2015•Industrial & Engineering Chemistry ResearchRequires access

Application of Mechanical Vapor Recompression Heat Pump to Double-Effect Distillation for Separating N,N-Dimethylacetamide/Water Mixture

Xiaoxin Gao, Jun Chen, Jiankan Tan, Ying Wang, Zhengfei Ma, Limin Yang

Open publisher page 33 citations

Abstract

A coupled separation system involving a mechanical vapor recompression heat pump (MVRHP) and double-effect distillation (MED) was proposed. In a case of separating N, N -dimethylacetamide (DMAC)/water mixture, four distillation schemes (i.e., conventional distillation, top MVRHP distillation, double-effect distillation, and double-effect distillation with double MVRHP) were conceptually constructed and simulated by using Aspen Plus with the binary interaction parameters of the NRTL thermodynamic model. We evaluated these four schemes to choose the best one with the goal of the minimum total annual cost (TAC). Compared to the conventional distillation, the TACs for double-effect distillation with double MVRHPs, top MVRHP distillation, and double-effect distillation were decreased by 47.76, 32.23, and 5.45%, respectively. It indicates that the double-effect distillation with double MVRHPs has obvious advantages over the other three distillation schemes in terms of economic efficiency.

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What this paper is about

A coupled separation system involving a mechanical vapor recompression heat pump (MVRHP) and double-effect distillation (MED) was proposed. In a case of separating N, N -dimethylacetamide (DMAC)/water mixture, four distillation schemes (i.e., conventional distillation, top MVRHP distillation, double-effect distillation, and double-effect distillation with double MVRHP) were conceptually constructed and simulated by using Aspen Plus with the binary interaction parameters of the NRTL thermodynamic model. We evaluated these four schemes to choose the best one with the goal of the minimum total annual cost (TAC). Compared to the conventional distillation, the TACs for double-effect distillation with double MVRHPs, top MVRHP distillation, and double-effect distillation were decreased by 47.76, 32.23, and 5.45%, respectively. It indicates that the double-effect distillation with double MVRHPs has obvious advantages over the other three distillation schemes in terms of economic efficiency.

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Available abstract

A coupled separation system involving a mechanical vapor recompression heat pump (MVRHP) and double-effect distillation (MED) was proposed. In a case of separating N, N -dimethylacetamide (DMAC)/water mixture, four distillation schemes (i.e., conventional distillation, top MVRHP distillation, double-effect distillation, and double-effect distillation with double MVRHP) were conceptually constructed and simulated by using Aspen Plus with the binary interaction parameters of the NRTL thermodynamic model. We evaluated these four schemes to choose the best one with the goal of the minimum total annual cost (TAC). Compared to the conventional distillation, the TACs for double-effect distillation with double MVRHPs, top MVRHP distillation, and double-effect distillation were decreased by 47.76, 32.23, and 5.45%, respectively. It indicates that the double-effect distillation with double MVRHPs has obvious advantages over the other three distillation schemes in terms of economic efficiency.

Key concepts: Distillation, Multiple-effect distillation, Dimethylacetamide, Chemistry, Non-random two-liquid model, Continuous distillation, Thermodynamics, Steam distillation

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