emisiones atm

Hoja1T (C) NMX-AA-054-SCFI-1978.27 g de C4H10 consumidosHnVACV2Pbcircular28Columna1GASES% Columna2PMColumna3peso total de humedadM2 (g)M1 (g)# moles de la humedadvolumen del vaporcondiciones a las que se encuentra el gasometro% humedadVgcPresin de vapor de aguaVaPresin barometricaDiametro 8D2Dlargo de la tuberiapuntodistancia del puntonumero de puntosNmero de punto transversal Factores de longitud, % Nmero de puntos transversales29O214.748688524632recacions que se llevan a cabo23.004.000.000.00ERROR:#DIV/0!ERROR:#DIV/0!ERROR:#DIV/0!23.00ERROR:#DIV/0!23.0030.00240.0060.00300.000.0551.6532468101214161820222430N285.23759508228Presion 1 (mm de Hg)30.000.1323.96610.1460.0670.0040.0330.0250.0210.0180.0160.0140.0130.0110.01130CO0.001260655728C4H10 +13/2 O2 4 CO2 + 5H2O88.88%Presion 2 (mm de Hg)30.000.236.9920.8540.250.1470.1050.0820.0670.0570.0480.0440.0390.0350.03230CO20.010085245944Temperatura 130.00030.750.2950.1940.1460.1160.0990.0850.0750.0670.060.05530SO2064C4H10 + 9/2 O2 4 CO + 5H2O11.20%Temperatura 230.00040.9330.7050.3230.2260.1270.1460.1250.1090.0970.0870.07830NO0.002370491839Presin manmetrica correspondiente al gasometro (mm de Hg)30.00050.8530.6770.3420.250.2010.1690.1460.1290.1160.10530C4H1056ESTEQUIMETRIA30.00060.9560.8060.6580.3550.2690.220.1880.1650.1460.1323030.00070.8950.7740.6450.3660.2830.2360.2040.180.16130MASA TANQUE GAS INICIAL 5.77KG30.00080.9670.8540.750.6340.3750.2960.250.2180.19430MASA TANQUE GAS FINAL 5.5KGC4H10130.00090.9180.8230.7310.6250.3820.3060.2810.2330MASA GAS 0.27KG CO2430.000100.8820.7990.7170.6180.3880.3150.27230MOLES DE L GAS (C4H10)0.0048214286CO430.000110.9330.8540.780.7040.6120.3930.32330H2O50120.9790.9010.8310.7640.6940.5070.39830O2(CO2)6.50O2(CO)4.5ABD AD B0PRODUCTOS DE GASES DE COMBUSTIONN23.7619047619cuadrados o rectangulares30150150Kmollextlado Alado BDiametropuntospuntos CO20.0169714286ERROR:#DIV/0!ERROR:#DIV/0!9CO0.0023142857OXIGENO QUE SE NECESITA PARA COMBUSTION COMPLETA0.0012H2O0.0241071429Q = A *V0.03133928570.00O2(CO2)0.0275785714BALANCEDE OXIGENO 0.00O2(CO)0.00260357140.00115714290.00N20.11354234690.000.000CM0.00no son circulares o cuadradosDATOS DE CHIMENEALOCALIZACION PUNTOS 4.80.00diametro Area interna de la seccion transversalPerimetro interno del conducto de la seccion transversalpuntodistancia de punto0.00ERROR:#DIV/0!ERROR:#DIV/0!DIAMETROCM0GASES DE COMBUSTION A LA SALIDA ERROR:#DIV/0!ERROR:#DIV/0!ALTURA 0%ERROR:#DIV/0!ERROR:#DIV/0!0CM CO20.016971428610.735136077119.2ERROR:#DIV/0!ERROR:#DIV/0!CO0.00231428571.4638821923ERROR:#DIV/0!ERROR:#DIV/0!H2O0.024107142915.2487728369O20.00115714290.7319410962N20.113542346971.82026779750.1580923469100

5.00

PARA APLICAR NMX 035

GASES% PMlado Alado BDiametrolargo de la tuberiaO214.7486885246322.003.002.405.00N285.2375950822884.7512271631CO0.001260655728CO20.010085245944SO2064NO0.002370491839nmx-035

H2O15.2487728369% humedadPMPM de la mezcla gaseosa en base humedadensidad normal de los gases kg/m3% CO20.4428.001.25% CO0.28PM2.7447791106H20% O20.323.9999022448O2% N2100.000.2820.2271741942N20.0002991579CO0.0037608427CO20SO20.0007835181NO26.9766990684d =1.2043169227

Hoja2Tiempo (min)% O2% N2CO (ppm)CO2 (ppm)SO2 (ppm)NO (ppm)020.9279.080000113.7286.2816128024213.1386.8723184026313.1986.8114112026415.3384.671080021513.786.313104026613.6486.361188027714.4185.591188025813.9286.0813104026914.9985.019720241014.0285.9812960271113.6886.3211880281213.8886.1210800281316.3483.668640191413.9186.09141120261513.4486.56131040291614.285.8151200251713.9686.04151200261814.3985.61191520241916.5183.49131040172014.4485.56151200242114.1785.83131040262214.4785.53171360252315.9984.01131040202414.4585.55151200252514.0485.96161280262614.485.6141120252715.884.212960212814.3585.65161280252914.1985.81151200263014.4485.56151200263115.2184.799720213215.9884.028640203314.6285.3811880243415.6784.338640213514.7885.229720243614.7485.269720243714.6685.3410800253815.4284.588640233914.6285.3810800254014.4185.5911880264114.5585.4510800264216.4983.519720184314.3885.6212960254414.7585.2510800244514.7985.2112960244615.184.911880224714.9585.05131040234814.3885.62141120264914.685.4141120255016.3283.6811880185115.0284.98131040235214.5385.47131040255314.5485.46161280255414.385.7141120265514.8685.1412960245615.0884.92161280235714.4285.58191520255814.4585.55211680225914.7985.21141120246015.2484.76118802214.748688524685.251311475412.606557377100.8524590164023.7049180328

Hoja3Nmero de punto transversal Factores de longitud, % Nmero de puntos transversales2468101214161820222410.1460.0670.0040.0330.0250.0210.0180.0160.0140.0130.0110.01120.8540.250.1470.1050.0820.0670.0570.0480.0440.0390.0350.032Diametro 8D2Dlargo de la tuberiapuntodistancia del puntonumero de puntos30.750.2950.1940.1460.1160.0990.0850.0750.0670.060.05530.00240.0060.00300.000.0852.55340.9330.7050.3230.2260.1270.1460.1250.1090.0970.0870.0780.226.6650.8530.6770.3420.250.2010.1690.1460.1290.1160.1050.62518.75960.9560.8060.6580.3550.2690.220.1880.1650.1460.132070.8950.7740.6450.3660.2830.2360.2040.180.161080.9670.8540.750.6340.3750.2960.250.2180.194090.9180.8230.7310.6250.3820.3060.2810.230100.8820.7990.7170.6180.3880.3150.2720110.9330.8540.780.7040.6120.3930.3230120.9790.9010.8310.7640.6940.5070.39800cuadrada o rectangularno son circulares o cuadradoslado Alado BDiametropuntospuntosdiametro Area interna de la seccion transversalPerimetro interno del conducto de la seccion transversalpuntodistancia de puntoERROR:#DIV/0!ERROR:#DIV/0!9ERROR:#DIV/0!ERROR:#DIV/0!