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                   Acronym           Type    Table 4.1.  Simulation packages      Internet address
                                                      Source
                                                                                  http//www.—
                   ASPEN             steady-state     Aspen Technology Inc.       Aspentech.com
                                                      Ten Canal Park,
                   Aspen DPS                          Cambridge, MA
                                                      02141-2201,
                                                      USA
                   DESIGN II         steady-state     WinSim Inc.                 winsim.com
                                                      P.O. Box 1885,
                                                      Houston,
                                                      TX 77251-1885, USA
                   HYSYS             steady-state     Hyprotech                   hyprotech.com
                                                      Suite 900, 125-9 Avenue SE,
                                     dynamic          Calgary, Alberta,
                                                      T2G-OP6, Canada
                                                      Merged with Aspen Tech
                   PRO/II            steady-state     SimSci-Esscor               simsci.com
                                                      5760 Fleet Street,
                   DYNSIM            dynamic          Suite 100, Carlsbad,
                                                      CA 92009, USA
                   CHEMCAD           steady-state     Chemstations Inc.           chemstations.net
                                                      2901 Wilcrest, Suite 305,
                                                      Houston, TX 77042
                                                      USA
                   Note: Contact the web site to check the full features of the current versions of the programs.

                     Detailed discussion of these programs is beyond the scope of this book. For a general
                   review of the requirements, methodology and application of process simulation programs
                   the reader is referred to the books by: Husain (1986), Wells and Rose (1986), Leesley
                   (1982), Benedek (1980), Mah and Seider (1980), Westerberg et al. (1979) and Crowe
                   et al. (1971); and the paper by Panelides (1988).
                     Process simulation programs can be divided into two basic types:
                   Sequential-modular programs: in which the equations describing each process unit
                   (module) are solved module-by-module in a stepwise manner; and iterative techniques
                   used to solve the problems arising from the recycle of information.
                     They simulate the steady-state operation of the process and can be used to draw-up
                   the process flow sheet, and to size individual items of equipment, such as distillation
                   columns.
                   Equation based programs: in which the entire process is described by a set of differential
                   equations, and the equations solved simultaneously: not stepwise, as in the sequential
                   approach. Equation based programs can simulate the unsteady-state operation of processes
                   and equipment.
                     In the past, most simulation programs available to designers were of the sequential-
                   modular type. They were simpler to develop than the equation based programs, and
                   required only moderate computing power. The modules are processed sequentially, so
                   essentially only the equations for a particular unit are in the computer memory at one
                   time. Also, the process conditions, temperature, pressure, flow-rate, are fixed in time.
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