Gpa Standard 2145-09

PHYSICAL PROPERTIES OF SELECTED HYDROCARBONS - GPA STANDARD 2145 - 09 (FPS) BECOMES EFFECTIVE JANUARY1, 2009

C6+ 47/35/17 PROPANE i-BUTANE n-BUTANE NEOPENTANE i-PENTANE n-PENTANE NITROGEN METHANE CARBON DIOXIDE ETHANE

HV inf MJ/M3 HV Sup MJ/Kg Gross Dry BTU Net Dry BTU HV Sup MJ/M3 HV inf MJ/Kg Gals/1000 SCF Reid Vapor LBs/Gal Rel Dens Gal Rel Dens Lqd Mole Weight 5276.5 4889.307 196.983 182.518 48.557 44.9878 0.446214 3.019 5.669 3.313 0.680 95.9558 2516.1 2315 93.934 86.42 50.369 46.34 0.275429 188.62 4.2285 1.5225 0.50719 44.0956 3251.9 3000 121.4 112 49.388 45.564 0.327158 72.644 4.6925 2.0068 0.56283 58.1222 3262.3 3011 121.79 112.4 49.546 45.726 0.315183 51.567 4.8706 2.0068 0.5842 58.1222 3993.9 3691.4 148.76 137.49 48.75 45.06 0.383 35.9 4.975 2.4911 0.5967 72.15 4000.9 3699 149.36 138.1 48.95 45.258 0.365621 20.474 5.212 2.4911 0.62514 72.1488 4008.7 3707 149.65 138.4 49.045 45.356 0.362396 15.576 5.2584 2.4911 0.63071 72.1488 0.0 0 0 0 0 0 0.10999 0 6.7271 0.9672 0.80687 28.0134 1010.0 909.4 37.706 33.95 55.575 50.038 0.169487 5000 2.5 0.5539 0.3 16.0425 0.0 0 0 0 0 0 0.170618 0 6.8129 1.5195 0.81716 44.0095 1769.7 1619 66.066 60.43 51.951 47.519 0.267369 800 2.9704 1.0382 0.35628 30.069

CALCULO PORCENTAJES PARA C6+ 47/35/17 (C6, C7 Y C8) Gross Dry BTU Net Dry BTU Gross Dry BTU (SI) Net Dry BTU (SI) Gross Dry BTU (SI) C6 4755.9 4404 177.550 164.39 48.715 c7 5502.6 5100 205.420 190.39 48.474 c8 6249 5796 233.290 216.38 48.29 47/36/17 C6/C7/C8 METHOD C6 47% 2257.435 2090.403 84.276 78.029 23.123 0.000 C7 35% 1944.619 1802.340 72.595 67.284 17.131 0.000 C8 17 % 1074.453 996.564 40.112 37.204 8.303 0.000 C6+ 5276.507 4889.307 196.983 182.518 48.557 0.000 NOTA

Se realizo el cambio total de la tabla de componentes según la Tabla GPA 2145-2009

