User:Milton Beychok/Sandbox: Difference between revisions
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{| class = "wikitable" align="center" | {| class = "wikitable" align="center" | ||
|+ Table 1: Higher Heating Value (HHV) Of Various Fuels | |+ Table 1: Higher Heating Value (HHV) Of Various Fuels | ||
! Fuel!! Phase !! [[Molecular mass|Molecular <br>Weight]]!!k[[Joule|J]]/[[Mole (unit)|mol]]!! MJ/[[kg]] !! MJ/[[Metre (unit)|m]]<sup>3</sup> !! [[U.S. customary units|Btu]]/[[U.S. customary units|lb]] !! Btu/[[U.S. customary units|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"|gas | |||
| align="center"|2.016 | |||
| align="center"|286.84 | |||
| align="center"|141.79 | |||
| align="center"|12.75 | |||
| align="center"|60,986 | |||
| align="center"|324 | |||
|- | |||
| align="center"|[[Methane]] <ref name=Perry/><ref name=NIST>[http://webbook.nist.gov/chemistry/ NIST Chemistry WebBook]</ref> | |||
| align="center"|gas | |||
| align="center"|16.043 | |||
| align="center"|890.31 | |||
| align="center"|55.50 | |||
| align="center"|39.72 | |||
| align="center"|23,870 | |||
| align="center"|1,009 | |||
|- | |||
| align="center"|[[Ethane]] <ref name=Perry/><ref name=NIST/> | |||
| align="center"|gas | |||
| align="center"|30.069 | |||
| align="center"|1,559.88 | |||
| align="center"|51.88 | |||
| align="center"|69.59 | |||
| align="center"|22,313 | |||
| align="center"|1,768 | |||
|- | |||
| align="center"|[[Propane]] <ref name=Perry/><ref name=NIST/> | |||
| align="center"|gas | |||
| align="center"|44.096 | |||
| align="center"|2,220.05 | |||
| align="center"|50.35 | |||
| align="center"|99.05 | |||
| align="center"|21,654 | |||
| align="center"|2,516 | |||
|- | |||
| align="center"|[[Butane]] <ref name=Perry/><ref name=NIST/> | |||
| align="center"|gas | |||
| align="center"|58.122 | |||
| align="center"|2,878.52 | |||
| align="center"|49.53 | |||
| align="center"|128.43 | |||
| align="center"|21,301 | |||
| align="center"|3,263 | |||
|- | |||
| align="center"|[[Ethanol]] <ref name=NIST/> | |||
| align="center"|liquid | |||
| align="center"|46.086 | |||
| align="center"|1,368.49 | |||
| align="center"|29.69 | |||
| align="center"| | |||
| align="center"|12,722 | |||
| align="center"| | |||
|- | |||
| align="center"|[[Gasoline]] <ref>HHV assumed same as [[iso-octane]] in ''[[Perry's Chemical Engineers' Handbook]]''</ref> | |||
| align="center"|liquid | |||
| align="center"|110 | |||
| align="center"|5,461.33 | |||
| align="center"|49.65 | |||
| align="center"| | |||
| align="center"|21,354 | |||
| align="center"| | |||
|- | |||
| align="center"|[[Kerosene]] <ref name=Various>Average of various sources</ref> | |||
| align="center"|liquid | |||
| align="center"|175 | |||
| align="center"|8,084.99 | |||
| align="center"|46.20 | |||
| align="center"| | |||
| align="center"|19,871 | |||
| align="center"| | |||
|- | |||
| align="center"|[[Diesel oil]] <ref name=Various/> | |||
| align="center"|liquid | |||
| align="center"|225 | |||
| align="center"|10,124.98 | |||
| align="center"|45.00 | |||
| align="center"| | |||
| align="center"|19,355 | |||
| 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"|solid | |||
| align="center"|13.33 | |||
| align="center"|340.98 | |||
| align="center"|25.58 | |||
| align="center"| | |||
| align="center"|11,002 | |||
| align="center"| | |||
|- | |||
| 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"| | |||
| align="center"| | |||
| align="center"|21.14 | |||
| align="center"| | |||
| align="center"|9,093 | |||
| align="center"| | |||
|- | |||
| align="center"|[[Peat]] (dry) <ref>[http://www.diva-portal.org/diva/getDocument?urn_nbn_se_kth_diva-3164-2_fulltext.pdf 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</ref> | |||
| align="center"|solid | |||
| align="center"| | |||
| align="center"| | |||
| align="center"|22.09 | |||
| align="center"| | |||
| align="center"|9,500 | |||
| align="center"| | |||
|} | |||
{| class = "wikitable" align="center" | |||
|+ Table 1: Lower Heating Value (HHV) Of Various Fuels | |||
! Fuel!! Phase !! [[Molecular mass|Molecular <br>Weight]]!!k[[Joule|J]]/[[Mole (unit)|mol]]!! MJ/[[kg]] !! MJ/[[Metre (unit)|m]]<sup>3</sup> !! [[U.S. customary units|Btu]]/[[U.S. customary units|lb]] !! Btu/[[U.S. customary units|ft]]<sup>3 </sup> | ! Fuel!! Phase !! [[Molecular mass|Molecular <br>Weight]]!!k[[Joule|J]]/[[Mole (unit)|mol]]!! MJ/[[kg]] !! MJ/[[Metre (unit)|m]]<sup>3</sup> !! [[U.S. customary units|Btu]]/[[U.S. customary units|lb]] !! Btu/[[U.S. customary units|ft]]<sup>3 </sup> | ||
|- | |- |
Revision as of 22:23, 20 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) [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 | 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 [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