User:Milton Beychok/Sandbox: Difference between revisions
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! Fuel!! Phase !! Molecular <br>Weight!!kJ/mol!! MJ/kg !! MJ/m<sup>3</sup> !! Btu/lb !! Btu/ft<sup>3 </sup> | ! Fuel!! Phase !! Molecular <br>Weight!!kJ/mol!! MJ/kg !! MJ/m<sup>3</sup> !! Btu/lb !! Btu/ft<sup>3 </sup> | ||
|- | |- | ||
| align="center"|Hydrogen <ref name=Perry>{{cite book|author=Perry, R.H. and Green, D.W. (Editors)|title=[[Perry's Chemical Engineers' Handbook]]|edition=7th Edition|publisher=McGraw Hill|year=1997|id=ISBN ISBN 0-07-049841-5}}</ref> | | align="center"|[[Hydrogen]] <ref name=Perry>{{cite book|author=Perry, R.H. and Green, D.W. (Editors)|title=[[Perry's Chemical Engineers' Handbook]]|edition=7th Edition|publisher=McGraw Hill|year=1997|id=ISBN ISBN 0-07-049841-5}}</ref> | ||
| align="center"|gas | | align="center"|gas | ||
| align="center"|2.016 | | align="center"|2.016 | ||
| Line 12: | Line 12: | ||
| align="center"|324 | | align="center"|324 | ||
|- | |- | ||
| 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 | ||
| Line 21: | Line 21: | ||
| align="center"|1,009 | | align="center"|1,009 | ||
|- | |- | ||
| 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 | ||
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| align="center"|1,768 | | align="center"|1,768 | ||
|- | |- | ||
| 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 | ||
| Line 39: | Line 39: | ||
| align="center"|2,516 | | align="center"|2,516 | ||
|- | |- | ||
| 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 | ||
| Line 48: | Line 48: | ||
| align="center"|3,263 | | align="center"|3,263 | ||
|- | |- | ||
| 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 | ||
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| align="center"| | | align="center"| | ||
|- | |- | ||
| align="center"|Gasoline <ref>HHV assumed same as iso-octane in ''[[Perry's Chemical Engineers' Handbook]]''</ref> | | align="center"|[[Gasoline]] <ref>HHV assumed same as [[iso-octane]] in ''[[Perry's Chemical Engineers' Handbook]]''</ref> | ||
| align="center"|liquid | | align="center"|liquid | ||
| align="center"|110 | | align="center"|110 | ||
| Line 66: | Line 66: | ||
| align="center"| | | align="center"| | ||
|- | |- | ||
| align="center"|Kerosene <ref name=Various>Average of various sources</ref> | | align="center"|[[Kerosene]] <ref name=Various>Average of various sources</ref> | ||
| align="center"|liquid | | align="center"|liquid | ||
| align="center"|175 | | align="center"|175 | ||
| Line 75: | Line 75: | ||
| align="center"| | | align="center"| | ||
|- | |- | ||
| align="center"|Diesel oil <ref name=Various/> | | align="center"|[[Diesel oil]] <ref name=Various/> | ||
| align="center"|liquid | | align="center"|liquid | ||
| align="center"|225 | | align="center"|225 | ||
| Line 84: | Line 84: | ||
| align="center"| | | align="center"| | ||
|- | |- | ||
| align="center"|Coal <ref>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.</ref> | | align="center"|[[Coal]] <ref>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.</ref> | ||
| align="center"|solid | | align="center"|solid | ||
| align="center"|13.33 | | align="center"|13.33 | ||
| Line 93: | Line 93: | ||
| align="center"| | | align="center"| | ||
|- | |- | ||
| align="center"|Wood <ref>[http://www.fpl.fs.fed.us/documnts/fplgtr/fplgtr13.pdf 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.</ref> | | align="center"|[[Wood]] (dry) <ref>[http://www.fpl.fs.fed.us/documnts/fplgtr/fplgtr13.pdf 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.</ref> | ||
| align="center"|solid | | align="center"|solid | ||
| align="center"| | | align="center"| | ||
| Line 100: | Line 100: | ||
| align="center"| | | align="center"| | ||
| align="center"|9,093 | | align="center"|9,093 | ||
| align="center"| | |||
|- | |||
| align="center"|[[Peat]] (dry) <ref name=Various/> | |||
| align="center"|solid | |||
| align="center"| | |||
| align="center"| | |||
| align="center"|21.09 | |||
| align="center"| | |||
| align="center"|9,500 | |||
| align="center"| | | align="center"| | ||
|} | |} | ||
Revision as of 22:47, 19 September 2008
| Fuel | Phase | Molecular Weight |
kJ/mol | MJ/kg | MJ/m3 | Btu/lb | Btu/ft3 |
|---|---|---|---|---|---|---|---|
| Hydrogen [1] | gas | 2.016 | 286.84 | 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) [4] | solid | 21.09 | 9,500 |
References
- ↑ 1.0 1.1 1.2 1.3 1.4 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 NIST Chemistry WebBook
- ↑ HHV assumed same as iso-octane in Perry's Chemical Engineers' Handbook
- ↑ 4.0 4.1 4.2 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.