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• W4234264310 abstract "The different pressure thermally coupled reactive distillation (DPT-RD) process is an attractive heat-integrated design in chemical engineering development processes. In this study, a rigorous simulation of the DPT-RD process for amyl acetate synthesis in a neat operation mode is performed using the Aspen Plus simulator. The economic feasibility and controllability of the DPT-RD process were evaluated based on the research of steady-state optimization and dynamic control. The optimum DPT-RD process in terms of the total annual cost (TAC) is screened. The results show that 33.74% reduction in energy consumption and 7.96% savings in TAC can be achieved by the DPT-RD process compared to the conventional reactive distillation. The control strategy of the DPT-RD process was developed and the basic control structure with proportional control and the improved control structure with temperature/composition cascade control were presented. The dynamic results indicate that the improved control structure can effectively handle disturbances of ±20% in feed flow rate and of 5% in feed composition. Overall results demonstrate that the DPT-RD process is a promising approach for amyl acetate synthesis." @default.
• W4234264310 created "2022-05-12" @default.
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• W4234264310 date "2017-11-01" @default.
• W4234264310 modified "2023-09-26" @default.
• W4234264310 title "Design and control of different pressure thermally coupled reactive distillation for amyl acetate synthesis" @default.
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• W4234264310 doi "https://doi.org/10.1016/j.cep.2017.09.002" @default.
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