Advantages of Supplementary Firing in HRSGs
Advantages of Supplementary Firing in HRSGs
As discussed in Chapter 1, there is lot of oxygen in turbine exhaust gases that can be utilized to fire additional fuel to the exhaust gas and thus increase its temperature. Increase in inlet gas temperature generates additional steam in the evaporator, which increases the capac- ity of the heat sink, which is the economizer. Hence, the exit gas temperature beyond the economizer will be lower in the fired mode compared to the unfired mode. Since additional air is also not added, the lower exit gas temperature helps to increase the fuel utilization sig- nificantly. It can be shown through performance calculations that supplementary firing is an excellent way of generating additional steam in HRSGs and fuel utilization is nearly 100% or even more. That is, one can generate additional steam with nearly the same amount or lesser amount of fuel. In conventional steam generators, the LHV efficiency is about 93%, while in HRSGs, it can be close to 100% or even more. A layman’s explanation for this is as follows: when we increase excess air in steam generators, the efficiency decreases. In gas turbine HRSGs, we decrease the excess air by firing fuel into the oxygen-rich exhaust gas and hence efficiency is higher. In addition, the exit gas temperature from the economizer exit is lower when inlet gas temperature is higher and that contributes to the higher efficiency as well. The economizer acts as a larger heat sink in the fired mode due to the larger flow of water through it and hence is able to cool the exhaust gases to a lower temperature. Chapter 5 on simulation gives examples of improved fuel utilization with supplementary firing.
In Example 4.1, one may check the fuel utilization also. The difference in energy recovered between the unfired and fired cases for vendor A is (22.51 − 8.71) = 13.80 MM kcal/h, while only 13.0 MM kcal/h is fired on LHV basis. That means the fired case is more than 100% efficient. In the case of steam generators, the efficiency on LHV basis was shown to be about 93.5%. That is, by firing in an HRSG, we straightaway get more than 100% fuel utilization. If we look at vendor B, the additional energy from steam = 22.51 − 8.21 = 14.3 MM kcal/h, while
14.0 MM kcal/h is fired! Here again, it is more than 100% efficient. Thus, plant engineers may analyze the HRSG performance in both fired and unfired cases and understand how well the fuel energy is utilized. (The HRSG should have an economizer to be more efficient in the fired
Waste Heat Boilers 205
mode if it is a single-pressure unit. If we did not have an economizer, the exit gas temperature will be higher without an economizer and hence efficiency in fired mode will be lower.)
Thus, supplementary firing is one way to improve the efficiency of gas turbine HRSGs. That is because we are not adding any combustion air while firing but utilizing the oxygen in the exhaust. In effect, we are reducing the excess air. The heat losses from the boiler are also lowered due to the lower exit gas temperature in the fired case. This is due to the fact that a larger heat sink is available in the form of the economizer in the fired mode with the gas flow remaining the same. Plant engineers while planning future projects with HRSGs in cogeneration plants may consider supplementary- or furnace-fired HRSGs as they are more efficient. Since the cross section of an HRSG is determined by the gas flow, it does not matter whether the steam output is 15 t/h or 60 t/h, as the same exhaust gas flow with dif- ferent temperatures and analysis flows through the HRSG. The size of drums may be larger for the higher capacity, but the overall cost should not be much more than an unfired unit.
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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