6 Temmuz 2014 Pazar
Calculating Vapor Pressures of Mixtures
Component | % vol. at 70°F | lb/gal. at 70°F | lb. per 100 gal. at 70°F | % mass |
a | b | c =a * b | d = 100 * c / total c | |
Ethane | 0.57 | 3.200 | 1.824 | 0.41 |
Propane | 30.94 | 4.175 | 129.175 | 28.69 |
Isobutane | 62.69 | 4.646 | 291.258 | 64.70 |
N-butane | 5.80 | 4.817 | 27.939 | 6.20 |
Totals | 100.00 | 450.196 | 100.00 | |
Component | Molecular mass | lb.mols/ 100 gal. | Mol fraction | Vapor pressure at 70°F absolute, psi |
e | f=d / e | g = f / total f | h | |
Ethane | 30.068 | 0.061 | 0.007 | 570 |
Propane | 44.094 | 2.93 | 0.345 | 124 |
Isobutane | 58.120 | 5.011 | 0.591 | 46 |
N-butane | 58.120 | 0.481 | 0.057 | 31 |
Totals | 8.483 | 1.000 | ||
Component | Partial Pressure absolute, psi | Composition of vapor in equilibrium with liquid % by vol. |
||
i=g * h | j = 100 * i / total i | |||
Ethane | 3.99 | 5.27 | ||
Propane | 42.78 | 56.50 | ||
Isobutane | 27.19 | 35.90 | ||
N-butane | 1.77 | 2.33 | ||
Totals | 75.72 | 100.00 |
Flame Temperatures of Hydrocarbon Gases
Flame Temperature | Flame Speed in 1" Tube |
|||
°F | °C | in/s | m/s | |
Methane | 3416 | 1880 | 26 | 0.66 |
Ethane | 3443 | 1895 | 34 | 0.86 |
Propane | 3497 | 1925 | 32 | 0.81 |
N-butane | 3443 | 1895 | 33 | 0.84 |
Isobutane | 3452 | 1900 | 33 | 0.84 |
Ethylene | 3587 | 1975 | 65 | 1.65 |
Propylene | 3515 | 1935 | 39 | 0.99 |
Butylene | 3506 | 1930 | 38 | 0.97 |
Physical Properties of Hydrocarbons
NAME | METHANE | ETHENE | ETHANE | PROPENE | PROPANE | ISO-BUTANE | BUTENE-I | ISO-BUTENE | N-BUTANE | ISO-PENTANE | PENTENE-I | N-PENTANE |
FORMULA | CH4 | C2H4 | C2H6 | C3H6 | C3H8 | C4H10 | C4H8 | C4H8 | C4H10 | C5H12 | C5H10 | C5H12 |
Vapor pressure at 100F/17,8C | ||||||||||||
psi, gauge | 212.5 | 175.8 | 57.5 | 47.6 | 48.9 | 36.9 | 5.7 | 0.9 | ||||
psi, absolute | 780.0 | 227.2 | 190.0 | 72.2 | 62.3 | 63.6 | 51.6 | 20.4 | 19.4 | 15.6 | ||
bar, gauge | 14.7 | 12.1 | 4.0 | 3.3 | 3.4 | 2.5 | 0.4 | 0.1 | ||||
kilopascal, absolute | 5374.2 | 1565.4 | 1309.1 | 497.5 | 429.2 | 438.2 | 355.5 | 140.6 | 133.7 | 107.5 | ||
Normal state at 60F/15,6C and atmospheric pressure | gas | gas | gas | gas | gas | gas | gas | gas | gas | liquid | liquid | liquid |
Boiling point at atmospheric pressure | ||||||||||||
Fahrenheit | -258.7 | -154.7 | -127.5 | -53.9 | -43.7 | 10.9 | 20.7 | 19.6 | 31.1 | 82.1 | 85.9 | 96.9 |
Celsius | -161.5 | -103.7 | -88.6 | -47.7 | -42.1 | -11.7 | -6.3 | -6.9 | -0.5 | 27.9 | 30.0 | 36.1 |
Weight of liquid at 60F/15,6C | ||||||||||||
pound/US gal | 2.50 | 3.30 | 3.11 | 4.35 | 4.23 | 4.69 | 5.01 | 5.00 | 4.86 | 5.20 | 5.39 | 5.25 |
kg/m3 | 300 | 395 | 373 | 521 | 507 | 562 | 600 | 600 | 582 | 623 | 646 | 629 |
Specific gravity (water=1) | 0.300 | 0.374 | 0.522 | 0.508 | 0.563 | 0.601 | 0.600 | 0.584 | 0.625 | 0.646 | 0.631 | |
API gravity | 340.0 | 247.0 | 139.7 | 147.2 | 119.8 | 103.9 | 104.3 | 110.6 | 95.0 | 87.5 | 92.7 | |
Weight of vapor at 60F/15,6C and atmospheric pressure | ||||||||||||
pound/100 cubic feet | 4.23 | 7.39 | 7.92 | 11.09 | 11.62 | 15.31 | 14.79 | 14.79 | 15.31 | 19.01 | 19.01 | |
kg/m3 | 0.68 | 1.18 | 1.27 | 1.78 | 1.86 | 2.45 | 2.37 | 2.37 | 2.45 | 3.05 | 3.05 | |
Gross heat of combustion | ||||||||||||
BTU/pound | 23891 | 21650 | 22329 | 21060 | 21670 | 21265 | 20860 | 20740 | 21315 | 21046 | 20720 | 21094 |