0.000 0.000 0.000 0.000

4.961 1.619 0.5349

5.5364 5.7379 5.8907

2.9754 3.4597 3.944

0.66406 0.68823 0.70655

86.1754 100.2019 114.2285

2.355 0.572 0.092 3.019

2.628 2.028 1.013 5.669

1.412 1.223 0.678 3.313

0.315 0.243 0.121 0.680

40.904 35.411 19.640 95.9558

AGA 8 C6mix1 PROPANE i-BUTANE n-BUTANE i-PENTANE i-PENTANE n-PENTANE NITROGEN METHANE CO2 ETHANE



Gross Dry BTU Net Dry BTU HV Sup MJ/M3 HV inf MJ/M3 HV Sup MJ/Kg HV inf MJ/Kg Gals/1000 SCF Reid Vapor LBs/Gal Rel Dens Gal Rel Dens Lqd Mole Weight 5276.5 4889.31 196.983 182.521 48.558 44.989 0.44618 3.01956 5.6689 3.31351 0.67996 95.9557 C6mix1 2516.2 2315 93.936 86.419 50.37 46.34 0.27534 188.69 4.2301 1.5227 0.50738 44.096 PROPANE 3252 3000 121.4 112.01 49.389 45.568 0.32709 72.484 4.6934 2.0071 0.56295 58.122 i-BUTANE 3262.4 3011 121.79 112.4 49.547 45.726 0.31525 51.683 4.8696 2.0071 0.58408 58.122 n-BUTANE 3993.9 3691.4 148.76 137.49 48.75 45.06 0.383 35.9 4.975 2.4911 0.5967 72.15 i-PENTANE 4000.9 3699 149.36 138.09 48.95 45.255 0.36594 20.456 5.2074 2.4914 0.6246 72.149 i-PENTANE 4008.7 3707 149.66 138.38 49.046 45.35 0.36216 15.558 5.2618 2.4914 0.63113 72.149 n-PENTANE 0 0 0 0 0 0 0.10965 0 6.727 0.9673 0.80687 28.013 NITROGEN 1010 909 37.707 33.949 55.576 50.037 0.26412 5000 2.5 0.55397 0.3 16.042 METHANE 0 0 0 0 0 0 0.16946 0 6.8534 1.5197 0.82203 44.01 CO2 1769.7 1619 66.067 60.429 51.952 47.518 0.26729 800 2.9716 1.0383 0.35643 30.069 ETHANE

FPS


VARIABLE EN GPA BTU GROSS BTU NEY REID VAPOR DENS. ABS DENS. REL GAS DENS. REL LIQUID MOLAR WEIGHT

SI

FPS

Gross Dry BTU Net Dry BTU HV Sup MJ/M3 HV inf MJ/M3 HV Sup MJ/Kg HV inf MJ/Kg Gals/1000 SCF Reid Vapor LBs/Gal Rel Dens Gal Rel Dens Lqd Mole Weight -0.007394 0.003120 0.000000 0.003000 0.001200 0.001200 -0.000034 0.000646 0.000372 0.000417 0.000053 -0.000115114 C6mix1 0.100000 0.000000 0.002000 -0.001000 0.001000 0.000000 -0.000089 0.070000 0.001600 0.000200 0.000190 0.0004 PROPANE 0.100000 0.000000 0.000000 0.010000 0.001000 0.004000 -0.000068 -0.160000 0.000900 0.000300 0.000120 -0.0002 i-BUTANE 0.100000 0.000000 0.000000 0.000000 0.001000 0.000000 0.000067 0.116000 -0.001000 0.000300 -0.000120 -0.0002 n-BUTANE 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 0.0000 i-PENTANE 0.000000 0.000000 0.000000 -0.010000 0.000000 -0.003000 0.000319 -0.018000 -0.004600 0.000300 -0.000540 0.0002 i-PENTANE 0.000000 0.000000 0.010000 -0.020000 0.001000 -0.006000 -0.000236 -0.018000 0.003400 0.000300 0.000420 0.0002 n-PENTANE 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 -0.000340 0.000000 -0.000100 0.000100 0.000000 -0.0004 NITROGEN 0.000000 -0.400000 0.001000 -0.001000 0.001000 -0.001000 0.094633 0.000000 0.000000 0.000070 0.000000 -0.0005 METHANE 0.000000 0.000000 0.000000 0.000000 0.000000 0.000000 -0.001158 0.000000 0.040500 0.000200 0.004870 0.0005 CO2 0.000000 0.000000 0.001000 -0.001000 0.001000 -0.001000 -0.000079 0.000000 0.001200 0.000100 0.000150 0.0000 ETHANE

COLUMNAS QUE SE TIENEN QUE CAMBIAR DATOS MON2000 Gross Dry BTU Net Dry BTU Reid Vapor LBs/Gal Rel Dens Gal Rel Dens Lqd Mole Weight



