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Constraints include valve, pump, temperature and vapor/liquid traffic limits. The embedded LP in the PredictPro controller allows costs to be used to drive the unit to the most profitable region. The controller can be configured with up to five different operating strategies that are selectable by the operator. Total unit charge rate is controlled in a separate module that splits the feed between furnace passes. A pass balancing control block is used to equalize outlet temperatures from each of the heater passes.
Licensor. Emerson Process Management. CLICK HERE to e-mail for more information home pr o c e s s i nd e x c om pa ny i nd e x Cracking furnace Application. Advanced control pass balancing implements one of the time-honored process control philosophy objectives: maximize unit performance while staying within the constraints of the individual passes. In this example, the balancing strategy is applied to ethylene cracking furnaces. Total feed flow to each furnace is set by outside considerations.
Licensor. Invensys Performance Solutions. CLICK HERE to e-mail for more information home pr o c e s s i nd e x c om pa ny i nd e x Catalytic reformer Application. Applying advanced process control to catalytic reforming units is economically advantageous because of the large spread between reactant values, high operating costs, difficult process dynamics and catalyst deactivation. Aspen Technology addresses these issues by combining the DMCplus multivariable control technology and the Aspen Reformer Inferred Properties Package with the Aspen Plus Optimizer real-time optimization technology and the kinetic reformer model, Aspen Catref.