Method and apparatus for controlling pulp refiners

Claim 2

A control system for controlling the quality of the output stock of a group of pulp refiners which include a plurality of base refiners and tickler refiner means the output stock of the tickler refiner means being used to manufacture sheet material and where the coupling between the base refiners and the tickler refiner means includes a significant time delay said system comprising: first control means associated with said tickler refiner means and responsive to a first input control signal for loading said tickler refiner means in accordance with such signal; second control means associated with said base refiners and responsive to second input control signal means for loading said base refiners in accordance with such signal means; means for sensing the quality of the output stock from said tickler refiner means and comparing such quality to a target value to provide an error signal; means associated with said base refiners and responsive to said error signal for causing said second output control signal means to load said base refiners to fully compensate for said error signal; feedforward means responsive to said error signal for causing said first output control signal to change from an optimum operating value to initially load said tickler refiner means to fully compensate for said error signal and thereafter gradually change said loading back to said optimum value in accordance with said time delay.

Claim 3

A system as in claim 1 where said second control means includes means for determining the energy distribution of said plurality of base refiners and maintaining said distribution constant even while said second input control signal varies the loading of said base refiners.

Claim 4

A system as in claim 2 where said determining and maintaining means includes means for initially determining the participation factor of each of said base refiners, means for determining at every control interval the specific energy required from each of said refiners in accordance with said error signal and said participation factors, and means for adjusting the loading on said base refiners in accordance with any change in said specific energy.

Claim 7

A control system for controlling a predetermined process variable said system having first and second manipulated variables upon which said process variable is dependent with disparate response times comprising: first processing means for manipulating said fisrt variable said processing means having relatively fast dynamic response for allowing high frequency control of said variable but being restricted in control range; second processing means for manipulating said second variable said processing means having a large control range relative to said first processing means but a much longer response time relative to said fast dynamic response, said first processing means being series coupled to the output of said second processing means; means for sensing said process variable at the output of said first processing means and comparing said sensed process variable to a target value to provide an error signal, means responsive to said error signal for causing said second processing means to manipulate said second variable to fully compensate for said error signal; feedforward means responsive to said error signal for causing said first processing means to change said first manipulated variable from an optimum operating value to a value which fully compensates for said error signal and thereafter which gradually changes said value back to said optimum value in accordance with said response time of said second processing means.

Claim 8

A control system for controlling a predetermined process variable said system having first and second manipulated variables upon which said process variable is dependent with disparate response times comprising: first processing means for manipulating said fisrt variable said processing means having relatively fast dynamic response for allowing high frequency control of said variable but being restricted in control range; second processing means for manipulating said second variable said processing means having a large control range relative to said first processing means but a much longer response time relative to said fast dynamic response, said first processing means being series coupled to the output of said second processing means; means for sensing said process variable at the output of said first processing means and comparing said sensed process variable to a target value to provide an error signal, means responsive to said error signal for causing said second processing means to manipulate said second variable to fully compensate for said error signal; feedforward means responsive to said error signal for causing said first processing means to change said first manipulated variable from an optimum operating value to a value which fully compensates for said error signal and thereafter which gradually changes said value back to said optimum value in accordance with said response time of said second processing means.

Claim 9

A system as in claim 5 where said control system is for pulp, said process variable is freeness, said second processing means includes a plurality of base refiners, said first processing means includes tickler refiner means, said first and second manipulated variables are the specific energy targets of said tickler refiner means and said base refiners respectively, and where said response time includes both transport lag and time constants.