Distribution of Radiation to Tube Banks
Distribution of Radiation to Tube Banks
When boiler screen section or superheater is located at the furnace exit, direct radiation from the furnace is absorbed by these heating surfaces and increases the heat flux inside the tubes and hence the tube wall temperature. This radiation is generally absorbed completely within the first four to five rows of tubes depending on the tube spacing. Figure 2.11 shows the distribution of external radiation to different rows depending on tube spacing. Direct radiation adds to the energy absorbed by the tubes and increases the metal tem- perature and may cause overheating and thermal expansion problems. Hence, one should
be careful while locating superheaters at the furnace exit. When a screen section is used at the furnace exit, the tubes will not be overheated as these tubes operate at slightly above saturation temperature of steam, while a superheater operates at much higher temperature.
The following formula predicts the radiation to the tubes:
where a = fraction of energy absorbed by row 1. The second row absorbs (1 − a)a, the third
row, [1 − {a + (1 − a)a}a], and so on.
62 Steam Generators and Waste Heat Boilers: For Process and Plant Engineers
Tube diameter is d N
1.2 2 in. on 4 in. centers 1 3 in. on 3.75 in. centers
factor 0.6 ew
Angle from vertical
FIGURE 2.10
(a) View factor estimation. (b) View factors for 2 in OD tube on 4 in and 3 in OD tube on 3.75 in. spacing around tube periphery.
Steam Generator Furnace Design
h = 0.25, 0.5, 1.0 in. 1.0 in.
0.5 in tip—sat temp.)
(F
Heat flux inside tubes 2h
h = Membrane height
(c)
Heat flux
FIGURE 2.10 (Continued)
(c) Relating fin tip temperature to heat flux.
TABLE 2.1
View Factors for Typical Configurations of Membranes
Angle from Horizontal θ
View Factor—Case 1
View Factor—Case 2
Quarter point on fin 0.83 0.57 Midpoint of fin
Note: Case 1:2 in. OD tubes on 4 in. spacing. Case 2:3 in. OD tube on 3.75 in. spacing.
Example 2.5
A superheater with 50 mm OD tubes at 200 mm spacing is exposed to direct furnace radiation. Estimate the energy absorbed by the first four rows. Assume Qr the direct radiation is 1 MW. (The radiation to the superheater may be estimated based on the heat flux and opening area of the exit plane as discussed earlier.)
Solution
d = 50 mm, S T = 200 mm. a = 3.14 × 50/2/200 −50/200[sin −1 (50/200) + {(200/50) 2 − 1} 0.5 − 200/50] = 0.3925 − 0.25(0.2526 + 15 0.5 – 4) = 0.361. Hence, first row absorbs 0.361 MW. (See Figure 2.11, which
gives the total energy absorbed from external radiation for a certain number of rows. For two rows, the total absorbed is 0.6 MW as seen from the figure.)
The second row absorbs (1 − 0.361) × 0.361 = 0.2306 MW (total of two rows absorb nearly 0.6 MW). The third row receives [1 − (0.361 + 0.2306)] × 0.361 = 0.147 MW. The fourth row = [1 − (0.361 + .2306 + 0.147)] × 0.361 = 0.094 MW and so on. Typically, a minimum of four rows will absorb the external radiation completely. If
the tube spacing were smaller, then a large amount of radiation is absorbed within the first few rows resulting in high heat flux to these tubes; hence, it is better to use a wider
64 Steam Generators and Waste Heat Boilers: For Process and Plant Engineers
2 No. of rows de
Distribution of external radiation to tubes.
spacing when the external radiation is large so that the radiation is spread over more rows, and heat flux is not intense in the first two or three rows. Screen tubes in boilers and heaters perform this function. Good boiler designs shield the superheater from fur- nace radiation by using more than six to eight rows of screen tubes. This is discussed in Chapter 3 on steam generators.
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
Show more