k1Presion Sist.50psidato asumido nv0.001Temp.100o Ff(nv)ComponenteZiPvaporKjzi*(ki-1)zi*(ki-1)/kinv*(ki-1)+1f(nv)c30.21893.780.55600.40891.0028i-c40.1721.440.04400.01341.0004n-c40.1511.020.00200.00001.0000i-c50.220.440.4088-0.11820.17100.9994n-c50.215.570.3114-0.13770.30450.9993c60.24.9560.09912-0.18021.63760.99910.16592.53556.00110.027639

k2Determinar la Razon de EquilibrioPresion (psi)1000Temp(oF)150SGc7+0.8527Corr. Wilsona1.8Corr. Standingc0.685ComponenteComposicionPeso molecularPresion Crit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.biFiConst. Equil.psioRoRwkkCO20.009441071547.9350.750.2252.0923318152.202.027N20.00328.013493227.6139.550.0416.342725503.047.642C10.53516.043667.8343.37201.270.01047.155378062.684.346C20.11530.07707.8550.09332.50.09861.2634114141.941.335C30.08844.097616.3666.01416.250.15240.3491618011.370.551I-C40.02358.123529.1734.98470.780.18480.1436820380.990.300N-C40.02358.123550.7765.65491.080.2010.1062221550.860.243I-C50.01572.15490.4829.1542.120.22230.0464223860.490.137N-C50.01572.15488.6845.7556.920.25390.0362324820.390.116C60.01586.177436.9913.7615.720.30070.013492781-0.040.059C7+0.159198.71245.911246.96939.830.6050.000034668-2.690.0011.000Determinacion de las propiedades criticas C7+nay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)wMetodo Rowes14.052.430.491246.96245.91939.830.605Metodo de Standing1374.03291.41a16124.30496918.016StandingRzasasPresion de Convergenciaa2-2753.2538-3110.07677239747a3415.42049469.2594277.2

PbDeterminar la Razon de Equilibrio y Presion de BurbujaPresion (psi)3925Temp(oF)200SGc7+0.8605Corr. WilsonComponenteComposicionPeso molecularPresion Crit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.Calc. Pres.ComposicionpsioRoRwkBurbuja Ini.Nuev.CO20441071547.9350.750.2250.834050.000000.000000N2028.013493227.6139.550.044.875770.000000.000000C10.4216.043667.8343.37201.270.01042.297633787.637050.965003C20.0530.07707.8550.09332.50.09860.4816694.525710.024083C30.0544.097616.3666.01416.250.15240.1484229.126540.007421I-C40.0358.123529.1734.98470.780.18480.065437.704580.001963N-C40.0258.123550.7765.65491.080.2010.049973.922700.000999I-C50.0172.15490.4829.1542.120.22230.023250.912410.000232N-C50.0172.15488.6845.7556.920.25390.018720.734790.000187C60.0186.177436.9913.7615.720.30070.007590.298090.000076C7+0.4216230.421279.67975.700.6100.000020.027520.0000071.00039251.000Determinacion de las propiedades criticas C7+nay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)wMetodo Rowes15.292.400.471279.67230.42975.700.610Metodo de Standing1394.15270.45a16124.30495691.562StandingRzasasPresion de Convergenciaa2-2753.2538-2558.70987609750a3415.42049386.0673518.9Presion de Burbuja Inicial3925

PdDeterminar la Razon de Equilibrio y Presion de RocioPresion (psi)623Temp(oF)250SGc7+0.8Corr. WilsonComponenteComposicionPeso molecularPresion Crit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.Zi/KiCalc. Pres.ComposicionPcTcTbZipsioRoRwkRocio Ini.Nuev.Psio Ro