Method and apparatus for pump protection without the use of traditional sensors

• US 8,303,260 B2
• Filed: 11/17/2006
• Issued: 11/06/2012
• Est. Priority Date: 03/08/2006
• Status: Active Grant

• Current Assignee: ITT Manufacturing Enterprises, Inc. (ITT, Inc.)
• Original Assignee: ITT Manufacturing Enterprises, Inc. (ITT, Inc.)
• Inventors: Stavale, Anthony E., Ganzon, Nicolas W.
• Primary Examiner(s): Freay, Charles
• Assistant Examiner(s): BOBISH, CHRISTOPHER S
• Application Number:
  US11/601,373
• Publication Number:
  US 20070212229A1
• Time in Patent Office: 2,181 Days
• Field of Search: 417/42, 417/43, 417/53, 738/61, 731/95, 731/96
• US Class Current: 417/43
• CPC Class Codes: F04D 15/0088 Testing machines
• CPC Class Codes: F04D 15/0209 responsive to a condition of the working fluid F04D15/029 takes precedence
• CPC Class Codes: F04D 15/0218 the condition being a liquid level or a lack of liquid supply

Abstract

The present invention provides protection for centrifugal pumps while differentiating between dangerous operating conditions (e.g. dry running, minimum flow and runout) and/or conditions where transient conditions (e.g. closed valve operation) may occur and the protection can be revoked once the condition clears. The methodology utilizes a calculated flow value which can be mathematically determined from a calibrated closed valve power vs speed curve and/or various pump and motor parameters such as speed, torque, power and/or differential pressure or from calibrated flow curves stored in the evaluation device. The calculated flow value is then compared to threshold values of flow associated with these adverse operating conditions.

Claims

1. A method for controlling the operation of a pump, including a centrifugal pump, centrifugal mixer, centrifugal blower or centrifugal compressor, comprising:

determining an actual flow value without using a flow or pressure sensor based at least partly on a comparison of speed and power sensed in relation to the current operation of the pump and information contained in a calibrated curve of speed versus closed valve power together with published pump performance data, including best efficiency power, closed valve power and best efficiency flow at rated pump speed;

determining a corrected threshold flow value based at least partly on a flow value associated with an unfavorable operating condition of the pump and corrected based on a relationship between a current operating speed of the pump and a rated operating speed of the pump; and

controlling the operation of the pump based at least partly on a comparison between the actual flow value and the corrected threshold flow value in order to provide pump protection for the pump.

2. A method according to claim 1, wherein the method further comprises adapting the operation of the pump based at least partly on the comparison, including using a user settable delay in reacting to the condition prior to issuing either a warning only, warning and reduction in speed to a safe operating speed, faulting and shutting down the motor or automatically resetting the fault and restarting the pump and motor to check if the condition has cleared, and where if the condition clears the adaptation is revoked and the pump resumes normal operation.

3. A method according to claim 1, wherein the relationship is a ratio of the current operating speed of the pump divided by the rated operating speed of the pump.

4. A method according to claim 1, wherein the corrected threshold flow value includes a runout condition value, a minimum flow value, or some combination thereof.

5. A method according to claim 1, wherein the method includes comparing a runout condition value to an actual runout flow value in order to determine a runout condition of the pump.

6. A method according to claim 1, wherein the method includes comparing a corrected minimum flow value to an actual minimum flow value in order to determine either a normal flow condition or a possible minimum flow condition of the pump.

7. A method according to claim 1, wherein the method further comprises comparing, a corrected minimum threshold flow value to an actual flow value and also comparing an actual power value to a closed valve power value at the current speed of the pump in order to determine either a minimum flow condition or a dry run condition of the pump.

8. A method according to claim 1, wherein the method further comprises comparing a corrected minimum threshold flow value to an actual flow value and also comparing an actual power value to a closed valve power value at the current speed of the pump in order to determine either a minimum flow condition or a dry run condition of the pump, where the closed valve power value is interpolated from a calibrated power vs speed curve stored in a memory device.

9. A method according to claim 1, wherein a Dry Run condition is declared if P_ACT is less than K_DR×

P<sub>SO—

N</sub>, where P_ACT is an actual power corrected for a specific gravity of 1, where K_DR is a coefficient multiplied by a closed valve power at a current operating speed, and where P<sub>SO—

N</sub> is the closed valve power at the current speed corrected for the specific gravity of 1.

