Hoja1Sistema:Acetonitrilo(A)Nitrometano(B)Sistema:Benceno(A)Etilbenceno(B)Constantes de AntoineA114.272414.2043Constantes de AntoineA113.885814.0045presin en KiloPa y T en CA22945.472972.64presin en KiloPa y T en CA22788.513279.47A3224209A3220.79213.2Sistema:Benceno(A)Etilbenceno(B)Sistema:1-Clorobutano(A)Benceno(B)Constantes de AntoineA113.885814.0045Constantes de AntoineA113.9613.8858presin en KiloPa y T en CA22788.513279.47presin en KiloPa y T en CA22826.262788.51A3220.79213.2A3224.1220.79Sistema:1-Clorobutano(A)Clorobenceno(B)Sistema:n-Pentano(A)n-Hexano(B)Constantes de AntoineA113.9613.9926Constantes de AntoineA113.818313.8216presin en KiloPa y T en CA22826.263295.12presin en KiloPa y T en CA22477.072697.55A3224.1217.55A3233.21224.37Sistema:Acetona(A)Acetonitrilo(B)Sistema:n-Hexano(A)Trietilamina(B)Constantes de AntoineA114.546314.2724A1presin en KiloPa y T en CA22940.462945.47A2A3237.22224A3Sistema:n-Pentano(A)n-Heptano(B)Constantes de AntoineA113.818313.8587presin en KiloPa y T en CA22477.072911.32A3233.21216.64Sistema:Benceno(A)Tolueno(B)Constantes de AntoineA113.885813.9987presin en KiloPa y T en CA22788.513096.52A3220.79219.48

Hoja2SEPARACIN FLASHIngresaTR,F32Presin , psia=4Constantes de AntoineSistema:Benceno(A)Tolueno(B)Tempe, F=128.541presin en PSIA y T en FA15.6583755.944251Condiciones del separador ISOTRMICO: no hay vlvulaA25307.8135836.287PUNTO DE BURBUJAP, psia =18A3379.456374.745CompuestozFPvapor, psiaKzF*KxyT, F =217Fracc V/F0.5198289Nuevo V/F0.5198288996Pc, psia714.2587.8A0.55.93594086631.48398521660.74199260830.50.7419926083B0.52.06323481490.51580870370.25790435190.50.2579043519F, lbmol/h =1000.999896960210.9998969602zF(A)=0.5PvKzF*KzF/Kgg^2/zFxyHvLambdaHl0.0001030398PF, psia=18Benceno(A)27.95567145091.55309285840.77654642920.3219382520.21479106550.09227040360.38834539670.60313646223961.687777597813571.2747989611-9609.5870213633Calor especifico vapores idealesa11.63928200E+012.11772200E+01IngresaTF, F=200Tolueno(B)11.67904834010.64883601890.32441800940.7706107328-0.21479106560.09227040370.61165460330.39686353785022.698019919315161.0507052181-10138.3526852988T en F, Cp en Btu/lbmolFa24.02036900E-024.63954600E-02Presin , psia=15Pv A21.53210052151.10096443861.0925489848-0.0000000001-0.1845408073114382.764055836-9933.0089741781a36.92539900E-069.96136800E-06Tempe, F=211.2Pv B8.7239321956Q Btu/h796299.35726638Entalpia mezclaEntalpia mezclaa4-4.11420200E-08-4.62826400E-08PUNTO DE ROCIOsuma(z*K)0.8404453533a52.39809800E-112.58578700E-11CompuestozFPvapor, psiaKzF/Kyxsuma(z/K)1.4496254682A0.525.61649202521.7077661350.29278013530.50.2927801353Hv A Btu/lb mol3540.9639564819B0.510.59273901680.70618260110.70803217070.50.7080321707Hv B Btu/lbmol4490.0372579286Condiciones del separador ADIABATICO: vlvula adiabtica1.00081230611.000812306lambda A Btu/lb mol13665.7618015467P, psia =9Fracc V/F0.00008103Nuevo V/F-8.1030E-05-8.12306E-04lambda B Btu/lbmol15273.740147218T, F =169.861Hv mezcla4015.5006072052Hl mezcla-10454.2503671771HF-10454.25PvKzF*KzF/Kgg^2/zFxyHvLambdaHlBenceno(A)13.02629219211.44736579910.72368289960.34545517130.22367479130.10006082460.49998187560.7236566672822.704359469413848.5740152526-11025.8696557832Tolueno(B)4.97341588170.55260176460.27630088230.904810719-0.22370722770.10008984740.5000181270.27631089933581.972502889715491.9939468999-11910.02144401020.99998378191.2502658903G1-0.0000324363-0.2001506721.00000000260.99996756633032.4068722425-11467.9616058927Entalpia mezclaEntalpia mezcla