RCO2044493227350.7430.227670.142140.000000.000000.000493227350.743N2028.0131070547139.5490.04036.192760.000000.000000.0001070547139.549C10.7816.03666.4344201.270.011517.590780.044340.000070.044666344201C20.0530.07706.5549.96332.50.10194.304000.011620.000020.012707550333C30.0444.097616666.06416.250.15831.453010.027530.000040.028616666416I-C40.0358.123527.9734.46470.780.18980.679930.044120.000070.044528734471N-C40.0258.123550.6765.62491.080.20610.532110.037590.000060.038551766491I-C50.0372.15490.4829.1542.120.23300.259240.115720.000190.116490829542N-C50.0272.15488.6845.8556.920.25700.215650.092740.000150.093489846557C60.00586.177436.9913.6615.720.30470.094050.053170.000090.053437914616C7+0.025140396.00972.36668.840.35070.043570.573730.000920.5743969726691.0001.00060.00161.001623Determinacion de las propiedades criticas C7+nay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)wMetodo Rowes9.862.540.541106.34316.59796.210.589Metodo de Standing1276.38370.36a16124.30492743.689StandingRzasasPresion de Convergenciaa2-2753.2538-1233.45842004505a3415.42049186.1081696.3

Op. Sep1Optimizacion de la Presion de SeparacionPresion (psi)500Etapa de Sep.Presion Sep.Temp. o FTemp(oF)72150072225072314.760Separacion FlashSGc7+0.8429Vapor=0.391V0.390.380.389763347PMc7252Liquido=0.609L0.610.620.610236653Corr. WilsonYi=Xi*K1ComponenteComposicionPeso molecularZ*PMDensidad iVol = PM/Dens.Pcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.XiYiX*PMY*PMVol = PM/Dens.PB(PSIA)PD(PSIA)lb/pcpcpsioRoRwkpcCO20440.00051.260.0001071547.9350.750.2251.75968420.00000.0000.0000.0000.00000.00000.0011365676000N2028.0130.00040.880.000493227.6139.550.0424.08079080.00000.0000.0000.0000.00000.00000.0000830538000C10.4216.0436.73818.720.360667.8343.37201.270.01049.14503320.10040.9181.61014.7250.08607362.49490.00021869790.10056115680.10256128240.1006075888C20.0530.071.50422.220.068707.8550.09332.50.09861.15829480.04710.0551.4161.6400.0637819.99590.00172667620.0470927320.04716304770.0470943936C30.0544.0972.20531.630.070616.3666.01416.250.15240.25931290.07040.0183.1040.8050.0981402.41620.00771269020.07031043190.06958565510.0702931055I-C40.0358.1231.74435.120.050529.1734.98470.780.18480.09339290.04650.0042.7010.2520.0769126.13790.02141490940.04640922380.04576733790.0463938255N-C40.0258.1231.16236.440.032550.7765.65491.080.2010.06483380.03150.0021.8330.1190.050359.40470.03084809650.03148192390.03102521970.0314709605I-C50.0172.150.72238.980.019490.4829.1542.120.22230.02509790.01620.0001.1660.0290.029914.63140.07968787130.01613454430.01588468450.0161285405N-C50.0172.150.72239.380.018488.6845.7556.920.25390.01843480.01620.0001.1710.0220.029710.79240.10849067860.01620247760.01594883080.0161963818C60.0186.1770.86241.420.021436.9913.7615.720.30070.00582070.01640.0001.4100.0080.03404.10300.34360207640.01633266190.01607169620.0163263882C7+0.4252100.80052.601.916203.031338.591042.650.6200.00000080.65680.000165.5170.0003.14690.06302627.95290370770.65573738590.64516098940.65548308771.000116.4572.5531.00140.998179.9317.60013.61568800.039326291.0000.9890.999994272PSIAPSIA00Determinacion de las propiedades criticas C7+(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)w00nay1338.59203.031042.650.6200.10036542660.917845154Metodo Rowes17.862.340.431429.18220.490.04708571190.0545391341Metodo de Standing0.07038374080.01825141130.04647440410.0043403783a16124.304918067.618StandingRzasas0.03152833490.0020441025Presion de Convergenciaa2-2753.2538-8122.51210920186320.01615996330.0004055815a3415.420491225.5530.01622828670.000299164611170.70.01635922530.0000952219Volumen= (Mol)0.6568141290.0000004999Densidad=(PMo/Vo) (lb/pc)49.76249.7636218602Den.sc48.80101.00139922260.9978206482Vg liberado=(379,4*Nv) pc/mol148.353Vo ocupado=(NL*MW)/Den. Pet pc/mol2.204Sgo=(Den.pet/62,4)0.805SGg=PMYI/28,9640.6086API =( 141,5/Sgo )-131,5467GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)378.298Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.61011Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,248143.2289

