DatosDATOS DE LABORATORIOARREGLO EN PARALELOCada de presin15psiFlujo de AguaFlujo de VaporTemp pared exterior del tubo interiorm3/sT6(in) CT7(out) Cm3/sT5(in) CT1(out) CTw4(in) CTw3(inter) CTw2(out) C0.0001322.9062.900.0000132128.00126.40127.4127.71260.0001722.8056.600.0000130127.00124.80126.4127.8124.50.0002322.9049.100.0000142128.90126.30128.1127.7124.8Cada de presin20psiFlujo de AguaFlujo de VaporTemp pared exterior del tubo interiorm3/sT6(in) CT7(out) Cm3/sT5(in) CT1(out) CTw4(in) CTw3(inter) CTw2(out) C0.0001322.9066.500.0000133132.60130.80132.00131.50128.400.0001722.9058.800.0000147133.30132.50132.70132.10129.900.0002322.9050.800.0000143132.60131.00131.20130.50128.60Cada de presin30psiFlujo de AguaFlujo de VaporTemp pared exterior del tubo interiorm3/sT6(in) CT7(out) Cm3/sT5(in) CT1(out) CTw4(in) CTw3(inter) CTw2(out) C0.0001322.968.20.0000227139.2137.6138.5138131.20.0001722.960.10.0000245139138.2138.7137.9127.20.0002322.952.30.0000307138.8138.81138.3137.3127.9ARREGLO EN CONTRACORRIENTECada de presin15psiFlujo de AguaFlujo de VaporTemp pared exterior del tubo interiorm3/sT6(in) CT7(out) Cm3/sT1(in) CT5(out) CTw2(in) CTw3(inter) CTw4(out) C0.0001322.4055.500.0000158121.10120.80120.20119.30118.400.0001722.6050.700.0000085122.80121.00120.60120.20118.800.0002322.6045.100.0000102124.50121.30120.20119.80118.40Cada de presin20psiFlujo de AguaFlujo de VaporTemp pared exterior del tubo interiorm3/sT6(in) CT7(out) Cm3/sT1(in) CT5(out) CTw2(in) CTw3(inter) CTw4(out) C0.0001322.7058.800.0000117127.60126.20125.40125.20123.200.0001722.6051.200.0000113127.80125.10124.40124.20123.500.0002322.7046.100.0000115128.20126.40125.20126.20123.20Cada de presin30psiFlujo de AguaFlujo de VaporTemp pared exterior del tubo interiorm3/sT6(in) CT7(out) Cm3/sT1(in) CT5(out) CTw2(in) CTw3(inter) CTw4(out) C0.0001323.162.60.0000203136.2133.9133.1133.9134.40.0001723.154.90.0000228134.4133.9132.9133.9126.50.0002323.147.70.0000288138.6133.4133.2133.4126.7

