The body of information presented in this paper is directed to engineers and scientists concerned with control of automobile emissions and exhaust gases from some industrial processes. The differential equations describing heat and mass transfer in a monolithic honeycomb catalyst are developed. Foll
Heat and mass transfer in monolithic honeycomb catalysts—III: Radiation model
✍ Scribed by Jiří Sinkule; Vladimír Hlaváček
- Publisher
- Elsevier Science
- Year
- 1978
- Tongue
- English
- Weight
- 531 KB
- Volume
- 33
- Category
- Article
- ISSN
- 0009-2509
No coin nor oath required. For personal study only.
✦ Synopsis
An analysis IS made of the effect of radlatton exchange upon the behavior of an exothermlc catalytic reactlon occurring on a surface of a cyhndncal passage An n pnon model was developed for calculation of temperature and conversion profiles m the passage and sohd phase as well The model postulates plug flow and gas-to-sohd heat and mass transfer The gas IS assumed to be transparent but radial exchange wlthm the passage, lonfltudmal conductlon of the solid phase and exothermlc reactlon occumng on the catalyst surface are taken mto account The governmg equations descnbmg this model represent a nonhnear boundary value problem for ordmary dtfferentlal equations and mtegro-ddFerentml equation of Fredholm type subJect to Integral boundary condttlons The resultmg set of nonhnear drfferentml and mtegrodlfferenttal equattons was approxtmated by a specud fimtedlfference scheme and quadrature formulas The set of nonlmear algebrluc equations was solved by the Newton-Raphson method It was found that radlatlon exchange can cause slgmficant changes of temperature dlstrlbutlon m the passage Calculated examples mdlcated that the model suggests the existence of multiple steady states
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Heat and mass gas-to-solid coefficients associated with the vaporisation of water and some hydrocarbons from the surface of a porous, monolithic structure were experimentally established. The mass transfer results are correlated using Reynolds and Schmidt number and the length-to-diameter ratio. The
## Abstract A model for the mass‐ and heat‐transfer phenomena in an osmotic evaporation process was developed based on the transfer of solvent from one aqueous solution to be concentrated to a second one separated by a macroporous hydrophobic membrane. The transfer is realized in vapor phase throug