Air Heaters
Air Heaters
Air heaters are used in steam generators when low BTU fuels are fired or in a few waste heat boilers for preheating combustion air. Incineration plants and reformer furnaces also use preheated air. Decades ago, they were used in boilers firing oil, gas, and solid fuels. However, with NO x emission limitations throughout the world, as discussed in Chapter 1, they are used only if the fuel combustion process warrants it. If the gaseous fuel has a low heating value or if the solid fuel has significant amount of moisture, then hot air is required for drying the fuel and also to ensure combustion with a stable flame. A gas to gas heater, which is similar to the tubular air heater (Figure 4.41), is also used in incineration plants.
Air heaters can be of tubular type or regenerative or heat pipes (Figure 4.41). In the tubu- lar air heater, air or flue gas could flow inside the tubes. If the flue gas contains dust or ash particles, it is preferable to make the flue gas flow inside the tubes so that cleaning is easier. The air then takes a multipass route outside the tubes.
One of the concerns with air heaters is low-temperature corrosion at the cold end. The tube wall temperature at the cold end falls below the acid dew point temperature of the flue gas if the inlet air temperature is low or during part loads when both the air and flue gas flows are reduced. Steam is often used to preheat air to mitigate this concern and raise the air inlet temperature, which in turn raises the flue gas exit temperature and thus the average tube wall temperature. Some boiler suppliers use corten steel tubes to minimize corrosion concerns.
There are two types of regenerative air heaters, one in which the heater matrix rotates (Ljungstrom) and the other in which the connecting air and flue gas duct rotate (Rothemuelle). The energy from the hot flue gas is transferred to the slowly rotating matrix (1–5 rpm) made of enamel or alloy steel material, which absorbs the heat and transfers the energy to the cold air as it rotates. The elements are contained in baskets, which makes
Waste Heat Boilers 251
Seal sector
Gas out
Gas sector
Air sector
(a) Tubular and (b) regenerative air heaters. cleaning or replacement easier. The air- and gas-side pressure drops are high in both types
of air heaters, adding to the fan power consumption. Due to the low air- and gas-side heat transfer coefficients and low overall U and the low LMTD, the surface area required is large. However, in the case of Ljungstrom air heater, a lot of surface area can be packed into each basket and hence can be made compact while the tubular air heater (where finned tubes are not effective as discussed in Appendix E) will be huge often as large as the steam generator itself.
One of the problems with regenerative-type air heaters is the leakage (from 5% to 10%) from air to flue gas side (air is often at higher pressure), and this affects the performance even with good design of seals.
In case of low-temperature corrosion, the cold-end baskets can be made of alloy or corten material, while in the case of tubular type, the entire tube has to be replaced.
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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