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=18Constantes de AntoineSistema:Benceno(A)Tolueno(B)Tempe, F=210.85presin 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, psia714.2587.8A0.525.48036792251.41557599570.70778799780.50.7077879978B0.510.52986565760.58499253650.29249626830.50.2924962683F, lbmol/h =1001.000284266111.0002842661zF(A)=0.5PvKzF*KzF/Kgg^2/zFxyHvLambdaHl-0.0002842661PF, 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=18Pv A21.53210052151.10096443861.0925489848-0.0000000001-0.1845408073114382.764055836-9933.0089741781a36.92539900E-069.96136800E-06Tempe, F=222.5Pv 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)1.4496254682A0.530.32366535341.68464807520.29679789350.50.2967978935Hv A Btu/lb mol3540.9639564819B0.512.78947950380.71052663910.70370338350.50.7037033835Hv B Btu/lbmol4490.0372579286Condiciones del separador ADIABATICO: vlvula adiabtica1.00050127711.000501277lambda A Btu/lb mol13665.7618015467P, psia =9Fracc V/F0.00008103Nuevo V/F-8.1030E-05-5.01277E-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

Hoja2 (2)SEPARACIN FLASHIngresaTR,F32Presin , psia=4Constantes de AntoineSistema:Benceno(A)Tolueno(B)Tempe, F=128.55presin 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, psia714.2587.8A0.55.93703976561.48425994140.74212997070.50.7421299707B0.52.06366270810.5159156770.25795783850.50.2579578385F, lbmol/h =1001.000087809211.0000878092zF(A)=0.5PvKzF*KzF/Kgg^2/zFxyHvLambdaHl-0.0000878092PF, 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=4Pv A21.53210052151.10096443861.0925489848-0.0000000001-0.1845408073114382.764055836-9933.0089741781a36.92539900E-069.96136800E-06Tempe, F=140.5Pv 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)1.4496254682A0.57.5484449291.88711123230.2649552350.50.264955235Hv A Btu/lb mol3540.9639564819B0.52.70048209020.67512052250.74060850370.50.7406085037Hv B Btu/lbmol4490.0372579286Condiciones del separador ADIABATICO: vlvula adiabtica1.005563738711.0055637387lambda A Btu/lb mol13665.7618015467P, psia =9Fracc V/F0.06898903Nuevo V/F6.8989E-02-5.56374E-03lambda B Btu/lbmol15273.740147218T, F =170.636256Hv mezcla4015.5006072052T+0.01F =170.646256Hl mezcla-10454.2503671771HF-10454.25PvKzF*KzF/Kgg^2/zFxyHv iLambdaHl iPvKgHvlambdaHlBenceno(A)13.20489298621.46721033180.73360516590.34078276930.22631063380.1024330060.48438704890.71069768272840.733170431813843.6045703699-11002.871399938113.20720936531.46746770730.22643140822840.965878344613843.5405669937-11002.574688649Tolueno(B)5.04975832080.56108425790.28054212890.8911317561-0.22631064130.10243301270.51561295160.28930231033604.754511954815486.0571903496-11881.30267839485.05074924730.5611943608-0.22625209863605.048573789915485.9807300137-11880.93215622381.01414729481.2319145253-0.0000000075-0.20486601871.00000000050.9999999933061.7662898614-11455.80194990290.00000009571.38867620730.0001793096-0.00000000750.01793171043062.0167476041-11455.46718076690.00003156170.00000009570.0031465918G1(V/F)G1'(V/F)Hv mHl mG2(V/F)G2'(V/F)G1(T+DT)G1(T)G1'(T)G2(T+DT)G2(T)G2'(T)Entalpia mezclaEntalpia mezclaPTV/FQT para Q=0V/F para Q=09169.90.00008103Pto burbuja-96297170.66820385520.0646307449Q0.100091728jacobianoMatriz inversa del jacobianoGJ-1GNuevo0.06898896190.06898903181.81Pto rocio1395409-0.20486601870.0179317104-0.12317370980.701938931-0.00000000750.0000000681V/F=0.06898896191bar=100 KpaFC170.6362556391170.6362561.38867620730.003146591854.35989484158.01950460150.00000009570.0000003609T=170.63625563911atm=760 mm Hg3204128.50.00007-231977130.4154802410.15629725591atm=14,696 psi140.76112527881atm=1,01325 bar1atm=101,325 Kpa15199.50813.501199.493558946-0.0005505174211.211478516.01V/FTG1G20.06817987170.613031-0.00025073-0.0012048530.06899476170.636318-0.00000006970.0000081455

