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Volumn 29, Issue 2, 2002, Pages 141-151

Heat and mass transfer model approach to optimum design of cryogenic air separation plant by packed columns with structured packing

Author keywords

Cryogenic air separation; Mass transfer; Simulation model; Structured packing; Ternary distillation

Indexed keywords

AIR; ARGON; COLUMNS (STRUCTURAL); HEAT TRANSFER; INDUSTRIAL PLANTS; MASS TRANSFER; SEPARATION;

EID: 0036837380     PISSN: 13835866     EISSN: None     Source Type: Journal    
DOI: 10.1016/S1383-5866(02)00070-9     Document Type: Article
Times cited : (14)

References (20)
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  • 8
    • 0034926228 scopus 로고    scopus 로고
    • Heat and mass transfer model approach to prediction of separation performance of cryogenic air separation plant by packed columns with structured packing
    • (2001) J. Chem. Eng. Jpn , vol.34 , pp. 22-29
    • Egoshi, N.1    Kawakami, H.2    Asano, K.3
  • 14
    • 0001798775 scopus 로고
    • Experimental data on liquid-vapor equilibrium in the oxygen-argon system at 90.5, 100, 110 and 120° K
    • (1957) Kislorod , vol.3 , pp. 9-16
    • Narinskii, G.B.1
  • 15
    • 0000391928 scopus 로고
    • Liquid-vapor equilibrium in the argon-nitrogen system, I. Experimental data, and their verification
    • (1966) Russ. J. Phys. Chem , vol.40 , pp. 1093-1096
    • Narinskii, G.B.1


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.