op sep2Optimizacion de la Presion de Separacion segunda etapaPresion (psi)250Temp(oF)72Separacion FlashVapor=0.065Liquido=0.935Corr. WilsonYi=Xi*KComponenteComposicionPeso molecularX*PMDensidad iVol = PM/Dens.Pcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.XiYiX*PMY*PMVol = PM/Dens.lb/pcpcpsioRoRwkpcCO20.0000440.00051.260.0001071547.9350.750.2253.519370.000000.000000.0000.0000.0000N20.000028.0130.00040.880.000493227.6139.550.0448.161580.000000.000000.0000.0000.0000C10.100416.0431.61018.720.086667.8343.37201.270.010418.290070.047260.864320.75813.8660.0405C20.047130.071.41622.220.064707.8550.09332.50.09862.316590.043370.100481.3043.0210.0587C30.070444.0973.10431.630.098616.3666.01416.250.15240.518630.072660.037683.2041.6620.1013I-C40.046558.1232.70135.120.077529.1734.98470.780.18480.186790.049070.009172.8520.5330.0812N-C40.031558.1231.83336.440.050550.7765.65491.080.2010.129670.033420.004331.9420.2520.0533I-C50.016272.151.16638.980.030490.4829.1542.120.22230.050200.017220.000861.2430.0620.0319N-C50.016272.151.17139.380.030488.6845.7556.920.25390.036870.017310.000641.2490.0460.0317C60.016486.1771.41041.420.034436.9913.7615.720.30070.011640.017480.000201.5070.0180.0364C7+0.6568252165.51752.603.147203.031338.591042.650.6200.0000020.702470.00000177.0240.0003.36571.0014179.9273.6161.00031.018191194Determinacion de las propiedades criticas C7+(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)wMetodo Rowesnay1338.59203.031042.650.620Metodo de Standing17.862.340.431429.18220.49a16124.304918067.618StandingRzasasPresion de Convergenciaa2-2753.2538-8122.512109208789a3415.420491225.55311170.7Densidad=(PMo/Vo) (lb/pc)50.28Den.sc50.31Vg liberado=(379,4*Nv) pc/mol24.66Vo ocupado=(NL*MW)/Den. Pet pc/mol3.55Sgo=(Den.pet/62,4)0.81SGg=PMYI/28,9640.672API =( 141,5/Sgo )-131,544GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)39Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.070Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,24868.3

op sep3Optimizacion de la Presion de Separacion segunda etapaPresion (psi)14.7Temp(oF)60Separacion FlashVapor=0.156Liquido=0.844Corr. WilsonYi=Xi*KComponenteComposicionPeso molecularX*PMDensidad iVol = PM/Dens.Pcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.XiYiX*PMY*PMVol = PM/Dens.lb/pcpcpsioRoRwkpcCO20.0000440.00051.260.0001071547.9350.750.22551.190410.00000.0000.0000.0000.0000N20.000028.0130.00040.880.000493227.6139.550.04775.135370.00000.0000.0000.0000.0000C10.047316.0430.75818.720.040667.8343.37201.270.0104286.906310.00100.2970.0174.7700.0009C20.043430.071.30422.220.059707.8550.09332.50.098634.224380.00700.2400.2117.2190.0095C30.072744.0973.20431.630.101616.3666.01416.250.15247.376200.03640.2691.60611.8480.0508I-C40.049158.1232.85235.120.081529.1734.98470.780.18482.593420.03930.1022.2845.9240.0650N-C40.033458.1231.94236.440.053550.7765.65491.080.2011.780040.02980.0531.7323.0820.0475I-C50.017272.151.24338.980.032490.4829.1542.120.22230.674170.01810.0121.3090.8830.0336N-C50.017372.151.24939.380.032488.6845.7556.920.25390.489790.01880.0091.3570.6650.0345C60.017586.1771.50741.420.036436.9913.7615.720.30070.150110.02020.0031.7370.2610.0419C7+0.7025252177.02452.603.366203.031338.591042.650.6200.0000160.83230.000209.7430.0033.98771.0003191.0833.8011.00300.986220354Determinacion