 |
|
|
|
Combustion Data and Basic Calculations
For more detail and expanded information on multiple fuels, see North American Combustion Handbook, Vol. 1, B&W Steam book, and Perry’s Chemical Engineers’ Handbook.
RULES OF THUMB FOR COMBUSTION AIR ESTIMATION
For air volume:
Btu/hr input/6,000 = combustion air flow, scfm
For air mass:
765 lb/air required to burn 1 MM Btu of fuel
Example:
A 10 MM Btu/hr burner running at 0% excess air requires:
10,000,000/6,000 = 1,670 scfm air or 10 x 765 = 7,650 lb/hr air
CALCULATE ADIABATIC FLAME TEMPERATURE (AFT)
Q = M x Cp x temperature difference
Temperature difference = Q/(M x Cp)
Example: 1 mole CH4, 16 lb X LHV 21,500 Btu/lb = 344,000 Btu
At 100% excess air, M = 568 lb for air plus fuel
Temp diff = 344,000/(568 lb x 0.282) = 2,150 F
With 60 F base temperature at standard conditions:
Adiabatic Flame Temp = 60 + temp diff = 2,210 F
Caution: Cp varies with gas temp and gas; Use integrated heat capacities of gases in place of specific heat via equations or tables
|
SELECTED COMBUSTION CONSTANTS
|
COMPONENT
|
Mol
Weight
|
HHV Btu
per lb fuel
|
lb air reg'd
per lb fuel
|
Methane |
16
|
23,896
|
17.3
|
Ethane |
30
|
22,282
|
16.2
|
Propane |
44
|
21,523
|
15.7
|
Hydrogen |
2
|
60,991
|
34.3
|
Carbon Monoxide |
28
|
4,323
|
2.42
|
Carbon Dioxide |
44
|
--
|
--
|
Oxygen |
32
|
--
|
--
|
Nitrogen |
28
|
--
|
--
|
|
HEAT EXCHANGER EFFECTIVENESS
E = Ch * (Th in - Th out)/Cmin * (Th in - Tc in)
Where Cmin is the smaller of mhcph or mccpc, the hourly heat capacity
The rate of heat exchange is
Q = E Cmin * (Th in - Tc in)
Reference: F. Kreith, 3rd ed. Principles of Heat Transfer, Intext Education Publisher, NY, 1973
|
|
|
|
|
Copyright 2022 TMTS Associates, All Rights Reserved.
Click here for 1-page flyer
TMTS Associates, Inc. 399 Pavillion Street, Atlanta, GA 30315. 404-217-5410
tfmcgowan@tmtsassociates.com
|
 |