Hoja1CONDICIONES DE OPERACINPROPIEDADESAmoniacoAguaAGUAAMONIACO(gas)AMONIACO LIQUIDOTent604DeltaTaguaRHO997.712.207608.7Tsal(sat)21160.9944082013MIU1.00E-031.10E-051.50E-04Pent(Kpa)900Tsalenf4.9944082013Cp(Kj/Kg.K)4.193.54.75K0.182.95E-020.49Hfg(Kj/Kg)1180.9ALFA1.44E-042.21E-05H106.7Pr9.451.31E+00mpunto(Kg/s)0.5956228315.2530619723MIUCINEM9.80E-071.92E-05Qcond703.37163.5529559658Q(kj/s)766.9239559658R39.21930646671.4S0.0177572893Rf0.0001760.000176F0.97NTU CondNTUdesobTm40.510condensacione69%e70%TuberiaBWG=16DESOBRECALENTAMIENTOLMTDc9.4590370131NTU1.1635002362DoDiTubos(AGUA)Usupuesto900El desobrecalentamiento se desprecia con respecto a la condensacionDN0.019050.0157438017Uinicial300A82.6218707304ho1000tw0.001651LMTD11.7459887159F0.95Tw11.5474836906Tmt10.4972041007Kw63.9LMTDr11.1586892801Nt460.1812470429Tms21DELTAPDELTAPDm0.0173444135A18.9845940894K10.249Db0.5755226675corazatubosA1tubo0.1795420202n12.207Nr24.168930917f0.5175891669f0.03Pitchratio1.25Ntubo106Db0.2955751456ho10410.0036171461Re663.6501190156P8.5800830992L3Ntuxpaso53Ds0.35157514561/U0.0010538384As0.0809328459pasos2Atransv0.0001946745Re2.33E+04U948.9120958523Gs7.3594697392Pitch0.0238125Atranxpaso0.0102923445L/Di190.5511811024Ac78.3630896712DeltaP4.4713810747Dcoraza0.3515751456Q0.0152882249Jh4.00E-03Lc75%Vtubos1.4853977064Nus1.96E+02C0.0047625hi2239.0702233159B0.3515751456CorazaAt103.9789570699As0.0247210166Nt579por pasoDeq0.0135264525L3Q0.0487935471Ds0.636132242Vshe1.973767824Nt en dos pasos2900.2186237333Re29595.2980830429jh4.00E-03Uparacontrl769.9159920446Nuss1.30E+02ho2.82E+021/U0.0044976587U222.3379024491Atdes25.6158673987

Hoja2

Hoja3