Filtracion c&t - Método de Ruth
6
FILTRACIÓN 1RA CORRIDA 2DA CORRIDA 3RA CORRIDA 35 psi y 27⁰C 52 psi y 30⁰C Vaso 4 Vacío 28.8095 gr. Vaso 2 Vacío ### Vaso 5 Vacío ### 71.7942 gr. ### ### +Sólidos 30.3443 gr. +Sólidos ### +Sólidos ### Vaso 3 Vacío 28.5675 gr. Vaso 8 Vacío ### Vaso 6 Vacío ### 66.9000 gr. ### ### +Sólidos 29.4295 gr. +Torta seca ### +Torta seca ### Vaso 1 Vacío 28.5875 gr. 70.9831 gr. +Torta seca 62.3232 gr. Intervalo t(s) t(s) V(mL) Intervalo t(s) t(s) V(mL) Intervalo t(s) t(s) V(mL) 28.7 28.7 970 20.3 20.3 970 4.0 4.0 960 106.9 78.2 975 31.8 11.5 1000 11.3 7.3 960 144.6 37.7 910 38.7 6.9 940 20.1 8.8 1000 226.5 81.9 940 50.3 11.6 1000 30.1 10.0 980 313.6 87.1 950 103.4 53.1 930 41.3 11.2 1000 403.5 89.9 970 117.3 13.9 940 52.2 10.9 950 453.7 50.2 910 134.8 17.5 955 108.3 56.1 980 550.2 96.5 975 154.5 19.7 985 121.2 12.9 1020 647.3 97.1 930 215.9 61.4 990 137.4 16.2 1040 754.6 107.3 970 238.5 22.6 970 152.7 15.3 900 859.7 105.1 940 303.9 65.4 980 210.5 57.8 940 1006.5 146.8 925 330.3 26.4 970 230.6 20.1 940 1180.9 174.4 960 358.4 28.1 970 248.9 18.3 950 1238.5 57.6 960 427.8 69.4 950 311.3 62.4 980 1401.2 162.7 970 500.4 72.6 980 334.5 23.2 930 1528.1 126.9 960 531.5 31.1 925 359.0 24.5 990 1701.5 173.4 970 603.5 72.0 920 424.5 65.5 1000 1836.5 135.0 930 635.8 32.3 980 452.4 27.9 950 2021.9 185.4 960 713.8 78.0 980 519.3 66.9 930 2210.7 188.8 935 752.9 39.1 960 546.5 27.2 920 2409.3 198.6 950 834.3 81.4 960 615.3 68.8 910 2620.5 211.2 955 914.9 80.6 960 646.2 30.9 930 2847.8 227.3 955 957.3 42.4 930 719.5 73.3 975 3135.6 287.8 960 1046.5 89.2 960 754.9 35.4 970 3458.2 322.6 960 1138.6 92.1 930 825.4 70.5 940 3930.2 472.0 960 1230.6 92.0 930 858.0 32.6 935 4435.6 505.4 680 1331.8 101.2 980 936.4 78.4 960 1434.5 102.7 960 1016.5 80.1 970 1542.5 108.0 930 1100.4 83.9 1000 1659.4 116.9 1000 1148.5 48.1 970 1820.7 161.3 950 1232.6 84.1 950 1953.2 132.5 955 1320.4 87.8 950 2141.5 188.3 935 1411.9 91.5 940 2422.6 281.1 960 1505.9 94.0 930 2743.4 320.8 650 1605.4 99.5 945 1710.6 105.2 980 1824.5 113.9 950 1948.7 124.2 980 2126.5 177.8 900 2410.4 283.9 960 2705.3 294.9 500 17 psi y 23⁰C +Suspensión inicial +Suspensión final +Suspensión final +Suspensión final +Torta húmeda +Torta húmeda +Torta húmeda
-
Upload
branco-jose-figueroa-ayala -
Category
Documents
-
view
1 -
download
0
description
metodo de ruth
Transcript of Filtracion c&t - Método de Ruth
datos experimentalesFILTRACIN 1RA CORRIDA2DA CORRIDA3RA
CORRIDA17 psi y 23C35 psi y 27C52 psi y 30CVaso 4Vaco28.8095Vaso
2Vaco28.107Vaso 5Vaco30.2156+Suspensin inicial71.7942+Suspensin
final65.8409+Suspensin
final60.3985+Slidos30.3443+Slidos28.4385+Slidos30.4229Vaso
3Vaco28.5675Vaso 8Vaco32.7003Vaso 6Vaco65.425+Suspensin
final66.9+Torta hmeda72.2803+Torta
hmeda111.7349+Slidos29.4295+Torta seca64.6241+Torta
seca102.3483Vaso 1Vaco28.5875+Torta hmeda70.9831+Torta
seca62.3232Intervalo t(s)t(s)V(mL)Intervalo t(s)t(s)V(mL)Intervalo
