Datos La VertienteCOMPOSICION DEL GAS NATURAL, CAMPO: "LA VERTIENTE"

ItemComp.% molarziPc (psia)Tc ( F)Tc ( R)wiMiMa=yi*Mi1N22.210.0221493-232.7227.970.037228.0130.61908732CO20.060.0006107187.87548.540.266744.010.0264063C186.920.8692667.8-116.68343.990.012616.04313.94457564C26.580.0658707.890.1550.770.097830.071.9786065C32.860.0286616.3206.01666.680.154144.0971.26117426i-C40.350.0035529.1274.96735.630.18458.1240.2034347n-C40.660.0066550.7305.62766.290.201558.1240.38361848i-C50.150.0015490.4369.03829.700.228672.1510.10822659n-C50.130.0013488.6385.6846.270.252472.1510.093796310C60.060.0006436.9453.6914.270.299886.1780.051706811C7+0.020.0002320.3512.71139.400.5069100.2050.020041Total.-100118.6907

D. Separ. Horiz.Diseno de un Separador Horizontal

DATOSUnidadesFlujo de Gas (MMSCFD)15.09Temperatura( R)520.00Presion (psia)900.00Factor de Compresibilidad0.5076Diametro de la Particula Liquida micrasDensidad fase gaslb/ft^37.344Densidad Fase Liquidalb/ft^321.40Viscosidad Fase GascP1.298E-02Flujo de Liquidobpd2309

D. Separ. Vert.e) Calculo del Diseno de un Separador Vertical y Horizontal IsotermicosDiseno de un Separador Vertical Isotermico

Fase Controlante: Fase Gas

VariablesValores obtenidos con HYSYSUnidadesFlujo de Gas 15.09(MMSCFD)Temperatura390( R)Presion 892(psia)Factor de Compresibilidad0.5076Diametro de la Particula Liquida 100micrasDensidad fase gas7.344lb/ft^3Densidad Fase Liquida21.40lb/ft^3Sg=0.3428API=281Viscosidad Fase Gas1.298E-02cPFlujo de Liquido2309bpd

Sup. CDCalcular Vt (ft/s)Calcular ReCalcular CDEcuaciones de Calculo de Cd, Vt y Re0.34000.282378.27550.98570.98570.165845.97211.30451.30450.144139.96141.41511.41510.138438.36761.44991.44990.136737.90561.46041.46040.136237.76821.46361.46360.136137.72701.46461.46460.136037.71471.46491.46490.136037.71101.46491.46490.136037.70991.46501.46500.136037.70951.4650

Calculo del diametro (d)DiametroValorUnidadd^2=1475.53d=38.4126pulgCalculos Fase Controlante - Fase LiquidaSuponer Tr (min)Suponer d (in)Calcular d^2*hCalcular h (in)Calcular Lss (ft)Calcular Lss/d33657725.0044.54110.0453.34834257725.0032.7249.5602.73234857725.0025.0549.4212.35523638483.3329.6948.8082.93624238483.3321.8168.6512.47224838483.3316.7038.7252.18113619241.6714.8477.5712.524Resumen de Calculo14219241.6710.9087.7422.212d=30pulg14819241.678.3518.0292.007Lss=8pies32457725.00100.21714.6857.342tr=1min33057725.0064.13911.6784.67122438483.3366.81111.9015.95023038483.3342.7599.8973.95912419241.6733.4069.1174.55913019241.6721.3808.1153.246

Diseno de un Separador Horizontal IsotermicoVariablesValores obtenidos con HYSYSUnidadesFlujo de Gas 15.09(MMSCFD)Temperatura389.69( R)Presion 892(psia)Factor de Compresibilidad0.5076Diametro de la Particula Liquida 100micrasDensidad fase gas7.344lb/ft^3Densidad Fase Liquida21.40lb/ft^3Sg=0.3428API =281Viscosidad Fase Gas1.298E-02cPFlujo de Liquido2309bpdSup. CDCalcular Vt (ft/s)Calcular ReCalcular CDEcuaciones de Calculo de Cd, Vt y Re0.34000.282378.27550.98570.98570.165845.97211.30451.30450.144139.96141.41511.41510.138438.36761.44991.44990.136737.90561.46041.46040.136237.76821.46361.46360.136137.72701.46461.46460.136037.71471.46491.46490.136037.71101.46491.46490.136037.70991.46501.46500.136037.70951.4650

Fase Controlante: Fase Gas

DiametroValorUnidad(dLeff)^2=122.96d*Leff =11.08876pulgCalculo de la Longitud de costura a costura "Lss"

Suponer d (pulg)Calcular Leff (pies)Calcular Lss (pies)Calcular Lss/d12.750.8701.9321.8193