10. A method according to claim 7, wherein either the actual power value, the closed valve power value or the combination thereof are corrected for specific gravity of the medium being pumped.

11. A method according to claim 7, wherein the corrected Minimum Flow Threshold value is based at least partly on the equation Q_MIN—

_COR=Q_MIN×

(N_ACT/N_RATED), where Q<sub>MIN—

COR</sub> is a minimum flow corrected for speed, where Q_MIN is the minimum flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

12. A method according to claim 5, wherein the runout condition value is a corrected Runout Flow Threshold value that is based at least partly on the equation Q_RO—

_COR=Q_RO×

(N_ACT/N_RATED), where Q<sub>RO—

COR</sub> is a runout flow corrected for speed, where Q_RO is the runout flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

39. A method according to claim 4, wherein the method includes comparing a runout condition value to an actual runout flow value in order to determine a runout condition of the pump.

40. A method according to claim 8, wherein a Dry Run condition is declared if P_ACT is less than K_DR X P_SO—

_N, where P_ACT is an actual power corrected for a specific gravity of 1, where K_DR is a coefficient multiplied by a closed valve power at a current operating speed, and where P<sub>SO—

N</sub> is the closed valve power at the current speed corrected for the specific gravity of 1.

41. A method according to claim 7, wherein the corrected Minimum Flow Threshold value is based at least partly on the equation Q_MIN—

_COR=Q_MIN×

(N_ACT/N_RATED), where Q<sub>MIN—

COR</sub> is a minimum flow corrected for speed, where Q_MIN is the minimum flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

42. A method according to claim 5, wherein the corrected Runout Flow Threshold value is based at least partly on the equation Q_RO—

_COR=Q_RO×

(N_ACT/N_RATED), where Q<sub>RO—

COR</sub> is a runout flow corrected for speed, where Q_RO is the runout flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

43. A method according to claim 7, wherein the actual flow value is calculated from a calibrated speed vs closed valve power curve stored in the evaluation device, motor signals for speed and power (or torque) and basic published pump performance data such as best efficiency power, closed valve power and best efficiency flow at the rated pump speed.

13. A controller for controlling the operation of a pump, including a centrifugal pump, centrifugal mixer, centrifugal blower or centrifugal compressor, comprising:

at least one module configured to

determine an actual flow value without using a flow or pressure sensor based at least partly on a comparison of speed and power sensed in relation to the current operation of the pump and information contained in a calibrated curve of speed versus closed valve power together with published pump performance data, including best efficiency power, closed valve power and best efficiency flow at rated pump speed;

determine a corrected threshold flow value based at least partly on a flow value associated with an unfavorable operating condition of the pump and corrected based on a relationship between a current operating speed of the pump and a rated operating speed of the pump; and

control the operation of the pump based at least partly on a comparison between the actual flow value and the corrected threshold flow value in order to provide pump protection for the pump.

14. A controller according to claim 13, wherein the module is configured to adapt the operation of the pump based at least partly on the comparison, including using a user settable delay in reacting to the condition prior to issuing either a warning only, warning and reduction in speed to a safe operating speed, faulting and shutting down the motor or automatically resetting the fault and restarting the pump and motor to check if the condition has cleared, and where the condition clears the adaptation is revoked and the pump resumes normal operation.

15. A controller according to claim 13, wherein the relationship is a ratio of the current operating speed of the pump divided by the rated operating speed of the pump.

16. A controller according to claim 13, wherein the corrected threshold flow value includes a runout condition value, a minimum flow value, or some combination thereof.

17. A controller according to claim 13, wherein the at least one module is configured to compare a runout condition value to an actual runout flow value in order to determine a runout condition of the pump.

18. A controller according to claim 13, wherein the at least one module is configured to compare a corrected minimum flow value to an actual minimum flow value in order to determine either a normal flow condition or a possible minimum flow condition of the pump.

19. A controller according to claim 13, wherein the at least one module is configured to compare a corrected minimum threshold flow value to an actual flow value and also compare an actual power value to a closed valve power value at the current speed of the pump in order to determine either a minimum flow condition or a dry run condition of the pump.

