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For: Almeida-Rivera CP, Grievink J. Process Design Approach for Reactive Distillation Based on Economics, Exergy, and Responsiveness Optimization. Ind Eng Chem Res 2007. [DOI: 10.1021/ie061521j] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.4] [Reference Citation Analysis] [What about the content of this article? (0)] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/29/2022]
Number Cited by Other Article(s)
1
ŽivkoviĿ LA, NikaĿeviĿ NM. A method for reactor synthesis based on process intensification principles and optimization of superstructure consisting of phenomenological modules. Chem Eng Res Des 2016. [DOI: 10.1016/j.cherd.2016.07.008] [Citation(s) in RCA: 7] [Impact Index Per Article: 0.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 10/21/2022]
2
Zapata RB, Villa AL, de Correa CM, Ricardez-Sandoval L, Elkamel A. Dynamic Modeling and Optimization of a Batch Reactor for Limonene Epoxidation. Ind Eng Chem Res 2010. [DOI: 10.1021/ie100737y] [Citation(s) in RCA: 4] [Impact Index Per Article: 0.3] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
3
Bardow A, Steur K, Gross J. Continuous-Molecular Targeting for Integrated Solvent and Process Design. Ind Eng Chem Res 2010. [DOI: 10.1021/ie901281w] [Citation(s) in RCA: 111] [Impact Index Per Article: 7.9] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Indexed: 11/30/2022]
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