Steam Pressure
Steam Pressure
Steam pressure also affects the furnace size and, of course, the boiler arrangement. If the pressure is low, then the latent heat of steam is high, and hence, the furnace and evaporator heating surface will be larger compared to the case where steam pressure is very high as in utility boilers. Figure 2.5a shows the distribution of energy as a function of steam pres- sure. Since the total sensible or liquid plus latent heat of steam is absorbed in the econo- mizer, evaporator tubes, and furnace, proper proportioning of duty is a must among these surfaces. Very high-pressure boilers may have simply a furnace followed by superheaters and an economizer as the latent heat is small (Figure 2.5b), while low-pressure boilers will have a furnace, a large evaporator (sometimes called a boiler bank), and an economizer (Figure 2.5c and d). To minimize furnace size, the evaporator surface is sometimes added in the furnace itself as water platens.
Figure 2.5b shows a steam generator for low- to medium-pressure steam generation (1500–5000 kPa). A large evaporator in the form of boiler bank tubes is used. The latent heat is absorbed in the furnace and in the bank tubes, which is a three-pass evaporator.
S team G
en er
125 psig, sat.
14 86 Heating
at or sa
650 psig, 750°F
20 64 16 Industrial
Sensible heat
dW n
Latent heat
a ste H
1500 psig, 880°F
32 46 22 Large industrial
Super heat
2620 psig, 1000°F/1000°F
:F (reheat) rs or P
26 23 35 16 Utility
(a)
ro
ce ss a
n dP
la n tE n g in
ee rs
S team G
Steam drum
Hanger tube
F.S.H
P.S.H–II low
Gas f
P.S.H–I
Air Heater
Air from
FD fan
(b)
General arrangement of high pressure and temperature oil & gas fired boiler
FIGURE 2.5
(a) Distribution of energy in boilers as a function of steam pressure. (b) High-pressure steam generator. (Courtesy of ISGEC Heavy Engineering Ltd, India.)
(Continued)
Steam drum
LHS
RHS
Design parameters:
03. Super heater outlet pressure 02. Design temperature 01. Design pressure
: 320 °C : 77.0 kg/cm (g)
team G
05. Total evaporation 04. Super heater outlet temperature : 500 °C Side wall
Main steam
: 67 kg/cm 2 (g)
: 25000 kg/hr Top HDR.
Brief description of boiler:
at or sa
Natural circulation, Bi–Drum, bottom supported,
LRSB C L of
membrane type, fluidised bed combustion boiler.
dW
man hole & C L of
peep hole
Water drum Eco.outlet HDR.
EW CL of bo iler
:F
or P
C L of over
C L fire air at
of over
L.H.S & R.H.S fire air at
ECO.coil Tube
ro
L.H.S & R.H.S
ce ss a
CL of spreader
man hole & L C of
CL of manhole
dP
peep hole
& peep holes
la n
Fu ture
Fu ture
ture Fu
View–E
evaporator
Bed evaporator
View–A
(c)
rs
S team G
Steam drum
S.S.H
Bank tubes
P.S.H
Air preheater–II
to windbox Hot air
Air preheater–I
Air from FD fan
Mud drum
Hot air from air heater
(d)
General arrangement of medium pressure and temperature oil & gas fired boiler
FIGURE 2.5 (Continued)
(c) Steam generator for medium-pressure steam. (Courtesy of Thermodyne Technologies, Chennai, India.) (d) Low-pressure steam generator with large evaporator. (Courtesy ISGEC Heavy Engineering Ltd, India.)
52 Steam Generators and Waste Heat Boilers: For Process and Plant Engineers
The liquid heat or the energy absorbed in the economizer is not much compared to high- pressure boilers, and hence, it is small.
Figure 2.5c shows a steam generator for a high-pressure boiler (11,000 kPa). The liquid heat (or the energy absorbed in the economizer) is large, and hence, we see a large econo- mizer. The latent heat is small, and hence, we have only the furnace to absorb the latent heat and a large superheater for the superheat. Since the design pressure is rather high, an external steam drum is used with high ligament efficiency in order to reduce its thickness. Locating the drum up above also helps in improving circulation through the furnace tubes.
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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