t(s)t(s)V(mL)28.728.797020.320.39704.04.0960106.978.297531.811.5100011.37.3960144.637.791038.76.994020.18.81000226.581.994050.311.6100030.110.0980313.687.1950103.453.193041.311.21000403.589.9970117.313.994052.210.9950453.750.2910134.817.5955108.356.1980550.296.5975154.519.7985121.212.91020647.397.1930215.961.4990137.416.21040754.6107.3970238.522.6970152.715.3900859.7105.1940303.965.4980210.557.89401006.5146.8925330.326.4970230.620.19401180.9174.4960358.428.1970248.918.39501238.557.6960427.869.4950311.362.49801401.2162.7970500.472.6980334.523.29301528.1126.9960531.531.1925359.024.59901701.5173.4970603.572.0920424.565.510001836.5135.0930635.832.3980452.427.99502021.9185.4960713.878.0980519.366.99302210.7188.8935752.939.1960546.527.29202409.3198.6950834.381.4960615.368.89102620.5211.2955914.980.6960646.230.99302847.8227.3955957.342.4930719.573.39753135.6287.89601046.589.2960754.935.49703458.2322.69601138.692.1930825.470.59403930.2472.09601230.692.0930858.032.69354435.6505.46801331.8101.2980936.478.49601434.5102.79601016.580.19701542.5108.09301100.483.910001659.4116.910001148.548.19701820.7161.39501232.684.19501953.2132.59551320.487.89502141.5188.39351411.991.59402422.6281.19601505.994.09302743.4320.86501605.499.59451710.6105.29801824.5113.99501948.7124.29802126.5177.89002410.4283.99602705.3294.9500
17 psi METODO DE RUTH - METODO DIFERENCIALP=17 lb/pulg2t
AcumuladoVolumen(L)V
(L)tt/V28.70.9700.97028.729.59106.91.9450.97578.280.21144.62.8550.91037.741.43226.53.7950.94081.987.13313.64.7450.95087.191.68403.55.7150.97089.992.68453.76.6250.91050.255.16550.27.6000.97596.598.97647.38.5300.93097.1104.41754.69.5000.970107.3110.62859.710.4400.940105.1111.811006.511.3650.925146.8158.701180.912.3250.960174.4181.671238.513.2850.96057.660.001401.214.2550.970162.7167.731528.115.2150.960126.9132.191701.516.1850.970173.4178.761836.517.1150.930135.0145.162021.918.0750.960185.4193.132210.719.0100.935188.8201.932409.319.9600.950198.6209.052620.520.9150.955211.2221.152847.821.8700.955227.3238.013135.622.8300.960287.8299.79(aqu)3458.223.7900.960322.6336.043930.224.7500.960472.0491.674435.625.4300.680505.4743.24Datos
experimentalesVaso 4Vaco28.8095Suspensin InicialPeso de
Solidos1.5348Caracteristicas de Filtracinpresion (psi)17+Suspensin
inicial71.7942Peso de Agua41.4499N de Marcos1temperatura
(C)23+Slidos30.3443mf (solidos/suspension)0.0357Suspensin
InicialSuspensin FinalPromedioLargo (m)0.152Vaso
3Vaco28.5675Suspensin FinalPeso de Solidos0.862Concentracion de
slidos corregida, Cm ( Kg/m3 )37.292323.085230.1888Ancho
(m)0.152Propiedades Fisicas a 23 C+Suspensin final66.9Peso de
Agua37.4705Radio de la Esquina0.025Densidad del Agua
(Kg/m3)997.57+Slidos29.4295mf (solidos/suspension)0.0225Altura
(m)0.012Viscocidad del Agua (Kg/m.s)0.0009358Vaso
1Vaco28.5875TortaTorta Hmeda42.3956mf
(solidos/suspension)0.03570.02250.0291rea Efectiva
(m2)0.0211Densidad del CaCO3 (Kg/m3)2700+Torta hmeda70.9831Torta
Seca33.7357rea Total (m2)0.0423+Torta seca62.3232m (torta humeda/
torta seca)1.2567Para filtracin a Presin Constante :De la grfica se
obtienen los valores :Por las ecuaciones de Ruth se tiene
:Resistencia Especifica de la TortaResistencia del Medio
filtrantePorosidad de la torta :Densidad de la torta seca
(pts):entiendase como lecho ( solido + interticios)Volumen de
Suspensin Requerido :Volumen del Marco (m3)0.00025Solidos en la