Gross Dry BTU Gross Dry BTU Net Dry BTU Net Dry BTU HV Sup MJ/M3 HV Sup MJ/M3 HV inf MJ/M3 HV inf MJ/M3 HV Sup MJ/Kg HV Sup MJ/Kg HV inf MJ/Kg HV inf MJ/Kg Gals/1000 SCF Gals/1000 SCF Reid Vapor Reid Vapor LBs/Gal LBs/Gal Rel Dens Gal Rel Dens Gal Rel Dens Lqd Rel Dens Lqd Mole Weight Mole Weight 5276.5 5276.5 4889.307 4889.31 196.983 196.983 182.518 182.521 48.557 48.558 44.9878 44.989 0.446214 0.44618 3.019 3.01956 5.669 5.6689 3.313 3.31351 0.680 0.67996 95.9558 95.9557 2516.1 2516.2 2315 2315 93.934 93.936 86.42 86.419 50.369 50.37 46.34 46.34 0.275429 0.27534 188.62 188.69 4.2285 4.2301 1.5225 1.5227 0.50719 0.50738 44.0956 44.096 3251.9 3252 3000 3000 121.4 121.4 112 112.01 49.388 49.389 45.564 45.568 0.327158 0.32709 72.644 72.484 4.6925 4.6934 2.0068 2.0071 0.56283 0.56295 58.1222 58.122 3262.3 3262.4 3011 3011 121.79 121.79 112.4 112.4 49.546 49.547 45.726 45.726 0.315183 0.31525 51.567 51.683 4.8706 4.8696 2.0068 2.0071 0.5842 0.58408 58.1222 58.122 3993.9 3993.9 3691.4 3691.4 148.76 148.76 137.49 137.49 48.75 48.75 45.06 45.06 0.383 0.383 35.9 35.9 4.975 4.975 2.4911 2.4911 0.5967 0.5967 72.15 72.15 4000.9 4000.9 3699 3699 149.36 149.36 138.1 138.09 48.95 48.95 45.258 45.255 0.365621 0.36594 20.474 20.456 5.212 5.2074 2.4911 2.4914 0.62514 0.6246 72.1488 72.149 4008.7 4008.7 3707 3707 149.65 149.66 138.4 138.38 49.045 49.046 45.356 45.35 0.362396 0.36216 15.576 15.558 5.2584 5.2618 2.4911 2.4914 0.63071 0.63113 72.1488 72.149 0.0 0 0 0 0 0 0 0 0 0 0 0 0.10999 0.10965 0 0 6.7271 6.727 0.9672 0.9673 0.80687 0.80687 28.0134 28.013 1010.0 1010 909.4 909 37.706 37.707 33.95 33.949 55.575 55.576 50.038 50.037 0.169487 0.26412 5000 5000 2.5 2.5 0.5539 0.55397 0.3 0.3 16.0425 16.042 0.0 0 0 0 0 0 0 0 0 0 0 0 0.170618 0.16946 0 0 6.8129 6.8534 1.5195 1.5197 0.81716 0.82203 44.0095 44.01 1769.7 1769.7 1619 1619 66.066 66.067 60.43 60.429 51.951 51.952 47.519 47.518 0.267369 0.26729 800 800 2.9704 2.9716 1.0382 1.0383 0.35628 0.35643 30.069 30.069

CALCULO PORCENTAJES PARA C6+ 47/35/17 (C6, C7 Y C8) C6 c7 c8 C6 47% C7 35% C8 17 % C6+ NOTA

Gross Dry BTU 4755.9 5502.6 6249

Net Dry BTU 4404 5100 5796

Gross Dry BTU (SI) 177.550 205.420 233.290

Net Dry BTU (SI) 164.39 190.39 216.38

Gross Dry BTU (SI) 48.715 48.474 48.29

2257.435 1944.619 1074.453 5276.507

2090.403 1802.340 996.564 4889.307

84.276 72.595 40.112 196.983

78.029 67.284 37.204 182.518

23.123 17.131 8.303 48.557

Se realizo el cambio total de la tabla de componentes según la Tabla GPA 2145-2009

47/36/17 C6/C7/C8 METHOD 0.000 0.000 0.000 0.000

0.000 0.000 0.000 0.000

4.961 1.619 0.5349

5.5364 5.7379 5.8907

2.9754 3.4597 3.944

0.66406 0.68823 0.70655

86.1754 100.2019 114.2285

2.355 0.572 0.092 3.019

2.628 2.028 1.013 5.669

1.412 1.223 0.678 3.313

0.315 0.243 0.121 0.680

40.904 35.411 19.640 95.9558

AGA 8 C6mix1 PROPANE i-BUTANE n-BUTANE i-PENTANE i-PENTANE n-PENTANE NITROGEN METHANE CO2 ETHANE

Gpa Standard 2145-09

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