PTV/FQT para Q=0V/F para Q=0G2-0.09685406819169.8610.00008103Pto burbuja-101253.6641170.66853766440.0676377947Q-101253.6641034911790.74940.9726181.81351Pto rocio1397418.7491750.42710.5081bar=100 KpaFC1740.34770.3951atm=760 mm Hg3204128.5450.00007-237874.1127130.4454904730.15564572151730.26730.28051atm=14,696 psi140.7611291011.3661720.18520.1641atm=1,01325 bar171.50.143280.1051atm=101,325 Kpa15199.50-1696.87596199.51341511560.0011465911170.50.05702778-0.0106211.211478234.365170.20.030432056-0.054170.60.065813234-0.00447170.80.083270470.020110842170.70.0745604640.007844052170.640.0693166560.000461302

Hoja3SEPARACIN FLASHIngresaTR,F32G1xV/FPresin , psia=5-0.069360.250.6Constantes de AntoineSistema:Metanol(A)Agua(B)Tempe, F=146.42-0.01560.2904720.48329presin en PSIA y T en FA17.5133346.53247Condiciones del separador ISOTRMICO-0.01160.3269650.45416223A26468.1017173.79PUNTO DE BURBUJAP, psia =20-0.00460.3424810.430736916A3396.2652389.4747CompuestozFPvapor, psiax=zFgammaKzF*KxyT, F =185Fracc V/F0.41581023Nuevo V/F0.4133479835-0.00250.3514510.42119217Pc, psia1153.63206.7A0.514.08737182780.51.12775495713.17742068221.58871034110.51.5887103411-0.00110.355613070.41581023B0.53.38346800980.51.21612141880.82294158330.41147079170.50.4114707917F, lbmol/h =1002.000181132812.0001811328zF(A)=0.5PvxgammaKzF*KzF/Kgg^2/zFxyHvLambdaHl-1.0001811328PF, psia=20Metanol(A)31.0733973040.355613071.2590661411.95617312150.97808656080.25560109920.34208010620.23403759810.35775959240.69983969861651.228086042615805.4409561713-14154.2128701287Calor especifico vapores idealesa19.80108400E+007.98574200E+00IngresaTF, F=150Agua(B)8.31368476070.644386931.12095574270.46596363380.23298181691.0730451129-0.34323652540.23562262480.64272125860.29948473321232.45953095517946.729406947-16714.269875992T en F, Cp en Btu/lbmolFa28.43064200E-034.63319100E-04Presin , psia=10Pv A15.23185686911.21106837771.328646212G1-0.0011564192-0.46966022291.00048085090.99932443171524.69777974-15806.4219976403a36.66918500E-061.40284100E-06Tempe, F=167.75Pv B3.6977910041Q Btu/h740187.609314972Entalpia mezclaEntalpia mezclaa4-8.20898100E-09-6.57838700E-10PUNTO DE ROCIOGamma A1.1277549571a52.50063800E-129.79528800E-14CompuestozFPvapor, psiaxsupuestogammaKzF/KyxGamma B1.2161214188A0.522.10981544240.146340261.66095555923.67234208730.13615289320.50.1361528932suma(z*K)0.5418691233en caso de vapor sobrecalentadoConstantes de van Laara0.83B0.55.64813552480.853659741.02456351970.57868736130.86402439980.50.8640243998suma(z/K)2.8058697196No usar la tabla de criterioCondiciones del separador ADIABATICOb0.511.00017729311.000177293Hv A Btu/lb mol1253.4872980717P, psia =1Fracc V/F1Nuevo V/F0.998729624-1.77293E-04Hv B Btu/lbmol948.8570368582T, F =82.19lambda A Btu/lb mol16005.0674068556lambda B Btu/lbmol18200.9593088912Hv mezcla1101.172167465PvxgammaKzF*KzF/Kgg^2/zFxyHvLambdaHlHl mezcla-16001.8411904084Metanol(A)2.8441339460.096190741.82762330165.19800547272.59900273630.09619074140.40380925860.32612383470.09619074140.5517.147018524916479.8810115045-15962.7339929796HF-16001.84119Agua(B)0.54659643310.903809261.01117804970.55270631520.27635315760.9046395639-0.40463956390.32746635340.90463956390.5402.376450924518807.962384669-18405.58593374442.8753558941.0008303053G1-0.0008303053-0.65359018811.00083030531459.7617347247-18185.8884497906Entalpia mezclaEntalpia mezcla

G21.0287318021Q1646160.29247247PTV/FQT para Q=0V/F para Q=0burbuja10146.420-5943.555146.49320335540.0034287286rocio167.7711727513.861

1bar=100 KpaFCburbuja5117.350-55326.98033118.02813952030.03152670951atm=760 mm Hg185.24585.1361111111rocio138.8611699597.061atm=14,696 psi327.245164.0251atm=1,01325 barburbuja15165024611.299164.6975230368-0.01430151131atm=101,325 Kparocio186.1511745499.291

burbuja160.40-159389.204362.32356441560.088277394rocio82.1911646160.292