Supplementary Firing
Supplementary Firing
Supplementary firing is an excellent way to generate additional steam in cogeneration plants. Steam generators firing oil or gas have a lower heating value (LHV) efficiency of about 93%, while it is nearly 100% when the HRSG operates in the fired mode. That is, if
8 MW of additional energy is to be added to steam, a maximum of 8 MW of fuel on LHV basis alone need be fired in an HRSG. With a steam generator, one would fire about 6% more fuel or about 8.5 MW fuel unless it has a condensing economizer, which is a special case. To illustrate this point, an example is provided.
Example 5.7
Saturated steam is generated at 40 kg/cm 2 g in a boiler. In the unfired mode with an
exhaust gas of 100,000 kg/h at 500°C, the HRSG makes about 15.4 t/h. Determine the fuel required to generate 25 t/h and 40 t/h of steam.
Solution
The HRSG was simulated using a pinch point of 8°C and an approach point of 7°C. Results are summarized in Tables 5.3 and 5.4, and Figures 5.4 and 5.5 show the off- design performance runs.
We see that the additional fuel requirement is less than the boiler duty in the fired modes. To generate 25,000 kg/h, we are using only 5.84 MW of fuel energy while the additional duty is 6.3 MW! Similarly, to generate 40 t/h, we are using only 15.53 MW
274 Steam Generators and Waste Heat Boilers: For Process and Plant Engineers
TABLE 5.3
HRSG Performance—Design Case
Gas Wat./Stm. US, Temp. in/
Appr. kcal/h Module Surf.
In/Out,
out, °C °C
MW
kg/cm 2 a kg/h
°C
ch., °C °C No.
65,692 1 Note: Project—Example 5.7 Units—METRIC Case—Example 5.7 Remarks—Amb. temp., C = 20 heat loss,
% = 1 gas temp. to HRSG C = 500 gas flow, kg/h = 100,000 % vol CO 2 = 3. H 2 O = 7. N 2 = 75. O 2 = 15. SO 2 =. ASME eff, % = 68.41, tot. duty, MW = 10.1
TABLE 5.4
Off-Design Fired Performance
40,000 Boiler duty, MW
10.1 16.4 26.3 Burner duty, MW
0 5.84 15.53 Additional boiler duty, MW
0 6.3 16.2 Exit gas temperature, °C
139 Pinch point, °C
8 12 18 Approach point, °C
additional fuel while the additional duty is 16.2 MW! That means we are generating the additional steam at more than 100% efficiency in these cases! Hence, supplementary firing is more than 100% efficient. This was also seen in Chapter 4. The exit gas tempera- ture is lower in the fired mode for reasons given in Chapter 4. Again, the economizer is acting as a bigger heat sink when we increase the steam flow. Hence, the HRSG is more efficient in the fired mode. In a steam generator, the exit gas temperature increases with increase in steam generation as discussed in Chapter 4, while in an HRSG, it is the other way around. By firing fuel in an HRSG, we are in effect reducing excess air as we do not add air for this fuel but only utilize the excess oxygen in the exhaust gas.
Note that we assume the pinch and approach points only in the design mode. In fired cases, the pinch and approach points fall in place as the surface area has been selected by assuming pinch and approach points. We see that the pinch is 18°C and approach is 62°C in the 40 t/h case. How will one know what pinch and approach points to use if we had started the design in the fired mode? Yet another reason that we should always start the design in the unfired mode!
Parts
» For Process and Plant Engineers
» A Few Typical Solved Problems
» Excess Air from Flue Gas Analysis
» Simplified Combustion Calculations
» Relating Oxygen and Energy Input in Turbine Exhaust Gases
» Evaluating Fuel Quantity Required to Raise Turbine Exhaust Gas Temperature
» Simplified Formulae for Boiler Efficiency
» Firing Fuels with Low Heating Values
» Boiler duty and efficiency calculations
» Acid Dew Point Temperature T dp
» Steam Generator Furnace Design
» Advantages of Water-Cooled Furnaces
» Furnace Exit Gas Temperature Evaluation
» Empirical Formula for Furnace Duty Estimation
» Distribution of Radiation to Tube Banks
» External Radiation to Heat Transfer Surfaces at Furnace Exit
» Correlations for CHF (Critical Heat Flux) and Allowable Steam Quality
» Guidelines for Good Circulation System Design
» Emissions Affect Steam Generator Designs
» Adding Condensate Heater to Improve Boiler Plant Efficiency
» Understanding Boiler Surface Areas
» Steam Generators for Oil Sands Application
» Radiant versus Convective Superheaters
» Steam Inlet and Exit Nozzle Location
» Case Study of a Superheater with Tube Failure Problems
» Problem at Low Loads with Inverted-Loop Superheaters
» Data Required for Performing Steam Generator Analysis
» Evaluating Part Load Performance
» Tube Wall Temperature Estimation at Economizer Inlet
» Methods to Minimize Low-Temperature Corrosion Problems
» Water Chemistry, Carryover, Steam Purity
» Sizing and Performance Calculations
» Flue Gas Composition and Gas Pressure
» Heat Recovery in Sulfur Plants
» Heat Recovery in Sulfuric Acid Plant
» Heat Recovery in Hydrogen Plants
» Combining Solar Energy with Heat Recovery Systems
» Natural versus Forced Circulation HRSGs
» Optimizing Pinch and Approach Points in HRSGs
» HRSG Performance and Evaluating Field Data
» Advantages of Supplementary Firing in HRSGs
» Performance with and without Export Steam
» Cement Plant Waste Heat Recovery
» Fluid Heaters and Film Temperature
» Boiling Heat Transfer Coefficient h o
» Off-Design Performance with Addition of Economizer
» Simulation of Fire Tube Boiler Performance
» Simplified Approach to Evaluating Performance of Fire Tube Boilers
» Heat Transfer Inside and Outside Tubes
» Specifying Waste Heat Boilers
» Understanding Pinch and Approach Points
» Estimating Steam Generation and Gas–Steam Temperature Profiles
» Why Cannot We Arbitrarily Select the Pinch and Approach Points?
» Off-Design Performance Evaluation
» Single- or Multiple-Pressure HRSG
» Cogeneration Plant Application
» Water Dew Point of Flue Gases
» Condensation Heat Transfer Calculations
» Condensation over Finned Tubes
» Drum Coil Heater: Bath Heater Sizing
» Checking Heat Transfer Equipment for Noise and Vibration Problems
» Steam Drum Calculations Steam Velocity in Drum
» Flow Instability in Two-Phase Circuits
» Superheater Design and Off-Design Calculation
» NTU Method of Performance Evaluation (Number of Transfer Units)
» Appendix B: Tube-Side Heat Transfer Coefficients and Pressure Drop
» Another Method of Estimating h c for Water
» Importance of Streams in Superheater, Economizer
» Simplified Procedure for Evaluating Performance of Plain Tube Bundles
» Appendix D: Nonluminous Heat Transfer Calculations
» Determination of Heat Transfer Coefficient h c Convective Heat Transfer Coefficient
» How Is Life of Superheater Affected by High Tube Wall Temperatures?
» Effect of h i on Fin Selection
» Reduce Weight of Tube Bundles Using Smaller Tubes
» Effect of Outside Fouling Factor
» Effect of Fin Thickness and Conductivity
» Why Are Fins Not Used in Gas–Gas Exchangers?
» Appendix F: Properties of Gases
» Flue Gas Mixture Properties Calculation
» Appendix G: Quiz on Boilers and HRSGs with Answers
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