WO2015157276A2 - Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring - Google Patents

Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring Download PDF

Info

Publication number
WO2015157276A2
WO2015157276A2 PCT/US2015/024703 US2015024703W WO2015157276A2 WO 2015157276 A2 WO2015157276 A2 WO 2015157276A2 US 2015024703 W US2015024703 W US 2015024703W WO 2015157276 A2 WO2015157276 A2 WO 2015157276A2
Authority
WO
WIPO (PCT)
Prior art keywords
pump
motor
power
signal processor
processing module
Prior art date
Application number
PCT/US2015/024703
Other languages
French (fr)
Other versions
WO2015157276A3 (en
Inventor
Andrew A. CHENG
James J. GU
Graham A. Scott
Original Assignee
Fluid Handling Llc
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Fluid Handling Llc filed Critical Fluid Handling Llc
Priority to CN201580029040.1A priority Critical patent/CN106461444B/en
Priority to RU2016139339A priority patent/RU2680474C2/en
Priority to EP15777215.3A priority patent/EP3129756A4/en
Priority to CA2944881A priority patent/CA2944881C/en
Priority to MX2016013258A priority patent/MX357724B/en
Publication of WO2015157276A2 publication Critical patent/WO2015157276A2/en
Publication of WO2015157276A3 publication Critical patent/WO2015157276A3/en

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B49/00Control, e.g. of pump delivery, or pump pressure of, or safety measures for, machines, pumps, or pumping installations, not otherwise provided for, or of interest apart from, groups F04B1/00 - F04B47/00
    • F04B49/06Control using electricity
    • F04B49/065Control using electricity and making use of computers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C14/00Control of, monitoring of, or safety arrangements for, machines, pumps or pumping installations
    • F04C14/08Control of, monitoring of, or safety arrangements for, machines, pumps or pumping installations characterised by varying the rotational speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D15/00Control, e.g. regulation, of pumps, pumping installations or systems
    • F04D15/0088Testing machines
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B2203/00Motor parameters
    • F04B2203/02Motor parameters of rotating electric motors
    • F04B2203/0208Power
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04BPOSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
    • F04B2203/00Motor parameters
    • F04B2203/02Motor parameters of rotating electric motors
    • F04B2203/0209Rotational speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C2270/00Control; Monitoring or safety arrangements
    • F04C2270/02Power
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04CROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; ROTARY-PISTON, OR OSCILLATING-PISTON, POSITIVE-DISPLACEMENT PUMPS
    • F04C2270/00Control; Monitoring or safety arrangements
    • F04C2270/80Diagnostics
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2260/00Function
    • F05D2260/82Forecasts
    • F05D2260/821Parameter estimation or prediction
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2270/00Control
    • F05D2270/30Control parameters, e.g. input parameters
    • F05D2270/304Spool rotational speed
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F05INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
    • F05DINDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
    • F05D2270/00Control
    • F05D2270/30Control parameters, e.g. input parameters
    • F05D2270/335Output power or torque

