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11. |
PROPAGATION OF GASLESS COMBUSTION FRONTS: NONZERO REACTION RATE IN THE WHOLE DOMAIN |
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Chemical Engineering Communications,
Volume 145,
Issue 1,
1996,
Page 173-193
L. CAROTENUTO,
G. CONTINILLO,
S. CRESCITELLI,
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摘要:
This paper deals with the gasless combustion problem in an infinite one-dimensional medium. The possibility of the existence of steadily propagating reaction waves is stated for system models with nonzero reaction rates everywhere but at the boundaries. Two forms for the chemical reaction rate dependence on the temperature are considered: the classical Arrhenius, and a modified Arrhenius incorporating and ignition temperature. The equations for the steadily propagating waves are studied in the phase-plane of the temperature and its derivative. The analysis first addresses the question of whether steadily propagating waves are admissible. Then bounds for the propagation velocity are sought and found. The results of the closed-form analysis are successfully tested against numerical experiments. Non-steady propagation regimes are also found, and regions in the parameter space associated with different asymptotic dynamical behaviour are identified.
ISSN:0098-6445
DOI:10.1080/00986449608936475
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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12. |
RECIRCULATING REACTOR FOR THE STUDY OF MULTIPHASE KINETICS |
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Chemical Engineering Communications,
Volume 145,
Issue 1,
1996,
Page 195-211
SILVIO SICARDI,
STEFANO FERRERO,
LUIGI MANNA,
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摘要:
A new laboratory reactor was set up to measure kinetic coefficients in a solid (catalyst)-liquid-gas reacting system.
ISSN:0098-6445
DOI:10.1080/00986449608936476
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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13. |
INFLUENCE OF MIXING INTENSITY ON THE MASS TRANSFER COEFFICIENT ACROSS LIQUID-LIQUID INTERFACES |
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Chemical Engineering Communications,
Volume 145,
Issue 1,
1996,
Page 213-227
MUTHANNAH. AL-DAHHAN,
CHARLESE. WICKS,
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PDF (485KB)
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摘要:
The influence of mixing intensity on the liquid-liquid mass transfer have been investigated using a binary system (water/n-butanol) in a modified stirred cell type contactor which overcomes the shortcomings associated with the previous contactors. It is observed that the mass transfer coefficient is affected by the degree of mixing intensity in both phases. The dependence of the aqueous and organic mass transfer coefficients on the mixing rate is about the same when both phases are agitated at the same speed and these coefficients become asymptotic values for the coefficients obtained at non identical agitation rate in both phases.
ISSN:0098-6445
DOI:10.1080/00986449608936477
出版商:Taylor & Francis Group
年代:1996
数据来源: Taylor
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