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Building Pulp and Paper Stock Models in FluidFlow

Model pulp and paper stock transfer in FluidFlow using TAPPI TIS 408-4 or Moller K. Check pressure drop, pressure profile, and velocities.

Purpose and requirement

Use this guide to build a pulp and paper stock network, select a stock friction-loss method, and review the calculated pressure drop, pressure profile, and pipe velocities.
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Required module: FluidFlow Slurry Module
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FluidFlow models Pulp / Paper stock as a distinct fluid type. Pressure loss is calculated using a hybrid framework that combines stock-specific correlations with conventional hydraulics. Beyond the applicable stock-correlation range, the solver reverts to the standard Darcy pressure-loss calculation as the contribution of pulp or fibers become insignificant.
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1. Select the friction-loss calculation method

Pup & Paper Stock Pressure Loss Correlation in FluidFlow

In the calculation options, select either TAPPI Technical Information Sheet (TIS) 408-4 or Moller K. Consider the oven-dry stock concentration and the stock data available for the selected method.

Method

Oven-dry concentration range

Method-specific setup

TAPPI TIS 408-4

2–6%

Select the applicable TAPPI pulp type from the calculation-options drop-down.

Moller K

0.9–6%

Specify fiber aspect ratio and pulp freeness in the calculation options.

TAPPI setup

The TAPPI model is based on the observation that pulp stock pressure loss depends on concentration, velocity, temperature, and pipe geometry.

TAPPI setup on FluidFlow Calculation Options


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Select the pulp type that represents the stock being modeled. TAPPI pulp types are stored in the database, which can be expanded when required. The selected type supplies the coefficients used by the correlation.
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Moller K setup

The Moller method is more mechanistic than TAPPI and reflects how fiber suspension behavior depends on the physical characteristics of the stock. In this suspension-based hydraulic correlation, friction loss is shaped by fiber properties, concentration, temperature, and wall roughness, rather than by the empirical TAPPI power law alone.

TAPPI setup on FluidFlow Calculation Options

Enter the stock's fiber aspect ratio and pulp freeness. Moller K uses these stock characteristics together with concentration, pipe roughness, temperature, velocity, and diameter to calculate pressure drop.
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2. Build the network

Build the network using the same general workflow as a standard liquid model, including the required boundaries, pipes, and system components.

FluidFlow standard liquid model

In the Input Editor of the inlet boundary:

  1. Set the fluid type to Pulp / Paper stock.

  2. Locate the additional input field for weight % oven-dry concentration that appears after selecting this fluid type.

  3. Enter the stock concentration as a weight percentage on the oven-dry basis.

Check that the concentration entered is consistent with the selected friction-loss method and its stated range.
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3. Calculate and examine the results

Calculate the network, then examine:

  • Pressure drop through the modeled system.

  • Pressure profile across the network.

  • Pipe flow velocities, particularly when interpreting TAPPI results because its calculation branch depends on velocity thresholds.

FluidFlow standard liquid model-loss correlation results

Interpret the results alongside the selected correlation, stock concentration, stock characteristics, and system information.

For the full range of settling, non-settling, and non-Newtonian slurry capabilities beyond pulp and paper stock, see the Slurry & Non-Newtonian Flow module.

FAQ

What is Canadian Standard Freeness (CSF)?

CSF refers to the freeness value obtained using the Canadian Standard Freeness method which expresses the time required to drain a specific volume of diluted pulp suspension.

How do I decide between TAPPI and Moller K?

Base it on the available data. Use TAPPI when your stock matches one of the pulp types stored in the database. Use Moller K when you have measured fiber aspect ratio and pulp freeness rather than a catalog match.
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What oven-dry concentration range is each method valid for?

TAPPI TIS 408-4 applies from 2–6% oven-dry concentration. Moller K applies over a wider range, 0.9–6%. Enter the concentration at the inlet boundary as weight % oven-dry and confirm it falls inside the range for the method selected.
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My stock doesn't match any of the TAPPI pulp types in the database. What should I do?

TAPPI pulp types are stored in a database that can be expanded when required. Alternatively, if you have measured fiber aspect ratio and freeness data, Moller K doesn't depend on a catalog match and may be the more direct method.
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Conclusion

Building a reliable pulp and paper stock model in FluidFlow comes down to matching the friction-loss method to the data on hand, keeping the oven-dry concentration inside that method's valid range. Both TAPPI TIS 408-4 and Moller K are hybrid correlations layered on top of conventional pipe hydraulics, so results stay traceable to standard Darcy behavior once the stock's fiber effects become small.
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Getting the method and concentration basis right means the pressure drop and pump duty calculated for a stock-transfer line reflect the furnish actually being pumped, rather than a generic liquid assumption that under- or overstates the real hydraulic load.​

See it on your own stock system

Build a pulp and paper stock network in FluidFlow and review the pressure drop, pressure profile, and velocities for yourself.

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