Definitions

  • the present invention builds on the family of technologies disclosed in the aforementioned related applications.
  • the present invention relates to a technique for controlling the operation of a pump; and more particularly, the present invention relates to a method and apparatus for controlling and/or monitoring a pump, e.g., including for domestic and commercial heating or cooling water systems.
  • Hydronic pumping system sensorless control and monitoring techniques are known in the art, e.g., including a 3D discrete and a mixed theoretical and 3D discrete sensorless conversion methods, consistent with that disclosed in the aforementioned related patent application identified as reference nos. 3-5.
  • the system pressure and flow rate may be resolved directly from a pair of motor readout values with a conversion error around 5-15% by the 3D discrete sensorless converter, e.g., based upon pump calibration data in the aforementioned reference no. 4.
  • the mixed theoretical and discrete sensorless converter disclosed in the aforementioned reference no. 3 yields a conversion error around 10-20% without a need of instrumentation calibration, even though a power distribution data with respect to system coefficient and motor speed is still needed to convert the system coefficient on a varying hydronic system.
  • the equivalent hydronic system characteristics coefficient is an unknown variable in general dependent on the valves open position and system dynamic friction loss as well.
  • the pump efficiency under such a varying hydronic system is a changing variable due to motor speed slip under the varying hydronic load as well as some pump mechanical friction induced thermal consumption effects, especially at low speed with system nearly shut off. Therefore, the inventors of this application also recognize and appreciate that it is a quite challenge job to formulate any theoretic expressions for the reconstruction of a pump sensorless converter which yields the system pressure and flow directly from motor readout values, such as power, current, torque, speed, and so on so forth.
  • the present invention provides a new and unique best-fit affinity sensorless conversion means or technique for deriving pump or system pressure and flow rate at a given pair of motor readout values of power and speed, e.g., based upon using pump and system characteristics equations together with an empirical power equation.
  • the pump characteristics equation and the empirical power equation may be reconstructed by a polynomial best-fit function together with the pump affinity laws or its modified version, e.g., based upon the pump curve published by pump manufacturers.
  • System pressures and flow rate may be, therefore, resolved at the stead state equilibrium point of pump and system
  • the present invention may include, or take the form of, apparatus featuring a signal processor or processing module configured at least to:
  • the signal processor or processing module may be configured to resolve pump differential pressures and flow rate at an equilibrium point of the pump or system pressure at a motor steady state condition.
  • the signal processor or processing module 1 0a may also be configured to provide corresponding signaling containing information about the pump or system pressure and the flow rate, including for pump differential pressure and flow monitoring.
  • the corresponding signaling may be used to control a hydronic pumping system.
  • the apparatus includes, or takes the form of, the hydronic pumping system, e.g., having such a signal processor or processing module.
  • the signaling received may be sensed and received from suitable sensors configured to measure motor readout values of power and speed.
  • the signaling received may be stored and received from suitable memory modules, e.g., configured with pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer.
  • the signal processor or processing module may include, or take the form of, at least one processor and at least one memory including computer program code, and the at least one memory and computer program code are configured to, with at least one processor, to cause the signal processor or processing module at least to receive the signaling (or, for example, associated signaling) and determine the adaptive pressure set point.
  • the signal processor or processing module may be configured to suitable computer program code in order to implement suitable signal processing algorithms and/or functionality, consistent with that set forth herein.
  • the apparatus may include, or take the form of, a pump control or controller, including a PID control, having the signal processor or signal processor module, e.g., including for monitoring pump differential pressure and flow.
  • the present invention may take the form of a method including steps for: receiving in a signal processor or processing module signaling containing information about motor readout values of power and speed, and also about pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer; and determining in the signal processor or processing module corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received.
  • the method may also include one or more of the features set forth herein, including providing from the signal processor or processing module corresponding signaling containing information about the pump or system pressure and the flow rate, e.g., which may be used to control a hydronic pumping system.
  • the present invention may also, e. g., take the form of a computer program product having a computer readable medium with a computer executable code embedded therein for implementing the method, e.g., when run on a signaling processing device that forms part of such a pump controller.
  • the computer program product may, e. g., take the form of a CD, a floppy disk, a memory stick, a memory card, as well as other types or kind of memory devices that may store such a computer executable code on such a computer readable medium either now known or later developed in the future.
  • the embodiments disclosed herein provides best-fit affinity sensorless conversion means or techniques for deriving pump or system pressure and flow rate at a given pair of motor readout values of power and speed, e.g., based upon using pump and system characteristics equations together with empirical power equations.
  • the pump characteristics equation and the empirical power equation may be constructed by the polynomial best-fit function together with the pump affinity laws based upon the pump curve published by pump
  • Pump differential pressures and flow rate may be resolved at the equilibrium point of pump and system pressures at the motor steady state accordingly.
  • the pump sensorless conversion means or technique disclosed herein may be much easier to be applied for most practical hydronic pumping control and monitoring applications with satisfactory accuracy.
  • Figure 1 is a schematic diagram of a hydronic sensorless pumping control system that is known in the art, e.g., in which the present invention may be implemented, according to some embodiment.
  • Figure 2 is a schematic diagram of sensorless conversion for pump pressure and flow rate from sensed power and speed.
  • Figure 3 is a graph of pressure (Ft) in relation to flow (GPM) showing pump, system and power characteristics curves and a pressure equilibrium point at a steady state, according to implementation of some embodiments of the present invention.
  • Figure 4 is a graph of power (hp) in relation to system characteristics
  • Figure 5 is a graph of pressure (Ft) with respect to flow (GPM) showing pump differential pressure versus system flow rate from the sensorless converter (see solid lines) and the measured or sensed data from sensors (see symbols (e.g., diamonds, triangles, stars, plus signs, minus signs, boxes, and "x"s) at various speeds, including 24Hz, 30Hz, 36Hz, 42Hz, 48Hz, 54Hz and 60Hz.
  • Ft pressure
  • GPM flow
  • Figure 6 is a block diagram of apparatus, e.g., having a signal processor or processing module configured for implementing the signal processing functionality, according to some embodiments of the present invention.
  • Figure 1 shows a hydronic sensorless pumping control system having a combination of a centrifugal pump connected to piping with a flow and a controller, e.g., in which the present invention may be implemented.
  • the system flow rate and pressure at a motor speed and a system position may be resolved at the steady state equilibrium point of pump and system pressures which is the intersection of the pump and system curves functions shown schematically in Figure. 3.
  • the system flow rate may be derived using Equation (1 ) as: where C v is the system coefficient, and a, b and c are the coefficients of a second order best-fit pump curve function at motor full speed of n ⁇ .
  • the corresponding dynamic system characteristic coefficient should typically be known first.
  • an empirical power and system characteristics relation based on the power curve at motor full speed n ⁇ as well as the affinity law may be used, which is schematically shown in Figure 4.
  • the motor power function at maximum speed with respect to the system coefficient may be reconstructed first by using a fitting or interpolating technique.
  • Equation (3) the system coefficient C v may be expressed explicitly in form of Equation (3) as:
  • Equation (4) ⁇ f A , (3)
  • w motor power at a speed of n
  • A, B and C are the coefficients of the second order best-fit motor power function at motor maximum speed with respect to the normalized system coefficient of C£ or? " .
  • ⁇ 0 (A ! (nfn max + B ! (n/n max ⁇ 2 + C' in/n, ⁇ ) 1 + D' (6)
  • A', B' C and D' are the coefficients of the third order best-fit power function of the power values normalized at maximum speed with respect to the normalized motor speed of njn max .
  • the modified affinity law is the third order polynomial approximation for representing power and speed relation, which is obtained through fitting or interpolating with an array of power values measured at a set of given speeds at a system position.
  • the system position can be anywhere from shut off to fully open, since the normalized power distribution of / * (n) is nearly identical at any system position.
  • Equations nos. 3- 6 may be presented in some other expressions as well if other kinds of curve fitting or interpolating approaches are used alternatively.
