User:Milton Beychok/Sandbox: Difference between revisions
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| align="center"|gas | | align="center"|gas | ||
| align="center"|2.016 | | align="center"|2.016 | ||
| align="center"| | | align="center"|285.84 | ||
| align="center"|141.79 | | align="center"|141.79 | ||
| align="center"|12.75 | | align="center"|12.75 | ||
Line 120: | Line 120: | ||
| align="center"|gas | | align="center"|gas | ||
| align="center"|2.016 | | align="center"|2.016 | ||
| align="center"| | | align="center"|241.83 | ||
| align="center"| | | align="center"|119.96 | ||
| align="center"| | | align="center"|10.79 | ||
| align="center"| | | align="center"|512,596 | ||
| align="center"| | | align="center"|274 | ||
|- | |- | ||
| align="center"|[[Methane]] <ref name=Perry/><ref name=NIST>[http://webbook.nist.gov/chemistry/ NIST Chemistry WebBook]</ref> | | align="center"|[[Methane]] <ref name=Perry/><ref name=NIST>[http://webbook.nist.gov/chemistry/ NIST Chemistry WebBook]</ref> | ||
| align="center"|gas | | align="center"|gas | ||
| align="center"|16.043 | | align="center"|16.043 | ||
| align="center"| | | align="center"|802.32 | ||
| align="center"| | | align="center"|50.01 | ||
| align="center"| | | align="center"|35.80 | ||
| align="center"| | | align="center"|21,511 | ||
| align="center"| | | align="center"|909 | ||
|- | |- | ||
| align="center"|[[Ethane]] <ref name=Perry/><ref name=NIST/> | | align="center"|[[Ethane]] <ref name=Perry/><ref name=NIST/> | ||
| align="center"|gas | | align="center"|gas | ||
| align="center"|30.069 | | align="center"|30.069 | ||
| align="center"|1, | | align="center"|1,427.84 | ||
| align="center"| | | align="center"|47.49 | ||
| align="center"| | | align="center"|63.70 | ||
| align="center"| | | align="center"|20,424 | ||
| align="center"|1, | | align="center"|1,618 | ||
|- | |- | ||
| align="center"|[[Propane]] <ref name=Perry/><ref name=NIST/> | | align="center"|[[Propane]] <ref name=Perry/><ref name=NIST/> | ||
| align="center"|gas | | align="center"|gas | ||
| align="center"|44.096 | | align="center"|44.096 | ||
| align="center"|2, | | align="center"|2,044.00 | ||
| align="center"| | | align="center"|46.35 | ||
| align="center"| | | align="center"|91.19 | ||
| align="center"| | | align="center"|19,937 | ||
| align="center"|2, | | align="center"|2,317 | ||
|- | |- | ||
| align="center"|[[Butane]] <ref name=Perry/><ref name=NIST/> | | align="center"|[[Butane]] <ref name=Perry/><ref name=NIST/> | ||
| align="center"|gas | | align="center"|gas | ||
| align="center"|58.122 | | align="center"|58.122 | ||
| align="center"|2, | | align="center"|2,658.45 | ||
| align="center"| | | align="center"|45.74 | ||
| align="center"| | | align="center"|118.61 | ||
| align="center"| | | align="center"|19,673 | ||
| align="center"|3, | | align="center"|3,013 | ||
|- | |- | ||
| align="center"|[[Ethanol]] <ref name=NIST/> | | align="center"|[[Ethanol]] <ref name=NIST/> | ||
| align="center"|liquid | | align="center"|liquid | ||
| align="center"|46.086 | | align="center"|46.086 | ||
| align="center"| | | align="center"| | ||
| align="center"| | | align="center"| | ||
| align="center"| | |||
| align="center"| | |||
| align="center"| | | align="center"| | ||
|- | |- |
Revision as of 23:05, 20 September 2008
Fuel | Phase | Molecular Weight |
