# Linearize Pulp Paper Process Model

This example shows how to linearize a process model at a steady-state operating point.

Thermo-mechanical pulping (TMP) is a process for producing mechanical pulp for newsprint. In this example, you use a typical process arrangement for a two-stage TMP operation:

In the first stage, the primary refiner produces a course pulp from a feed of wood chips and water.

In the second stage, the secondary refiner further develops the pulp bonding properties so that it is suitable for paper making.

Each refiner consists of two disks with overlaid grooved surfaces. When in operation, either the two disks rotate in opposite directions or one disk rotates while the other disk remains stationary.

The disk surfaces physically impact on a three-phase flow of wood fibers, steam, and water that passes from the center of the refiner disks to their periphery. The physical impact of the disk surfaces on the wood fibers:

Breaks rigid chemical and physical bonds between the fibers

Microscopically roughens the surface of individual fibers enabling them to mesh together on the paper sheet.

The primary objective of controlling the TMP plant is to apply sufficient energy to derive pulp with good physical properties without incurring excess energy costs or fiber damage due to the imposition of overly high stresses as fibers pass through the refiners. For practical purposes, this objective amounts to controlling the ratio of the total electrical energy applied by the two refiners to the dry mass flow rate of wood fibers, that is, controlling the estimated specific energy applied to the pulp.

A secondary control objective is to control the pulp consistency, that is the ratio of dry mass flow rate (fibers) to overall mass flow rate (water & fibers), to a value which optimizes a tradeoff between energy consumption and pulp quality.

The TMP process has the following inputs.

Feed rate of chips (Feed rpm)

Dilution water flow to each of the refiners (Primary and secondary dilution setpoints)

Setpoints to two regulatory controllers which control the gap between the rotating disks in each set of refiners.

The TMP process has the following outputs.

Primary and secondary refiner consistencies

Primary and secondary refiner motor loads

Vibration monitor measurements for the two refiners

Open the `scdtmp`

model, which implements the thermo-mechanical pulping process.

```
mdl = 'scdtmp';
open_system(mdl)
```

In this example, your goal is to find a linear model of this system at a steady-state operating condition for the following input setpoint conditions.

Feed Rate = 30

Primary Gap = 0.8

Primary Dilution = 170

Secondary Gap = 0.5

Secondary Dilution = 120

### Find Operating Points

To find the operating point, first create an operating point specification object using the `operspec`

function.

opspec = operspec(mdl)

opspec = Operating point specification for the Model scdtmp. (Time-Varying Components Evaluated at time t=0) States: ---------- x Known SteadyState Min Max dxMin dxMax ___________ ___________ ___________ ___________ ___________ ___________ ___________ (1.) scdtmp/TMP Refining Line/Fiber fill dynamics/Internal 3.5556 false true -Inf Inf -Inf Inf (2.) scdtmp/TMP Refining Line/Fiber water fill dynamics/Internal 6.8283 false true -Inf Inf -Inf Inf (3.) scdtmp/TMP Refining Line/Primary dilution/Internal 170 false true -Inf Inf -Inf Inf (4.) scdtmp/TMP Refining Line/Primary plate gap/Internal 0.8 false true -Inf Inf -Inf Inf (5.) scdtmp/TMP Refining Line/Primary refiner motor/LTI System/Internal 8.5 false true -Inf Inf -Inf Inf (6.) scdtmp/TMP Refining Line/Primary screw feeder/Internal 30 false true -Inf Inf -Inf Inf (7.) scdtmp/TMP Refining Line/Sec refiner motor/LTI System/Internal 6.7 false true -Inf Inf -Inf Inf (8.) scdtmp/TMP Refining Line/Secondary dilution/Internal 0.5 false true -Inf Inf -Inf Inf (9.) scdtmp/TMP Refining Line/Secondary plate gap/Internal 0.5 false true -Inf Inf -Inf Inf Inputs: ---------- u Known Min Max _____ _____ _____ _____ (1.) scdtmp/Feed rpm 0 false -Inf Inf (2.) scdtmp/Pri gap set point 0 false -Inf Inf (3.) scdtmp/Pri dil flow set point 0 false -Inf Inf (4.) scdtmp/Sec. gap set point 0 false -Inf Inf (5.) scdtmp/Sec. dilution set point 0 false -Inf Inf Outputs: ---------- y Known Min Max _____ _____ _____ _____ (1.) scdtmp/Out1 0 false -Inf Inf 0 false -Inf Inf 0 false -Inf Inf 0 false -Inf Inf 0 false -Inf Inf 0 false -Inf Inf