  • Equations 1 and 2 The system flow rate and pressure at the equilibrium point of pump and system pressure at a steady state motor speed associated with its corresponding power consumption can, therefore, be obtained by Equations 1 and 2, as far as the system coefficient of C v is obtained by use of Equations 3 and 4 or 5 accordingly, which may be called the so-called best-fit affinity sensorless converter in this disclosure.
  • the pressure and flow rate values may be collected from a pumping system and compared with the data measured from sensors.
  • the results shown in Figure 5 demonstrates quite satisfactory accuracy mostly around 5-10% error at whole speed regions from 30 up to 60 Hz in pump normal working hydronic region and around 10-20% error at low speed region and when system is nearly shut off in general.
  • the best-fit affinity sensorless converter disclosed herein may be used for most practical hydronic pumping control and monitoring applications, since it is formulated from pump, power characteristics equations as well as affinity law and reconstructed by polynomial best-fit based on the pump data published by pump manufacturers.
  • the converter is much easier to be set up while maintaining satisfactory accuracy. Most importantly above all, there may be no need for tedious and time consuming instrumentation calibration process, as long as manufacturers published data or curves are available.
  • Figure 6 shows apparatus 10 according to some embodiments of the present invention, e.g., featuring a signal processor or processing module 10a configured at least to:
  • the signal processor or processing module may be configured to resolve pump differential pressures and flow rate at an equilibrium point of the pump or system pressure at a motor steady state condition.
  • the signal processor or processing module 1 0a may also be configured to provide corresponding signaling containing information about the pump or system pressure and the flow rate, including for pump differential pressure and flow monitoring.
  • the corresponding signaling may be used to control a hydronic pumping system.
  • the present invention may be implemented using pump and system characteristics equations and empirical power equations, e.g., consistent with that set forth herein, as well as by using other types or kinds of pump and system characteristics equations and empirical power equations that are either now known or later developed in the future.
  • the functionality of the apparatus 10 may be implemented using hardware, software, firmware, or a combination thereof.
  • the apparatus 10 would include one or more microprocessor-based architectures having, e. g., at least one signal processor or microprocessor like element 10a.
  • a person skilled in the art would be able to program such a
  • the signal processor or processing module 10a may be configured, e.g., by a person skilled in the art without undue experimentation, to receive the signaling containing information about the motor readout values of power and speed, and also about the pump and system characteristics equations together with the empirical power equations that are constructed by the polynomial best-fit function together with the pump affinity laws based upon the pump curve published by the pump manufacturer, consistent with that disclosed herein.
  • the information about the motor readout values of power and speed may be included in sensed signaling received, processed and/or stored, e.g., in a suitable memory module that forms part of such a microprocessor-based architecture.
  • the information about the pump and system characteristics equations together with the empirical power equations that are constructed by the polynomial best-fit function together with the pump affinity laws based upon the pump curve published by the pump manufacturer may be received, processed and/or stored, in a suitable memory module that forms part of such a microprocessor-based architectures.
  • the signal processor or processing module 10a may be configured, e.g., by a person skilled in the art without undue experimentation, to determine the corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received, consistent with that disclosed herein.
  • the scope of the invention is not intended to be limited to any particular implementation using technology either now known or later developed in the future.
  • the scope of the invention is intended to include implementing the functionality of the processors 10a as stand-alone processor or processor module, as separate processor or processor modules, as well as some combination thereof.
  • the apparatus 10 may also include, e.g., other signal processor circuits or components 10b, including random access memory or memory module(RAM) and/or read only memory (ROM), input/output devices and control, and data and address buses connecting the same, and/or at least one input processor and at least one output processor .
  • other signal processor circuits or components 10b including random access memory or memory module(RAM) and/or read only memory (ROM), input/output devices and control, and data and address buses connecting the same, and/or at least one input processor and at least one output processor .
  • the present invention may include, or take the form of, one or more of the following various embodiments:
  • the present invention may be implemented using one preferred version of the best-fit affinity sensorless conversion means or technique for pump differential pressure and flow mentioned above, e.g., may include a solution of pump differential pressure, or system pressure, and flow rate at the steady state equilibrium point of the pump differential pressure and system pressure, which is the intersection of the pump and system curves schematically shown.
  • the present invention may be implemented using the pump curves equations in the best-fit affinity sensorless conversion means or technique mentioned above, e.g., that may include pump curve models which are developed based upon the pump characteristics equations at a motor speed and system flow rate.
  • the present invention may be implemented using the steady state pressure equilibrium point in the best-fit affinity sensorless conversion means or technique mentioned above, that may include the intersection point of the pump and system curves functions, as shown in Fig. 3.
  • the system pressure or pump differential pressure and flow rate may be solved at the pressures equilibrium point for a pair of motor readout values given, for instance, speed and power, as the sensorless output values converted.
  • the aforementioned Eqs. 1 and 2 presented as and
  • the equations for converting the system pressure and flow rate may be written in some other forms as well by following the stead state pressure equilibrium point approach, however, in case that the higher order fitting or interpolating functions or some other forms of functions are used, if desirable.
  • the present invention may be implemented using the empirical power function to resolve the equivalent system characteristics coefficient with respect to motor power and speed in the best-fit affinity sensorless conversion means or technique mentioned above, e.g., that may include the empirical power function of w(C V! ii) with respect to motor speed and system flow rate.
  • the power curve models mentioned here may be expressed approximately by function of w(C v , n) based upon the power curve at full speed, exactly corresponded to the pump curve, and affinity law.
  • the best-fit affinity approach may be used to formulate the power curve function of f w(C v ,n). For instance, a second order best-fit affinity polynomial function of Eq.
  • the present invention may be implemented using one preferred version of the empirical power function in the best-fit affinity sensorless conversion means for pump differential pressure and flow mentioned above, e.g., that may include a best-fit affinity polynomial function of the Equation
  • the modified power affinity law of f*(n) is obtained by fitting an array of power values normalized at its corresponding maximum value at full speed with a set of given speeds at a given system position ,which may be used to compensate the power variation at low speed region with system shut down.
  • the present invention may be implemented using the system characteristics coefficient conversion in the best-fit affinity sensorless conversion means or technique, e.g., that may include all forms of expressions either a close form solution or a solution using some discrete numerical methods.
  • the present invention may be implemented using the hydronic pumping system in the best-fit affinity sensorless conversion means or technique, e.g., that may include all close loop or open loop hydronic pumping systems, such as primary pumping systems, secondary pumping systems, water circulating systems, and pressure booster systems.
  • the systems mentioned here may consist of a single zone or multiple zones as well.
  • the present invention may be implemented using the pump and power curves data at motor maximum speed in the best-fit affinity sensorless conversion means or technique, e.g., that may include the pump and power curves data published by pump manufacturers or a few points of pump data acquired at motor full speed in field.
  • the motor power curve data may also be replaced by any potential motor electrical or mechanical readout signals, such as motor current or torque, and so forth.
  • the present invention may be implemented using the hydronic signals for in the best-fit affinity sensorless conversion means or technique, e.g., that may include pump differential pressure, system pressure or zone pressure, system or zone flow rate, and so forth.
  • control signals transmitting and wiring technologies e.g., that may include all conventional sensing and transmitting means that are used currently.
  • wireless sensor signal transmission technologies would be optimal and favorable.
  • the present invention may be implemented using the pumps mentioned above for the hydronic pumping systems, e.g., that may include a single pump, a circulator, a group of parallel ganged pumps or circulators, a group of serial ganged pumps or circulators, or their combinations.
  • the present invention may be implemented using systems flow regulation, e.g., that may include manual or automatic control valves, manual or automatic control circulators, or their combinations.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Computer Hardware Design (AREA)
  • Control Of Non-Positive-Displacement Pumps (AREA)
  • Measuring Volume Flow (AREA)
  • Combined Controls Of Internal Combustion Engines (AREA)