20. A controller according to claim 13, wherein the at least one module is configured to compare a corrected minimum threshold flow value to an actual flow value, and also compare an actual power value to a closed valve power value at the current speed of the pump, in order to determine either a minimum flow condition or a dry run condition of the pump, where the closed valve power value is interpolated from a calibrated power vs speed curve stored in a memory device.

21. A controller according to claim 13, wherein a Dry Run condition is declared if P_ACT is less than K_DR×

P<sub>SO—

N</sub>, where P_ACT is an actual power corrected for a specific gravity of 1, where K_DR is a coefficient multiplied by a closed valve power at a current operating speed, and where P<sub>SO—

N</sub> is the closed valve power at the current speed corrected for the specific gravity of 1.

22. A controller according to claim 19, wherein either the actual power value, the closed valve power value or the combination thereof are corrected for specific gravity of the medium being pumped.

23. A controller according to claim 19, wherein the corrected Minimum Flow Threshold value is based at least partly on the equation Q_MIN—

_COR=QMIN×

(N_ACT/N_RATED), where Q<sub>MIN—

COR</sub> is a minimum flow corrected for speed, where Q_MIN is a minimum flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

24. A controller according to claim 13, wherein the runout condition value is a corrected Runout Flow Threshold value that is based at least partly on the equation Q_RO—

_COR=Q_RO×

(N_ACT/N_RATED), where Q<sub>RO—

COR</sub> is a runout flow corrected for speed, where Q_RO is the runout flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

25. A controller according to claim 13, wherein the controller is a variable frequency controller or a programmable logic controller.

44. A controller according to claim 16, wherein the at least one module is configured to compare a runout condition value to an actual runout flow value in order to determine a runout condition of the pump.

45. A controller according to claim 20, wherein a Dry Run condition is declared if P_ACT is less than K_DR X P_SO—

_N, where P_ACT is an actual power corrected for a specific gravity of 1, where K_DR is a coefficient multiplied by a closed valve power at a current operating speed, and where P<sub>SO—

N</sub> is the closed valve power at the current speed corrected for the specific gravity of 1.

46. A controller according to claim 20 wherein the corrected Minimum Flow Threshold value is based at least partly on the equation Q_MIN—

_COR=Q_MIN×

(N_ACT/N_RATED), where Q<sub>MIN—

COR</sub> is a minimum flow corrected for speed, where Q_MIN is the minimum flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

47. A controller according to claim 17, wherein the corrected Runout Flow Threshold value is based at least partly on the equation Q_RO—

_COR=Q_RO×

(N_ACT/N_RATED), where Q<sub>RO—

COR</sub> is a runout flow corrected for speed, where Q_RO is the runout flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

48. A controller according to claim 19, wherein the actual flow value is calculated from a calibrated speed vs closed valve power curve stored in the evaluation device, motor signals for speed and power (or torque) and basic published pump performance data such as best efficiency power, closed valve power and best efficiency flow at the rated pump speed.

26. A centrifugal pump system or system with other centrifugal device such as a centrifugal mixer, centrifugal blower or centrifugal compressor having a controller for controlling the operation of a pump, including a centrifugal pump, centrifugal mixer, centrifugal blower or centrifugal compressor, the controller comprising:

at least one module configured to

determine an actual flow value without using a flow or pressure sensor based at least partly on a comparison of speed and power sensed in relation to the current operation of the pump and information contained in a calibrated curve of speed versus closed valve power together with published pump performance data, including best efficiency power, closed valve power and best efficiency flow at rated pump speed;

determine a corrected threshold flow value based at least partly on a flow value associated with an unfavorable operating condition of the pump and corrected based on a relationship between a current operating speed of the pump and a rated operating speed of the pump; and

control the operation of the pump based at least partly on a comparison between the actual flow value and the corrected threshold flow value in order to provide pump protection for the pump.

27. A pump system according to claim 26, wherein the at least one module is configured to adapt the operation of the pump based at least partly on the comparison, including using a user settable delay in reacting to the condition prior to issuing either a warning only, warning and reduction in speed to a safe operating speed, faulting and shutting down the motor or automatically resetting the fault and restarting the pump and motor to check if the condition has cleared, and where if the condition clears the adaptation is revoked and the pump resumes normal operation.