B.TermicoBALANCE TERMICO ESTABLECIENDO EL % DE ERROR POR PERDIDAS AL AMBIENTEARREGLO EN PARALELOARREGLO EN CONTRACORRIENTEPRESIN = 15 psiPRESIN = 15 psiFLUJO DE AGUAFLUJO DE AGUACAUDALT6 (C)T7 (C)T prom.DensidadW aguaCpQ aguaCAUDALT6 (C)T7 (C)T prom.DensidadW aguaCpQ aguaLPMinoutKKmol/m^3Kmol/sJ/Kmol.KJ/sLPMinoutKKmol/m^3Kmol/sJ/Kmol.KJ/s822.9062.90315.9054.970.00732975267.1822065.99822.4055.50311.9555.030.00733775277.2918281.781022.8056.60312.7055.020.00917075274.4723329.871022.6050.70309.6555.060.00917775288.6619415.251422.9049.10309.0055.070.01285075292.6425349.251422.6045.10306.8555.100.01285875308.2721786.50FLUJO DE CONDENSADOFLUJO DE CONDENSADOCAUDALT5 (C)T1 (C)T prom.DensidadW aguaQ cond.CAUDALT1 (C)T5 (C)T prom.DensidadW aguaQ cond.LPMinoutKKmol/m^3Kmol/sJ/KmolJ/sLPMinoutKKmol/m^3Kmol/sJ/KmolJ/s0.79128.00126.40400.2053.540.00070539461451.9427816.180.95121.10120.80393.9553.660.00085039783683.7833798.040.78127.00124.80398.9053.560.00069639529162.1327524.050.51122.80121.00394.9053.640.00045639735236.7618116.050.85128.90126.30400.6053.530.00075839440544.5329908.640.61124.50121.30395.9053.620.00054539684035.6421632.65% PERDIDA AL AMBIENTE% PERDIDA AL AMBIENTEQ aguaQ cond.Q perdido% PERDIDAQ aguaQ cond.Q perdido% PERDIDAJ/sJ/sJ/sJ/sJ/sJ/s22065.9927816.185750.1920.6718281.7833798.0415516.2645.9123329.8727524.054194.1815.2419415.2518116.051299.207.1725349.2529908.644559.3915.2421786.5021632.65153.850.71PRESIN = 20 psiPRESIN = 20 psiFLUJO DE AGUAFLUJO DE AGUACAUDALT6 (C)T7 (C)T prom.DensidadW aguaCpQ aguaCAUDALT6 (C)T7 (C)T prom.DensidadW aguaCpQ aguaLPMinoutKKmol/m^3Kmol/sJ/Kmol.KJ/sLPMinoutKKmol/m^3Kmol/sJ/Kmol.KJ/s822.9066.50317.7054.940.00732675266.3324039.74822.7058.80313.7555.000.00733475271.2419927.361022.9058.80313.8555.000.00916775270.9824770.441022.6051.20309.9055.060.00917775287.2219759.011422.9050.80309.8555.060.01284775287.5126986.021422.7046.10307.4055.100.01285675303.9122653.31FLUJO DE CONDENSADOFLUJO DE CONDENSADOCAUDALT5 (C)T1 (C)T prom.DensidadW aguaQ cond.CAUDALT1 (C)T5 (C)T prom.DensidadW aguaQ cond.LPMinoutKKmol/m^3Kmol/sJ/KmolJ/sLPMinoutKKmol/m^3Kmol/sJ/KmolJ/s0.80132.60130.80404.7053.450.00071339224224.3427953.260.70127.60126.20399.9053.540.00062539477109.7524659.690.88133.30132.50405.9053.430.00078439160206.5830684.890.68127.80125.10399.4553.550.00060739500560.0023973.230.86132.60131.00404.8053.450.00076639218901.8230044.580.69128.20126.40400.3053.530.00061639456228.3424291.06% PERDIDA AL AMBIENTE% PERDIDA AL AMBIENTEQ aguaQ cond.Q perdido% PERDIDAQ aguaQ cond.Q perdido% PERDIDAJ/sJ/sJ/sJ/sJ/sJ/s24039.7427953.263913.5314.0019927.3624659.694732.3319.1924770.4430684.895914.4519.2719759.0123973.234214.2317.5826986.0230044.583058.5610.1822653.3124291.061637.756.74PRESIN = 30 psiPRESIN = 30 psiFLUJO DE AGUAFLUJO DE AGUACAUDALT6 (C)T7 (C)T prom.DensidadW aguaCpQ aguaCAUDALT6 (C)T7 (C)T prom.DensidadW aguaCpQ aguaLPMinoutKKmol/m^3Kmol/sJ/Kmol.KJ/sLPMinoutKKmol/m^3Kmol/sJ/Kmol.KJ/s822.968.2318.5554.930.00732475266.7124971.32823.162.6315.8554.970.00732975267.2421790.481022.960.1314.5054.990.00916575269.4425662.331023.154.9312.0055.030.00917175277.0921954.351422.952.3310.6055.050.01284575283.4628429.581423.147.7308.4055.080.01285275296.6223806.31FLUJO DE CONDENSADOFLUJO DE CONDENSADOCAUDALT5 (C)T1 (C)T prom.DensidadW aguaQ cond.CAUDALT1 (C)T5 (C)T prom.DensidadW aguaQ cond.LPMinoutKKmol/m^3Kmol/sJ/KmolJ/sLPMinoutKKmol/m^3Kmol/sJ/KmolJ/s1.362139.2137.6411.4053.320.00121038862614.6147034.721.217136.2133.9408.0553.380.00108339044697.4942277.071.47139138.2411.6053.310.00130638851661.9350746.221.367134.4133.9407.1553.400.00121739093177.4147562.691.842138.8138.81411.8153.310.00163738840425.7763564.841.73138.6133.4409.0053.360.00153938993324.0959997.81% PERDIDA AL AMBIENTE% PERDIDA AL AMBIENTEQ aguaQ cond.Q perdido% PERDIDAQ aguaQ cond.Q perdido% PERDIDAJ/sJ/sJ/sJ/sJ/sJ/s24971.3247034.7222063.4046.9121790.4842277.0720486.5948.4625662.3350746.2225083.8949.4321954.3547562.6925608.3453.8428429.5863564.8435135.2555.2723806.3159997.8136191.5060.32