Abstract

The present invention provides apparatus, including a hydronic sensorless pumping system, that features a signal processor or processing module configured to receive signaling containing information about motor readout values of power and speed, and also about pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer; and determine corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received.

Description

BEST-FIT AFFINITY SENSORLESS CONVERSION MEANS OR TECHNIQUE FOR PUMP DIFFERENTIAL PRESSURE AND FLOW MONITORING
CROSS REFERENCE TO RELATED APPLICATION
This application claims benefit to U.S. provisional application no. 61/976,749 (Atty Dckt No. 91 1 -019.014-1 //F-B&G-X0012US01 ), filed 8 April 2014, entitled "A Best-fit affinity sensorless conversion means for pump differential pressure and flow monitoring," which is hereby incorporated by reference in its entirety.
This application is also related to a family of technologies developed by one or more of the inventors and disclosed in the following applications:
1 ) U.S. application serial no. 12/982,286 (Atty Dckt No. 91 1 -019.001 -
1 //F-B&G-1001 ), filed 30 December 2010, entitled "Method and apparatus for pump control using varying equivalent system characteristic curve, AKA an adaptive control curve," which issued as U.S. Patent No. 8,700,221 on 15 April 2014;
2) U.S. application serial no. 13/717,086 (Atty Dckt No. 91 1 -019.004- 2//F-B&G-X0001 ), filed 17 December 2012, entitled "Dynamic linear control methods and apparatus for variable speed pump control," which claims benefit to U.S. provisional application no. 61 /576,737, filed 16 December 201 1 , now abandoned;
3) U.S. application serial no. 14/091 ,795 (Atty Dckt No. 91 1 -019.009- 2//F-B&G-X0005), filed 27 November 2013, entitled "3D sensorless
conversion method and apparatus," which claims benefit to U.S. provisional application no. 61 /771 ,375, filed 1 March 2013, now abandoned;
4) U.S. application serial no. 14/187,817 (Atty Dckt No. 91 1 -019.010- 2//F-B&G-X0008), filed 24 February 2014, entitled "A Mixed Theoretical And Discrete Sensorless Converter For Pump Differential Pressure And Flow Monitoring," which claims benefit to U.S. provisional application no.
61 /803,258, filed 19 March 2013, now abandoned;
5) U.S. application serial no. 14/339,594 (Atty Dckt No. 91 1 -019.012- 2//F-B&G-X0010US01 ), filed 24 July 2014, entitled "A Best-fit and Affinity.
Sensorless Converter for Pump Differential Pressure and Flow Monitoring," which claims benefit to U.S. provisional application serial no. 61 /976,749 (Atty Dckt No. 91 1 -019.012-1 //F-B&G-X0010US01 ), filed 8 April 2014; and
6) U.S. provisional application serial no. 62/007,474 (Atty Dckt No. 91 1 - 019.015-1 //F-B&G-X0013), filed 4 June 2014, entitled "System and Flow
Adaptive Pumping Control Apparatus - A Minimum Pumping Energy
Operation Control System vs. Sensorless Application;"
which are all assigned to the assignee of the instant patent application, and all incorporated by reference in their entirety.
The present invention builds on the family of technologies disclosed in the aforementioned related applications.
BACKGROUND OF THE INVENTION
1 . Field of the Invention
The present invention relates to a technique for controlling the operation of a pump; and more particularly, the present invention relates to a method and apparatus for controlling and/or monitoring a pump, e.g., including for domestic and commercial heating or cooling water systems.
2. Brief Description of Related Art
Introduction
Hydronic pumping system sensorless control and monitoring techniques are known in the art, e.g., including a 3D discrete and a mixed theoretical and 3D discrete sensorless conversion methods, consistent with that disclosed in the aforementioned related patent application identified as reference nos. 3-5. The system pressure and flow rate may be resolved directly from a pair of motor readout values with a conversion error around 5-15% by the 3D discrete sensorless converter, e.g., based upon pump calibration data in the aforementioned reference no. 4. The mixed theoretical and discrete sensorless converter disclosed in the aforementioned reference no. 3, on the other hand, yields a conversion error around 10-20% without a need of instrumentation calibration, even though a power distribution data with respect to system coefficient and motor speed is still needed to convert the system coefficient on a varying hydronic system.
Pump sensorless data calibration, including the instrumentation and data acquisition process, is an interesting discussion topic on pump sensorless applications, which may not be easy achievable at all due to the lack of pressure and flow sensors for most pumping applications scenarios. In fact, it may be quite time consuming and tedious as well to collect the calibration data for a sensorless pump and motor combination product even to do it in manufacturing assembly lines, not to mention using expensive data acquisition instrumentations as well as hydronic pumping testing systems setups. Therefore, the inventors of this application recognize and appreciate that a sensorless means or technique with no need or less need on the calibration data may be more favorable for most sensorless pump control applications.
For a dynamic hydronic system with its flow rate regulated by valves or regulators, the equivalent hydronic system characteristics coefficient is an unknown variable in general dependent on the valves open position and system dynamic friction loss as well. The pump efficiency under such a varying hydronic system is a changing variable due to motor speed slip under the varying hydronic load as well as some pump mechanical friction induced thermal consumption effects, especially at low speed with system nearly shut off. Therefore, the inventors of this application also recognize and appreciate that it is a quite challenge job to formulate any theoretic expressions for the reconstruction of a pump sensorless converter which yields the system pressure and flow directly from motor readout values, such as power, current, torque, speed, and so on so forth. SUMMARY OF THE INVENTION
In summary, the present invention provides a new and unique best-fit affinity sensorless conversion means or technique for deriving pump or system pressure and flow rate at a given pair of motor readout values of power and speed, e.g., based upon using pump and system characteristics equations together with an empirical power equation. The pump characteristics equation and the empirical power equation may be reconstructed by a polynomial best-fit function together with the pump affinity laws or its modified version, e.g., based upon the pump curve published by pump manufacturers. System pressures and flow rate may be, therefore, resolved at the stead state equilibrium point of pump and system
pressures by the pump and system characteristics equations as well as the empirical power equation accordingly. The sensorless model and technique disclosed herein is much easier to be applied for most practical hydronic pumping sensorless control and monitoring applications with quite satisfactory accuracy without a need of the instrumentation calibration.
The instant application provides a technique that is a further development of, and builds on, the aforementioned family of technologies set forth above.
Particular Embodiments
According to some embodiments, the present invention may include, or take the form of, apparatus featuring a signal processor or processing module configured at least to:
receive signaling containing information about motor readout values of power and speed, and also about pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer; and
determine corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received. In operation, the signal processor or processing module may be configured to resolve pump differential pressures and flow rate at an equilibrium point of the pump or system pressure at a motor steady state condition.
In operation, the signal processor or processing module 1 0a may also be configured to provide corresponding signaling containing information about the pump or system pressure and the flow rate, including for pump differential pressure and flow monitoring. The corresponding signaling may be used to control a hydronic pumping system.
Embodiments are also envisioned in which the apparatus includes, or takes the form of, the hydronic pumping system, e.g., having such a signal processor or processing module.
The signaling received may be sensed and received from suitable sensors configured to measure motor readout values of power and speed.
The signaling received may be stored and received from suitable memory modules, e.g., configured with pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer.
By way of example, the signal processor or processing module may include, or take the form of, at least one processor and at least one memory including computer program code, and the at least one memory and computer program code are configured to, with at least one processor, to cause the signal processor or processing module at least to receive the signaling (or, for example, associated signaling) and determine the adaptive pressure set point. The signal processor or processing module may be configured to suitable computer program code in order to implement suitable signal processing algorithms and/or functionality, consistent with that set forth herein.
The apparatus may include, or take the form of, a pump control or controller, including a PID control, having the signal processor or signal processor module, e.g., including for monitoring pump differential pressure and flow.
According to some embodiments, the present invention may take the form of a method including steps for: receiving in a signal processor or processing module signaling containing information about motor readout values of power and speed, and also about pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer; and determining in the signal processor or processing module corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received.
The method may also include one or more of the features set forth herein, including providing from the signal processor or processing module corresponding signaling containing information about the pump or system pressure and the flow rate, e.g., which may be used to control a hydronic pumping system.
The present invention may also, e. g., take the form of a computer program product having a computer readable medium with a computer executable code embedded therein for implementing the method, e.g., when run on a signaling processing device that forms part of such a pump controller. By way of example, the computer program product may, e. g., take the form of a CD, a floppy disk, a memory stick, a memory card, as well as other types or kind of memory devices that may store such a computer executable code on such a computer readable medium either now known or later developed in the future.
In conclusion, the embodiments disclosed herein provides best-fit affinity sensorless conversion means or techniques for deriving pump or system pressure and flow rate at a given pair of motor readout values of power and speed, e.g., based upon using pump and system characteristics equations together with empirical power equations. The pump characteristics equation and the empirical power equation may be constructed by the polynomial best-fit function together with the pump affinity laws based upon the pump curve published by pump