Torta (Kg)0.4041Peso Suspensin Alimentada (Kg)13.8890Densidad de la
Suspensin (Kg/m3)1,016.2Volumen de Suspensin (m3)0.01367Volumen de
Filtrado Obtenido :Volumen de Filtrado (m3)0.01328Velocidad
Promedio de Filtracin :Velocidad de Filtracin (m3/h)0.022Tiempo de
Filtracin :Tiempo de filtracin (s)2,131.57Tiempo de filtracin
(min)35.53P=17lb/plg20.971.94499999999999982.8553.79499999999999994.74500000000000015.71499999999999997.68.52999999999999949.510.4411.36512.32499999999999914.25500000000000116.18499999999999918.07499999999999919.00999999999999819.95999999999999720.91499999999999621.86999999999999422.82999999999999529.58762886597938380.20512820512820441.42857142857141687.12765957446809891.68421052631582392.68041237113399798.974358974359035104.40860215053753110.618556701031111.8085106382979158.70270270270265181.66666666666677167.73195876288665178.76288659793823193.12500000000011201.92513368983927209.05263157894777221.15183246073281238.01047120418869299.7916666666664Curva21.86999999999999422.82999999999999523.78999999999999624.74999999999999625.429999999999996238.01047120418869299.7916666666664336.04166666666657491.66666666666669743.23529411764775
V(L)
t/V
35 psiMETODO DE RUTH - METODO DIFERENCIALP=35 lb/pulg2t
AcumuladoVolumen(L)Vtt/V20.30.9700.97020.320.9331.81.9701.00011.511.5038.72.9100.9406.97.3450.33.9101.00011.611.60103.44.8400.93053.157.10117.35.7800.94013.914.79134.86.7350.95517.518.32154.57.7200.98519.720.00215.98.7100.99061.462.02238.59.6800.97022.623.30303.910.6600.98065.466.73330.311.6300.97026.427.22358.412.6000.97028.128.97427.813.5500.95069.473.05500.414.5300.98072.674.08531.515.4550.92531.133.62603.516.3750.92072.078.26635.817.3550.98032.332.96713.818.3350.98078.079.59752.919.2950.96039.140.73834.320.2550.96081.484.79914.921.2150.96080.683.96957.322.1450.93042.445.591046.523.1050.96089.292.921138.624.0350.93092.199.031230.624.9650.93092.098.921331.825.9450.980101.2103.271434.526.9050.960102.7106.981542.527.8350.930108.0116.131659.428.8351.000116.9116.901820.729.7850.950161.3169.791953.230.7400.955132.5138.74(aqu)2141.531.6750.935188.3201.392422.632.6350.960281.1292.812743.433.2850.650320.8493.54Datos
experimentalesVaso 3Vaco28.5675Suspensin InicialPeso de
Solidos0.862Caracteristicas de Filtracinpresion (psi)35+Suspensin
inicial66.9Peso de Agua37.4705N de Marcos1temperatura
(C)27+Slidos29.4295mf (solidos/suspension)0.0225Suspensin
InicialSuspensin FinalPromedioLargo (m)0.152Vaso
2Vaco28.107Suspensin FinalPeso de Solidos0.3315Concentracion de
slidos corregida, Cm ( Kg/m3 )23.05268.851315.9519Ancho
(m)0.152Propiedades Fisicas a 27 C+Suspensin final65.8409Peso de
Agua37.4024Radio de la Esquina0.025Densidad del Agua
(Kg/m3)996.55+Slidos28.4385mf (solidos/suspension)0.0088Altura
(m)0.012Viscocidad del Agua (Kg/m.s)0.0008545Vaso
8Vaco32.7003TortaTorta Hmeda39.58mf
(solidos/suspension)0.02250.00880.0156rea Efectiva
(m2)0.0211Densidad del CaCO3 (Kg/m3)2700+Torta hmeda72.2803Torta
Seca31.9238rea Total (m2)0.0423+Torta seca64.6241m (torta humeda/
torta seca)1.2398Para filtracin a Presin Constante :De la grfica se
obtienen los valores :Por las ecuaciones de Ruth se tiene
