Fire Tube Boilers
Fire Tube Boilers
Oil- and gas-fired fire tube package boilers are widely used in cogeneration plants (Figure 3.43). They generate low-pressure saturated steam, and steam capacity is limited to about 20−35 t/h as larger sizes would involve large-diameter shells and may be uneconomical. The burner is located in the large central pipe called the Morrison pipe, which is a cor- rugated pipe to handle the differential thermal expansion between the first pass and the other passes that are fixed to the tube sheets. The number of passes can be three or even four to improve the efficiency. An economizer may also be added if required. Figure 3.44 shows a fire tube boiler with a superheater. Note that it is somewhat cumbersome to add
a superheater in a fire tube boiler. In a water tube boiler, the superheater can be located after any number of evaporator tubes. However, in a fire tube boiler, it can only be at the end of the second pass or between the boiler and economizer. The flue gas temperature at the exit of the third pass may not be significant to add a superheater, and at part loads, the gas temperature will drop off significantly. In Chapter 4, a fire tube waste heat boiler with a superheater and an economizer beyond the evaporator is shown. However, the steam temperature will be low.
Some boiler suppliers use grooved tubes (Figure 3.45) to improve the tube-side heat transfer coefficient and thus either reduce the number of passes or improve the performance.
FIGURE 3.43
Fire tube boilers in a process plant. (Courtesy of Cleaver Brooks Inc., Thomasville, GA.)
158 Steam Generators and Waste Heat Boilers: For Process and Plant Engineers
CL of boiler
CL of furnace
FD fan FD fan
FIGURE 3.44
Fire tube boiler with a superheater. (Courtesy of Thermodyne Technologies, Chennai, India.)
FIGURE 3.45
Grooved tubes used in fire tube boilers to improve energy transfer. (Courtesy of Cleaver Brooks Inc., Thomasville, GA.)
Fire tube boilers are classified as dry back or wet back depending on how the turn- around section of the first pass is built (Figure 3.46). Wet back boilers do not use refrac- tory in the turnaround section thus decreasing the maintenance costs and improving the boiler life; however, they are slightly more expensive. As discussed in Chapter 4 on waste heat boilers, using smaller-diameter tubes in fire tube boilers helps reduce weight and length of the boiler.
Steam Generators 159
Insulation
C.L. vessel Furnace
Surner (a)
Insulation
C.L. vessel Furnace
Surner (b)
FIGURE 3.46
(a) Dry back and (b) wet back boilers.
Oil and gaseous fuels are generally fired in package fire tube boilers. Solid fuels such as wood chips have also been fired. The boiler capacity is limited to about 35 t/h of steam as it becomes very expensive to build these boilers beyond this capacity. The heat transfer coefficient when flue gas flows inside the tubes is generally lower than when it flows out- side the tubes. Besides, extended surfaces cannot be used to make the boiler compact as in water tube boilers, though grooved tubes help to some extent.
NO x control methods such as FGR or low NO x burners have been used with fire tube boilers. Due to the large amount of water inventory compared to an equivalent water tube boiler, fire tube boilers take a little more time to start up. Steam purity is poorer than what
160 Steam Generators and Waste Heat Boilers: For Process and Plant Engineers
you get in water tube boilers unless one specifically uses an elevated drum design with chevron separator. Steam purity in a typical fire tube can be in the range of 3–15 ppm due to the use of simple devices for steam–water separation.
Sizing procedures for fire tube boilers are similar to that of water tube boilers.
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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