Pump controller system and method
US-9328727-B2 · May 3, 2016 · US
US10048701B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10048701-B2 |
| Application number | US-201213717086-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 17, 2012 |
| Priority date | Dec 16, 2011 |
| Publication date | Aug 14, 2018 |
| Grant date | Aug 14, 2018 |
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Apparatus, such as a pump controller, features a signal processor configured at least to: receive signaling containing information about a linear set point control curve based at least partly on an adaptive set point control curve related to fluid being pumped by a pump in a pumping system, and determine a control set point based at least partly on the signaling received. The signal processor may be configured to provide a control signal containing information to control the pump based on the control set point determined.
Opening claim text (preview).
What we claim is: 1. A pump controller for providing an adaptive pump control to reduce energy consumption and operating cost of a heating and water cooling system, comprising: a signal processor configured at least to: receive signaling containing information about a linear set point control curve derived from adaptive and constant set point control curves related to fluid being pumped by a pump in a pumping system, and determine corresponding signal containing information about a control set point to control and vary adaptively the speed of the pump in the pumping system using an adaptive control algorithm that obtains the control set point from the linear set point control curve derived, based at least partly on the signaling received. 2. The pump controller according to claim 1 , wherein the signal processor is configured to provide the corresponding signaling as a control signal containing information to control the pump based at least partly on the control set point determined. 3. The pump controller according to claim 1 , wherein the linear set point control curve is derived from the adaptive set point control curve with respect to system flow and pressure, including being derived from by the signal processor. 4. The pump controller according to claim 1 , wherein the signal processor is configured to determine a pressure set point P*(t) with respect to a requested flow rate Q*(t) using the linear set point control curve based at least partly on the following equation: P *( t )= P 0 Q *( t )/ Q max +b 0 , where P 0 is a constant pressure set point, Q*(t) is a requested flow rate Q max is a maximum system flow rate, Q max is a maximum adaptive flow rate, and b 0 is a pressure threshold. 5. The pump controller according to claim 4 , wherein the signal processor is configured to determine a system flow rate as a summation of each individual zone flow rate, based as least partly on the following equation: Q * ( t ) = ∑ i = 1 n Q i * ( t ) , where Q i * is a flow rate at zone i and n is the total number of zones. 6. The pump controller according to claim 5 , wherein the signal processor is configured to determine the system flow rate if zone temperature control parameters are used, based at least partly on the following equation: Q * ( t ) = α ∑ i = 1 n Q i , max ( T i * ( t ) - T outdoor ) / ( T i , max - T outdoor ) , where T i * is a temperature set point for zone i, Q i,max is a maximum flow rate to obtain a maximum temperature, T i,max is designated for a zone i, T outdoor is the outdoor temperature, and α is a compensate coefficient. 7. The pump controller according to claim 1 , wherein the signal processor is configured to determine a requested flow rate Q* (t) based at least partly on the following equation: Q * ( t ) = ( 1 - r ) C v 2 ( t ) / C _ v m ( t ) ( 1 +
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