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Mathematical modelling of heat and mass transfer in a fixed biomass fuel bed. Part 2, Pyrolysis

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EN
Abstrakty
EN
Heat and mass transfer in a fixed bed of biomass during thermal degradation of biomass in a hot inert gas (pyrolysis) is modeled. Biomass fuel decomposes to give gas, tar and char as a result of hot gas flowing through it upwards from a combustion char below. The main heating mode at this stage is conduction and convection. The fuel bed is assumed to be a porous homogenous layer composedof uniformely distributed coarse particles that are randomly oriented. The mathematical model formulates the basic equations and solves them numerically to describe the temperature and solid fuel degradation to tar, gas and char. Thermal non-equilibrium between the gas phase and the solid particle surfaces is assumed, conseqently the use of separate equations for gas and solid phase equations is necessary
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  • The Royal Institute of Technology at University of Michigan
Bibliografia
  • [1] GULLET B. K., SMITH P.: Thermogravimetric study of the decomposition of pelletized cellulose at 315°C - 800°C, Combustion and Flame 67(1987), 143-151.
  • [2] ROBERTS A. F., CLOUGH G.: Thermal decomposition of wood in an inert atmosphere, Ninth Symposium (International) on Combustion, the Combustion Institute,1963, 158-166.
  • [3] KUNG, H.-CH.: Combustion and Flame, 18(1972), 185-195.
  • [4] KUNG H.-CH., KALELKAR A. S.: On the heat of reaction in wood pyrolysis, Combustion and Flame 20(1973), 91-103.
  • [5] SPIGA G., SPIGA M.: A rigorous solution to heat transfer, two phase model in porous media and packed bed, Int. J. Heat Mass Transfer 24(1981), 355-364.
  • [6] WARD S. M., BRASLAW J.: Experimental weight loss kinetics of wood pyrolysis under vacuum, Combustion and Flame 61(1985), 261-269.
  • [7] KOUFOPANOS C. A., MASCHIO G. I., LUCCHESI, A.: The Canadian Journal of Chemical Engineering, 67(1989), 75-84.
  • [8] GHALY A. E., ERGUDENLER, AL TAWEEL A. M.: Biomass and Bioenergy, 5(1993), No. 6., 457-465.
  • [9] PYLE, D. L., ZAROR: Chemical Engineering Science, 39(1984), No. 1, 147-158.
  • [10] HAJALIGOL M R., HOWARD J. B., LONGWELL J. P., PETERS W.: A., Ind. Eng. Process Des. Dev. 21(1982), 457-465.
  • [11] ROBERTS A. F.: Combustion and Flame 14(1970), 261-272.
  • [12] SEKI N., SHOICHIRO F., INABA H.: Heat transfer in a confined rectangular cavity packed with porous media, Int. J. Heat Mass Transfer, 21(1978), 985-989.
  • [13] SINGH A. N., KRAVAN S., GUPTA P. SEN: Rate of mass transfer in a semifluidized bed, Int. J. Heat Mass Transfer, 23(1980), 279-282.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BGPK-0055-1533
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