Hoja3SEPARACIN FLASHIngresaTR,F32G1xV/FPresin , psia=45-0.069360.250.6Constantes de AntoineSistema:Metanol(A)Agua(B)Tempe, F=222.2-0.01560.2904720.48329presin en PSIA y T en FA17.5133346.53247Condiciones del separador ISOTRMICO-0.01160.3269650.45416223A26468.1017173.79PUNTO DE BURBUJAP, psia =45-0.00460.3424810.430736916A3396.2652389.4747CompuestozFPvapor, psiax=zFgammaKzF*KxyT, F =235Fracc V/F0.74327122Nuevo V/F0.7432712191-0.00250.3514510.42119217Pc, psia1153.63206.7A0.560.68317156730.51.12775495711.52079438990.7603971950.50.760397195-0.00110.355613070.41581023B0.517.76721049170.51.21612141880.48015744960.24007872480.50.2400787248F, lbmol/h =1001.000475919811.0004759198zF(A)=0.5PvxgammaKzF*KzF/Kgg^2/zFxyHvLambdaHl-0.0004759198PF, psia=45Metanol(A)75.0179077060.308867381.09949886041.83293564520.91646782260.27278644580.25722226560.13232658790.30881409280.56603635842240.974075995915560.3915467174-13319.4174707216Calor especifico vapores idealesa19.80108400E+007.98574200E+00IngresaTF, F=220Agua(B)22.59544758550.256713831.25040308160.62785371760.31392685880.796363844-0.25722226590.13232658810.69118590740.43396364151639.729154189317635.4435988503-15995.7144446609T en F, Cp en Btu/lbmolFa28.43064200E-034.63319100E-04Presin , psia=45Pv A58.45933505671.23039468141.0691502898G1-0.0000000002-0.2646531761.00000000020.99999999991980.0556401621-15169.2362254365a36.66918500E-061.40284100E-06Tempe, F=242.5Pv B17.0307423179Q Btu/h1246438.85016431Entalpia mezclaEntalpia mezclaa4-8.20898100E-09-6.57838700E-10PUNTO DE ROCIOGamma A1.1277549571a52.50063800E-129.79528800E-14CompuestozFPvapor, psiaxsupuestogammaKzF/KyxGamma B1.2161214188A0.584.60828639540.146340261.66095555923.12290230320.16010747420.50.1601074742suma(z*K)0.9626583934en caso de vapor sobrecalentadoConstantes de van Laara0.83B0.525.89577145020.853659741.02456351970.58959694980.84803695160.50.8480369516suma(z/K)1.427637996No usar la tabla de criterioCondiciones del separador ADIABATICOb0.511.008144425811.0081444258Hv A Btu/lb mol2061.3595299191P, psia =1Fracc V/F1Nuevo V/F0.998729624-8.14443E-03Hv B Btu/lbmol1517.2685220034T, F =82.19lambda A Btu/lb mol15629.5369669771lambda B Btu/lbmol17723.1903664198Hv mezcla1789.3140259613PvxgammaKzF*KzF/Kgg^2/zFxyHvLambdaHlHl mezcla-14887.0496407372Metanol(A)2.8441339460.096190741.82762330165.19800547272.59900273630.09619074140.40380925860.32612383470.09619074140.5517.147018524916479.8810115045-15962.7339929796HF-14887.04964Agua(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

G21.0308833346Q1534681.13747247PTV/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