UoDETERMINACION DEL COEFICIENTE GLOBAL EXPERIMENTAL UoDETERMINACION DEL COEFICIENTE GLOBAL EXPERIMENTAL UoARREGLO EN PARALELOARREGLO EN CONTRACORRIENTECALCULOS Y RESULTADOSDo =26.270mmL =3.280mDo =26.270mmBalance Termico estableciendo el % de error por perdidas.Ao =0.271m^2L =3.280mPRESIN = 15 psiAo =0.271m^2Calor ganado por el AguaQ aguaT6 (C)T7 (C)T5 (C)T1 (C)LMTDUoPRESIN = 15 psiJ/sinoutinoutKW/m^2.KQ aguaT6 (C)T7 (C)T1 (C)T5 (C)LMTDUo22065.9922.9062.90128.00126.4082.561987.338J/sinoutinoutKW/m^2.K23329.8722.8056.60127.00124.8084.9321014.74118281.7822.4055.50121.10120.8080.895834.85925349.2522.9049.10128.90126.3090.8401030.86419415.2522.6050.70122.80121.0084.570848.09521786.5022.6045.10124.50121.3088.700907.356Donde:PRESIN = 20 psimagua : flujo masico de agua liquida[Kmol/s]Q aguaT6 (C)T7 (C)T5 (C)T1 (C)LMTDUoPRESIN = 20 psiCp : Capacidad Calorfica del agua[J/Kmol.K]J/sinoutinoutKW/m^2.KQ aguaT6 (C)T7 (C)T1 (C)T5 (C)LMTDUo: Variacin de Temperatua[K]24039.7422.9066.50132.60130.8084.9891044.924J/sinoutinoutKW/m^2.K24770.4422.9058.80133.30132.5090.8171007.58019927.3622.7058.80127.60126.2084.972866.338Calor perdido por el Vapor26986.0222.9050.80132.60131.0094.1811058.49719759.0122.6051.20127.80125.1088.922820.86222653.3122.7046.10128.20126.4092.480904.897PRESIN = 30 psiQ aguaT6 (C)T7 (C)T5 (C)T1 (C)LMTDUoPRESIN = 30 psiJ/sinoutinoutKW/m^2.KQ aguaT6 (C)T7 (C)T1 (C)T5 (C)LMTDUoDonde:24971.3222.968.2139.2137.690.8411015.487J/sinoutinoutKW/m^2.K25662.3322.960.1139138.295.848989.07521790.4823.162.6136.2133.990.935885.216: Densidad del Condensado[Kmol/m3]28429.5822.952.3138.8138.81100.4901045.11521954.3523.154.9134.4133.994.286860.18123806.3123.147.7138.6133.4100.287876.921: Calor Latente de Vaporizacin[J/Kmol]Porcentaje por PerdidaEcuaciones para el calculo de:Densidad :C1 =5.459C2 =0.30542C3 =647.13C4 =0.081TKM =18.015Cp :C1 =276370C2 =-2090C3 =8.125TKC4 =-0.014116C5 =9.37E-06Calor Latente de Vaporizacion :C1 =5.21E+07C2 =0.3199C3 =-0.212C4 =0.25795

