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Volumn 21, Issue C, 2006, Pages 1323-1328

Static/dynamic analysis and controllability issues in reactive distillation columns

Author keywords

controllability; dynamic simulation; passivity; reactive distillation; steady state multiplicity

Indexed keywords


EID: 77956778304     PISSN: 15707946     EISSN: None     Source Type: Book Series    
DOI: 10.1016/S1570-7946(06)80230-0     Document Type: Article
Times cited : (6)

References (12)
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    • Byrnes, C.I.1    Isidori, A.2    Willems, J.C.3
  • 4
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    • Distillation stability using passivity and thermodynamics
    • Coffey D.P., Ydstie B.E., and Farschman C.A. Distillation stability using passivity and thermodynamics. Comp. Chem. Eng. 24 (2000) 317-322
    • (2000) Comp. Chem. Eng. , vol.24 , pp. 317-322
    • Coffey, D.P.1    Ydstie, B.E.2    Farschman, C.A.3
  • 5
    • 0032071307 scopus 로고    scopus 로고
    • Methyl-tert-butyl-eter catalytic distillation column. Part I: Multiple steady states
    • Eldarsi H.S., and Doglas P.L. Methyl-tert-butyl-eter catalytic distillation column. Part I: Multiple steady states. Trans IchemE 76 Part A (1998) 509-516
    • (1998) Trans IchemE , vol.76 , Issue.PART A , pp. 509-516
    • Eldarsi, H.S.1    Doglas, P.L.2
  • 6
    • 0032144696 scopus 로고    scopus 로고
    • Process systems and inventory control
    • Farschman C.A., Nismanath P., and Ydstie B.E. Process systems and inventory control. AIChE J. 44 8 (1998) 1841-1857
    • (1998) AIChE J. , vol.44 , Issue.8 , pp. 1841-1857
    • Farschman, C.A.1    Nismanath, P.2    Ydstie, B.E.3
  • 7
    • 0031192097 scopus 로고    scopus 로고
    • An Integrated Computer-Aided System for Integrated, Design of Chemical Processes
    • Gani R., Hytoft G., Jaksland C., and Jensen A.K. An Integrated Computer-Aided System for Integrated, Design of Chemical Processes. Comp. Chem. Eng. 21 (1997) 1135-1146
    • (1997) Comp. Chem. Eng. , vol.21 , pp. 1135-1146
    • Gani, R.1    Hytoft, G.2    Jaksland, C.3    Jensen, A.K.4
  • 9
    • 0029271751 scopus 로고
    • Why methyl tert-butyl ether production by reactive distillation may yield multiple solutions
    • Hauan S., Hertzberg T., and Lien K.M. Why methyl tert-butyl ether production by reactive distillation may yield multiple solutions. Ind. Eng. Chem. Res. 34 (1995) 987-991
    • (1995) Ind. Eng. Chem. Res. , vol.34 , pp. 987-991
    • Hauan, S.1    Hertzberg, T.2    Lien, K.M.3
  • 10
    • 0030617240 scopus 로고    scopus 로고
    • Reactive separation systems I. Computation of physical and chemical equilibrium
    • Pérez-Cisneros E.S., Gani R., and Michelsen M.L. Reactive separation systems I. Computation of physical and chemical equilibrium. Chem. Eng. Sci. 52 (1997) 527-543
    • (1997) Chem. Eng. Sci. , vol.52 , pp. 527-543
    • Pérez-Cisneros, E.S.1    Gani, R.2    Michelsen, M.L.3
  • 11
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    • Modeling reactive distillation
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  • 12
    • 0037412107 scopus 로고    scopus 로고
    • Effect of interaction multiplicity on control system design for a MTBE reactive distillation column
    • Wang S.J., Wong D.S.H., and Lee E.K. Effect of interaction multiplicity on control system design for a MTBE reactive distillation column. J. Proc. Control 13 (2003) 503-515
    • (2003) J. Proc. Control , vol.13 , pp. 503-515
    • Wang, S.J.1    Wong, D.S.H.2    Lee, E.K.3


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.