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HYSIM

The model is predictive and uses a method of contributing groups to determine the parameters of interaction with water. It is generally used by simulation programs such as HYSIM or PR02. Nevertheless the accuracy of the model is limited and the average error is about 40%. Use the results with caution. [Pg.170]

Characteristics ASPEN PLUS Chemcad II Desiga-II Hysim Pio-11 Oiiasilin Span SPEEDUP... [Pg.74]

HYSIM Steady-state process simulation www.hyprotech.com... [Pg.282]

By the early 1990s, advances in user interfaces made the simulation packages much easier to use. HYSIM from Hyprotech was the first package to be developed specifically for a personal computer (PC) platform. All commonly used process simulators (including PRO/II from Simulation Sciences) are now available on a PC platform, with interfaces that allow flowsheet simulations to be formulated rapidly. Icons representing feed and product streams and unit operations are placed directly on a sim-... [Pg.133]

Russell s method is one of the methods used in the MULTIFRAC option for multiple columns in ASPENPlus and is the column method in HYS1M of Hyprotech of Calgary, Alberta. Russell s method as written by Richard Russell is in the PD+Plus system available from Deer-haven Technical Software in Deer haven, Massachusetts. The HYSIM and PD+Plus versions of Russell s method have been found to work well for refinery fractionators with sidestrippers and other similar columns including columns for which a version of Boston s method failed. [Pg.179]

HYSIM User s Guide, Version C1.0, Hyprotech Ltd., Calgary, Alberta, 1989. [Pg.211]

Figure 3.35 presents the page of a modem commercial simulator (Hysim 1995) where we can identify the different elements of the process specified in this block-oriented simulator. [Pg.98]

Figure 3.35 Presentation page of a block-oriented simulator for the analysis of a coupled FCC reactor-fractionator (Hysim 1995). Figure 3.35 Presentation page of a block-oriented simulator for the analysis of a coupled FCC reactor-fractionator (Hysim 1995).
Process simulators are used as an aid in the formulation and solution of material and energy balances. The larger simulators can handle up to 40 components and 50 or more processing units when their outputs are specified. ASPEN, PROSYS, DESIGN II, and HYSIM are examples of such process simulators. [Pg.4]

Hydraulic efficiency of pumps, 517 Hydraulic radius for fluid flow, 486 for heat transfer, 594-595 Hypalon, 435 HYSIM, 127... [Pg.903]

ParametersISolver tab for the block should do the trick. Also, switching the solving method to Modified HYSIM Inside Out may also help. Note that the equivalent approach was necessary for the Aspen Plus absorber example using MEA in Section 4.5. [Pg.211]

HYSIM HYSYS (mid-1990s) Hyprotech, Calgary, Canada (In... [Pg.292]

The development and the design of new processes are today extensively based on mathematical modelling and simulation. The entire process is modelled through combining individual unit operation models. Several flowsheeting programs (Aspen+ , HySim , ChemCAD Pro II etc.) have already found their place in engineering... [Pg.762]

These programs were included in a list published Manning and Thompson (1991). Some may no longer be available. Also, most of the commercial process plant simulation programs (PRO/II, Hysim, Aspen Plus) have amine plant simulation capability. Of all the cmnmeicial amine plant simubiots. TSWEET is probably the most popular. [Pg.110]

See other pages where HYSIM is mentioned: [Pg.85]    [Pg.62]    [Pg.2146]    [Pg.5]    [Pg.7]    [Pg.106]    [Pg.202]    [Pg.189]    [Pg.115]    [Pg.322]    [Pg.127]    [Pg.1902]    [Pg.97]    [Pg.127]    [Pg.902]    [Pg.103]    [Pg.383]    [Pg.2150]    [Pg.108]    [Pg.192]    [Pg.694]    [Pg.1431]    [Pg.290]    [Pg.106]    [Pg.108]    [Pg.286]    [Pg.678]    [Pg.89]    [Pg.233]   
See also in sourсe #XX -- [ Pg.127 ]

See also in sourсe #XX -- [ Pg.97 ]



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