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Heat transfer in boilers
Heat Engines & Boilers
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Combustion chamber calculation
Radiation heat transfer Adiabatic flame temperature Heat transfer in combustion chamber Retention time in fire chamber Flame size variation
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Heat transfer forms from gas to solid surface
Convection Radiation By means of Fluid flow and conduction through boundary layer Electromagnetic radiation Contact in between gas and solid surface Necessary Not necessary (even in vacuum) Depends mainly on Fluid flow type and velocity Temperature difference raising to the 4th power Equilibrium state Q = 0 In case of equal temperature T1 = T2 Even in case of different temperatures T1 T2
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Incident radiation Absorption a = Ia/ Itotal - absorption coefficient a = black body Reflection r = Ir/ Itotal - reflection coefficient r = absolute mirror body Transmission d = Id/ Itotal - transmission coefficient (diffraction) d = transparent body a + r + d = 1 - in each case
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Radiation emission of black body
The Planck law with Wien type simplification Where: c - velocity of light in vacuum c = 3*108 [m/s] h - Planck constant h = 6.625* [Js] k – Boltzmann constant k = 1,38* [J/K]
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Radiation emission of black body
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Radiation energy density of black-body - - Stefan-Boltzman law
where: - Stefan-Boltzman constant
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Flame and fire chamber connection Heat transfer by means of radiation in between two bodies are in totally enveloping surface position
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Heat transfer by radiation
where: Emissivity factor A - effective water wall surfaces subject to radiation; [m2] Tf - average flame temperatur [K] Tw - average wall temperature [K]
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Emissivity factor variation in real
Black body - theoretical maximum Grey body - solid body radiation emissivity is constant Color body - gas radiation emissivity is not constant
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Combustion process in real
Parallel procedures running at the same time having dependence on one another: Chemical reaction Fluid flow Heat transfer Simplification model: Chemical reaction happens first Hot flue-gas radiates heat
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Adiabatic flame temperature
Maximal theoretical temperature of flue-gas without any heat transfer
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Calculation of adiabatic flame temperature
Heat flow into the combustion chamber: adiabatic flame temperature where: - B: mass flow rate of fuel [ kg/s] - v: specific flue gas amount, [kgfluegas/kgfuel] considering excess air and flue-gas recirculation - cpfg: mean specific heat of flue gas [kJ\kg K]
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Heat balance in combustion chamber
Qr = Qin - Qfgout Outlet flugas heat capacity where:
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Emissivity variation in case of different fuels
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Flame size variation
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Flame size variation
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Retention time in fire chamber needed for 99.99% oxidization
Needed temperature [°C] Material 0,5 sec 1 sec 2,0 sec At retention time Benzene 880 830 790 Butane 930 900 870 Ethane 1090 990 910 Methane 950 920 Tetrachloromethane Toluene 1260 1220 1180 Vinyl chloride 770 740 720
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Retention time calculation
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Summary of combustion chamber calculation
You are already familiar with: Radiation heat transfer Adiabatic flame temperature Heat transfer in combustion chamber Flame size variation Retention time in fire chamber
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Convective heat transfer calculation
Definition of convective surfaces Types and arrangements of convective heating surfaces Calculation method Heat balance Radiation / Convective heat transfer variation
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Definition We call “Convective Heating Surfaces” surfaces which are built in the boiler after the combustion chamber until the boiler exhaust. Where heat transfer happens mainly by combustion: These can be: - superheater - evaporator - water heater (economizer) - combustion air heater Each heating surface can not be found in every boiler.
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Flue-gas flow can be inside tubes
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Convective heating surface construction Fluegas is streaming around water tubes
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Convective heating surface construction
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Typical superheater arrangements
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Tube arrangement examples
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Finned watertube type heating surface constructions
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Heat transfer calculation
Input data: sizes of the heating surface construction of the heating surface built in materials flue gas - inlet temperature - inlet pressure - mass flow rate heat absorp.fluid - inlet temperature (water/steam/air) - inlet pressure
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Iteration process Outlet temperature of the flue gas and the heat absorption fluid has to be estimated. Then average temperatures can be calculated flue gas: heat abs.fluid:
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Characteristic features
Knowing the average temperatures you can determine the characteristic features belonging to the temperature and pressure both of the flue gas and the heat abs. fluid, which is needed to the calculation. These can be: density thermal conductivity Prandtl number Pr specific heat cp kinematic viscosity etc.
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Heat transfer coefficient calculation
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Explanation of different quantities
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Turbulent fluid flow inside tubes
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Fluid flow around (between) tubes
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Heat transfer coefficient in case of water boiling
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Ranges of heat transfer coefficients
These are only examples. According to the surface arrangement you can find several cases in the literature. Heat transfer coefficient has different value range at different types of fluid: In case of: water boiling: < < W/m2K In case of water flow: < < W/m2K In case of steam flow: < < W/m2K In case of air or flue gas: < < W/m2K
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Heat transmission coefficient
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Convective heat transfer
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Convective heat transfer modification in case of deposit formation flue gas side medium side
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Transferred heat
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Simple heat balance
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Radiation / Convective heat transfer variation
Radiation and convective heat transfer has different principal Radiation heat transfer is proportional with ~T4 Convective heat transfer is proportional with velocity In case of part load operation less fuel is burnt - less fuel produce less fluegas on same cross section gives less velocity - combustion reaction temperature remains nearly the same Consequently radiation/convection heat transfer ratio increases with power load decrease
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Summary of convective heat transfer calculation
You are already familiar with Definition of convective surfaces Types and arrangements of convective heating surfaces Calculation method Heat balance Radiation / Convective heat transfer variation (see calculation example)
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Thank You for Your Attention !
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ZH eredmények
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