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!!&nbsp;Phase&nbsp;!!&nbsp;[[Molecular mass|Molecular&nbsp;<br>Weight]]!!k[[Joule|J]]/[[Mole (unit)|mol]]!!&nbsp;MJ/[[kg]]&nbsp;!!&nbsp;MJ/[[Metre (unit)|m]]<sup>3</sup>&nbsp;!!&nbsp;[[U.S. customary units|Btu]]/[[U.S. customary units|lb]]&nbsp;!!&nbsp;Btu/[[U.S. customary units|ft]]<sup>3&nbsp;</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!!&nbsp;Phase&nbsp;!!&nbsp;[[Molecular mass|Molecular&nbsp;<br>Weight]]!!k[[Joule|J]]/[[Mole (unit)|mol]]!!&nbsp;MJ/[[kg]]&nbsp;!!&nbsp;MJ/[[Metre (unit)|m]]<sup>3</sup>&nbsp;!!&nbsp;[[U.S. customary units|Btu]]/[[U.S. customary units|lb]]&nbsp;!!&nbsp;Btu/[[U.S. customary units|ft]]<sup>3&nbsp;</sup>  
! Fuel!!&nbsp;Phase&nbsp;!!&nbsp;[[Molecular mass|Molecular&nbsp;<br>Weight]]!!k[[Joule|J]]/[[Mole (unit)|mol]]!!&nbsp;MJ/[[kg]]&nbsp;!!&nbsp;MJ/[[Metre (unit)|m]]<sup>3</sup>&nbsp;!!&nbsp;[[U.S. customary units|Btu]]/[[U.S. customary units|lb]]&nbsp;!!&nbsp;Btu/[[U.S. customary units|ft]]<sup>3&nbsp;</sup>  
|-  
|-  

Revision as of 22:23, 20 September 2008

Table 1: Higher Heating Value (HHV) Of Various Fuels
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


Table 1: Lower Heating Value (HHV) Of Various Fuels
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. ↑ 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. ↑ 2.0 2.1 2.2 2.3 2.4 2.5 2.6 2.7 2.8 2.9 NIST Chemistry WebBook
  3. ↑ HHV assumed same as iso-octane in Perry's Chemical Engineers' Handbook
  4. ↑ 4.0 4.1 4.2 4.3 Average of various sources
  5. ↑ 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.
  6. ↑ 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.
  7. ↑ 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
  8. ↑ HHV assumed same as iso-octane in Perry's Chemical Engineers' Handbook
  9. ↑ 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.
  10. ↑ 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.
  11. ↑ 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
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