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Application examples:  

Refiner (TMP) Optimization (freeness throughput and energy consumption)

The MultiSimplex® Controller optimizes the following control variables:

-         Dilution water flow

-         Disc gap

-  Production rate

  To achive the optimal joint response based on the following response variables:

-         Freeness

-         Specific energy consumption

-         Production rate

 

Screening (pulp) Optimization (freeness, shives and long fiber content)

The MultiSimplex® Controller optimizes the following control variables:

-         Dilution water flow

-        Reject flow / rate

  To achive the optimal joint response based on the following response variables:

-         Freeness

-         Shive and/or long fiber content

-         Reject flow

 

SNCR Optimization (NOx, NH3 and cost minimization)

The MultiSimplex® Controller optimizes the following control variables:

-         NH3 flow nozzle 1 - n (Based on a non-linear function using temperature, if available)

-         NH3 conc.

  To achive the optimal joint response based on the following response variables:

-         Cost (emission taxes + chemical costs)

-         emissions (NOx, NH3)

 

Combustion Optimization (NOx and CO minimization, power maximization))

The MultiSimplex® Controller optimizes the following control variables:

-         Primary air distribution

-         Over fire air distribution (Secondary, tertiary, etc air flows)

-     O2 set point.

-     Air / fuel ratio

-     Fuel infeed rate

  To achive the optimal joint response based on the following response variables:

-         Power / Energy output

-         emissions (NOx, CO)

 

Optimization of an oxygen reactor (Pulp mill)

The MultiSimplex® Controller controls the following control variables:

-         Amount of NaOH

-         Pulp temperature

-         Amount of O2

 

The MultiSimplex® Controller reads and optimizes the following response variables:

-         Kappa number in

-         Kappa number out

-         pH out

-         Temperature before reactor

-         Temperature in reactor

-         Temperature after reactor

 

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Optimization of the formation process on a paper machine

The MultiSimplex® Controller controls the following control variables:

-         Discharge Ratio

-         Vacuum valve, forming roll

-         Vacuum valve, zone X

-         Vacuum valve, zone Y

-         Vacuum valve, zone Z

 

The MultiSimplex® Controller reads and optimizes the following response variables:

-         Formation (Signal from a Measurex or similar density/weight distribution analyzer)

-         Discharge Ratio

 

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Optimization of the board density profile out of a panel board press (MDF or Particleboard):

The MultiSimplex® Controller controls the following control variables:

-         Press temperature (One or two zones)

-         Pressure or position, Zone A

-         Pressure or position, Zone B

-         Pressure or position, Zone C

-         Pressure or position, Zone D

-         Pressure or position, Zone E

-         Pressure or position, Zone F

 

The MultiSimplex® Controller reads and optimizes the following response variables:

-         Core density

-         Surface density

-         Sanding allowance (Distance from peak density to surface)

-         Width of “high density zones”

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Optimization of forming on a panel board production line (MDF or Particleboard):

The MultiSimplex® Controller controls the following control variables:

-         Control variable A

-         Control variable B

-         Control variable C

-         Control variable D

-         Control variable E

 

The MultiSimplex® Controller reads and optimizes the following response variables:

-         Weight distribution cross wise

-         Weight distribution length wise

 

Optimization of Ultimate Tensile Strength UTS (MPa) in steel rod plant

The process involves the cooling of coils of steel rod after rolling to

Size. During cooling, the steel transforms from one crystalline structure to another, and the rate of cooling determines what the final properties of the rod are.

The coils are cooled on a conveyor system, which has sets of air blowers to cool the coils as they pass over them. Obviously the cooling conditions will depend upon the diameter of the rod being cooled. It is important that the transformation has completed on the conveyor, but if the cooling is too rapid then unwanted brittle phases can appear in the coil.

 

The MultiSimplex® Controller controls the following control variables:

-         Laying Temperature (i.e. start temperature)

-         Conveyor Speed

Air Blowers:

-         Zone A 

-         Zone B 

-         Zone C

-         Zone D 

-         Zone E

 

The MultiSimplex® Controller reads and optimizes the following response variables:

-         Ultimate Tensile Strength UTS (i.e. stress to fracture the rod)

-         Ductility (i.e. amount of distortion before fracture)

-         UTS variation caused by overlapping coils affecting cooling

-         (Brittle phase formation.)

 

 



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