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126  PLANT DESIGN AND ECONOMICS FOR CHEMICAL ENGINEERS

             Flow-sheeting is applied to steady-state conditions. The unsteady-state
        features of normally steady-state processes-start up, shutdown, disturbances,
        control actions-are usually analyzed separately from the process-design task.
        This results in a major simplification of the design problem, because time
        variations and integration with respect to time need not be performed (although
        integration with respect to space may still be required in models for particular
        operations, such as that of a plug-flow chemical reactor). The flow-sheeting
        language SPEED-UP is an exception in that it includes unsteady-state capability
        in its code.?
            The solution to the problem is obtained by solving mass and energy
        balances to yield the quantity and state (i.e., composition, temperature, pres-
        sure) of all the streams and the utility requirements. Additional parameters for
        the process equipment, sufficient so that stream specifications are met and the
        cost of the equipment can be estimated, are calculated. The cost of equipment,
        raw materials, and utilities is estimated and an economic analysis is carried out.
        Methods of cost estimation and economic analysis are presented later in this
        text. This entire procedure may be repeated many times to examine modifica-
        tions of the process flow sheet or to find optimal values of key process variables.
        Computer software can greatly simplify these repetitive calculations for the
        engineer. But even without the need for repetition, the software may simplify
        the calculations and provide detail and accuracy that would have been impossi-
        ble otherwise.
            Certain features of chemical process calculations contribute to their dif-
        ficulty, complexity, and challenge. These include: large sets of nonlinear, alge-
        braic equations, the need for large amounts of physical and chemical property
        data, the presence of operations that require very complex models, and the
        occurrence of recycle streams. The property issue has been discussed and the
        other matters are discussed in the following sections.
            The flow-sheeting program  FL,OWTRAN    is available to universities
        through CACHE. This program was developed by the Monsanto Company in
       the 1960s and made available for university use in 1973. FLOWTRAN is well
        documented with a manual and examples.+ It can be installed on many main-
        frame computers, but not on personal computers. FLOWTRAN is available
       through Chemical Engineering Departments at most universities. CHEMCAD
        IITM  is a flow-sheeting program  for personal computers offered by
       COADE/Chemstations, Inc. PROCESS TM, the product of Simulation Sciences,




        t.J.  D. Perkins and R. W. H. Sargent, SPEED-UP: A Computer Program  for Steady-State and
        Dynamic Simulation and Design of Chemical Processes, “Selected Topics on Computer-Aided
        Process Design and Analysis,” R. S. H. Mah and G. V. Reklaitis, eds.,  AIChE  Symposium Series,
        Vol. 78, No, 214, American Institute of Chemical Engineers, New York, 1982.
        $J.  D. Seader, W. D. Seider, and A. C. Pauls, “FLOWTRAN Simulation--An Introduction,” 3rd
        ed., CACHE, 1987; J. P. Clark, T. P. Koehler, and J. T. Sommerfeld, “Exercises in Process
        Simulation Using FLOWTRAN,” 2nd ed., CACHE,  1980.
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