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Volumn 79-80, Issue , 2003, Pages 341-348

Alternating motion of liquid in catalyst pores in a liquid/liquid-gas reaction with heat or gas production

Author keywords

Effective diffusion; Kinetics; Multiphase reaction; Oscillation model

Indexed keywords

BUBBLE FORMATION; CHEMICAL REACTIONS; FLOW OF FLUIDS; GAS FUEL MANUFACTURE; HEAT RADIATION; MASS TRANSFER; POROUS MATERIALS;

EID: 0037544156     PISSN: 09205861     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0920-5861(03)00061-0     Document Type: Conference Paper
Times cited : (22)

References (10)
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    • Thiele, E.W.1
  • 4
    • 0037526280 scopus 로고    scopus 로고
    • Some theoretical aspects of catalyst behaviour in a catalyst particle at liquid-gas reaction with gas production: Oscillation motion in catalyst pores
    • in press
    • L. Datsevich, Some theoretical aspects of catalyst behaviour in a catalyst particle at liquid-gas reaction with gas production: oscillation motion in catalyst pores, Applied Catalysis A: General (2003) in press.
    • (2003) Applied Catalysis A: General
    • Datsevich, L.1
  • 6
    • 0030170418 scopus 로고    scopus 로고
    • Evaluation of trickle bed reactor models for a liquid limited reaction
    • Wu Y., Al-Dahan M.H., Khadilkar M.R., Dudukovich M.P. Evaluation of trickle bed reactor models for a liquid limited reaction. Chem. Eng. Sci. 51:1996;2721.
    • (1996) Chem. Eng. Sci. , vol.51 , pp. 2721
    • Wu, Y.1    Al-Dahan, M.H.2    Khadilkar, M.R.3    Dudukovich, M.P.4
  • 7
    • 0032005264 scopus 로고    scopus 로고
    • A trickle-bed reactor model for hydrogenation of 2,4-dinitrotoluene: Experimental verification
    • Rajashekharam M.V., Jaganathan R., Chaudhari R.V. A trickle-bed reactor model for hydrogenation of 2,4-dinitrotoluene: experimental verification. Chem. Eng. Sci. 53:1998;787.
    • (1998) Chem. Eng. Sci. , vol.53 , pp. 787
    • Rajashekharam, M.V.1    Jaganathan, R.2    Chaudhari, R.V.3
  • 9
    • 0019437227 scopus 로고
    • Mass transfer in trickle-bed reactors at low Reynolds number
    • Turek F., Lange R. Mass transfer in trickle-bed reactors at low Reynolds number. Chem. Eng. Sci. 36:1981;569.
    • (1981) Chem. Eng. Sci. , vol.36 , pp. 569
    • Turek, F.1    Lange, R.2
  • 10
    • 0000751941 scopus 로고
    • The temperature produced by heat of reaction in the interior porous particle
    • Prater C.D. The temperature produced by heat of reaction in the interior porous particle. Chem. Eng. Sci. 8:1958;284.
    • (1958) Chem. Eng. Sci. , vol.8 , pp. 284
    • Prater, C.D.1


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.