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Volumn 54, Issue 21, 1999, Pages 4791-4799

A numerical comparison of alternative three-phase reactors with a conventional trickle-bed reactor. The advantages of countercurrent flow for hydrodesulfurization

Author keywords

Countercurrent flow; Gas liquid mass transfer; Gas liquid solid reactors; Hydrodesulfurization; Modeling

Indexed keywords

COMPUTER SIMULATION; FLOW OF FLUIDS; GASES; HYDROGEN SULFIDE; LIQUIDS; MASS TRANSFER; POROSITY; SOLIDS;

EID: 0033231955     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0009-2509(99)00196-7     Document Type: Article
Times cited : (54)

References (17)
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  • 2
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  • 5
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  • 7
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    • in press
    • Lebens, P. J. M., Stork, M. M., Kapteijn, F., Sie, S. T. & Moulijn, J. A. (1999). Hydrodynamics and mass transfer issues in a gas-liquid countercurrent internally finned monolith reactor. Chemical Engineering Science, in press.
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  • 9
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    • Papayannakos, N., & Marangozis, J. (1984). Kinetics of catalytic hydrodesulfurization of a petroleum residue in a batch-recycle trickle bed reactor. Chemical Engineering Science, 39, 1051-1061.
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  • 12
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    • Pressure drop and liquid holdup for two phase concurrent flow in packed beds
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  • 13
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    • Hydrotreating catalysis
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  • 17
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    • The influence of pressure on the liquid hold-up in a cocurrent gas-liquid trickle-bed reactor operating at low gas velocities
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* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.