Method and apparatus for robust tuning of model-based process controllers used with uncertain multiple-input, multiple-output (MIMO) processes

Patent metadata

Field	Value
Publication number	US-9971318-B2
Application number	US-201514729930-A
Country	US
Kind code	B2
Filing date	Jun 3, 2015
Priority date	Mar 18, 2014
Publication date	May 15, 2018
Grant date	May 15, 2018

Abstract

A method includes obtaining information identifying (i) uncertainties associated with multiple time-domain parameters of a model and (ii) time-domain performance specifications for a model-based industrial process controller. The model mathematically represents a MIMO industrial process. The method also includes generating multiple tuning parameters for the controller based on the uncertainties and the time-domain performance specifications. The tuning parameters include vectors of tuning parameters associated with the controller, and each vector includes values associated with different outputs of the industrial process. The time-domain parameters could include a process gain, a time constant, and a time delay for each input-output pair of the model. The time-domain performance specifications could include requirements related to worst-case overshoots, settling times, and total variations. The uncertainties could be specified as intervals in which the time-domain parameters lie.

First claim

What is claimed is:

1. A method for controlling a web processing system by a model-based industrial process controller that controls associated processes of a web process facility in the web processing system comprising:
obtaining information based on at least one sensor located in the web process facility communicating to the model-based industrial process controller through a network;
identifying (i) uncertainties associated with multiple time-domain parameters of a model and (ii) time-domain performance specifications for the model-based industrial process controller, the model mathematically representing a multiple-input, multiple-output (MIMO) industrial process; and
generating multiple tuning parameters for the controller based on the uncertainties and the time-domain performance specifications, the tuning parameters including vectors of tuning parameters associated with the controller, each vector including values associated with different outputs of the industrial process, wherein generating the multiple tuning parameters comprises:
constructing multiple multiple-input, single-output (MISO) tuning problems based on a MIMO tuning problem, each MISO tuning problem associated with a different output of the MIMO industrial process, and
solving each MISO tuning problem to identify one of the values in each vector, wherein solving each MISO tuning problem comprises:
identifying the values in a first of the vectors assuming fixed values in a second of the vectors; and
identifying, the values in the second vector that minimize settling times for the outputs of the MIMO industrial process;

controlling, by the controller, the associated processes of the web process facility in the web processing system network utilizing the multiple tuning parameters.

2. The method of claim 1 , further comprising:
generating a graphical display identifying (i) multiple expected step responses of the MIMO industrial process based on the tuning parameters of the controller and (ii) an envelope around the one or more expected step responses based on the uncertainties associated with the time-domain parameters of the model;
wherein the envelope is generated using different combinations of extreme values of the time-domain parameters, the extreme values based on the uncertainties of the time-domain parameters.

3. The method of claim 2 , wherein:
the time-domain parameters comprise a process gain, a time constant, and a time delay for each input-output pair of the model;
the time-domain performance specifications comprise requirements related to worst-case overshoots, settling times, and total variations; and
the uncertainties are specified as intervals in which the time-domain parameters lie.

4. The method of claim 1 , wherein:
the first vector comprises a vector of reference tracking performance ratios, each reference tracking performance ratio defining a ratio between a desired closed-loop reference tracking response time of the controller and an open-loop response time for one output of the MIMO industrial process; and
the second vector comprises a vector of disturbance rejection performance ratios, each disturbance rejection performance ratio defining a ratio between a desired closed-loop disturbance rejecting response time of the controller and the open-loop response time of the one output of the MIMO industrial process.

5. The method of claim 1 , further comprising:
predicting a tuning time of the controller prior to generating the tuning parameters for the controller.

6. The method of claim 1 , wherein obtaining the information identifying the uncertainties and the performance specifications comprises receiving the information from a user.

7. An apparatus for controlling a web processing system by a model-based industrial process controller that controls associated processes of a web process facility in the web processing system comprising:
at least one memory configured to store information, obtained based on at least one sensor located in the web process facility communicating to the model-based industrial process controller through a network, identifying (i) uncertainties associated with multiple time-domain parameters of a model and (ii) time-domain performance specifications for the model-based industrial process controller, the model mathematically representing a multiple-input, multiple-output (MIMO) industrial process; and
at least one processing device configured to generate multiple tuning parameters for the controller based on the uncertainties and the time-domain performance specifications, the tuning parameters including vectors of tuning parameters associated with the controller, each vector including values associated with different outputs of the industrial process, wherein the multiple tuning parameters are utilized by the controller to control the associated processes of the web process facility in the web processing system, wherein the at least one processing device is configured to:
construct multiple multiple-input, single-output IMISO) tuning problems based on a MIMO tuning problem, each MISO tuning problem associated with a different output of the MIMO industrial process; and
solve each MISO tuning problem to identify one of the values in each vector, wherein the at least one processing device is configured to:
identify the values in a first of the vectors assuming fixed values in a second of the vectors; and
identify the values in the second vector that minimize settling times for the outputs of the MIMO industrial process.

8. The apparatus of claim 7 , wherein the at least one processing device is further configured to:
generate a graphical display identifying (i) multiple expected step responses of the MIMO industrial process based on the tuning parameters of the controller and (ii) an envelope around the one or more expected step responses based on the uncertainties associated with the time-domain parameters of the model;
generate the envelope using different combinations of extreme values of the time-domain parameters, the extreme values based on the uncertainties of the time-domain parameters.

9. The apparatus of claim 8 , wherein:
the time-domain parameters comprise a process gain, a time constant, and a time delay for each input-output pair of the model;
the time-domain performance specifications comprise requirements related to worst-case overshoots, settling times, and total variations; and
the uncertainties are specified as intervals in which the time-domain parameters lie.

10. The apparatus of claim 7 , wherein:
the first vector comprises a vector of reference tracking performance ratios, each reference tracking performance ratio defining a ratio between a desired closed-loop reference tracking response time of the controller and an open-loop response time for one output of the MIMO industrial process; and
the second vector comprises a vector of disturbance rejection performance ratios, each disturbance rejection performance ratio defining a ratio between a desired closed-loop disturbance rejecting response time of the controller and the open-loop response time of the one output of the MIMO industrial process.

11. The apparatus of claim 7 , wherein the at least one processing device is further configured to:
predict a tuning time of the controller prior to generation of the tuning parameters for the controller.

12. A non-transitory computer readable medium containing instructions that when executed cause at least one processing device to control a web processing system by a model-based industrial process controller that controls associated processes of a web process facility in the web processing system:
obtain informatio

Assignees

• Honeywell Asca Inc
• Honeywell Ltd

Inventors

• He Ning
• Shi Dawei
• Forbes Michael
• Backstrom Johan U
• Chen Tongwen

Classifications

• G05B13/042

  in which a parameter or coefficient is automatically adjusted to optimise the performance · CPC title

• G05B15/02

  electric · CPC title

• G05B13/047 Primary

  the criterion being a time optimal performance criterion · CPC title

• G06F17/10

  Complex mathematical operations {(function generation by table look-up G06F1/03; evaluation of elementary functions by calculation G06F7/544)} · CPC title

• G05B13/04 Primary

  involving the use of models or simulators · CPC title