:Resistencia Especifica de la TortaResistencia del Medio
filtrantePorosidad de la torta :Densidad de la torta seca
(pts):entiendase como lecho ( solido + interticios)Volumen de
Suspensin Requerido :Volumen del Marco (m3)0.00025Solidos en la
Torta (Kg)0.4178Peso Suspensin Alimentada (Kg)26.7212Densidad de la
Suspensin (Kg/m3)1,006.5Volumen de Suspensin (m3)0.02655Volumen de
Filtrado Obtenido :Volumen de Filtrado (m3)0.02609Velocidad
Promedio de Filtracin :Velocidad de Filtracin (m3/h)0.033Tiempo de
Filtracin :Tiempo de filtracin (s)2,854.70Tiempo de filtracin
(min)47.58P=35lb/plg20.978.709999999999999110.6613.5514.53000000000000116.37500000000000418.33500000000000420.25500000000000621.21500000000000723.10500000000000824.03500000000000724.96500000000000725.94500000000000726.90500000000000827.83500000000000828.83500000000000830.74000000000000620.92783505154639262.02020202020202866.73469387755099573.05263157894741374.08163265306119278.26086956521739179.59183673469388584.79166666666664383.95833333333335792.91666666666671499.03225806451602998.924731182795696103.26530612244903106.97916666666671116.12903225806451116.90000000000009138.743455497382230.74000000000000631.67500000000000432.63500000000000533.285000000000004138.7434554973822201.39037433155073292.81249999999994493.53846153846177
V(L)
t/V
52 psiMETODO DE RUTH - METODO DIFERENCIALP=52 lb/pulg2t
AcumuladoVolumen(L)Vtt/V4.00.9600.9604.04.1711.31.9200.9607.37.6020.12.9201.0008.88.8030.13.9000.98010.010.2041.34.9001.00011.211.2052.25.8500.95010.911.47108.36.8300.98056.157.24121.27.8501.02012.912.65137.48.8901.04016.215.58152.79.7900.90015.317.00210.510.7300.94057.861.49230.611.6700.94020.121.38248.912.6200.95018.319.26311.313.6000.98062.463.67334.514.5300.93023.224.95359.015.5200.99024.524.75424.516.5201.00065.565.50452.417.4700.95027.929.37519.318.4000.93066.971.94546.519.3200.92027.229.57615.320.2300.91068.875.60646.221.1600.93030.933.23719.522.1350.97573.375.18754.923.1050.97035.436.49825.424.0450.94070.575.00858.024.9800.93532.634.87936.425.9400.96078.481.671016.526.9100.97080.182.581100.427.9101.00083.983.901148.528.8800.97048.149.591232.629.8300.95084.188.531320.430.7800.95087.892.421411.931.7200.94091.597.341505.932.6500.93094.0101.081605.433.5950.94599.5105.291710.634.5750.980105.2107.351824.535.5250.950113.9119.891948.736.5050.980124.2126.73(aqu)2126.537.4050.900177.8197.562410.438.3650.960283.9295.732705.338.8650.500294.9589.80Datos
experimentalesVaso 2Vaco28.107Suspensin InicialPeso de
Solidos0.3315Caracteristicas de Filtracinpresion (psi)52+Suspensin
inicial65.8409Peso de Agua37.4024N de Marcos1temperatura
(C)30+Slidos28.4385mf (solidos/suspension)0.0088Suspensin
InicialSuspensin FinalPromedioLargo (m)0.152Vaso
5Vaco30.2156Suspensin FinalPeso de Solidos0.2073Concentracion de
slidos corregida, Cm ( Kg/m3 )8.84476.89797.8713Ancho
(m)0.152Propiedades Fisicas a 30 C+Suspensin final60.3985Peso de
Agua29.9756Radio de la Esquina0.025Densidad del Agua
(Kg/m3)995.68+Slidos30.4229mf (solidos/suspension)0.0069Altura
(m)0.012Viscocidad del Agua (Kg/m.s)0.0008007Vaso
6Vaco65.425TortaTorta Hmeda46.3099mf
(solidos/suspension)0.00880.00690.0078rea Efectiva