hi-hoDETERMINACION EXPERIMENTAL DEL COEFICIENTE DE PELICULA DEL AGUA hiDETERMINACION EXPERIMENTAL DEL COEFICIENTE DE PELICULA DEL AGUA hiy DEL LADO DEL VAPOR hoy DEL LADO DEL VAPOR hoARREGLO EN PARALELOARREGLO EN CONTRACORRIENTEDeterminacin experimental del coeficiente de pelcula del agua hi y del lado delvapor ho, utilizando las ecuaciones 9 y 10 respectivamente.Di =20.930mmDi =20.930mmDo =26.270mmDo =26.270mmCalculo para el lado del AguaL =3.280mL =3.280mK =44.892W/m.CK =44.892W/m.CAi =0.216m^2Ai =0.216m^2Ao =0.271m^2Ao =0.271m^2PRESIN = 15 psiPRESIN = 15 psiQ aguaTW4TW3TW2Tp promTiQ aguaTW2TW3TW4Tp promTiJ/sCCCCCJ/sCCCCC22065.99127.4127.7126127.033121.61318281.78120.20119.30118.40119.300114.810Calculando la diferencia de temperatura entre las paredes interna y externa del tubo interior:23329.87126.4127.8124.5126.233120.50319415.25120.60120.20118.80119.867115.09825349.25128.1127.7124.8126.867120.64021786.50120.20119.80118.40119.467114.115Q aguaT6 (C)T7 (C)TiLMTDihiQ aguaT6 (C)T7 (C)TiLMTDihiJ/sinoutCKW/m^2.KJ/sinoutCKW/m^2.K22065.9922.9062.90121.61376.991328.9218281.7822.4055.50114.8174.641135.6723329.8722.8056.60120.50379.611358.7719415.2522.6050.70115.1077.601160.0525349.2522.9049.10120.64083.961399.9021786.5022.6045.10114.1279.741266.87Q aguaT5 (C)T1 (C)TW4TW2LMTDohoQ aguaT1 (C)T5 (C)TW2TW4LMTDohoJ/sinoutCCKW/m^2.KJ/sinoutCCKW/m^2.K22065.99128.00126.40127.40126.000.49165257.8518281.78121.10120.80120.20118.401.4048370.9423329.87127.00124.80126.40124.500.43199127.7319415.25122.80121.00120.60118.801.5645874.51Calculo para el lado del vapor25349.25128.90126.30128.10124.801.1184093.5421786.50124.50121.30120.20118.402.9227573.04PRESIN = 20 psiPRESIN = 20 psiQ aguaTW4TW3TW2Tp promTiQ aguaTW2TW3TW4Tp promTiJ/sCCCCCJ/sCCCCC24039.74132.00131.50128.40130.633124.72919927.36125.40125.20123.20124.600119.70524770.44132.70132.10129.90131.567125.48219759.01124.40124.20123.50124.033119.18026986.02131.20130.50128.60130.100123.47222653.31125.20126.20123.20124.867119.302Q aguaT6 (C)T7 (C)TiLMTDihiQ aguaT6 (C)T7 (C)TiLMTDihiJ/sinoutCKW/m^2.KJ/sinoutCKW/m^2.K24039.7422.9066.50124.72978.011428.8819927.3622.7058.80119.70577.561191.2924770.4422.9058.80125.48283.351377.9919759.0122.6051.20119.18081.441124.8826986.0222.9050.80123.47285.871457.1922653.3122.7046.10119.30284.361245.06Q aguaT5 (C)T1 (C)TW4TW2LMTDohoQ aguaT1 (C)T5 (C)TW2TW4LMTDohoJ/sinoutCCKW/m^2.KJ/sinoutCCKW/m^2.K24039.74132.60130.80132.00128.401.3068395.5519927.36127.60126.20125.40123.202.1134859.6324770.44133.30132.50132.70129.901.3667089.2219759.01127.80125.10124.40123.501.9836806.4426986.02132.60131.00131.20128.601.8653732.8622653.31128.20126.40125.20123.202.6631428.42PRESIN = 30 psiPRESIN = 30 psiQ aguaTW4TW3TW2Tp promTiQ aguaTW2TW3TW4Tp promTiJ/sCCCCCJ/sCCCCC24971.32138.5138131.2135.900129.76621790.48133.1133.9134.4133.800128.44825662.33138.7137.9127.2134.600128.29721954.35132.9133.9126.5131.100125.70728429.58138.3137.3127.9134.500127.51723806.31133.2133.4126.7131.100125.253Q aguaT6 (C)T7 (C)TiLMTDihiQ aguaT6 (C)T7 (C)TiLMTDihiJ/sinoutCKW/m^2.KJ/sinoutCKW/m^2.K24971.3222.966.50129.7783.171392.1321790.4823.158.80128.4586.271171.1525662.3322.958.80128.3086.201380.3021954.3523.151.20125.7187.811159.2728429.5822.950.80127.5289.951465.5123806.3123.146.10125.2590.161224.23Q aguaT5 (C)T1 (C)TW4TW2LMTDohoQ aguaT1 (C)T5 (C)TW2TW4LMTDohoJ/sinoutCCKW/m^2.KJ/sinoutCCKW/m^2.K24971.32139.2137.6138.50131.22.5835814.4321790.48136.2133.9133.10134.401.2365277.8025662.33139138.2138.70127.22.9731912.1021954.35134.4133.9132.90126.503.3424293.9628429.58138.8138.81138.30127.93.3831101.7023806.31138.6133.4133.20126.702.8630712.65

M. WilsonCALCULO DEL COEFICIENTE PELICULAR DE CONDENSADO USANDOCALCULO DEL COEFICIENTE PELICULAR DE CONDENSADO USANDOEL METODO DE WILSONEL METODO DE WILSONARREGLO EN PARALELOARREGLO EN PARALELOPRESIN = 15 psiSea :Sea :Entonces :Entonces :Di =20.930mmDi =20.930mmDo =26.270mmDo =26.270mmL =3.280mL =3.280mK =44.892W/m.CK =44.892W/m.CArea o =5.420E-04m^2Area o =5.420E-04m^2Ao =0.271m^2Ao =0.271m^2PRESIN = 15 psiPRESIN = 15 psiCAUDALVUo11CAUDALVUo11LPMm/sW/m^2.KV^0.8UoLPMm/sW/m^2.KV^0.8Uo0.792.429E-02987.33819.5721.013E-030.952.921E-02834.85916.8871.198E-030.782.398E-021014.74119.7729.855E-040.511.568E-02848.09527.7761.179E-030.852.614E-021030.86418.4589.701E-040.611.876E-02907.35624.0691.170E-03Aplicando una Regresion Linealr = 0.68Aplicando una Regresion Linealr = 0.79A =5.890E-04A =1.229E-03RwRohoRwRohoK/WK/WW/m^2.KK/WK/WW/m^2.K2.456E-043.434E-0410758.33994460832.456E-049.834E-043756.6055188835PRESIN = 20 psiPRESIN = 20 psiCAUDALVUo11CAUDALVUo11LPMm/sW/m^2.KV^0.8UoLPMm/sW/m^2.KV^0.8Uo0.802.460E-021044.92419.3769.570E-040.702.152E-02866.33821.5601.154E-030.882.706E-021007.58017.9539.925E-040.682.091E-02820.86222.0661.118E-030.862.644E-021022.49718.2879.780E-040.692.122E-02904.89721.8101.105E-03Aplicando una Regresion Linealr = 0.98Aplicando una Regresion Linealr = 0.33A =1.412E-03A =2.630E-03RwRohoRwRohoK/WK/WW/m^2.KK/WK/WW/m^2.K2.456E-041.166E-033167.20826420782.456E-042.384E-031549.3175991893PRESIN = 30 psiPRESIN = 30 psiCAUDALVUo11CAUDALVUo11LPMm/sW/m^2.KV^0.8UoLPMm/sW/m^2.KV^0.8Uo1.364.188E-021015.48712.6599.847E-041.223.742E-02885.21613.8521.130E-031.474.520E-02989.07511.9091.011E-031.374.203E-02860.18112.6221.163E-031.845.664E-021045.1159.9439.568E-041.735.320E-02876.92110.4541.160E-03Aplicando una Regresion Linealr = 0.99Aplicando una Regresion Linealr = 0.72A =8.257E-04A =1.245E-03RwRohoRwRohoK/WK/WW/m^2.KK/WK/WW/m^2.K2.456E-045.801E-046368.39951870592.456E-049.994E-043696.4623009721