manufacturers, e.g., that may be stored in suitable memory module and processed accordingly. Pump differential pressures and flow rate may be resolved at the equilibrium point of pump and system pressures at the motor steady state accordingly. The pump sensorless conversion means or technique disclosed herein may be much easier to be applied for most practical hydronic pumping control and monitoring applications with satisfactory accuracy.
BRIEF DESCRIPTION OF THE DRAWING
The drawing includes the following Figures, which are not necessarily drawn to scale:
Figure 1 is a schematic diagram of a hydronic sensorless pumping control system that is known in the art, e.g., in which the present invention may be implemented, according to some embodiment.
Figure 2 is a schematic diagram of sensorless conversion for pump pressure and flow rate from sensed power and speed. Figure 3 is a graph of pressure (Ft) in relation to flow (GPM) showing pump, system and power characteristics curves and a pressure equilibrium point at a steady state, according to implementation of some embodiments of the present invention.
Figure 4 is a graph of power (hp) in relation to system characteristics
(Cv/CvDuty) flow (GPM) showing motor power and system characteristics, according to implementation of some embodiments of the present invention.
Figure 5 is a graph of pressure (Ft) with respect to flow (GPM) showing pump differential pressure versus system flow rate from the sensorless converter (see solid lines) and the measured or sensed data from sensors (see symbols (e.g., diamonds, triangles, stars, plus signs, minus signs, boxes, and "x"s) at various speeds, including 24Hz, 30Hz, 36Hz, 42Hz, 48Hz, 54Hz and 60Hz.
Figure 6 is a block diagram of apparatus, e.g., having a signal processor or processing module configured for implementing the signal processing functionality, according to some embodiments of the present invention.
DETAILED DESCRIPTION OF THE INVENTION
Figure 1 shows a hydronic sensorless pumping control system having a combination of a centrifugal pump connected to piping with a flow and a controller, e.g., in which the present invention may be implemented. The sensorless
conversion for pump differential pressure and flow rate associated with the equivalent hydronic system characteristics coefficient variable at the discharge of a pump and the motor power and speed at the other end of a motor drive is shown schematically in Figure 2. Pump, system and power characteristics curves as well as the corresponding pressure equilibrium point of pump and system pressures at a steady state for a close loop system with a static suction pressure are presented schematically in Figure. 3.
Considering a close loop system with a static suction pressure, the system flow rate and pressure at a motor speed and a system position may be resolved at the steady state equilibrium point of pump and system pressures which is the intersection of the pump and system curves functions shown schematically in Figure. 3. Here, the instant pump characteristic curve, which is the pump differential pressure P with respect to flow rate Q and motor speed of n, may be represented approximately in a polynomial form of P = f (Q, n) based upon the pump curve at motor full speed n^ as well as the pump affinity law. The system flow rate may, therefore, be resolved by the pump differential pressure function of F = f{Q, n) together with the system flow equation of Cv = Q /yfp subsequently. The pump affinity laws cited here denotes the equations for pump flow, differential pressure and motor power, i.e., Q/Qmax = n/nniajc, P/Pmax = (n/n,nfl.v)2and , w/wmax = (n/nmax)3, respectively.
Following the approach described above by, e.g., using a second order best- fit affinity pump curve function together with system flow equation specifically, for instance, the system flow rate may be derived using Equation (1 ) as:
Figure imgf000011_0001
where Cv is the system coefficient, and a, b and c are the coefficients of a second order best-fit pump curve function at motor full speed of n^ . The pump differential pressure function of P = f(Q, n) used here may be in form of Equation (2) as: P(n , Q) = (aQ2 + bin/n,max : ) l Q + i"/' )?':>. (2)
Noted that other expressions of system flow rate and pump differential equations may be derived as well if other kinds of curve fitting or interpolating approaches may be chosen, for instance, a third order polynomial form of fitting or interpolating may be instead of that set forth herein.
To resolve the system flow rate and pressure at a steady pressure equilibrium point from a given pair of motor power and speed by Eqs. 1 and 2, the corresponding dynamic system characteristic coefficient should typically be known first. For a varying hydronic system with flow regulated by valves or other flow regulators, however, there is no simple close form solution on that. As disclosed herein, an empirical power and system characteristics relation based on the power curve at motor full speed n^ as well as the affinity law may be used, which is schematically shown in Figure 4. Here, the motor power function at maximum speed with respect to the system coefficient may be reconstructed first by using a fitting or interpolating technique. The motor power at a given motor speed of, e.g., w = w(Cv, n.)f may then be formulated by utilizing pump affinity laws accordingly.
By using a second order best-fit affinity power function following the approach described above specifically, for instance, the system coefficient Cv may be expressed explicitly in form of Equation (3) as:
cr B
rm (w( H) = ± f A , (3) where w is motor power at a speed of n, A, B and C are the coefficients of the second order best-fit motor power function at motor maximum speed with respect to the normalized system coefficient of C£or?" . The motor power function at any instant speed, w = n), may be expressed in form of Equation (4) as:
Figure imgf000013_0001
In case if there may be any accuracy requirement at low speed region and with system nearly shut down, the pump power affinity law may not be sufficient to represent the relation of motor power and speed well due to motor speed slip in that region. Slightly larger power value at low speed region results in a little larger the system coefficient value from the power inversion by Eq. 3, so a little larger flow rate from Eq. 1 as well consequently. A modified affinity law for motor power and speed representation may, therefore, be needed and Eq. 4 may be rewritten in the form of Equation (5) as:
w (C„, n) = r(nXA (cZ + i)* + (c -£)> - <5> where is the modified affinity law in form of the third order polynomial approximation in the form of Equation (6) as:
Γ0 = (A!(nfnmax + B!(n/nmax}2 + C' in/n,^)1 + D' (6) where A', B' C and D' are the coefficients of the third order best-fit power function of the power values normalized at maximum speed with respect to the normalized motor speed of njnmax. Instead of the pump power affinity law of
w/wma.x = (n/n.max)3, the modified affinity law is the third order polynomial approximation for representing power and speed relation, which is obtained through fitting or interpolating with an array of power values measured at a set of given speeds at a system position. The system position can be anywhere from shut off to fully open, since the normalized power distribution of /*(n) is nearly identical at any system position. Similarly, and by way of further example, Equations nos. 3- 6 may be presented in some other expressions as well if other kinds of curve fitting or interpolating approaches are used alternatively.
The system flow rate and pressure at the equilibrium point of pump and system pressure at a steady state motor speed associated with its corresponding power consumption can, therefore, be obtained by Equations 1 and 2, as far as the system coefficient of Cv is obtained by use of Equations 3 and 4 or 5 accordingly, which may be called the so-called best-fit affinity sensorless converter in this disclosure. By using the best-fit affinity sensorless converter, the pressure and flow rate values may be collected from a pumping system and compared with the data measured from sensors. The results shown in Figure 5 demonstrates quite satisfactory accuracy mostly around 5-10% error at whole speed regions from 30 up to 60 Hz in pump normal working hydronic region and around 10-20% error at low speed region and when system is nearly shut off in general.
The best-fit affinity sensorless converter disclosed herein may be used for most practical hydronic pumping control and monitoring applications, since it is formulated from pump, power characteristics equations as well as affinity law and reconstructed by polynomial best-fit based on the pump data published by pump manufacturers. The converter is much easier to be set up while maintaining satisfactory accuracy. Most importantly above all, there may be no need for tedious and time consuming instrumentation calibration process, as long as manufacturers published data or curves are available.
Figure 6:
By way of example, Figure 6 shows apparatus 10 according to some embodiments of the present invention, e.g., featuring a signal processor or processing module 10a configured at least to:
receive signaling containing information about motor readout values of power and speed, and also about pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer; and
determine corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received.
In operation, the signal processor or processing module may be configured to resolve pump differential pressures and flow rate at an equilibrium point of the pump or system pressure at a motor steady state condition.
In operation, the signal processor or processing module 1 0a may also be configured to provide corresponding signaling containing information about the pump or system pressure and the flow rate, including for pump differential pressure and flow monitoring. The corresponding signaling may be used to control a hydronic pumping system.
As a person skilled in the art would appreciate and understand, the present invention may be implemented using pump and system characteristics equations and empirical power equations, e.g., consistent with that set forth herein, as well as by using other types or kinds of pump and system characteristics equations and empirical power equations that are either now known or later developed in the future.
As a person skilled in the art would appreciate and understand, the present invention may be implemented using pump curves published by pump
manufacturers, e.g., consistent with that set forth herein that are known in the art for pumps that are also known in the art at the time of the present invention. However, embodiments are envisioned, and the scope of the invention is intended to include, using other types or kinds of pump curves published by pump manufacturers for pumps that are later developed after the time of the present invention.
By way of example, the functionality of the apparatus 10 may be implemented using hardware, software, firmware, or a combination thereof. In a typical software implementation, the apparatus 10 would include one or more microprocessor-based architectures having, e. g., at least one signal processor or microprocessor like element 10a. A person skilled in the art would be able to program such a