(m2)0.0211Densidad del CaCO3 (Kg/m3)2700+Torta hmeda111.7349Torta
Seca36.9233rea Total (m2)0.0423+Torta seca102.3483m (torta humeda/
torta seca)1.2542Para filtracin a Presin Constante :De la grfica se
obtienen los valores :Por las ecuaciones de Ruth se tiene
:Resistencia Especifica de la TortaResistencia del Medio
filtrantePorosidad de la torta :Densidad de la torta seca
(pts):entiendase como lecho ( solido + interticios)Volumen de
Suspensin Requerido :Volumen del Marco (m3)0.00025Solidos en la
Torta (Kg)0.4041Peso Suspensin Alimentada (Kg)51.6340Densidad de la
Suspensin (Kg/m3)1,000.6Volumen de Suspensin (m3)0.05160Volumen de
Filtrado Obtenido :Volumen de Filtrado (m3)0.05124Velocidad
Promedio de Filtracin :Velocidad de Filtracin (m3/h)0.023Tiempo de
Filtracin :Tiempo de filtracin (s)8,070.97Tiempo de filtracin
(min)134.52P=52lb/plg24.90000000000000045.850000000000000510.7313.616.5218.39999999999999920.2322.13500000000000224.04500000000000225.9426.9127.9129.8330.77999999999999831.7232.6533.59499999999999934.57499999999999635.52499999999999936.50499999999999511.47368421052632211.47368421052632211.19999999999999611.47368421052632211.19999999999999611.47368421052632211.19999999999999611.47368421052632261.48936170212767463.67346938775511265.571.93548387096771575.60439560439554975.179487179487147581.66666666666664382.57731958762889283.90000000000009188.526315789473692.42105263157914497.340425531914903101.07526881720429105.29100529100529107.34693877551003119.89473684210536126.7346938775510736.50499999999999537.40499999999999438.36499999999999538.864999999999995126.73469387755107197.55555555555549295.7291666666668589.80000000000018
V(L)
t/V
compresibilidadMETODO DE RUTH - METODO DIFERENCIALP (psi)P
(Pa) (m/Kg)LOG PLOG
17117,2101.4110E+115.069011.149535241,3152.3790E+115.382611.376452358,5245.8270E+115.554511.7654De
la grfican1.2019Log 05.018001.0423E+05PorosidadP
(psi)porosidad170.41350.39520.415.06896429541747215.38258341838947365.554518717673997411.14952701375434811.37639444203726711.76544501809015
LOG(P)
LOG
1735520.410.390.41P(kPa)
comparacinMETODO DE RUTH - METODO
DIFERENCIALP=17lb/pulg2P=35lb/pulg2P=52lb/pulg2t
AcumuladoVolumen(L)V (L)tt/Vt AcumuladoVolumen(L)Vtt/Vt
AcumuladoVolumen(L)Vtt/V28.70.9700.97028.729.5920.30.9700.97020.320.934.00.9600.9604.04.17106.91.9450.97578.280.2131.81.9701.00011.511.5011.31.9200.9607.37.60144.62.8550.91037.741.4338.72.9100.9406.97.3420.12.9201.0008.88.80226.53.7950.94081.987.1350.33.9101.00011.611.6030.13.9000.98010.010.20313.64.7450.95087.191.68103.44.8400.93053.157.1041.34.9001.00011.211.20403.55.7150.97089.992.68117.35.7800.94013.914.7952.25.8500.95010.911.47453.76.6250.91050.255.16134.86.7350.95517.518.32108.36.8300.98056.157.24550.27.6000.97596.598.97154.57.7200.98519.720.00121.27.8501.02012.912.65647.38.5300.93097.1104.41215.98.7100.99061.462.02137.48.8901.04016.215.58754.69.5000.970107.3110.62238.59.6800.97022.623.30152.79.7900.90015.317.00859.710.4400.940105.1111.81303.910.6600.98065.466.73210.510.7300.94057.861.491006.511.3650.925146.8158.70330.311.6300.97026.427.22230.611.6700.94020.121.381180.912.3250.960174.4181.67358.412