ec. hiCalculo de los coeficientes de transferencia peliculares utilizando modelos empricos.CALCULO DE hi MEDIANTE LAS ECUACIONES 15,17,18,20,21CALCULO DE hi MEDIANTE LAS ECUACIONES 15,17,18,20,21Ec. 15 Ecuacin de GnielinskiARREGLO EN PARALELOARREGLO EN CONTRACORRIENTEPRESIN = 15 psiPROPIEDADES FISICASPROPIEDADES FISICASDi =20.930mmDi =20.930mmL =3.280mL =3.280mPRESIN = 15 psiPRESIN = 15 psiT6 (C)T7 (C)TbDensidadCpubuwKT6 (C)T7 (C)TbDensidadCpubuwKinoutKKg/m^3J/Kg.KKg/m.sKg/m.sW/m.KinoutKKg/m^3J/Kg.KKg/m.sKg/m.sW/m.K22.9062.90318.55989.554178.006.210E-042.390E-040.64122.4055.50318.55989.554178.006.210E-042.390E-040.641Ec. 17 Ecuacin de Sieder Tate22.8056.60314.50990.654178.156.210E-042.390E-040.64122.6050.70314.50990.654178.156.210E-042.390E-040.64122.9049.10310.60991.704178.936.830E-042.390E-040.63422.6045.10310.60991.704178.936.830E-042.390E-040.634NUMEROS ADIMENSIONALESNUMEROS ADIMENSIONALESW aguaNReNPrNPrffNUSSELTNUSSELTNUSSELTNUSSELTNUSSELTW aguaNReNPrNPrffNUSSELTNUSSELTNUSSELTNUSSELTNUSSELTKg/sbbwec. 15ec. 21ec. 15ec. 17ec. 18ec. 20ec. 21Kg/sbbwec. 15ec. 21ec. 15ec. 17ec. 18ec. 20ec. 210.13212923.454.0481.5580.0070.02995.70095.70378.29157.30483.4600.007718.744.0481.5580.0200.079-4.5149.4867.7609.6618.886Ec. 19 Ecuacin de Dittus Boelter0.16516168.464.0481.5580.0070.028116.548114.48893.65968.090100.1520.009898.994.0481.5580.0180.072-1.51911.3469.28210.62110.4690.23120601.704.5021.5750.0060.026152.392145.925118.63482.762128.1430.0131145.204.5021.5750.0160.0652.13514.45811.75411.92413.024n: 0.40 para el calentamientoCALCULANDO hi (W/m^2.K)CALCULANDO hi (W/m^2.K)n: 0.30 para el enfriamientohihihihihihihihihihiec. 15ec. 17ec. 18ec. 20ec. 21ec. 15ec. 17ec. 18ec. 20ec. 212930.882930.982397.731754.982556.04-138.25290.52237.66295.88272.153569.373506.312868.392085.303067.24-46.51347.47284.26325.28320.61Ec. 20 Ecuacin de Sleicher Rouse4616.184420.263593.592506.983881.6564.66437.96356.05361.20394.51PRESIN = 20 psiPRESIN = 20 psiT6 (C)T7 (C)TbDensidadCpubuwKT6 (C)T7 (C)TbDensidadCpubuwKinoutKKg/m^3J/Kg.KKg/m.sKg/m.sW/m.KinoutKKg/m^3J/Kg.KKg/m.sKg/m.sW/m.K22.9066.50317.70989.784177.986.210E-042.390E-040.64122.7058.80318.55989.554178.006.210E-042.390E-040.64122.9058.80313.85990.834178.246.210E-042.390E-040.64122.6051.20314.50990.654178.156.210E-042.390E-040.64122.9050.80309.85991.904179.166.830E-042.390E-040.63422.7046.10310.60991.704178.936.830E-042.390E-040.634Ec. 17 Ecuacin de Petukhov PopovNUMEROS ADIMENSIONALESNUMEROS ADIMENSIONALESW aguaNReNPrNPrffNUSSELTNUSSELTNUSSELTNUSSELTNUSSELTW aguaNReNPrNPrffNUSSELTNUSSELTNUSSELTNUSSELTNUSSELTKg/sbbwec. 15ec. 21ec. 15ec. 17ec. 18ec. 20ec. 21Kg/sbbwec. 15ec. 21ec. 15ec. 17ec. 18ec. 20ec. 210.13212917.054.0481.5580.0070.02995.65795.66578.26057.28283.4260.007718.394.0481.5580.0200.079-4.5209.4827.7579.6598.8830.16516163.394.0481.5580.0070.028116.517114.46193.63668.074100.1270.009898.934.0481.5580.0180.072-1.52011.3459.28110.62110.4680.23120596.974.5021.5750.0060.026152.365145.900118.61582.749128.1220.0131145.034.5021.5750.0160.0652.13214.45611.75311.92313.022CALCULANDO hi (W/m^2.K)CALCULANDO hi (W/m^2.K)hihihihihihihihihihiec. 15ec. 17ec. 18ec. 20ec. 21ec. 15ec. 17ec. 18ec. 20ec. 212929.592929.822396.771754.312555.00-138.44290.40237.57295.82272.053568.423505.462867.702084.823066.49-46.54347.45284.24325.27320.604615.374419.533593.012506.603881.0164.59437.90356.01361.18394.47PRESIN = 30 psiPRESIN = 30 psiT6 (C)T7 (C)TbDensidadCpubuwKT6 (C)T7 (C)TbDensidadCpubuwKinoutKKg/m^3J/Kg.KKg/m.sKg/m.sW/m.KinoutKKg/m^3J/Kg.KKg/m.sKg/m.sW/m.K22.968.254.931045.3610204.216.210E-042.390E-040.64123.162.6315.85990.284178.036.210E-042.390E-040.64122.960.154.991045.3510199.736.210E-042.390E-040.64123.154.9312.00991.334178.586.210E-042.390E-040.64122.952.355.051045.3410195.466.830E-042.390E-040.63423.147.7308.40992.294179.666.830E-042.390E-040.634NUMEROS ADIMENSIONALESNUMEROS ADIMENSIONALESW aguaNReNPrNPrffNUSSELTNUSSELTNUSSELTNUSSELTNUSSELTW aguaNReNPrNPrffNUSSELTNUSSELTNUSSELTNUSSELTNUSSELTKg/sbbwec. 15ec. 21ec. 15ec. 17ec. 18ec. 20ec. 21Kg/sbbwec. 15ec. 21ec. 15ec. 17ec. 18ec. 20ec. 210.13212914.019.8863.8050.0070.029135.225128.807111.83682.704121.8870.007717.984.0481.5580.0200.079-4.5289.4787.7549.6578.8790.16516160.529.8813.8030.0070.028165.645154.096133.78998.990146.9600.009898.424.0481.5580.0180.072-1.52811.3409.27710.61810.4640.23120592.7910.9833.8430.0060.026217.066196.378169.432120.933188.1820.0131144.724.5031.5760.0160.0652.12814.45411.75111.92213.021CALCULANDO hi (W/m^2.K)CALCULANDO hi (W/m^2.K)hihihihihihihihihihiec. 15ec. 17ec. 18ec. 20ec. 21ec. 15ec. 17ec. 18ec. 20ec. 214141.373944.843425.082532.883732.90-138.67290.27237.46295.75271.945073.034719.344097.413031.664500.79-46.79347.31284.12325.20320.476575.245948.565132.343663.225700.3164.46437.84355.96361.15394.41

