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Volumn 21, Issue SUPPL.1, 1997, Pages

Mixed integer optimization of combined solvent extraction and distillation processes

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EID: 0042233424     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/s0098-1354(97)87559-x     Document Type: Article
Times cited : (11)

References (14)
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  • 2
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  • 3
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    • Superstructures for the mixed integer optimization of nonideal and azeotropic distillation sequences
    • Bauer, M. H.. and Stichlmair, J.; 1996, Superstructures for the mixed integer optimization of nonideal and azeotropic distillation sequences, Comp. Chem. Eng., 20, Suppl., S25-S30
    • (1996) Comp. Chem. Eng. , vol.20 , Issue.SUPPL.
    • Bauer, M.H.1    Stichlmair, J.2
  • 4
    • 0024138150 scopus 로고
    • Synthesis of Distillation Sequences with Several Multicomponent Feed and Product Streams
    • Floudas, C. A. and Anastasiadis, S. H.; 1988, Synthesis of Distillation Sequences with Several Multicomponent Feed and Product Streams, Chem. Eng. Sci., 43, 9, 2407-2419
    • (1988) Chem. Eng. Sci. , vol.43 , Issue.9 , pp. 2407-2419
    • Floudas, C.A.1    Anastasiadis, S.H.2
  • 5
    • 0029231457 scopus 로고
    • Mixed-Integer Nonlinear Programming Techniques for Process System Engineering
    • Grossmann, I. E. and Kravanja, Z.; 1995, Mixed-Integer Nonlinear Programming Techniques for Process System Engineering, Comp. Chem. Eng., 19, Suppl., S189-S204
    • (1995) Comp. Chem. Eng. , vol.19 , Issue.SUPPL.
    • Grossmann, I.E.1    Kravanja, Z.2
  • 6
    • 0025623478 scopus 로고
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    • (1990) Comp. Chem. Eng. , vol.14 , Issue.12 , pp. 1363-1378
    • Kravanja, Z.1    Grossmann, I.E.2
  • 7
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    • New Developments and Capabilities in PROSYN - An Automated Topology and Parameter Process Synthesizer
    • Kravanja, Z. and Grossmann, I. E.; 1994, New Developments and Capabilities in PROSYN - An Automated Topology and Parameter Process Synthesizer, Comp. Chem. Eng., 18, 1097-1114
    • (1994) Comp. Chem. Eng. , vol.18 , pp. 1097-1114
    • Kravanja, Z.1    Grossmann, I.E.2
  • 8
    • 0029140086 scopus 로고
    • Design strategy for acetic acid recovery
    • Kürüm, S.; Fonyo, Z.; Kut, Ö. M.; 1995, Design strategy for acetic acid recovery, Chem. Eng. Comm., 135, 161-176
    • (1995) Chem. Eng. Comm. , vol.135 , pp. 161-176
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  • 9
    • 0029395174 scopus 로고
    • Global Optimization for the Phase and Chemical Equilibrium Problem: Application to the NRTL Equation
    • McDonald, C. M.; Floudas, C. A.; 1995, Global Optimization for the Phase and Chemical Equilibrium Problem: Application to the NRTL Equation, Comput. Chem. Eng., 19, 11, 1111-1139
    • (1995) Comput. Chem. Eng. , vol.19 , Issue.11 , pp. 1111-1139
    • McDonald, C.M.1    Floudas, C.A.2
  • 11
    • 0011017448 scopus 로고
    • III. Computation of phase and chemical equilibrium: A review, Computer Applications to Chemical Engineering
    • Seider, W. D.; Gautam, R.; White, C. W.; 1980, III. Computation of phase and chemical equilibrium: A review, Computer Applications to Chemical Engineering, ACS Symp. Ser., 5, 124, p. 115
    • (1980) ACS Symp. Ser. , vol.5 , Issue.124 , pp. 115
    • Seider, W.D.1    Gautam, R.2    White, C.W.3
  • 12
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    • Entrainment and extraction efficiency of mixer-settlers
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  • 13
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  • 14
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    • Optimal Feed Locations and Number of Trays for Distillation Columns with Multiple Feeds
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    • Viswanathan, J.1    Grossmann, I.E.2


* 이 정보는 Elsevier사의 SCOPUS DB에서 KISTI가 분석하여 추출한 것입니다.