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Plantwide Control of Methanol Process

To conclude our examples of Aspen Dynamics simulation of tubular reactor systems, we study a very important industrial process for the production of methanol from synthesis [Pg.344]


In Chapter 8 we explored the steady-state design of the TAME reactive distiUalion system. The reactive column is part of a multiunit process that includes other columns for recovery of the methanol reactant. The recovery is necessary because the presence of methanol/C5 azeotropes unavoidably removes methanol from the reactive column in the distillate stream. The economics of two alternative methanol recovery systems were evaluated in Chapter 8. In this chapter the dynamic control of the process is studied, and an effective plantwide control structure is developed. The process has three distillation columns one reactive column, one extractive distillation column, and one methanol/water separation column from which methanol and water are recycled. [Pg.389]

Systems that have the most potential for reactive distillation are those where the reaction is reversible, heat of reaction is not excessively large, and the products have the correct volatilities in relation to the reactants. Those systems reach chemical equilibrium (i.e., reaction stops) unless the reactants are in large excess or the products are continuously removed. An example system has been reported in the literature by Eastman Chemical (Agreda et al., 1990) for the production of methyl acetate from methanol and acetic acid. The discussion about process operation and the control strategy shown in the paper certainlv adhere to the plantwide control principles we have outlined in this book. [Pg.193]

There are two key plantwide material balance loops associated with column C3. The level in the reflux drum provides a good indication of the inventory of methanol in the system. If this level is going down, more methanol is being consumed in the reaction than is being fed into the process. Therefore, the control structure maintains the reflux drum level in C3 by manipulating the methanol fresh feed. [Pg.271]


See other pages where Plantwide Control of Methanol Process is mentioned: [Pg.344]    [Pg.345]    [Pg.347]    [Pg.349]    [Pg.351]    [Pg.353]    [Pg.355]    [Pg.359]    [Pg.361]    [Pg.363]    [Pg.365]    [Pg.367]    [Pg.344]    [Pg.345]    [Pg.347]    [Pg.349]    [Pg.351]    [Pg.353]    [Pg.355]    [Pg.359]    [Pg.361]    [Pg.363]    [Pg.365]    [Pg.367]    [Pg.465]   


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