Batch Control Gets Easier

Loop tuning package doesn’t demand steady-state operation.

By John Gaines, Evonik Jayhawk Fine Chemicals, and Dennis Nash, Control Station, Inc.

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The nonlinear dynamics of most exothermic and endothermic batch reactions require expert attention to assure quality production. For instance, introducing reactants often results in dramatic swings in temperature. Maintaining production tolerances in such an environment tests the effectiveness of any proportional-integral-derivative (PID) controller and the associated tuning parameters.

As a global leader in specialty chemicals, Evonik Industries AG understands the economic implications of good versus poor control of batch processes. Headquartered in Essen, Germany, the company produces a wide spectrum of polyamides, coating adhesives and other specialty chemicals. It maintains operations in more than 100 countries; it has more than 25 production facilities in the U.S., including Evonik Jayhawk Fine Chemicals in Galena, Kan. The management team at Galena has been implementing cutting-edge control technologies that are significantly reducing production cycle times and increasing the plant’s overall profitability.

The Galena facility manufactures pharmaceutical intermediates, specialty chemicals and herbicides, and industrial solvents. One of the production processes has two exothermic reactions that are regulated via a cascaded temperature-to-flow control architecture (Figure 1). Unlike most batch reactor processes, control is managed through adjustments to reactant flow. The primary control loop maintains reactor temperature within a range of 48°C to 52°C. The secondary loop adjusts the rate of reactant flow into the process. This architecture enables Evonik to meet the process’ tight temperature tolerance and operating specifications.

cascade loop
Figure 1 -- Cascade control:
Adjustment of reactant flow
regulates the reactor temperature.
Click on illustration for a larger image.


However, dramatic changes to temperature regularly occurred as reactant was introduced, creating the equivalent of a process upset and resulting in frequent overshoot. Oscillations within the process were such that the production cycle was longer than necessary, averaging 27 hours.

Startup Challenges
Without operator intervention, during startup the process would overshoot as the reactor warmed up (Figure 2a). This and other process dynamics proved difficult for plant staff to control. Manual PID tuning failed to achieve the desired results.

 Evonik hoped that commercial tuning packages could accurately model the batch dynamics. However, using most such software tools posed a major problem.

Almost every commercial PID tuning package requires an initial steady-state operation. By beginning at a steady state, these tools establish a known value of operation that becomes the basis for application of their respective modeling algorithms. Bump tests then generate dynamic process data that these tuning packages use to model the relationship between the controller output and the measured process variable (PV). The software relies on that relationship to calculate tuning parameters for the PID controllers.

before
after
Figure 2 -- Better startup: (before, top; after, bottom)
PID control eliminated set-point

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