Cloroformo-MetanolSEPARACIN FLASHIngresaTR,F32Presin , psia=30Constantes de AntoineSistema:Cloroformo (A)Metanol (B)Tempe, F=168.520575.8447222222 presin en PSIA y T en FA15.8940577.513334Condiciones del separador ISOTRMICOTV/FQ/FQA25289.3856468.101PUNTO DE BURBUJAP, psia =301650.44072458441.1261031676844112.610316759A3393.075396.2652CompuestozFPvapor, psiax=zFgammaKzF*KxyT, F =165.25Fracc V/F0.50913203Nuevo V/F0.509132033165.250.509132039438.0219325596943802.19325596Pc, psia793.61153.6A0.323.38606900020.51.51893005261.18406010050.35521803020.30.3552180302165.50.5745858510395.95154053791039595.15405379B0.722.4584430260.51.23042910950.92111740180.64478218120.70.6447821812F, lbmol/h =1001660.7071796212345.49317519721234549.317519721.000000211411.0000002114zF(A)=0.5PvxgammaKzF*KzF/Kgg^2/zFxyHvLambdaHl166.50.8429007614353.16505100481435316.50510048-0.0000002114PF, psia=45Metanol(A)22.13078852280.359773041.77206515621.30723997410.6536199870.38248524370.1328403420.03529311290.4323667270.5652070692131.580775020613163.7748470031-11032.19407198241670.9828813616436.13876698021643613.87669802Calor especifico vapores idealesa11.48400000E+019.80108000E+00IngresaTF, F=220Agua(B)21.00926577850.640226961.09376748750.76597506150.38298753070.6527627662-0.13284034180.03529311280.56763327290.43479293111426.808043399115914.8728923429-14488.0648489438T en F, Cp en Btu/lbmolFa21.24500000E-028.43064000E-03Presin , psia=30Pv A51.57336477111.03660751781.03524800990.0000000002-0.07058622570.99999999991.00000000011825.1505735012-12993.8613105734a3-6.49500000E-066.66919000E-06Tempe, F=164.3173.5055555556Pv B58.4593350567Q Btu/h943802.19325596G1G1'Entalpia mezclaEntalpia mezclaa41.25900000E-09-8.20898000E-09PUNTO DE ROCIOGamma A1.5189300526a50.00000000E+002.50064000E-12CompuestozFPvapor, psiaxsupuestogammaKzF/KyxGamma B1.2304291095A0.321.78001818310.31.88944970531.37174163120.21870007670.30.2187000767suma(z*K)1.6696266804en caso de vapor sobrecalentadoConstantes de van Laara0.9356B0.720.60735233210.71.05968939560.72791309130.96165326380.70.9616532638suma(z/K)0.6000268626No usar la tabla de criterioCondiciones del separador ADIABATICOb1.8861.180353340511.1803533405Hv A Btu/lb mol3062.5906134407P, psia =1Fracc V/F0.17Nuevo V/F0.750047651-1.80353E-01Hv B Btu/lbmol2066.164104139T, F =62lambda A Btu/lb mol12914.6479874941T+0.01F =62.01lambda B Btu/lbmol15629.5369669771Hv mezcla2564.3773587898PvxgammaKzF*KzF/Kgg^2/zFxyHvLambdaHlPvxygammaKgHvLambdaHlHl mezcla-11707.7151184457Metanol(A)2.57933206160.437318361.62800231574.19915856932.09957928470.11907147391.03609293442.14697713750.32386420121.3599571356462.313783412513807.411120862-13345.09733744962.57999092050.32386420121.35995713561.84195262274.75222104241.1454522287462.469656328213807.3337287991-13344.864072471HF-14887.04964Agua(B)1.5677762990.562681641.15723893231.81429177040.90714588520.27558963130.35763817530.25581012890.43920151020.7968396855306.37701670116650.0701569915-16343.69314029061.56825922940.67613579880.79683968551.07199598211.68116759270.3052377281306.480511693916649.9819254325-16343.50141373863.00672516990.39466110521.3937311097-2.40278726630.76306571132.1567968211872.8602942514-11500.17399790930.36879647780.83112736181.45068995691.39373110975.6958847148356.9998114091-15372.3501266680.14701966180.3687964778-22.1776816011G1G1'Entalpia mezclaEntalpia mezclaG2G2'G1(T+DT)G1(T)G1'G2(T+DT)G2(T)G2'

t=0.03Q549029.147175804JacobianoJacobiano-1GNuevos0.19039595930.142PTV/FQT para Q=0V/F para Q=0-2.40278726635.6958847148-0.4567609168-0.11730971571.3937311097-0.6798653094V/F=0.190395959362.00126323166burbuja10146.450-525.977146.45648636590.00030438130.8311273618-22.1776816011-0.0171175014-0.04948665660.3687964778-0.0421076989T=62.001263231rocio167.7611727494

1bar=100 KpaFCburbuja5117.350-55326.98033118.02814290540.0315268668fi=-0.27373040131atm=760 mm Hg185.24585.1361111111rocio138.8611699588.31atm=14,696 psi327.245164.0251atm=1,01325 barburbuja160.40-159389.262.31570883780.08828151331atm=101,325 Kparocio82.111646076

TV/FG1G271.80.619-0.0080.55070.3033344967.360.4766-0.020.371620.138501424467.24010.195630.14080.0760.0256006467.2430.201390.137870.083190.02592871367.34760.3926270.0312170.288430.08416636667.260.128880.17594-0.0030090.0309639377660.1290.13329-0.0098660.0178635621660.140.1280390.0032770.0164047242660.170.11350.038480.0143629604640.170.0494170.0257070.0031028897620.17-0.012780.0132140.0003379382

Entalpas PonchonSEPARACIN FLASHTR,F32

Constantes de AntoineSistema:Cloroformo (A)Metanol (B)presin en PSIA y T en FA15.8940577.513334A25289.3856468.101A3393.075396.2652Pc, psia793.61153.6F, lbmol/h =100zF(A)=0.5PF, psia=45Calor especifico vapores idealesa11.48400000E+019.80108000E+00TF, F=220T en F, Cp en Btu/lbmolFa21.24500000E-028.43064000E-03Pv A51.5733647711a3-6.49500000E-066.66919000E-06Pv B58.4593350567a41.25900000E-09-8.20898000E-09Gamma A1.5189300526a50.00000000E+002.50064000E-12Gamma B1.2304291095suma(z*K)1.6696266804Constantes de van Laara0.9356suma(z/K)0.6000268626b1.886Hv A Btu/lb mol3062.5906134407Hv B Btu/lbmol2066.164104139lambda A Btu/lb mol12914.6479874941lambda B Btu/lbmol15629.5369669771Hv mezcla2564.3773587898Hl mezcla-11707.7151184457HF-14887.04964