microcontroller-based, or microprocessor-based, implementation to perform the functionality described herein without undue experimentation. For example, the signal processor or processing module 10a may be configured, e.g., by a person skilled in the art without undue experimentation, to receive the signaling containing information about the motor readout values of power and speed, and also about the pump and system characteristics equations together with the empirical power equations that are constructed by the polynomial best-fit function together with the pump affinity laws based upon the pump curve published by the pump manufacturer, consistent with that disclosed herein. By way of example, the information about the motor readout values of power and speed may be included in sensed signaling received, processed and/or stored, e.g., in a suitable memory module that forms part of such a microprocessor-based architecture. Similarly, by way of example, the information about the pump and system characteristics equations together with the empirical power equations that are constructed by the polynomial best-fit function together with the pump affinity laws based upon the pump curve published by the pump manufacturer may be received, processed and/or stored, in a suitable memory module that forms part of such a microprocessor-based architectures.
Moreover, the signal processor or processing module 10a may be configured, e.g., by a person skilled in the art without undue experimentation, to determine the corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received, consistent with that disclosed herein.
The scope of the invention is not intended to be limited to any particular implementation using technology either now known or later developed in the future. The scope of the invention is intended to include implementing the functionality of the processors 10a as stand-alone processor or processor module, as separate processor or processor modules, as well as some combination thereof.
The apparatus 10 may also include, e.g., other signal processor circuits or components 10b, including random access memory or memory module(RAM) and/or read only memory (ROM), input/output devices and control, and data and address buses connecting the same, and/or at least one input processor and at least one output processor .
Various Points of Novelty
The present invention may include, or take the form of, one or more of the following various embodiments:
For example, according to some embodiments the present invention may take the form of, or may be implemented as, a best-fit affinity sensorless conversion means or technique for pump differential pressure and flow, e.g., that may include a pump sensorless converter which yields the pump differential pressure and system flow rate associated with a dynamic system with respect to motor speed and power readout signals based on the pump and system characteristics curves equations together with the empirical power equations represented as P = f(Q,n),
P = (Q/ Cv )2 and W = w(CV ! n), e.g., as schematically plotted in Figure 3.
According to some embodiments, the present invention may be implemented using one preferred version of the best-fit affinity sensorless conversion means or technique for pump differential pressure and flow mentioned above, e.g., may include a solution of pump differential pressure, or system pressure, and flow rate at the steady state equilibrium point of the pump differential pressure and system pressure, which is the intersection of the pump and system curves schematically shown.
According to some embodiments, the present invention may be implemented using the pump curves equations in the best-fit affinity sensorless conversion means or technique mentioned above, e.g., that may include pump curve models which are developed based upon the pump characteristics equations at a motor speed and system flow rate. The pump curve models mentioned here may be expressed approximately by function of P = f(Q, n) based upon the pump hydronic
characteristic curve at full speed (or pump curve) and pump affinity law. For a reasonably good representation with high accuracy, the best-fit approach may be used to formulate the pump curve function of P = f(Qf n). For instance, a second order best-fit affinity polynomial function of
P(n, Q) = f -^) (a i^^-X Q2 ÷ b ("··'■>■>·) Q + c) may be used for representing a pump curve at a speed of n. For a pump characteristics curve with a little
complicated curve shape, however, a higher order polynomial expression may be used to better represent pump curve, if achievable. Some other expressions may be obtained as well if other kinds of curve fitting or interpolating approaches are used alternatively. Curve fitting or interpolating approaches are known in the art, and the scope of the invention is not intended to be limited to any particular type or kind thereof either now known or later developed in the future.
According to some embodiments, the present invention may be implemented using the equivalent hydronic system characteristics curve equation in the best-fit affinity sensorless conversion means or technique mentioned above, e.g., that may include the flow equation of Cv = Qljp , or some of its alternative expressions or approximations, to represent the system characteristics curve.
According to some embodiments, the present invention may be implemented using the steady state pressure equilibrium point in the best-fit affinity sensorless conversion means or technique mentioned above, that may include the intersection point of the pump and system curves functions, as shown in Fig. 3. The system pressure or pump differential pressure and flow rate may be solved at the pressures equilibrium point for a pair of motor readout values given, for instance, speed and power, as the sensorless output values converted. For instance, for a second order best-fit affinity pump curve approximation, the aforementioned Eqs. 1 and 2 presented as
Figure imgf000020_0001
and
P(n, Q) = f— Y (a (≡≡) Q2 + b Q + c) (2)
may be the system flow rate and pressure expressions derived for the sensorless converter at a pair of motor speed and power given, respectively. The equations for converting the system pressure and flow rate may be written in some other forms as well by following the stead state pressure equilibrium point approach, however, in case that the higher order fitting or interpolating functions or some other forms of functions are used, if desirable.
According to some embodiments, the present invention may be implemented using the empirical power function to resolve the equivalent system characteristics coefficient with respect to motor power and speed in the best-fit affinity sensorless conversion means or technique mentioned above, e.g., that may include the empirical power function of w(CV! ii) with respect to motor speed and system flow rate. The power curve models mentioned here may be expressed approximately by function of w(Cv, n) based upon the power curve at full speed, exactly corresponded to the pump curve, and affinity law. For a reasonably good representation with high accuracy, similarly, the best-fit affinity approach may be used to formulate the power curve function of f w(Cv,n). For instance, a second order best-fit affinity polynomial function of Eq. 4,
Figure imgf000021_0001
may be used for representing a power curve function in term of motor speed of n and the normalized equivalent system characteristics coefficient of C orfn, based upon the corresponding power curve associated with the pump curve at maximum speed, schematically plotted in Figure 4. A higher polynomial expression or other form expressions may be introduced as well for better representing power curve functions, if needed.
According to some embodiments, the present invention may be implemented using one preferred version of the empirical power function in the best-fit affinity sensorless conversion means for pump differential pressure and flow mentioned above, e.g., that may include a best-fit affinity polynomial function of the Equation
(4):
Figure imgf000021_0002
with the modified power affinity law of /*(n) in form of the third order polynomial expression of Equation (6) as: f i n) =
Figure imgf000021_0003
(6) The modified power affinity law of f*(n) is obtained by fitting an array of power values normalized at its corresponding maximum value at full speed with a set of given speeds at a given system position ,which may be used to compensate the power variation at low speed region with system shut down.
According to some embodiments, the present invention may be implemented using the system characteristics coefficient conversion in the best-fit affinity sensorless conversion means or technique, e.g., that may include all forms of expressions either a close form solution or a solution using some discrete numerical methods. For example, Equation 3 of
Figure imgf000022_0001
may be close form solutions derived inversely for the equivalent system
characteristics coefficient expression by using empirical power function of Eq. 4.
According to some embodiments, the present invention may be implemented using the hydronic pumping system in the best-fit affinity sensorless conversion means or technique, e.g., that may include all close loop or open loop hydronic pumping systems, such as primary pumping systems, secondary pumping systems, water circulating systems, and pressure booster systems. The systems mentioned here may consist of a single zone or multiple zones as well.
According to some embodiments, the present invention may be implemented using the pump and power curves data at motor maximum speed in the best-fit affinity sensorless conversion means or technique, e.g., that may include the pump and power curves data published by pump manufacturers or a few points of pump data acquired at motor full speed in field. Here, the motor power curve data may also be replaced by any potential motor electrical or mechanical readout signals, such as motor current or torque, and so forth.
According to some embodiments, the present invention may be implemented using the hydronic signals for in the best-fit affinity sensorless conversion means or technique, e.g., that may include pump differential pressure, system pressure or zone pressure, system or zone flow rate, and so forth.
According to some embodiments, the present invention may be implemented using control signals transmitting and wiring technologies, e.g., that may include all conventional sensing and transmitting means that are used currently. Preferably, wireless sensor signal transmission technologies would be optimal and favorable.
According to some embodiments, the present invention may be implemented using the pumps mentioned above for the hydronic pumping systems, e.g., that may include a single pump, a circulator, a group of parallel ganged pumps or circulators, a group of serial ganged pumps or circulators, or their combinations.
According to some embodiments, the present invention may be implemented using systems flow regulation, e.g., that may include manual or automatic control valves, manual or automatic control circulators, or their combinations.
The aforementioned implementations are provided by way of example, and the scope of the invention is intended to include other types or kinds of
implementations consistent with that disclosed herein within the spirit of the present invention. The Scope of the Invention
It should be understood that, unless stated otherwise herein, any of the features, characteristics, alternatives or modifications described regarding a particular embodiment herein may also be applied, used, or incorporated with any other embodiment described herein. Also, the drawings herein are not drawn to scale.
Although the present invention is described by way of example in relation to a centrifugal pump, the scope of the invention is intended to include using the same in relation to other types or kinds of pumps either now known or later developed in the future.
Although the invention has been described and illustrated with respect to exemplary embodiments thereof, the foregoing and various other additions and omissions may be made therein and thereto without departing from the spirit and scope of the present invention.