de las propiedades criticas C7+(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)wMetodo Rowesnay1338.59203.031042.650.620Metodo de Standing17.862.340.431429.18220.49PresionGORAPIBopsiPC/BBLa16124.304921681.142StandingRzasasPresion de Convergenciaa2-2753.2538-9747.0141092011023500378461.610a3415.420491470.66325039441.07013404.814.792401.198Densidad (lb/pc)50.280.8057132339Densidad=(PMo/Vo) (lb/pc)51.50Den.sc52.06Vg liberado=(379,4*Nv) pc/mol59.19Vo ocupado=(NL*MW)/Den. Pet pc/mol3.61Sgo=(Den.pet/62,4)0.83SGg=PMYI/28,9641.196API =( 141,5/Sgo )-131,540GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)92Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.198Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,24810.7

op sep3

GORAPIBoPresion de SeparacionGOR, API, BoEfecto de la Presion de Separacion con GOR, API, Bo

Hoja3

OP SEP CORREGIDOOptimizacion de la Presion de SeparacionPresion (psi)500Etapa de Sep.Presion Sep.Temp. o FTemp(oF)72150072225072314.760Separacion FlashSGc7+0.8429Vapor=0.391V0.390.380.389763347PMc7252Liquido=0.609L0.610.620.610236653Corr. WilsonYi=Xi*K1ComponenteComposicionPeso molecularZ*PMDensidad iVol = PM/Dens.Pcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.XiYiX*PMY*PMVol = PM/Dens.PB(PSIA)PD(PSIA)lb/pcpcpsioRoRwkpcCO20440.00051.260.0001071547.9350.750.2251.75968420.00000.0000.0000.0000.00000.00000.0011365676000N2028.0130.00040.880.000493227.6139.550.0424.08079080.00000.0000.0000.0000.00000.00000.0000830538000C10.4216.0436.73818.720.360667.8343.37201.270.01049.14503320.10040.9181.61014.7250.08607362.49490.00021869790.10056115680.10256128240.1006075888C20.0530.071.50422.220.068707.8550.09332.50.09861.15829480.04710.0551.4161.6400.0637819.99590.00172667620.0470927320.04716304770.0470943936C30.0544.0972.20531.630.070616.3666.01416.250.15240.25931290.07040.0183.1040.8050.0981402.41620.00771269020.07031043190.06958565510.0702931055I-C40.0358.1231.74435.120.050529.1734.98470.780.18480.09339290.04650.0042.7010.2520.0769126.13790.02141490940.04640922380.04576733790.0463938255N-C40.0258.1231.16236.440.032550.7765.65491.080.2010.06483380.03150.0021.8330.1190.050359.40470.03084809650.03148192390.03102521970.0314709605I-C50.0172.150.72238.980.019490.4829.1542.120.22230.02509790.01620.0001.1660.0290.029914.63140.07968787130.01613454430.01588468450.0161285405N-C50.0172.150.72239.380.018488.6845.7556.920.25390.01843480.01620.0001.1710.0220.029710.79240.10849067860.01620247760.01594883080.0161963818C60.0186.1770.86241.420.021436.9913.7615.720.30070.00582070.01640.0001.4100.0080.03404.10300.34360207640.01633266190.01607169620.0163263882C7+0.4252100.80052.601.916203.031338.591042.650.6200.00000080.65680.000165.5170.0003.14690.06302627.95290370770.65573738590.64516098940.65548308771.000116.4572.5531.00140.998179.9317.60013.61568800.039326291.0000.9890.999994272PSIAPSIA00Determinacion de las propiedades criticas