Parameter estimation technique for closed loop system

Claim 1

A process control system, comprising: a controller for producing a control output for said process; means for providing a first response, resulting from a comparison of a process variable and a setpoint, to a summation unit; a model, connected to said controller and located in a feedback loop, for receiving said control output and providing an output to said summation unit; and means, connected to said summation unit, for providing a second response to said controller, said controller and said model including algorithm means for updating said model based on estimated process parameters of observed process gain, lag time constant, and deadtime in response to changes in the setpoint, said algorithm means numerically calculating the values of the following control area integrals as the control output approaches the setpoint ##EQU5## where: I 1 , I 2 =Control Area Integrals m ss =Final Value, Control Output m(t)=Control Output at time t SP=Change in setpoint α=Weighting Parameter=(τ m +T m ) -1 .

Claim 3

A method for controlling a process having a controller and a model of the process, and which has unknown or time varying deadtime, by measuring the response to a step setpoint change, which response can be directly related to observed process gain, lag time constant, and deadtime parameters representative of the process to update the model, comprising: providing a first setpoint to the controller; providing a process variable to the controller; providing a first new setpoint to the controller to create a step setpoint change thereto and start an estimation procedure which estimates the process parameters based on an observed process output response to said change; calculating numerically the values of the following control area integrals I 1 and I 2 as the process output approaches the first new setpoint ##EQU6## where: I 1 , I 2 =Control Area Integrals m ss =Final Value, Control Output m(t)=Control Output at time t ΔSP=Change in setpoint α=Weighting Parameter=(τ m +T m ) -1 ; and solving a set of three non-linear algebraic equations which relate the observed process gain, lag time constant, and deadtime, ##EQU7## where: k est , τ est , T est =Estimated Parameters m init =Initial Value, Control Output and: ##EQU8## to estimate the process deadtime, process gain and lag time and update the process model using these estimated parameters.

Claim 4

A method for controlling a process having a controller and a model of the process, and which has unknown or time varying deadtime, by measuring the response to a step setpoint change, which response can be directly related to observed process gain, lag time constant, and deadtime parameters representative of the process to update the model, comprising: providing a first setpoint to the controller; providing a process variable to the controller; providing a first new setpoint to the controller to create a step setpoint change thereto and start an estimation procedure which estimates the process parameters based on an observed process output response to said change; calculating numerically the values of the following control area integrals I 1 and I 2 as the process output approaches the first new setpoint ##EQU6## where: I 1 , I 2 =Control Area Integrals m ss =Final Value, Control Output m(t)=Control Output at time t ΔSP=Change in setpoint α=Weighting Parameter=(τ m +T m ) -1 ; and solving a set of three non-linear algebraic equations which relate the observed process gain, lag time constant, and deadtime, ##EQU7## where: k est , τ est , T est =Estimated Parameters m init =Initial Value, Control Output and: ##EQU8## to estimate the process deadtime, process gain and lag time and update the process model using these estimated parameters.