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Volumn 53, Issue 1, 1998, Pages 149-155

Modelling of fixed bed reactor: Two models of industrial reactor for selective hydrogenation of acetylene

Author keywords

Heterogeneous catalysis; Selective hydrogenation of acetylene; Simulation

Indexed keywords

ACETYLENE; CATALYSIS; CATALYSTS; COMPUTER SIMULATION; HYDROGENATION; MASS TRANSFER; MATHEMATICAL MODELS; PALLADIUM;

EID: 0031910404     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0009-2509(97)00282-0     Document Type: Article
Times cited : (40)

References (7)
  • 4
    • 0030150583 scopus 로고    scopus 로고
    • Kinetics of front-end acetylene hydrogenation in ethylene production
    • Schbib, N. S., Garcia, M. A., Gigola, C. A. and Errazu, A. F. (1996) Kinetics of front-end acetylene hydrogenation in ethylene production. Ind. Engng Chem. Res. 35, 1496-1505.
    • (1996) Ind. Engng Chem. Res. , vol.35 , pp. 1496-1505
    • Schbib, N.S.1    Garcia, M.A.2    Gigola, C.A.3    Errazu, A.F.4
  • 6
    • 0010612077 scopus 로고
    • Ph. D. thesis. Cracow Technical University, Poland
    • Szukiewicz, M. (1995) Ph. D. thesis. Cracow Technical University, Poland.
    • (1995)
    • Szukiewicz, M.1


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.