coef. pelicular vaporCOEFICIENTE PELICULAR DE VAPOR CONDENSADO EN LA SUPERFICIE EXTERNACOEFICIENTE PELICULAR DE VAPOR CONDENSADO EN LA SUPERFICIE EXTERNAARREGLO EN PARALELOARREGLO EN CONTRACORRIENTEPROPIEDADES FISICASPROPIEDADES FISICASDo =26.670mmDo =26.670mmL =3.280mL =3.280mg =9.810m/s^2g =9.810m/s^2PRESIN = 15 psiPRESIN = 15 psiTvTwTfToDensidadufKhoTvTwTfToDensidadufKhoCCKKKg/m^3J/KgKg/m.sW/m.KW/m^2.KCCKKKg/m^3J/KgKg/m.sW/m.KW/m^2.K127.20127.03400.120.17964.492192302.896.210E-040.68528324.06120.95119.30393.131.65966.882210204.656.210E-040.68516020.23125.90126.23399.070.33964.852196064.566.210E-040.68523832.30121.90119.87393.882.03966.632207513.156.210E-040.68515198.39127.60126.87400.230.73964.452191141.366.830E-040.68519093.84122.90119.47394.183.43966.522204668.656.830E-040.68513014.44PRESIN = 20 psiPRESIN = 20 psiTvTwTfToDensidadufKhoTvTwTfToDensidadufKhoCCKKKg/m^3J/KgKg/m.sW/m.KW/m^2.KCCKKKg/m^3J/KgKg/m.sW/m.KW/m^2.K131.70130.63404.171.07963.072179123.576.210E-040.68517767.94126.90124.60398.752.30964.962193172.766.210E-040.68514700.61132.90131.57405.231.33962.702175567.036.210E-040.68516793.74126.45124.03398.242.42965.132194475.566.210E-040.68514523.36131.80130.10403.951.70963.152178827.886.830E-040.68515441.95127.30124.87399.082.43964.842192012.696.830E-040.68514151.46PRESIN = 30 psiPRESIN = 30 psiTvTwTfToDensidadufKhoTvTwTfToDensidadufKhoCCKKKg/m^3J/KgKg/m.sW/m.KW/m^2.KCCKKKg/m^3J/KgKg/m.sW/m.KW/m^2.K138.40135.90410.152.50960.942159034.156.210E-040.68514311.12135.05133.80407.431.25961.922169149.866.210E-040.68517047.42138.60134.60409.604.00961.142158425.666.210E-040.68512724.99134.15131.10405.633.05962.562171843.196.210E-040.68513648.66138.81134.50409.654.31961.122157801.436.830E-040.68512198.64136.00131.10406.554.90962.232166295.786.830E-040.68511828.56

