The supplemental combustion in HRSG systems takes place in a burner which usually is located in the flue gas stream going to the HRSG. However, some systems because of high firing requirements and low O2 in the flue gas, may require to be fired externally to the flue gas stream and may reuire additional combustion air. The types of burners and how they function are not covered in detail in this section. The amount of heat released can be easily calculated for a gas when we know the composition of the fuel and the heating values of the various components. For liquid fuels, the heating values are obtained by a calorimeter test.
From these values and using the standard combustion equation, we can determine the composition of the flue gas leaving the burner. As an example, the combustion of methane could be stated :
The following Lower Heating Values(LHV) are used in this script:
Component | Btu/lb | Component | Btu/lb | Component | Btu/lb |
CH4 | 21,520 | C2H6 | 20,432 | C3H8 | 19,944 |
N-C4H10 | 19,680 | I-C4H10 | 19,629 | N-C5H12 | 19,517 |
I-C5H12 | 19,478 | C6H14 | 19,403 | CO | 4,347 |
H2 | 51,623 | N2 | 0 | CO2 | 0 |
C | 14,093 | S | 3,983 | C2H4 | 20,295 |
C3H6 | 19,691 | C4H8 | 19,496 | C6H6 | 17,480 |
H2O | 0 | O2 | 0 | H2S | 6,545 |
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The formulas, correlations, and methods presented herein should not be considered as being recommended by or used by the sponsors of this site. The purpose of this site is educational and the methods may or may not be suitable for actual design of equipment. Only a fired heater design engineer is qualified to decide if a calculation or procedure is correct for an application.