Mathematical modeling and optimal operation of industrial tubular reactor for naphtha cracking

Computer Aided Chemical Engineering

Volumn 27, Issue C, 2009, Pages 501-506

  Gao, G Y ^a   Wang, M ^b   Pantelides, C C ^c   Li, X G ^a   Yeung, H ^b  

^a TIANJIN UNIVERSITY   (China)

^b CRANFIELD UNIVERSITY   (United Kingdom)

^c IMPERIAL COLLEGE LONDON   (United Kingdom)

Author keywords

Case study; Ethylene furnace; Mathematical modeling; Tubular reactor

Indexed keywords

EID: 77649331402     PISSN: 15707946     EISSN: None     Source Type: Book Series    
DOI: 10.1016/S1570-7946(09)70304-9     Document Type: Conference Paper

References (9)

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7. Pantelides, C.C. (2003), The mathematical modelling of the dynamic behaviour of process systems, Centre for Process Systems Engineering, Imperial College London.
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9. th Ed), John Wiley & Sons, Inc.