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Volumn 47, Issue 1, 2001, Pages 19-30

Erratum: High interaction regime Lockhart-Martinelli model for pressure drop in trickle-bed reactors (AIChE Journal (January 2001) (19-30) DOI: 10.1002/aic.690470104);High interaction regime Lockhart-Martinelli model for pressure drop in trickle-bed reactors

Author keywords

[No Author keywords available]

Indexed keywords

MATHEMATICAL MODELS; PRESSURE DROP; SATURATION (MATERIALS COMPOSITION);

EID: 0035132878     PISSN: 00011541     EISSN: 15475905     Source Type: Journal    
DOI: 10.1002/aic.11395     Document Type: Erratum
Times cited : (13)

References (41)
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    • (1968) Chemie et Industrie-Genie Chimique , vol.99 , pp. 803
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  • 13
    • 0028542596 scopus 로고
    • Liquid-phase methanol synthesis: Catalyst, mechanism, kinetics, chemical equilibria, vapor-liquid equilibria, and modeling-a review
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    • Cybulski, A.1
  • 20
    • 0025841960 scopus 로고
    • Liquid phase methanol synthesis: Comparison between trickle-bed and bubble column slurry reactors
    • (1991) Chem. Eng. Sci. , vol.46 , pp. 2339
    • Kodra, D.1    Levec, J.2
  • 37
    • 0021285989 scopus 로고
    • A study of cocurrent downflow of nonfoaming gas-liquid systems in a packed bed. 1. Flow regimes: Search of a generalized flow map; 2. Pressure drop: Search for a correlation
    • (1984) Ind. Eng. Chem. Proces Des. Dev. , vol.23 , pp. 35
    • Tosun, G.1


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.