Claims

WHAT WE CLAIM IS:
1 . Apparatus comprising:
a signal processor or processing module configured at least to:
receive signaling containing information about motor readout values of power and speed, and also about pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer; and
determine corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received.
2. Apparatus according to claim 1 , wherein the signal processor or processing module is configured to resolve pump differential pressures and flow rate at an equilibrium point of the pump or system pressure at a motor steady state condition.
3. Apparatus according to claim 1 , wherein the signal processor or processing module is configured to provide the corresponding signaling containing information about the pump or system pressure and the flow rate, including for pump differential pressure and flow monitoring.
4. Apparatus according to claim 3, wherein the corresponding signaling contains information used to control a hydronic pumping system.
5. Apparatus according to claim 1 , wherein the signal processor or processing module is configured to resolve the pump or system pressure and the flow rate at a steady state equilibrium point of pump and system pressures which is at an intersection of pump and system curves functions determined.
6. Apparatus according to claim 5, wherein the signal processor or processing module is configured to determine or represent an instant pump characteristic curve, which is the pump differential pressure P with respect to flow rate Q and motor speed of n, using an approximation in a polynomial form of P = f _Qf n) based upon a pump curve at a motor full speed as well as the pump affinity laws.
7. Apparatus according to claim 6, wherein the signal processor or processing module is configured to resolve a system flow rate by using a pump differential pressure function of F = f(Q,n) together with the system flow equation of
Cv = Q l P subsequently.
8. Apparatus according to claim 7, wherein the signal processor or processing module is configured to use the pump affinity laws denoted by the equations for pump flow, differential pressure and motor power, as follows:
Q/Qmax = P/Pmax = (n/nmax)2 and w/wmax = (n/wma )3, respectively.
9. Apparatus according to claim 8, wherein the signal processor or processing module is configured to derive the system flow rate, using a second order best-fit affinity pump curve function together with a system flow equation as follows:
Q n, ) = (-h ± ^Jb2 - 4r(« - C } )/(« - C z), (1 )
£ nmax where Cv is the system coefficient, and a, b and c are the coefficients of the second order best-fit affinity pump curve function at motor full speed of n^ .
10. Apparatus according to claim 9, wherein the signal processor or processing module is configured to use a pump differential pressure function of P = f(Qs n) in the form of Equation (2) as follows: F(n, (?) = (aQ2 + Hn/n^ 'Q 1 (ji/nmax}zc).
1 1 . Apparatus according to claim 10, wherein the signal processor or processing module is configured to reconstruct a motor power function at maximum speed with respect to the system coefficient by using a fitting or interpolating technique, and formulating the motor power at a given motor speed of = w(Cv, n), by utilizing the pump affinity law.
12. Apparatus according to claim 1 1 , wherein the signal processor or processing module is configured to use a second order best-fit affinity motor power function and express a system coefficient Cv in form of the Equation as follows:
Figure imgf000028_0001
where w is motor power at a speed of n, A, B and C are the coefficients of the second order best-fit affinity motor power function at motor maximum speed with respect to the normalized system coefficient of C"orm.
13. Apparatus according to claim 12, wherein the signal processor or processing module is configured to express the motor power function at any instant speed, w = w(Cr , n ), in form of the Equation as follows:
Figure imgf000028_0002
14. Apparatus according to claim 12, wherein the signal processor or processing module is configured to use a modified affinity law for motor power and speed representation in the form of the Equation as follows:
w(Cp) n) = r(7i)(-(<rw + £)
Figure imgf000029_0001
where f *(n) is the modified affinity law in form of the third order polynomial approximation in the form of the Equation as follows: / ' («) = (A'(n/nmax + Br(n/nmax)2 + C'
Figure imgf000029_0002
+ D '), where A', B' C and D' are the coefficients of the third order best-fit power function of the power values normalized at maximum speed with respect to the normalized motor speed of n/nmax.
15. A method comprising:
receiving in a signal processor or processing module signaling containing information about motor readout values of power and speed, and also about pump and system characteristics equations together with empirical power equations that are constructed by a polynomial best-fit function together with pump affinity laws based upon a pump curve published by a pump manufacturer; and
determining in the signal processor or processing module corresponding signaling containing information about a pump or system pressure and a flow rate at the motor readout values of power and speed, based upon the signaling received.
16. A method according to claim 15, wherein the method further comprises resolving in the signal processor or processing module pump differential pressures and flow rate at an equilibrium point of the pump or system pressure at a motor steady state condition.
17. A method according to claim 15, wherein the method further comprises providing from the signal processor or processing module the corresponding signaling containing information about the pump or system pressure and the flow rate, including for pump differential pressure and flow monitoring.
18. A method according to claim 17, wherein the corresponding signaling contains information is used to control a hydronic pumping system.
PCT/US2015/024703 2014-04-08 2015-04-07 Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring WO2015157276A2 (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
CN201580029040.1A CN106461444B (en) 2014-04-08 2015-04-07 For being pumped difference no sensor conversion means similar with the best fit of traffic monitor or technology
RU2016139339A RU2680474C2 (en) 2014-04-08 2015-04-07 Device (options) and method for pump differential pressure and flow monitoring
EP15777215.3A EP3129756A4 (en) 2014-04-08 2015-04-07 Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring
CA2944881A CA2944881C (en) 2014-04-08 2015-04-07 Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring
MX2016013258A MX357724B (en) 2014-04-08 2015-04-07 Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US201461976749P 2014-04-08 2014-04-08
US61/976,749 2014-04-08

Publications (2)

Publication Number Publication Date
WO2015157276A2 true WO2015157276A2 (en) 2015-10-15
WO2015157276A3 WO2015157276A3 (en) 2015-12-03

Family

ID=54288527

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US2015/024703 WO2015157276A2 (en) 2014-04-08 2015-04-07 Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring

Country Status (6)

Country Link
EP (1) EP3129756A4 (en)
CN (1) CN106461444B (en)
CA (1) CA2944881C (en)
MX (1) MX357724B (en)
RU (1) RU2680474C2 (en)
WO (1) WO2015157276A2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160010639A1 (en) * 2011-12-16 2016-01-14 Fluid Handling Llc. Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring
WO2017214257A1 (en) * 2016-06-07 2017-12-14 Fluid Handling Llc Direct numeric 3d sensorless converter for pump flow and pressure
CN107784147A (en) * 2016-08-31 2018-03-09 北京普源精电科技有限公司 The control method and its device of the major-minor flow rate pump of high pressure pump
EP4365452A1 (en) * 2022-10-21 2024-05-08 BSH Hausgeräte GmbH Adaptive rotational speed adjustment of free-flow pumps in water-bearing domestic appliances

