Method for optimizing valve position and pump speed in a PID control valve system without the use of external signals

1. A controller comprising:

at least one module configured to determine flow reference data based at least partly on signalling containing information about various pump and motor parameters including speed, torque or power, or from calibrated flow curves stored in an evaluation device, or from an external flow reference including a flowmeter; and

at least one module, which is configured to utilize the flow reference data in order to provide corresponding signalling containing information to control a centrifugal pump, centrifugal blower, centrifugal mixer or centrifugal compressor, driven via a variable frequency drive, in a PID control valve system, wherein, once a PID control valve has reached its steady state normal condition, a calculated flow value is captured and compared to a current flow value obtained after the variable frequency drive has decreased in frequency (speed).

2. A controller according to claim 1 , wherein a valve position is optimized just prior to a speed threshold where a flow condition of an algorithm is no longer true.

3. A controller according to claim 1 , wherein a valve position is optimized just prior to reaching minimum speed if a flow condition remains true.

4. A controller according to claim 1 , wherein for pressure control applications a valve position is optimized if current flow is within 90-110% of a pump best efficiency flow at current speed.

5. A controller according to claim 1 , wherein a final check is made for a wide open control valve condition by increasing pump speed a set amount and comparing the current flow value to a saved flow value, and if there is no increase in flow a valve position is optimized.

6. A controller according to claim 1 , wherein if the controller has already reached its optimized state, and if either an actual motor torque increases by 5% or greater, or actual flow increases by 5% or greater for longer than a delay period, an valve optimization process is restarted at maximum speed.

7. A controller according to claim 1 , wherein if the controller has already reached its optimized state, and if either an actual motor torque decreases by 5% or more, or actual flow decreases by 5% or more, a valve optimization process restarts at a current operating point.

8. A controller according to claim 1 , wherein a secondary user selectable wide open valve check is made if a change in an actual motor torque is 2% or more but less than 5% of an optimized state for a response delay period, and if this condition is true and actual flow is greater than an optimized flow value after a speed increment change, an optimization process is restarted at maximum speed.

9. A method comprising:

determining in at least one module flow reference data as a function of various pump and motor parameters including speed, torque or power, or from calibrated flow curves stored in an evaluation device, or from an external flow reference including a flowmeter; and

utilizing in at least one module the flow reference data in order to control a centrifugal pump centrifugal blower, centrifugal mixer or centrifugal compressor, driven via a variable frequency drive, in a PID control valve system, wherein, once a PID control valve has reached its steady state normal condition, a calculated flow value is captured and compared to a current flow value obtained after the variable frequency drive has decreased in frequency (speed).

10. A method according to claim 9 , wherein a valve position is optimized just prior to a speed threshold where a flow condition of an algorithm is no longer true.

11. A method according to claim 9 , wherein a valve position is optimized just prior to reaching minimum speed if a flow condition remains true.

12. A method according to claim 9 , wherein for pressure control applications a valve position is optimized if current flow is within 90-110% of a pump best efficiency flow at current speed.

13. A method according to claim 9 , wherein a final check is made for a wide open control valve condition by increasing pump speed a set amount and comparing the current flow value to a saved flow value, and if there is no increase in flow a valve position is optimized.

14. A method according to claim 9 , wherein if the controller has already reached its optimized state, and if either an actual motor torque increases by 5% or greater, or actual flow increases by 5% or greater for longer than a delay period, a valve optimization process is restarted at maximum speed.

15. A method according to claim 9 , if the controller has already reached its optimized state, and if either an actual motor torque decreases by 5% or more, or the actual flow decreases by 5% or more, the valve optimization process restarts at a current operating point.

16. A method according to claim 9 , wherein a secondary user selectable wide open valve check is made if a change in an actual motor torque is 2% or more but less than 5% of an optimized state for a response delay period, and if this condition is true and actual flow is greater than an optimized flow value after a speed increment change, an optimization process is restarted at maximum speed.