C7+(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)w00nay1338.59203.031042.650.6200.10036542660.917845154Metodo Rowes17.862.340.431429.18220.490.04708571190.0545391341Metodo de Standing0.07038374080.01825141130.04647440410.0043403783a16124.304918067.618StandingRzasas0.03152833490.0020441025Presion de Convergenciaa2-2753.2538-8122.51210920186320.01615996330.0004055815a3415.420491225.5530.01622828670.000299164611170.70.01635922530.00009522190.6568141290.0000004999Densidad=(PMo/Vo) (lb/pc)49.76249.7636218602Den.sc48.80101.00139922260.9978206482Vg liberado=(379,4*Nv) pc/mol148.353Vo ocupado=(NL*MW)/Den. Pet pc/mol2.204Sgo=(Den.pet/62,4)0.805SGg=PMYI/28,9640.6086API =( 141,5/Sgo )-131,5467GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)378.298Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.61011Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,248143.2289

PRACTICOOPTIMIZACIN DE LA PRESION DE SEPARACIN 1ERAEtapa de Sep.Presion Sep.Temp. o F150072225072314.760INTERPOLADOSGc7+0.8429NV0.390.38980.38PMc7252NL0.610.61020.62ComponenteComposicionPeso molecularZi*PMDensidad iPcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)XiYiXi*PMYi*PMVOL=(mol)Zimolr (i)psiaRR(adim)k(adim)(xi*PM)/dens(i)CO20.00440.00051.261071547.9350.750.2251.75970.00000.00000.00000.00000.00000.00000.00000.0000N20.0028.0130.00040.88493227.6139.550.0424.08080.00000.00000.00000.00000.00000.00000.00000.0000C10.4216.0436.73818.72667.8343.37201.270.01049.14500.10060.10060.10260.10060.92011.614014.76050.0862C20.0530.071.50422.22707.8550.09332.50.09861.15830.04710.04710.04720.04710.05451.41611.64030.0637C30.0544.0972.20531.63616.3666.01416.250.15240.25930.07030.07030.06960.07030.01823.09970.80380.0980I-C40.0358.1231.74435.12529.1734.98470.780.18480.09340.04640.04640.04580.04640.00432.69650.25180.0768N-C40.0258.1231.16236.44550.7765.65491.080.2010.06480.03150.03150.03100.03150.00201.82920.11860.0502I-C50.0172.150.72238.98490.4829.1542.120.22230.02510.01610.01610.01590.01610.00041.16370.02920.0299N-C50.0172.150.72239.38488.6845.7556.920.25390.01840.01620.01620.01590.01620.00031.16860.02150.0297C60.0186.1770.86241.42436.9913.7615.720.30070.00580.01630.01630.01610.01630.00011.40700.00820.0340C7+0.40252.00100.80052.614203.011338.701042.770.61970.0000010.65570.65550.64520.65550.0000165.18170.00013.139511.00031.00000.98921.00001.0000179.576617.63413.6079DETERMINACIN DE LAS PROPIEDADES CRITICASnay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)(w)c7+Metodo Rowes17.85712.33700.43421338.70203.011042.770.6197Volumen= (Mol)3.60791Densidad=(PMo/Vo) (lb/pc)49.772Vg liberado=(379,4*Nv) pc/mol147.883Vo ocupado=(NL*MW)/Den. Pet pc/mol2.204Sgo=(Den.pet/62,4)0.805SGg=PMYI/28,9640.616API =( 141,5/Sgo )-131,545.9567GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)3778Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,2048143.639Den.sc48.78710Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.60611OPTIMIZACIN DE LA PRESION DE SEPARACIN 2DAEtapa de Sep.Presion Sep.Temp. o F125072225072314.760INTERPOLADOSGc7+0.8429NV0.10.07110.09PMc7252NL0.90.92890.91ComponenteComposicionPeso molecularZi*PMDensidad iPcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)XiYiXi*PMYi*PMVOL=(mol)Zimolr (i)psiaRR(adim)k(adim)(xi*PM)/dens(i)CO20.00440.00051.261071547.9350.750.2253.51940.00000.00000.00000.00000.00000.00000.00000.0000N20.0028.0130.00040.88493227.6139.550.0448.16160.00000.00000.00000.00000.00000.00000.00000.0000C10.1016.0431.61418.72667.8343.37201.270.010418.29010.03690.04510.03940.04510.82560.724213.24590.0387C20.0530.071.41622.22707.8550.09332.50.09862.31660.04160.04310.04210.04310.09981.29502.99990.0583C30.0744.0973.10031.63616.3666.01416.250.15240.51860.07380.07280.07350.07280.03773.20951.66450.1015I-C40.0558.1232.69735.12529.1734.98470.780.18480.18680.05050.04920.05010.04920.00922.86190.53460.0815N-C40.0358.1231.82936.44550.7765.65491.080.2010.12970.03450.03350.03410.03350.00431.94980.25280.0535I-C50.0272.151.16438.98490.4829.1542.120.22230.05020.01780.01730.01760.01730.00091.24790.06260.0320N-C50.0272.151.16939.38488.6845.7556.920.25390.03690.01790.01740.01770.01740.00061.25440.04630.0319C60.0286.1771.40741.42436.9913.7615.720.30070.01160.01810.01760.01790.01760.00021.51320.01760.0365C7+0.66252.00165.18252.614203.011338.701042.770.61970.000001520.72830.70560.72030.70560.0000011177.81810.00033.37971.001.01951.00161.01271.00160.9784191.874118.82453.8135DETERMINACIN DE LAS PROPIEDADES CRITICASnay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)(w)c7+Metodo Rowes17.85712.33700.43421338.70203.011042.770.6197Volumen= (Mol)3.81351Densidad=(PMo/Vo) (lb/pc)50.312Vg liberado=(379,4*Nv) pc/mol26.963Vo ocupado=(NL*MW)/Den. Pet pc/mol3.544Sgo=(Den.pet/62,4)0.815SGg=PMYI/28,9640.656API =( 141,5/Sgo )-131,544.0467GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)438Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,204865.919Den.sc50.34110Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.07711OPTIMIZACIN DE LA PRESION DE SEPARACIN 3RAEtapa de Sep.Presion Sep.Temp. o F114.760225072314.760INTERPOLADOSGc7+0.8429NV0.160.14690.15PMc7252NL0.840.85310.85ComponenteComposicionPeso molecularZi*PMDensidad iPcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)XiYiXi*PMYi*PMVOL=(mol)Zimolr (i)psiaRR(adim)k(adim)(xi*PM)/dens(i)CO20.00440.00051.261071547.9350.750.22551.19040.00000.00000.00000.00000.00000.00000.00000.0000N20.0028.0130.00040.88493227.6139.550.04775.13540.00000.00000.00000.00000.00000.00000.00000.0000C10.0516.0430.72418.72667.8343.37201.270.0104286.90630.00100.00110.00100.00110.30130.01684.83340.0009C20.0430.071.29522.22707.8550.09332.50.098634.22440.00680.00730.00720.00730.25070.22037.53810.0099C30.0744.0973.21031.63616.3666.01416.250.15247.37620.03600.03760.03720.03760.27721.657412.22560.0524I-C40.0558.1232.86235.12529.1734.98470.780.18482.59340.03920.03990.03970.03990.10352.31926.01470.0660N-C40.0358.1231.95036.44550.7765.65491.080.2011.78000.02980.03010.03000.03010.05361.74943.11400.0480I-C50.0272.151.24838.98490.4829.1542.120.22230.67420.01820.01820.01820.01820.01221.31060.88360.0336N-C50.0272.151.25439.38488.6845.7556.920.25390.48980.01890.01880.01880.01880.00921.35600.66420.0344C60.0286.1771.51341.42436.9913.7615.720.30070.15010.02030.02010.02010.02010.00301.72910.25950.0417C7+0.71252.00177.81852.614203.011338.701042.770.61970.00000.84000.82710.83010.82710.0000208.42770.00323.96151.001.01041.00011.00251.00011.0107218.786535.53644.2485DETERMINACIN DE LAS PROPIEDADES CRITICASnay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)(w)c7+Metodo Rowes17.85712.33700.43421338.70203.011042.770.6197Volumen= (Mol)4.24851Densidad=(PMo/Vo) (lb/pc)51.502Vg liberado=(379,4*Nv) pc/mol55.723Vo ocupado=(NL*MW)/Den. Pet pc/mol3.624Sgo=(Den.pet/62,4)0.835SGg=PMYI/28,9641.236API =( 141,5/Sgo )-131,540.0137GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)868Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,204810.969Den.sc52.04410Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.18511

