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• W2610418773 abstract "Complex distillation systems, such as extractive distillation systems and thermally coupled distillation systems have important applications in chemical industry. However, simultaneous optimization of all the variables in these systems with the rigorous MESH model is still difficult because of both the convergence problem and integer optimization problem. In this work, based on the pseudo-transient continuation (PTC) approach, a simple and robust PTC distillation model was developed in the equation-oriented (EO) environment. It was based on the dynamic simulation but with a pseudo-hold-up correlation, which resulted in a well-posed and easily solved differential algebraic equation (DAE) system. Then, three optimization cases were studied to validate the performance of the bypass efficiency method and the new PTC model." @default.
• W2610418773 created "2017-05-12" @default.
• W2610418773 creator A5003890494 @default.
• W2610418773 creator A5025126697 @default.
• W2610418773 creator A5039358967 @default.
• W2610418773 date "2017-05-18" @default.
• W2610418773 modified "2023-09-27" @default.
• W2610418773 title "Simultaneous Optimization of Complex Distillation Systems with a New Pseudo-transient Continuation Model" @default.
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• W2610418773 doi "https://doi.org/10.1021/acs.iecr.7b00380" @default.
• W2610418773 hasPublicationYear "2017" @default.
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