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Process control

Assignee: Applied Automation Inc
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Filing: 1980-03-11
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Granted: 1982-08-24
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Expires: 2000-03-11
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Abstract

Abstract A process control system is provided in which a process variable is compared to a set point for the process variable by a process controller with the results of the comparison being utilized to control the process in such a manner that the process variable will be substantially equal to the set point for the process variable. A critically damped response of the process variable to a change in the set point is achieved by utilizing a process controller which has the characteristics of a proportional-integral-derivative controller followed by a first order lag. Tuning of the process controller is accomplished by changing a time constant which is common to the proportional, integral and derivative terms of the proportional-integral-derivative controller and also common to the first order lag.

Inventors

  • 👤 Robert W. Rutledge

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-25 07:57
CPC Classifications
G; G05; G05B; G05B11/00; G05B11/01; G05B11/36; G05B11/42; G05D; G05D23/00; G05D23/19; G05D23/1917; G05D23/20

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 178 words
A method for maintaining the value of a controlled process variable substantially equal to a desired value for said controlled process variable, wherein said controlled process variable is responsive to changes in a manipulated process variable, and wherein said process can be represented by a general second order equation of the form ##EQU9## where G P =process transfer function; K 1 =process gain; τ 1 and τ 2 =process time constants; and S=Laplace operator; said method comprising the steps of: establishing a first signal which is representative of the actual value of said controlled process variable; establishing a second signal representative of the desired value of said controlled process variable; establishing a third signal representative of the difference (E) between said first signal and said second signal in response to said first signal and said second signal; supplying said third signal to a process controller having a transfer function given by ##EQU10## where G C =process controller transfer function; λ=C(τ 1 +τ 2 )/2; C has a value in the range of about 0.75 to about 1.25; and
Claim 2
Independent Claim 178 words
A method for maintaining the value of a controlled process variable substantially equal to a desired value for said controlled process variable, wherein said controlled process variable is responsive to changes in a manipulated process variable, and wherein said process can be represented by a general second order equation of the form ##EQU9## where G P =process transfer function; K 1 =process gain; τ 1 and τ 2 =process time constants; and S=Laplace operator; said method comprising the steps of: establishing a first signal which is representative of the actual value of said controlled process variable; establishing a second signal representative of the desired value of said controlled process variable; establishing a third signal representative of the difference (E) between said first signal and said second signal in response to said first signal and said second signal; supplying said third signal to a process controller having a transfer function given by ##EQU10## where G C =process controller transfer function; λ=C(τ 1 +τ 2 )/2; C has a value in the range of about 0.75 to about 1.25; and
Claim 3
Dependent Claim 167 words
τ 1 . τ 2 , K 1 and S are as previously defined; said process controller providing a manipulated variable control signal equal to ##EQU11## and manipulating said manipulated variable in response to said manipulated variable control signal to thereby maintain said controlled process variable substantially equal to the desired value for said control process variable, wherein said method additionally comprises the steps of: (a) calculating a plurality of values for λ; (b) substituting a calculated value for λ into the transfer function of said process controller; (c) noting the response of said controlled process variable to a change in the desired value of said controlled process variable; (d) repeating steps (b) and (c) until all of the calculated values of λ have been tested; and (e) selecting the value of λ for which the response of said controlled process variable to a change in the desired value of said controlled process variable most closely approximates a critically damped response to thereby tune said process controller.
Claim 4
Dependent Claim 167 words
τ 1 . τ 2 , K 1 and S are as previously defined; said process controller providing a manipulated variable control signal equal to ##EQU11## and manipulating said manipulated variable in response to said manipulated variable control signal to thereby maintain said controlled process variable substantially equal to the desired value for said control process variable, wherein said method additionally comprises the steps of: (a) calculating a plurality of values for λ; (b) substituting a calculated value for λ into the transfer function of said process controller; (c) noting the response of said controlled process variable to a change in the desired value of said controlled process variable; (d) repeating steps (b) and (c) until all of the calculated values of λ have been tested; and (e) selecting the value of λ for which the response of said controlled process variable to a change in the desired value of said controlled process variable most closely approximates a critically damped response to thereby tune said process controller.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1985-08-23 1986-02-22 1986-08-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1989-08-23 1990-02-22 1990-08-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1993-08-23 1994-02-22 1994-08-24 $7700.00 Window Closed / Lapsed

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