PRIMER PARCIALOPTIMIZACIN DE LA PRIMERA ETAPA DE SEPARACINEtapa de Sep.Presion Sep.Temp. o F1600100230080314.760INTERPOLADOSGc7+0.87NV0.460.45710.45PMc7270NL0.540.54290.55ComponenteComposicionPeso molecularZi*PMDensidad iPcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)XiYiXi*PMYi*PMVOL=(mol)Zimolr (i)psiaRR(adim)k(adim)(xi*PM)/dens(i)CO20.00440.00051.261071547.9350.750.2252.05760.00000.00000.00000.00000.00000.00000.00000.0000N20.0028.0130.00040.88493227.6139.550.0422.61370.00000.00000.00000.00000.00000.00000.00000.0000C10.4716.0437.54018.72667.8343.37201.270.01049.07920.09970.10020.10140.10020.90931.606814.58830.0858C20.0530.071.50422.22707.8550.09332.50.09861.30950.04380.04380.04390.04380.05741.31721.72480.0593C30.0544.0972.20531.63616.3666.01416.250.15240.31830.07280.07260.07210.07260.02313.20271.01950.1013I-C40.0358.1231.74435.12529.1734.98470.780.18480.12080.05040.05020.04960.05020.00612.91520.35210.0830N-C40.0258.1231.16236.44550.7765.65491.080.2010.08590.03450.03440.03400.03440.00301.99660.17160.0548I-C50.0172.150.72238.98490.4829.1542.120.22230.03490.01800.01790.01770.01790.00061.29100.04500.0331N-C50.0172.150.72239.38488.6845.7556.920.25390.02620.01810.01800.01780.01800.00051.30020.03410.0330C60.0186.1770.86241.42436.9913.7615.720.30070.00880.01840.01830.01810.01830.00021.57550.01390.0380C7+0.35270.0094.50054.305191.251364.261072.770.62480.00000115130.64810.64460.63640.64460.000000742174.05520.00023.205111.00380.99990.99090.99991.0001189.260417.94953.6935DETERMINACIN DE LAS PROPIEDADES CRITICASnay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)(w)c7+Metodo Rowes19.14292.30770.41651364.26191.251072.770.6248Volumen= (Mol)3.69351Densidad=(PMo/Vo) (lb/pc)51.242Vg liberado=(379,4*Nv) pc/mol173.413Vo ocupado=(NL*MW)/Den. Pet pc/mol2.014Sgo=(Den.pet/62,4)0.82095SGg=PMYI/28,9640.626API =( 141,5/Sgo )-131,540.867731.143678160940.871787063GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)4868Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,2048140.859Den.sc49.75810Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.78911OPTIMIZACIN DE LA PRESION DE SEPARACIN 2DAEtapa de Sep.Presion Sep.Temp. o F125072225072314.760INTERPOLADOSGc7+0.8429NV0.10.07020.09PMc7252NL0.90.92980.91ComponenteComposicionPeso molecularZi*PMDensidad iPcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)XiYiXi*PMYi*PMVOL=(mol)Zimolr (i)psiaRR(adim)k(adim)(xi*PM)/dens(i)CO20.00440.00051.261071547.9350.750.2253.51940.00000.00000.00000.00000.00000.00000.00000.0000N20.0028.0130.00040.88493227.6139.550.0448.16160.00000.00000.00000.00000.00000.00000.00000.0000C10.1016.0431.60718.72667.8343.37201.270.010418.29010.03670.04520.03920.04520.82730.725713.27250.0388C20.0430.071.31722.22707.8550.09332.50.09862.31660.03870.04010.03920.04010.09291.20572.79310.0543C30.0744.0973.20331.63616.3666.01416.250.15240.51860.07630.07520.07590.07520.03903