Specify the feed rate input value and indicate that this value is known.

opspec.Inputs(1).u = 30; opspec.Inputs(1).Known = 1;

Similarly, specify the known primary gap setpoint.

opspec.Inputs(2).u = 0.8; opspec.Inputs(2).Known = 1;

Specify the known primary dilution setpoint.

opspec.Inputs(3).u = 170; opspec.Inputs(3).Known = 1;

Specify the known secondary gap setpoint.

opspec.Inputs(4).u = 0.5; opspec.Inputs(4).Known = 1;

Specify the known secondary dilution setpoint.

opspec.Inputs(5).u = 120; opspec.Inputs(5).Known = 1;

Trim the model for the given operating point specifications using the `findop`

function.

op = findop(mdl,opspec);

Operating point search report: --------------------------------- opreport = Operating point search report for the Model scdtmp. (Time-Varying Components Evaluated at time t=0) Operating point specifications were successfully met. States: ---------- Min x Max dxMin dx dxMax __________ __________ __________ __________ __________ __________ (1.) scdtmp/TMP Refining Line/Fiber fill dynamics/Internal -Inf 3.5556 Inf 0 0 0 (2.) scdtmp/TMP Refining Line/Fiber water fill dynamics/Internal -Inf 6.8283 Inf 0 0 0 (3.) scdtmp/TMP Refining Line/Primary dilution/Internal -Inf 170 Inf 0 0 0 (4.) scdtmp/TMP Refining Line/Primary plate gap/Internal -Inf 0.8 Inf 0 0 0 (5.) scdtmp/TMP Refining Line/Primary refiner motor/LTI System/Internal -Inf 8.4952 Inf 0 0 0 (6.) scdtmp/TMP Refining Line/Primary screw feeder/Internal -Inf 30 Inf 0 0 0 (7.) scdtmp/TMP Refining Line/Sec refiner motor/LTI System/Internal -Inf 6.6385 Inf 0 1.7355e-12 0 (8.) scdtmp/TMP Refining Line/Secondary dilution/Internal -Inf 120 Inf 0 0 0 (9.) scdtmp/TMP Refining Line/Secondary plate gap/Internal -Inf 0.5 Inf 0 0 0 Inputs: ---------- Min u Max ___ ___ ___ (1.) scdtmp/Feed rpm 30 30 30 (2.) scdtmp/Pri gap set point 0.8 0.8 0.8 (3.) scdtmp/Pri dil flow set point 170 170 170 (4.) scdtmp/Sec. gap set point 0.5 0.5 0.5 (5.) scdtmp/Sec. dilution set point 120 120 120 Outputs: ---------- Min y Max ________ ________ ________ (1.) scdtmp/Out1 -Inf 0.026027 Inf -Inf 0.39991 Inf -Inf 0.56757 Inf -Inf 8.4952 Inf -Inf 0.34914 Inf -Inf 6.6385 Inf

### Linearize Model

To linearize the model, first define the linearization input and output points.

For this example, use the following input points.

Feed rate

Primary gap

Primary dilution

Secondary gap

Secondary dilution

io(1) = linio('scdtmp/Feed rpm',1,'input'); io(2) = linio('scdtmp/Pri gap set point',1,'input'); io(3) = linio('scdtmp/Pri dil flow set point',1,'input'); io(4) = linio('scdtmp/Sec. gap set point',1,'input'); io(5) = linio('scdtmp/Sec. dilution set point',1,'input');

The output of the Mux block contains the six model outputs in the following order.

Primary vibration

Primary consistency

Secondary vibration

Primary motor load

Secondary consistency

Secondary motor load

io(6) = linio('scdtmp/Mux',1,'output');

Linearize the model at the computed steady-state operating point.

sys = linearize(mdl,op,io);

You can view the response for the resulting linear system from any input to any output. For example, plot the Bode response between the primary gap setpoint and the primary consistency.

bode(sys(2,2))

## See Also

`operspec`

| `findop`

| `linio`

| `linearize`