.6000.97028.128.97248.912.6200.95018.319.261238.513.2850.96057.660.00427.813.5500.95069.473.05311.313.6000.98062.463.671401.214.2550.970162.7167.73500.414.5300.98072.674.08334.514.5300.93023.224.951528.115.2150.960126.9132.19531.515.4550.92531.133.62359.015.5200.99024.524.751701.516.1850.970173.4178.76603.516.3750.92072.078.26424.516.5201.00065.565.501836.517.1150.930135.0145.16635.817.3550.98032.332.96452.417.4700.95027.929.372021.918.0750.960185.4193.13713.818.3350.98078.079.59519.318.4000.93066.971.942210.719.0100.935188.8201.93752.919.2950.96039.140.73546.519.3200.92027.229.572409.319.9600.950198.6209.05834.320.2550.96081.484.79615.320.2300.91068.875.602620.520.9150.955211.2221.15914.921.2150.96080.683.96646.221.1600.93030.933.232847.821.8700.955227.3238.01(aqu)957.322.1450.93042.445.59719.522.1350.97573.375.183135.622.8300.960287.8299.791046.523.1050.96089.292.92754.923.1050.97035.436.493458.223.7900.960322.6336.041138.624.0350.93092.199.03825.424.0450.94070.575.003930.224.7500.960472.0491.671230.624.9650.93092.098.92858.024.9800.93532.634.874435.625.4300.680505.4743.241331.825.9450.980101.2103.27936.425.9400.96078.481.671434.526.9050.960102.7106.981016.526.9100.97080.182.581542.527.8350.930108.0116.131100.427.9101.00083.983.901659.428.8351.000116.9116.901148.528.8800.97048.149.591820.729.7850.950161.3169.791232.629.8300.95084.188.531953.230.7400.955132.5138.74(aqu)1320.430.7800.95087.892.422141.531.6750.935188.3201.391411.931.7200.94091.597.342422.632.6350.960281.1292.811505.932.6500.93094.0101.082743.433.2850.650320.8493.541605.433.5950.94599.5105.291710.634.5750.980105.2107.351824.535.5250.950113.9119.891948.736.5050.980124.2126.73(aqu)2126.537.4050.900177.8197.562410.438.3650.960283.9295.732705.338.8650.500294.9589.8017
psi35 psi52 psipromedioPeso de Filtrado LbTiempo de filtracin,
minPresin de filtracin, lbs/pulg2Concentracion de slidos corregida,
Cm ( Kg/m3
)30.188815.95197.871318.00401020308.03.172.681.9214.67.666.124.22Volumen
del Marco
(m3)0.000250.000250.0002521.212.7510.107.1727.820.5015.1210.6334.429.2521.1214.83Solidos
en la Torta
(Kg)0.40410.41780.40410.408741.039.8027.8919.5041.652.1035.1824.9754.265.3043.8542.11Peso
Suspensin Alimentada
(Kg)13.889026.721251.634060.880.5053.87-------67.498.5066.66-------74.0124.70--------------Densidad
de la Suspensin (Kg/m3)1,016.21,006.51,000.6Nmero de
Malla325Dimetro de la partcula (mm)44Concentracin2%Volumen de
Suspensin (m3)0.013670.026550.05160Presin(psi)Presin(Kgf/m2)Caudal
Promedio(Kg/s)Volumen de Filtrado (m3)0.013280.026090.05124Tesis
Pedro Torres Arias3021110.709.73E-032014073.807.64E-03Velocidad de
Filtracin
(m3/h)0.0220.0330.023107036.904.49E-03Nuestros1711962.733.89E-033524629.151.06E-02Tiempo
de filtracin