kJ/mol | MJ/kg | MJ/m3 | Btu/lb | Btu/ft3 |
---|---|---|---|---|---|---|---|
Hydrogen [1] | gas | 2.016 | 285.84 | 141.79 | 12.75 | 60,986 | 324 |
Methane [1][2] | gas | 16.043 | 890.31 | 55.50 | 39.72 | 23,870 | 1,009 |
Ethane [1][2] | gas | 30.069 | 1,559.88 | 51.88 | 69.59 | 22,313 | 1,768 |
Propane [1][2] | gas | 44.096 | 2,220.05 | 50.35 | 99.05 | 21,654 | 2,516 |
Butane [1][2] | gas | 58.122 | 2,878.52 | 49.53 | 128.43 | 21,301 | 3,263 |
Ethanol [2] | liquid | 46.086 | 1,368.49 | 29.69 | 12,722 | ||
Gasoline [3] | liquid | 110 | 5,461.33 | 49.65 | 21,354 | ||
Kerosene [4] | liquid | 175 | 8,084.99 | 46.20 | 19,871 | ||
Diesel oil [4] | liquid | 225 | 10,124.98 | 45.00 | 19,355 | ||
Coal [5] | solid | 13.33 | 340.98 | 25.58 | 11,002 | ||
Wood (dry) [6] | solid | 21.14 | 9,093 | ||||
Peat (dry) [7] | solid | 22.09 | 9,500 |
Fuel | Phase | Molecular Weight |
kJ/mol | MJ/kg | MJ/m3 | Btu/lb | Btu/ft3 |
---|---|---|---|---|---|---|---|
Hydrogen [1] | gas | 2.016 | 241.83 | 119.96 | 10.79 | 512,596 | 274 |
Methane [1][2] | gas | 16.043 | 802.32 | 50.01 | 35.80 | 21,511 | 909 |
Ethane [1][2] | gas | 30.069 | 1,427.84 | 47.49 | 63.70 | 20,424 | 1,618 |
Propane [1][2] | gas | 44.096 | 2,044.00 | 46.35 | 91.19 | 19,937 | 2,317 |
Butane [1][2] | gas | 58.122 | 2,658.45 | 45.74 | 118.61 | 19,673 | 3,013 |
Ethanol [2] | liquid | 46.086 | |||||
Gasoline [8] | liquid | 110 | 5,461.33 | 49.65 | 21,354 | ||
Kerosene [4] | liquid | 175 | 8,084.99 | 46.20 | 19,871 | ||
Diesel oil [4] | liquid | 225 | 10,124.98 | 45.00 | 19,355 | ||
Coal [9] | solid | 13.33 | 340.98 | 25.58 | 11,002 | ||
Wood (dry) [10] | solid | 21.14 | 9,093 | ||||
Peat (dry) [11] | solid | 22.09 | 9,500 |
References
- ↑ 1.0 1.1 1.2 1.3 1.4 1.5 1.6 1.7 1.8 1.9 Perry, R.H. and Green, D.W. (Editors) (1997). Perry's Chemical Engineers' Handbook, 7th Edition. McGraw Hill. ISBN ISBN 0-07-049841-5.
- ↑ 2.0 2.1 2.2 2.3 2.4 2.5 2.6 2.7 2.8 2.9 NIST Chemistry WebBook
- ↑ HHV assumed same as iso-octane in Perry's Chemical Engineers' Handbook
- ↑ 4.0 4.1 4.2 4.3 Average of various sources
- ↑ There are a great many different coals. The values given here are of a single, specific bituminous coal on an "as received" basis which includes the ash and inherent moisture content of the coal.
- ↑ Table 1: Higher heating values for wood (oven dried) The values in this table are the average of oven-dried woods from 29 different species of trees, as listed in this publication of the U.S. Forest Service Laboratory.
- ↑ Thermal and Catalytic Upgrading in a Fuel Context: Peat, Biomass and Alkenes Thesis by Christina Hornell, Chemical Engineering Dept., Royal Institute of Technology, Stockholm, Sweden, 2001
- ↑ HHV assumed same as iso-octane in Perry's Chemical Engineers' Handbook
- ↑ There are a great many different coals. The values given here are of a single, specific bituminous coal on an "as received" basis which includes the ash and inherent moisture content of the coal.
- ↑ Table 1: Higher heating values for wood (oven dried) The values in this table are the average of oven-dried woods from 29 different species of trees, as listed in this publication of the U.S. Forest Service Laboratory.
- ↑ Thermal and Catalytic Upgrading in a Fuel Context: Peat, Biomass and Alkenes Thesis by Christina Hornell, Chemical Engineering Dept., Royal Institute of Technology, Stockholm, Sweden, 2001