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- W7396142 abstract "The objective of this paper is to demonstrate that with the aid of even a simple process model the economic optimisation of a batch process can be taken significantly further than is traditional at the predesign stage. The process used to demonstrate this is a complex one, itself developed with modelling assistance, in which chemical reaction and distillation steps are combined into an integrated system. The effects of prime design variables on the economic performance of the process around the optimum are highlighted. The approach used is a general one however and, with a suitable model, should be widely applicable." @default.
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- W7396142 date "1987-01-01" @default.
- W7396142 modified "2023-09-25" @default.
- W7396142 title "DYNAMIC MODEL BASED OPTIMISATION IN THE DESIGN OF A BATCH PROCESS INVOLVING SIMULTANEOUS REACTION AND DISTILLATION" @default.
- W7396142 cites W2058964075 @default.
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- W7396142 doi "https://doi.org/10.1016/b978-0-85295-205-4.50018-9" @default.
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