.31481.71910.1048I-C40.0558.1232.91535.12529.1734.98470.780.18480.18680.05460.05320.05410.05320.00993.09180.57750.0880N-C40.0358.1231.99736.44550.7765.65491.080.2010.12970.03760.03660.03730.03660.00472.12660.27580.0584I-C50.0272.151.29138.98490.4829.1542.120.22230.05020.01980.01920.01960.01920.00101.38330.06940.0355N-C50.0272.151.30039.38488.6845.7556.920.25390.03690.01990.01930.01970.01930.00071.39450.05140.0354C60.0286.1771.57641.42436.9913.7615.720.30070.01160.02030.01960.02010.01960.00021.69300.01970.0409C7+0.64252.00162.45252.614203.011338.701042.770.61970.00000.71630.69330.70840.69330.0000174.72140.00033.32081.001.02021.00181.01341.00180.9758189.656718.77883.7768DETERMINACIN DE LAS PROPIEDADES CRITICASnay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)(w)c7+Metodo Rowes17.85712.33700.43421338.70203.011042.770.6197Volumen= (Mol)3.77681Densidad=(PMo/Vo) (lb/pc)50.222Vg liberado=(379,4*Nv) pc/mol26.643Vo ocupado=(NL*MW)/Den. Pet pc/mol3.514Sgo=(Den.pet/62,4)0.805SGg=PMYI/28,9640.656API =( 141,5/Sgo )-131,544.3897GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)438Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,204866.549Den.sc50.26810Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.07711OPTIMIZACIN DE LA PRESION DE SEPARACIN 3RAEtapa de Sep.Presion Sep.Temp. o F114.760225072314.760INTERPOLADOSGc7+0.8429NV0.160.14850.15PMc7252NL0.840.85150.85ComponenteComposicionPeso molecularZi*PMDensidad iPcrit.Temp. Crit.Temp. Eboll.Factor Acent.Const. Equil.Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)Xi=zi/(NL+K*NV)XiYiXi*PMYi*PMVOL=(mol)Zimolr (i)psiaRR(adim)k(adim)(xi*PM)/dens(i)CO20.00440.00051.261071547.9350.750.22551.19040.00000.00000.00000.00000.00000.00000.00000.0000N20.0028.0130.00040.88493227.6139.550.04775.13540.00000.00000.00000.00000.00000.00000.00000.0000C10.0516.0430.72618.72667.8343.37201.270.0104286.90630.00100.00100.00100.00100.29860.01674.79000.0009C20.0430.071.20622.22707.8550.09332.50.098634.22440.00630.00680.00670.00680.23120.20326.95300.0091C30.0844.0973.31531.63616.3666.01416.250.15247.37620.03720.03860.03840.03860.28481.702512.55780.0538I-C40.0558.1233.09235.12529.1734.98470.780.18482.59340.04240.04300.04290.04300.11162.50016.48380.0712N-C40.0458.1232.12736.44550.7765.65491.080.2011.78000.03250.03280.03280.03280.05841.90583.39240.0523I-C50.0272.151.38338.98490.4829.1542.120.22230.67420.02020.02010.02020.02010.01361.45360.98000.0373N-C50.0272.151.39539.38488.6845.7556.920.25390.48980.02100.02090.02090.02090.01021.50880.73900.0383C60.0286.1771.69341.42436.9913.7615.720.30070.15010.02270.02250.02250.02250.00341.93760.29090.0468C7+0.69252.00174.72152.614203.011338.701042.770.61970.00000.82540.81430.81570.81430.0000205.19880.00323.90011.001.00891.00001.00111.00001.0117216.427136.19004.2098DETERMINACIN DE LAS PROPIEDADES CRITICASnay(Tc) c7+ ( o R )(Pc)c7+ (psi)(Tb)c7+ (o R)(w)c7+Metodo Rowes17.85712.33700.43421338.70203.011042.770.6197Volumen= (Mol)4.20981Densidad=(PMo/Vo) (lb/pc)51.412Vg liberado=(379,4*Nv) pc/mol56.353Vo ocupado=(NL*MW)/Den. Pet pc/mol3.584Sgo=(Den.pet/62,4)0.825SGg=PMYI/28,9641.256API =( 141,5/Sgo )-131,540.3047GOR=(5,615*379,4*Nv)/(NL*PM/Den. Pet)888Rs=SGg*((P/18,2)+1,4)*10^(0,0125*API-0,00091(T-460))^1,204811.289Den.sc51.99010Bo = (Pmo * Den pet)/(Den pet*NL*PM)1.18811