#*------------------------------------------------------------------- * EMSO Model Library (EML) Copyright (C) 2004 - 2007 ALSOC. * * This LIBRARY is free software; you can distribute it and/or modify * it under the therms of the ALSOC FREE LICENSE as available at * http://www.enq.ufrgs.br/alsoc. * * EMSO Copyright (C) 2004 - 2007 ALSOC, original code * from http://www.rps.eng.br Copyright (C) 2002-2004. * All rights reserved. * * EMSO is distributed under the therms of the ALSOC LICENSE as * available at http://www.enq.ufrgs.br/alsoc. * *-------------------------------------------------------------------- * Sample file for model centrifugal_pump and pump (simplified) *-------------------------------------------------------------------- * * This sample file needs VRTherm DEMO (www.vrtech.com.br) to run. * *---------------------------------------------------------------------- * Author: Estefane S. Horn, Paula B. Staudt * $Id: sample_pump.mso 372 2007-09-21 22:17:36Z arge $ *--------------------------------------------------------------------*# using "pressure_changers/pump"; FlowSheet Pump_P1 DEVICES S1 as source; P1 as centrifugal_pump; CONNECTIONS S1.Outlet to P1.Inlet; PARAMETERS PP as Plugin (Brief="External Physical Properties", Type="PP", Components = ["water", "benzene"], LiquidModel = "PR", VapourModel = "PR" ); Mw as positive (Brief = "Molar Mass", Unit = 'kg/kmol'); NComp as Integer (Default= 1); SET NComp = PP.NumberOfComponents; P1.N = 1000 * 'rpm'; P1.Lev = 0 * 'm'; P1.Meff = 0.95; P1.Eff = 0.72; P1.Beta = 425e-6 * '1/K'; SPECIFY S1.Outlet.F = 1000 * 'kmol/h'; S1.Outlet.P = 10 * 'atm'; S1.Outlet.T = 298 * 'K' ; S1.Outlet.z = [1,0]; P1.Pdrop = -8 * 'kPa'; #P1.Outlet.P = 2 * 'atm'; #P1.BPower = 1 * 'kW'; end FlowSheet pump_Test PARAMETERS PP as Plugin (Brief="External Physical Properties", Type="PP", Components = ["water", "benzene"], LiquidModel = "PR", VapourModel = "PR" ); NComp as Integer; SET NComp = PP.NumberOfComponents; DEVICES p1 as pump; s1 as source; CONNECTIONS s1.Outlet to p1.Inlet; SPECIFY s1.Outlet.F = 826 * 'kmol/h'; s1.Outlet.P = 549 * 'kPa'; s1.Outlet.T = 313 * 'K'; s1.Outlet.z = 1/NComp; #s1.Outlet.v = 0.68; p1.dP = 90 * 'kPa'; OPTIONS Dynamic = false; end