BTU/cubic foot vapor @ 60F | 1012 | 1601 | 1783 | 2335 | 2558 | 3354 | 3084 | 3066 | 3368 | 4003 | 3829 | 4015 |
BTU/US gallon liquid @ 60F | 70910 | 69433 | 87740 | 91044 | 99097 | 103480 | 104060 | 103047 | 108820 | 110850 | 110125 | |
kcal/kg | 13260 | 12016 | 12393 | 11688 | 12027 | 11802 | 11577 | 11511 | 11830 | 11681 | 11500 | 11707 |
kcal/m3 vapor @ 15,6C | 9012 | 14257 | 15878 | 20793 | 22779 | 29867 | 27463 | 27303 | 29992 | 35647 | 34097 | 35754 |
kcal/litre liquid @ 15,6C | 4723 | 4624 | 5843 | 6064 | 6600 | 6892 | 6930 | 6863 | 7247 | 7383 | 7334 | |
MJ/kg | 55.48 | 50.27 | 51.85 | 48.90 | 50.32 | 49.38 | 48.44 | 48.16 | 49.50 | 48.87 | 48.11 | 48.98 |
MJ/m3 vapor @ 15,6C | 37.71 | 59.65 | 66.43 | 87.00 | 95.31 | 124.97 | 114.91 | 114.23 | 125.49 | 149.15 | 142.66 | 149.59 |
MJ/litre liquid @ 15,6C | 0.00 | 19.76 | 19.35 | 24.45 | 25.37 | 27.61 | 28.84 | 29.00 | 28.71 | 30.32 | 30.89 | 30.69 |
Air to burn gas | ||||||||||||
volume/volume vapor ratio @ 60F/15.6C, atmospheric pressure | 9.53 | 14.29 | 16.67 | 21.44 | 23.82 | 30.97 | 28.58 | 28.58 | 30.97 | 38.11 | 35.73 | 38.11 |
mass/mass ratio | 17.24 | 14.76 | 16.13 | 14.76 | 15.71 | 15.49 | 14.76 | 14.76 | 15.49 | 15.35 | 14.76 | 15.35 |
Flammability limits | ||||||||||||
Lower % in air | 5.0 | 3.2 | 3.0 | 2.0 | 2.4 | 1.8 | 1.9 | 1.3 | 1.6 | 1.4 | ||
Upper % in air | 15.0 | 12.5 | 15.0 | 11.0 | 9.5 | 8.4 | 8.4 | 7.8 | ||||
Heat required to vaporize liquid at boiling point and atmospheric pressure | ||||||||||||
BTU/pound | 245 | 208 | 211 | 189 | 183 | 158 | 174 | 167 | 166 | 146 | 148 | 153 |
BTU/US gallon liquid | 712 | 686 | 696 | 822 | 774 | 741 | 872 | 836 | 797 | 759 | 797 | 803 |
kcal/kg | 136.0 | 115.4 | 117.1 | 104.9 | 101.6 | 87.7 | 96.6 | 92.7 | 92.1 | 81.0 | 82.1 | 84.9 |
kcal/litre liquid | 47.4 | 45.7 | 46.4 | 54.7 | 51.5 | 49.4 | 58.1 | 55.7 | 53.1 | 50.5 | 53.1 | 53.5 |
Molecular Mass | 16.042 | 28.052 | 30.068 | 42.079 | 44.094 | 58.120 | 56.105 | 56.105 | 56.105 | 58.120 | 72.146 | 70.131 |
Specific heat at 60F/15,6C and atmospheric pressure | ||||||||||||
BTU/lb.F | ||||||||||||
Cp liquid | 0.540 | 0.555 | 0.550 | 0.533 | 0.536 | |||||||
Cp vapor | 0.527 | 0.362 | 0.410 | 0.352 | 0.389 | 0.387 | 0.347 | 0.397 | 0.388 | 0.397 | ||
Cv vapor | 0.402 | 0.288 | 0.343 | 0.298 | 0.342 | 0.352 | 0.303 | 0.363 | 0.361 | 0.370 | ||
Cp/Cv vapor | 1.308 | 1.258 | 1.193 | 1.180 | 1.133 | 1.097 | 1.145 | 1.094 | 1.076 | 1.074 | ||
KJ/kg.K | ||||||||||||
Cp liquid | 2.261 | 2.324 | 2.303 | 2.232 | 2.244 | |||||||
Cp vapor | 2.207 | 1.516 | 1.717 | 1.474 | 1.629 | 1.620 | 1.453 | 1.662 | 1.624 | 1.662 | ||
Cv vapor | 1.683 | 1.206 | 1.436 | 1.248 | 1.432 | 1.474 | 1.269 | 1.520 | 1.511 | 1.549 | ||
Cp/Cv vapor | 5.476 | 5.267 | 4.995 | 4.940 | 4.744 | 4.593 | 4.794 | 4.580 | 4.505 | 4.497 | ||
Critical Conditions | ||||||||||||
Temperature, Fahrenheit | -116.5 | 49.8 | 90.1 | 196.5 | 206.2 | 273.2 | 297.0 | 292.5 | 305.6 | 370.0 | 394.0 | 387.0 |
Temperature, Celsius | -82.5 | 9.9 | 32.3 | 91.4 | 96.8 | 134.0 | 147.2 | 144.7 | 152.0 | 187.6 | 201.0 | 197.2 |
Pressure, psi(a) | 673 | 742 | 708 | 667 | 617 | 529 | 588 | 580 | 551 | 483 | 594 | 490 |
Pressure, bar(a) | 46.4 | 51.2 | 48.8 | 46.0 | 42.5 | 36.5 | 40.5 | 40.0 | 38.0 | 33.3 | 41.0 | 33.8 |
Density, lbs/US gal | 1.351 | 1.695 | 1.888 | 1.946 | 1.891 | 1.955 | 1.935 | |||||
Density, kg/m3 | 161.9 | 203.1 | 226.2 | 233.2 | 226.6 | 234.3 | 231.9 |