f. ensuciamientoCALCULO DEL FACTOR DE ENSUCIAMIENTOCALCULO DEL FACTOR DE ENSUCIAMIENTOARREGLO EN PARALELOARREGLO EN CONTRACORRIENTEDi =20.930mmDi =20.930mmDo =26.270mmDo =26.270mmL =3.280mL =3.280mK =44.892W/m.CK =44.892W/m.CAi =0.216m^2Ai =0.216m^2Ao =0.271m^2Ao =0.271m^2PRESIN = 15 psiPRESIN = 15 psiUohihoRdUohihoRdW/m^2.KW/m^2.KW/m^2.Km^2.K/WW/m^2.KW/m^2.KW/m^2.Km^2.K/W987.3381328.92165257.852.018E-03834.8591135.6748370.942.349E-031014.7411358.77199127.731.971E-03848.0951160.0545874.512.306E-031030.8641399.9084093.541.921E-03907.3561266.8727573.042.123E-03PRESIN = 20 psiPRESIN = 20 psiUohihoRdUohihoRdW/m^2.KW/m^2.KW/m^2.Km^2.K/WW/m^2.KW/m^2.KW/m^2.Km^2.K/W1044.9241428.8868395.551.887E-03866.3381191.2934859.632.246E-031007.5801377.9967089.221.955E-03820.8621124.8836806.442.373E-031058.4971457.1953732.861.854E-03904.8971245.0631428.422.148E-03PRESIN = 30 psiPRESIN = 30 psiUohihoRdUohihoRdW/m^2.KW/m^2.KW/m^2.Km^2.K/WW/m^2.KW/m^2.KW/m^2.Km^2.K/W1015.4871392.1335814.431.925E-03885.2161171.1565277.802.253E-03989.0751380.3031912.101.956E-03860.1811159.2724293.962.271E-031045.1151465.5131101.701.848E-03876.9211224.2330712.652.200E-03