17. A controller comprising:

at least one module configured to determine flow reference data based at least partly on signalling containing information about various pump and motor parameters including speed, torque or power, or from calibrated flow curves stored in an evaluation device, without using a flow sensor; and

at least one module, which is configured to utilize the flow reference data in order to provide corresponding signalling containing information to control a centrifugal pump, centrifugal blower, centrifugal mixer or centrifugal compressor, driven via a variable frequency drive, in a PID control valve system, wherein, once a PID control valve has reached its steady state normal condition, a calculated flow value is captured and compared to a current flow value obtained after the variable frequency drive has decreased in frequency (speed).

18. A controller according to claim 17 , wherein a valve position is optimized just prior to a speed threshold where a flow condition of an algorithm is no longer true.

19. A controller according to claim 17 , wherein a valve position is optimized just prior to reaching minimum speed if a flow condition remains true.

20. A controller according to claim 17 , wherein for pressure control applications a valve position is optimized if current flow is within 90-110% of a pump best efficiency flow at current speed.

21. A controller according to claim 17 , wherein a final check is made for a wide open control valve condition by increasing pump speed a set amount and comparing the current flow value to a saved flow value, and if there is no increase in flow a valve position is optimized.

22. A controller according to claim 17 , wherein if the controller has already reached its optimized state, and if either an actual motor torque increases by 5% or greater, or actual flow increases by 5% or greater for longer than a delay period, an valve optimization process is restarted at maximum speed.

23. A controller according to claim 17 , wherein if the controller has already reached its optimized state, and if either an actual motor torque decreases by 5% or more, or actual flow decreases by 5% or more, a valve optimization process restarts at a current operating point.

24. A controller according to claim 17 , wherein a secondary user selectable wide open valve check is made if a change in an actual motor torque is 2% or more but less than 5% of an optimized state for a response delay period, and if this condition is true and actual flow is greater than an optimized flow value after a speed increment change, an optimization process is restarted at maximum speed.

25. A method comprising:

determining in at least one module flow reference data based at least partly on signalling containing information about various pump and motor parameters including speed, torque or power, or from calibrated flow curves stored in an evaluation device, without using a flow sensor; and

utilizing in at least one module the flow reference data in order to control a centrifugal pump, centrifugal blower, centrifugal mixer or centrifugal compressor, driven via a variable frequency drive, in a PID control valve system, wherein, once a PID control valve has reached its steady state normal condition, a calculated flow value is captured and compared to a current flow value obtained after the variable frequency drive has decreased in frequency (speed).

26. A method according to claim 25 , wherein a valve position is optimized just prior to a speed threshold where a flow condition of an algorithm is no longer true.

27. A method according to claim 25 , wherein a valve position is optimized just prior to reaching minimum speed if a flow condition remains true.

28. A method according to claim 25 , wherein for pressure control applications a valve position is optimized if current flow is within 90-110% of a pump best efficiency flow at current speed.

29. A method according to claim 25 , wherein a final check is made for a wide open control valve condition by increasing pump speed a set amount and comparing the current flow value to a saved flow value, and if there is no increase in flow a valve position is optimized.

30. A method according to claim 25 , wherein if the controller has already reached its optimized state, and if either an actual motor torque increases by 5% or greater, or actual flow increases by 5% or greater for longer than a delay period, a valve optimization process is restarted at maximum speed.

31. A method according to claim 25 , if the controller has already reached its optimized state, and if either an actual motor torque decreases by 5% or more, or actual flow decreases by 5% or more, the valve optimization process restarts at a current operating point.

32. A method according to claim 25 , wherein a secondary user selectable wide open valve check is made if a change in an actual motor torque is 2% or more but less than 5% of an optimized state for a response delay period, and if this condition is true and actual flow is greater than an optimized flow value after a speed increment change, an optimization process is restarted at maximum speed.