(s)2,131.572,854.708,070.975236591.881.46E-02P=17lb/plg20.971.94499999999999982.8553.79499999999999994.74500000000000015.71499999999999996.6257.68.52999999999999949.510.4411.36512.32499999999999913.28514.25500000000000115.21516.18499999999999917.11499999999999818.07499999999999919.00999999999999819.95999999999999720.91499999999999621.86999999999999422.82999999999999523.78999999999999624.74999999999999625.42999999999999629.58762886597938380.20512820512820441.42857142857141687.12765957446809891.68421052631582392.68041237113399755.16483516483515498.974358974359035104.40860215053753110.618556701031111.8085106382979158.70270270270265181.6666666666667759.999999999999908167.73195876288665132.18749999999986178.76288659793823145.16129032258064193.12500000000011201.92513368983927209.05263157894777221.15183246073281238.01047120418869299.7916666666664336.04166666666657491.66666666666669743.23529411764775P=35lb/plg20.971.972.913.914.845.77999999999999946.73499999999999947.728.70999999999999919.6810.6611.6312.60000000000000113.5514.53000000000000115.45500000000000216.37500000000000417.35500000000000418.33500000000000419.29500000000000520.25500000000000621.21500000000000722.14500000000000723.10500000000000824.03500000000000724.96500000000000725.94500000000000726.90500000000000827.83500000000000828.83500000000000829.78500000000000730.74000000000000631.67500000000000432.63500000000000533.28500000000000420.92783505154639211.57.340425531914895911.59999999999999457.09677419354839114.78723404255318418.32460732984294819.99999999999998962.02020202020202823.29896907216494466.73469387755099527.2164948453608628.96907216494841873.05263157894741374.08163265306119233.62162162162164278.26086956521739132.9591836734693479.59183673469388540.72916666666669384.79166666666664383.95833333333335745.59139784946233992.91666666666671499.03225806451602998.924731182795696103.26530612244903106.97916666666671116.12903225806451116.90000000000009169.78947368421049138.7434554973822201.39037433155073292.81249999999994493.53846153846177P=52lb/plg20.961.922.923.94.90000000000000045.85000000000000056.837.858.899.790000000000000910.7311.6712.6213.614.5315.5216.5217.4718.39999999999999919.3220.2321.1622.13500000000000223.10524.04500000000000224.9825.9426.9127.9128.8829.8330.77999999999999831.7232.6533.59499999999999934.57499999999999635.52499999999999936.50499999999999537.40499999999999438.36499999999999538.8649999999999954.1666666666666677.60416666666666798.800000000000000710.20408163265306111.19999999999999611.47368421052632257.24489795918366812.64705882352941715.57692307692307816.99999999999998261.48936170212767421.3829787234042519.26315789473685763.67346938775511224.9462365591397724.74747474747474765.529.36842105263155771.93548387096771529.56521739130439775.60439560439554933.22580645161299675.1794871794871436.4948453608247197534.8663101604278381.66666666666664382.57731958762889283.90000000000009149.58762886597929188.526315789473692.42105263157914497.340425531914903101.07526881720429105.29100529100529107.34693877551003119.89473684210536126.73469387755107197.55555555555549295.7291666666668589.80000000000018
V(L)
t/V
Tesis21110.714073.8000000000017036.90000000000059.7303007994933906E-37.6437558755875594E-34.4861881849772786E-3Nuestros11962.73000000000124629.1536591.8800000000053.8859289293036395E-31.0564526162517414E-21.4632981930588986E-2Presin (Kgf/m2)
DV/Dt (Kg/s)
![Equipos de-filtracion-y-filtracion-por-membrana[1]](https://static.fdocuments.co/doc/165x107/58852d2b1a28abf7538b7e7d/equipos-de-filtracion-y-filtracion-por-membrana1.jpg)