calculo a b cCALCULO DE a b y c de la ec. 16CALCULO DE a b y c de la ec. 16ARREGLO EN PARALELOARREGLO EN CONTRACORRIENTEPRESIN = 15 psiPRESIN = 15 psiubuwNUSSELTNReNPrububuwNUSSELTNReNPrubKg/m.sKg/m.sec. 15uwKg/m.sKg/m.sec. 15uw0.0010.00095.70012923.4534.0482.5980.0010.0004.514718.7454.0482.5980.0010.000116.54816168.4624.0482.5980.0010.0001.519898.9914.0482.5980.0010.000152.39220601.6974.5022.8580.0010.0002.1351145.2004.5022.858tomando Ln a los numeros adimensionalestomando Ln a los numeros adimensionalesLn NusseltLn NreLn Pr*(ub/uw)Ln NusseltLn NreLn Pr*(ub/uw)4.5619.4672.3531.5076.5782.3534.7589.6912.3530.4186.8012.3535.0269.9332.5550.7587.0432.555tenemos :tenemos :a=a=b=b=c=c=PRESIN = 20 psiPRESIN = 20 psiubuwNUSSELTNReNPrububuwNUSSELTNReNPrubKg/m.sKg/m.sec. 15uwKg/m.sKg/m.sec. 15uw0.0010.00095.65712917.0484.0482.5980.0010.0004.520718.3934.0482.5980.0010.000116.51716163.3914.0482.5980.0010.0001.520898.9304.0482.5980.0010.000152.36520596.9724.5022.8580.0010.0002.1321145.0314.5022.858tomando Ln a los numeros adimensionalestomando Ln a los numeros adimensionalesLn NusseltLn NreLn Pr*(ub/uw)Ln NusseltLn NreLn Pr*(ub/uw)4.5619.4662.3531.5096.5772.3534.7589.6912.3530.4196.8012.3535.0269.9332.5550.7577.0432.555tenemos :tenemos :a=a=b=b=c=c=PRESIN = 30 psiPRESIN = 30 psiubuwNUSSELTNReNPrububuwNUSSELTNReNPrubKg/m.sKg/m.sec. 15uwKg/m.sKg/m.sec. 15uw0.0010.000135.22512914.0139.8862.5980.0010.0004.528717.9794.0482.5980.0010.000165.64516160.5199.8812.5980.0010.0001.528898.4194.0482.5980.0010.000217.06620592.79410.9832.8580.0010.0002.1281144.7244.5032.858tomando Ln a los numeros adimensionalestomando Ln a los numeros adimensionalesLn NusseltLn NreLn Pr*(ub/uw)Ln NusseltLn NreLn Pr*(ub/uw)4.9079.4663.2461.5106.5762.3535.1109.6903.2460.4246.8012.3535.3809.9333.4460.7557.0432.555tenemos :tenemos :a=a=b=b=c=c=

MBD000FF516.unknown

MBD00131D22.unknown

MBD001431DE.unknown

MBD001431E2.unknown

MBD001451B4.unknown

MBD00145C3B.unknown

MBD001431E3.unknown

MBD001431E0.unknown

MBD001431E1.unknown

MBD001431DF.unknown

MBD001431DA.unknown

MBD001431DC.unknown

MBD001431DD.unknown

MBD001431DB.unknown

MBD001332BF.unknown

MBD001431D8.unknown

MBD001431D9.unknown

MBD001332C0.unknown

MBD00131D23.unknown

MBD00100266.unknown

MBD00102AD6.unknown

MBD00102ADA.unknown

MBD00102ADC.unknown

MBD00102ADD.unknown

MBD00102ADB.unknown

MBD00102AD8.unknown

MBD00102AD9.unknown

MBD00102AD7.unknown

MBD00100EAE.unknown

MBD00102AD2.unknown

MBD00102AD4.unknown

MBD00102AD5.unknown

MBD00102AD3.unknown

MBD00100EB0.unknown

MBD00102AD0.unknown

MBD00102AD1.unknown

MBD00102ACE.unknown

MBD00102ACF.unknown

MBD00100EB1.unknown

MBD00100EAF.unknown

MBD00100268.unknown

MBD00100EAC.unknown

MBD00100EAD.unknown

MBD00100EAA.unknown

MBD00100EAB.unknown

MBD00100269.unknown

MBD00100267.unknown

MBD00100262.unknown

MBD00100264.unknown

MBD00100265.unknown

MBD00100263.unknown

MBD000FF518.unknown

MBD000FFBF4.unknown

MBD000FF517.unknown

MBD000FEC24.unknown

MBD000FEC2C.unknown

MBD000FEC30.unknown

MBD000FEC32.unknown

MBD000FEC33.unknown

MBD000FEC31.unknown

MBD000FEC2E.unknown

MBD000FEC2F.unknown

MBD000FEC2D.unknown

MBD000FEC28.unknown

MBD000FEC2A.unknown

MBD000FEC2B.unknown

MBD000FEC29.unknown

MBD000FEC26.unknown

MBD000FEC27.unknown

MBD000FEC25.unknown

MBD000FEC1C.unknown

MBD000FEC20.unknown

MBD000FEC22.unknown

MBD000FEC23.unknown

MBD000FEC21.unknown

MBD000FEC1E.unknown

MBD000FEC1F.unknown

MBD000FEC1D.unknown

MBD000D5AD3.unknown

MBD000D5AD5.unknown

MBD000D5AD6.unknown

MBD000D5AD4.unknown

MBD000D5ACD.unknown

MBD000D5ACF.unknown

MBD000D5AD0.unknown

MBD000D5ACE.unknown

MBD0009C95F.unknown

MBD0009C960.unknown

MBD0009C95D.unknown