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP3428454B1 (en) * 2017-07-14 2020-01-08 Grundfos Holding A/S Determination of a zero-flow characteristic curve of a pump in a multi-pump system
CN109578262B (en) * 2018-12-13 2020-02-07 保定申辰泵业有限公司 Control method and device for conveying viscous liquid by peristaltic pump and peristaltic pump

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070212210A1 (en) 2006-03-08 2007-09-13 Itt Manufacturing Enterprises, Inc. Method for determining pump flow without the use of traditional sensors
US20110200454A1 (en) 2010-02-10 2011-08-18 Abb Oy Method in connection with a pump driven with a frequency converter and frequency converter
US8700221B2 (en) 2010-12-30 2014-04-15 Fluid Handling Llc Method and apparatus for pump control using varying equivalent system characteristic curve, AKA an adaptive control curve

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3922760B2 (en) * 1997-04-25 2007-05-30 株式会社荏原製作所 Fluid machinery
DE19909745A1 (en) * 1999-03-05 2000-09-07 Linde Ag Hydrostatic pump circuit controls center round control valve with neutral center position giving medium valve-off pressure and sets valve-on pressure as function of medium flow rate.
DE10163987A1 (en) * 2001-12-24 2003-07-10 Grundfos As Method for controlling a variable speed heating circulation pump
DE602004003023T2 (en) * 2004-02-12 2007-06-06 Askoll Holding S.R.L., Povolaro Di Dueville Fluid circulation pump for heating and air conditioning systems, or the like
WO2006064990A1 (en) * 2004-12-17 2006-06-22 Korea Research Institute Of Standards And Science A trend monitoring and diagnostic analysis method for a vacuum pump and a trend monitoring and diagnostic analysis system therefor and computer-readable storage media including a computer program which performs the method
US20060292012A1 (en) * 2005-06-28 2006-12-28 Keurig, Incorporated Method and apparatus for pump control
TWI295340B (en) * 2005-12-02 2008-04-01 Chi Yi Wang Operation method of energy-saving fluid transporting machineries in parallel array with constant pressure
US8303260B2 (en) * 2006-03-08 2012-11-06 Itt Manufacturing Enterprises, Inc. Method and apparatus for pump protection without the use of traditional sensors
DE102007022348A1 (en) * 2007-05-12 2008-11-13 Ksb Aktiengesellschaft Device and method for fault monitoring
US7734441B2 (en) * 2008-09-30 2010-06-08 Mohsen Taravat Method and device for measuring and controlling the amount of flow/volume of liquid pumped/transferred by an electro-pump
US20120002189A1 (en) * 2009-03-18 2012-01-05 Koninklijke Philips Electronics N.V. Apparatus for determining a flow property of a fluid
US9181953B2 (en) * 2009-10-01 2015-11-10 Specific Energy Controlling pumps for improved energy efficiency
JP2011185190A (en) * 2010-03-10 2011-09-22 Ebara Corp Control device integrated type motor pump
CN104024965B (en) * 2011-12-16 2018-02-13 流体处理有限责任公司 Dynamic linear control method and device for variable speed pump control

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070212210A1 (en) 2006-03-08 2007-09-13 Itt Manufacturing Enterprises, Inc. Method for determining pump flow without the use of traditional sensors
US20110200454A1 (en) 2010-02-10 2011-08-18 Abb Oy Method in connection with a pump driven with a frequency converter and frequency converter
US8700221B2 (en) 2010-12-30 2014-04-15 Fluid Handling Llc Method and apparatus for pump control using varying equivalent system characteristic curve, AKA an adaptive control curve

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of EP3129756A4

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160010639A1 (en) * 2011-12-16 2016-01-14 Fluid Handling Llc. Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring
US9938970B2 (en) * 2011-12-16 2018-04-10 Fluid Handling Llc Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring
WO2017214257A1 (en) * 2016-06-07 2017-12-14 Fluid Handling Llc Direct numeric 3d sensorless converter for pump flow and pressure
CN109563827A (en) * 2016-06-07 2019-04-02 流体处理有限责任公司 For the direct numerical value 3D of pump discharge and pressure without transducer translating unit
US10670010B2 (en) 2016-06-07 2020-06-02 Fluid Handling Llc Direct numeric 3D sensorless converter for pump flow and pressure
CN109563827B (en) * 2016-06-07 2020-12-11 流体处理有限责任公司 Direct numerical 3D sensorless converter for pump flow and pressure
CN107784147A (en) * 2016-08-31 2018-03-09 北京普源精电科技有限公司 The control method and its device of the major-minor flow rate pump of high pressure pump
CN107784147B (en) * 2016-08-31 2023-04-18 北京普源精电科技有限公司 Method and device for controlling flow rate of main pump and auxiliary pump of high-pressure infusion pump
EP4365452A1 (en) * 2022-10-21 2024-05-08 BSH Hausgeräte GmbH Adaptive rotational speed adjustment of free-flow pumps in water-bearing domestic appliances

Also Published As

Publication number Publication date
MX2016013258A (en) 2017-05-30
EP3129756A4 (en) 2017-11-22
RU2680474C2 (en) 2019-02-21
CN106461444A (en) 2017-02-22
RU2016139339A (en) 2018-05-10
WO2015157276A3 (en) 2015-12-03
CA2944881C (en) 2020-02-25
MX357724B (en) 2018-07-19
RU2016139339A3 (en) 2018-08-30
CA2944881A1 (en) 2015-10-15
EP3129756A2 (en) 2017-02-15
CN106461444B (en) 2019-05-10

Similar Documents

Publication Publication Date Title
US9938970B2 (en) Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring
WO2015157276A2 (en) Best-fit affinity sensorless conversion means or technique for pump differential pressure and flow monitoring
RU2681390C2 (en) Sensorless adaptive pump control with self-calibration apparatus for hydronic pumping system
EP3074833B1 (en) 3d sensorless conversion method and apparatus for pump differential pressure and flow
WO2014149388A1 (en) Discrete sensorless converter for pump differential pressure and flow monitoring
WO2016131050A1 (en) No flow detection means for sensorless pumping control applications
CN107850060B (en) Sensorless converter for direct numerical value affinity pump
WO2017205584A1 (en) Direct numeric affinity multistage pumps sensorless converter
RU2678784C2 (en) System and flow adaptive sensorless pumping control apparatus for energy saving pumping applications
RU2750106C2 (en) Direct numerical three-dimensional sensorless transducer for pump flow and pressure
WO2016100322A1 (en) A discrete valve flow rate converter

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15777215

Country of ref document: EP

Kind code of ref document: A2

ENP Entry into the national phase

Ref document number: 2944881

Country of ref document: CA

REEP Request for entry into the european phase

Ref document number: 2015777215

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: 2015777215

Country of ref document: EP

WWE Wipo information: entry into national phase

Ref document number: MX/A/2016/013258

Country of ref document: MX

NENP Non-entry into the national phase

Ref country code: DE

ENP Entry into the national phase

Ref document number: 2016139339

Country of ref document: RU

Kind code of ref document: A

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 15777215

Country of ref document: EP

Kind code of ref document: A2