28. A pump system according to claim 26, wherein the relationship is a ratio of the current operating speed of the pump divided by the rated operating speed of the pump.

29. A pump system according to claim 26, wherein the corrected threshold flow value includes a runout condition value, a minimum flow value, or some combination thereof.

30. A pump system according to claim 26, wherein the at least one module is configured to compare a runout condition value to an actual runout flow value in order to determine a runout condition of the pump.

31. A pump system according to claim 26, wherein the at least one module is configured to compare a corrected minimum flow value to an actual minimum flow value in order to determine either a normal flow condition or a possible minimum flow condition of the pump.

32. A pump system according to claim 26, wherein the at least one module is configured to compare a corrected minimum threshold flow value to an actual flow value and also comparing an actual power value to a closed valve power value at the current speed of the pump in order to determine either a minimum flow condition or a dry run condition of the pump.

33. A pump system according to claim 26, wherein the method further comprises comparing, a corrected minimum threshold flow value to an actual flow value and also comparing an actual power value to a closed valve power value at the current speed of the pump in order to determine either a minimum flow condition or a dry run condition of the pump, and where the closed valve power value is interpolated from a calibrated power vs speed curve stored in a memory device.

34. A pump system according to claim 26, wherein a Dry Run condition is declared if P_ACT is less than K_DR×

P<sub>SO—

N</sub>, where P_ACT is an actual power corrected for a specific gravity of 1, where K_DR is a coefficient multiplied by a closed valve power at a current operating speed, and where P<sub>SO—

N</sub> is the closed valve power at the current speed corrected for the specific gravity of 1.

35. A pump system according to claim 26, wherein either the actual power value, the closed valve power value or the combination thereof are corrected for specific gravity of the medium being pumped.

36. A pump system according to claim 33, wherein the corrected Minimum Flow Threshold value is based at least partly on the equation Q_MIN—

_COR=Q_MIN×

(N_ACT/N_RATED), where Q<sub>MIN—

COR</sub> is a minimum flow corrected for speed, where Q_MIN is the minimum flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

37. A pump system according to claim 26, wherein the runout condition value is a corrected Runout Flow Threshold value that is based on the equation Q_RO—

_COR=Q_RO×

(N_ACT/N_RATED), where Q<sub>RO—

COR</sub> is a runout flow corrected for speed, where Q_RO is the runout flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

38. A pump system according to claim 26, wherein the controller is a variable frequency controller or a programmable logic controller.

49. A pump system according to claim 29, wherein the at least one module is configured to compare a runout condition value to an actual runout flow value in order to determine a runout condition of the pump.

50. A pump system according to claim 33, wherein a Dry Run condition is declared if P_ACT is less than K_DR X P_SO—

_N, where P_ACT is an actual power corrected for a specific gravity of 1, where K_DR is a coefficient multiplied by a closed valve power at a current operating speed, and where P<sub>SO—

N</sub> is the closed valve power at the current speed corrected for the specific gravity of 1.

51. A pump system according to claim 32, wherein either the actual power value, the closed valve power value or the combination thereof are corrected for specific gravity of the medium being pumped.

52. A pump system according to claim 32, wherein the corrected Minimum Flow Threshold value is based at least partly on the equation Q_MIN—

_COR=Q_MIN×

(N_ACT/N_RATED), where Q<sub>MIN—

COR</sub> is a minimum flow corrected for speed, where Q_MIN is the minimum flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

53. A pump system according to claim 30, wherein the corrected Runout Flow Threshold value is based at least partly on the equation Q_RO—

_COR=Q_RO×

(N_ACT/N_RATED), where Q<sub>RO—

COR</sub> is a runout flow corrected for speed, where Q_RO is the runout flow, where N_ACT is an actual speed, and where N_RATED is a rated speed.

54. A pump system according to claim 32, wherein the actual flow value is calculated from a calibrated speed vs closed valve power curve stored in the evaluation device, motor signals for speed and power (or torque) and basic published pump performance data such as best efficiency power, closed valve power and best efficiency flow at the rated pump speed.