein the controller includes a RUNOUT condition module that adjusts the operation of the pump, or issues a warning of the RUNOUT condition, or both.

36. A controller according to claim 35, wherein the RUNOUT condition module warns the user, adjusts the operation of the pump by decreasing the speed of the pump to meet C % requirement, auto resets the pump once a minimum speed is reached, performs a RUNOUT fault routine after a predetermined protection delay to avoid nuisance trips caused by system transients, or some combination thereof;

and then returns the controller back to the step for correcting for speed when done.

37. A controller according to claim 19, wherein the controller includes a DRY RUN condition module that determines the status of the pump to be not O.K. and in a DRY RUN condition it the comparison is less than a first percentage (A %), and either adjusts the operation of the pump, or issues a warning of the DRY RUN condition, or both.

38. A controller according to claim 37, wherein the DRY RUN condition module warns the user with no further action or warns the user and adjusts the operation of the pump by shutting down the pump.

39. A controller according to claim 37, wherein the DRY RUN condition module performs the DRY RUN fault routine after a predetermined protection delay to avoid nuisance trips caused by system transients.

40. A controller according to claim 37, wherein the DRY RUN condition module passes the controller to a step for performing standard operation functionality for the pump.

41. A controller according to claim 37, wherein the controller has a MIN FLOW condition module that determines the status of the pump to be not O.K. and in a MIN FLOW condition if the comparison is greater than a first percentage (A %).

42. A controller according to claim 41, wherein the MIN FLOW condition module either adjusts the operation of the pump, or issues a warning of the MIN FLOW condition, or both.

43. A controller according to claim 41, wherein the MIN FLOW condition module warns the user, adjusts the operation of the pump by going to a minimum speed (MINSPEED) or shutting down the pump, auto resets the pump after a predetermined time period performs the MIN FLOW fault routine after a predetermined protection delay to avoid nuisance trips caused by system transients, or some combination thereof.

44. A controller according to claim 41, wherein the MIN FLOW condition module passes the controller to a step for performing standard operation functionality for the pump.

45. A centrifugal pump, centrifugal blower, centrifugal mixer or centrifugal compressor having a controller for controlling the operation of the pump characterized in that

the controller either adjusts the operation of the pump, or issues a warning to a user of the pump of an undesirable operating condition, or both, based on a comparison of an actual torque value and a corrected torque value, where the corrected torque value is based on the current pump speed.

46. A pump according to claim 45, wherein the controller also compensates the corrected torque value based on a mechanical power off set correction.

47. A pump according to claim 45, wherein the corrected torque value is a best efficiency point (BEP) torque value.

48. A pump according to claim 45, wherein the corrected torque value is compensated for based on at least the current operating speed of the pump.

49. A pump according to claim 48, wherein the controller compensates the corrected torque value based on the square of the speed change of the pump.

50. A pump according to claim 45, wherein the comparison includes a ratio of the actual torque value to the corrected torque value.

51. A pump according to claim 48, wherein the ratio of the actual torque value to the corrected torque value is compared to ratios corresponding to either a dry run condition, a minimum flow condition, a runout condition, or some combination thereof.

52. A pump according to claim 45, wherein the controller detects and differentiates between different undesirable operating conditions, including either a dry run condition, a minimum flow condition, a runout condition, or some combination thereof, and controls the pump accordingly by either slowing the pump to a safe operating speed, shutting down the pump, restarting the pump after a time delay, or some combination thereof.

53. A pump according to claim 45, wherein a protection delay can be set to avoid nuisance trips caused by system transients.

54. A pump according to claim 45, wherein the controller is a variable frequency drive (VFD) or a programmable logic controller (PLC).

55. A pump according to claim 46, wherein the mechanical power offset correction is a negative mechanical power offset correction.

56. A pump according to claim 46, wherein the mechanical power offset correction is a positive mechanical power offset correction.

57. A device having a controller for controlling the operation of the device characterized in that

the controller either adjusts the operation of the pump, or issues a warning to a user of the pump of an undesirable operating condition, or both, based on a comparison of an actual torque value and a corrected torque value;

and

compensating the corrected torque value based on a mechanical power offset correction.

58. A device according to claim 57, wherein the corrected torque value is a best efficiency point (BEP) torque value.

59. A device according to claim 57, wherein the corrected torque value is compensated for based on at least the current operating speed of the pump.

60. A device according to claim 57, wherein the controller compensates the corrected torque value based on the square of the speed change of the pump.

61. A device according to claim 57, wherein the comparison includes a ratio of the actual torque value to the corrected torque value.

62. A device according to claim 57, wherein the device is a centrifugal pump, centrifugal blower, centrifugal mixer or centrifugal compressor.