Superstructure-based MINLP Formualtion for Design of Multi-effect Distillation Arrangements

碩士 === 國立臺灣大學 === 化學工程學研究所 === 96 === Owing to the rising cost of energy and the fact that new energy resources are not yet available to all, how to utilize energy in an efficient way has become an important issue for industrial processes. In normal chemical works, the distillation process plays the...

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Main Authors: Cheng-Hsi Hsu, 許正熹
Other Authors: 陳誠亮
Format: Others
Language:zh-TW
Published: 2008
Online Access:http://ndltd.ncl.edu.tw/handle/69950109238032081701
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spelling ndltd-TW-096NTU050630532016-05-11T04:16:51Z http://ndltd.ncl.edu.tw/handle/69950109238032081701 Superstructure-based MINLP Formualtion for Design of Multi-effect Distillation Arrangements 以數學規畫法作多效蒸餾系統設計 Cheng-Hsi Hsu 許正熹 碩士 國立臺灣大學 化學工程學研究所 96 Owing to the rising cost of energy and the fact that new energy resources are not yet available to all, how to utilize energy in an efficient way has become an important issue for industrial processes. In normal chemical works, the distillation process plays the most part in consuming energy and naturally turns into the major subject to be investigated by many savants. The main objective is to design an applicable mode for the manipulation of distillation columns which achieves the energy saving. Therefore, not only the operating cost can be reduced but the environmental impact will be also lowered. The concept of multi-effect distillation columns had been introduced in 1950 by Robinson and Gilliland: The temperature differences (for heat exchange) between distillation columns can be produced by increasing the pressure in some columns, and heat integration within the distillation system is then carried out for the purpose of energy recovery and energy saving. Based on a superstructure which incorporates all possible schemes, this work aims to propose a general mixed-integer nonlinear programming (MINLP) formulation for modeling and optimizing the multi-effect distillation system, where design objectives include the minimization of energy consumption and the minimization of total annual cost (TAC). Accordingly, optimal operating conditions can be obtained with different design objectives. For one thing, results from the proposed mathematical formulation will be compared with the results from Underwood’s method to confirm its validness. For the next, the results of multi-effect distillation system are also compared with the results of conventional distillation system to illustrate that the multi-effect distillation columns are actually capable of reducing the energy consumption and the total annual cost. Furthermore, the correlation between feed condition and resultant framework of distillation can be generalized through discussions on a series of examples. 陳誠亮 2008 學位論文 ; thesis 95 zh-TW
collection NDLTD
language zh-TW
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description 碩士 === 國立臺灣大學 === 化學工程學研究所 === 96 === Owing to the rising cost of energy and the fact that new energy resources are not yet available to all, how to utilize energy in an efficient way has become an important issue for industrial processes. In normal chemical works, the distillation process plays the most part in consuming energy and naturally turns into the major subject to be investigated by many savants. The main objective is to design an applicable mode for the manipulation of distillation columns which achieves the energy saving. Therefore, not only the operating cost can be reduced but the environmental impact will be also lowered. The concept of multi-effect distillation columns had been introduced in 1950 by Robinson and Gilliland: The temperature differences (for heat exchange) between distillation columns can be produced by increasing the pressure in some columns, and heat integration within the distillation system is then carried out for the purpose of energy recovery and energy saving. Based on a superstructure which incorporates all possible schemes, this work aims to propose a general mixed-integer nonlinear programming (MINLP) formulation for modeling and optimizing the multi-effect distillation system, where design objectives include the minimization of energy consumption and the minimization of total annual cost (TAC). Accordingly, optimal operating conditions can be obtained with different design objectives. For one thing, results from the proposed mathematical formulation will be compared with the results from Underwood’s method to confirm its validness. For the next, the results of multi-effect distillation system are also compared with the results of conventional distillation system to illustrate that the multi-effect distillation columns are actually capable of reducing the energy consumption and the total annual cost. Furthermore, the correlation between feed condition and resultant framework of distillation can be generalized through discussions on a series of examples.
author2 陳誠亮
author_facet 陳誠亮
Cheng-Hsi Hsu
許正熹
author Cheng-Hsi Hsu
許正熹
spellingShingle Cheng-Hsi Hsu
許正熹
Superstructure-based MINLP Formualtion for Design of Multi-effect Distillation Arrangements
author_sort Cheng-Hsi Hsu
title Superstructure-based MINLP Formualtion for Design of Multi-effect Distillation Arrangements
title_short Superstructure-based MINLP Formualtion for Design of Multi-effect Distillation Arrangements
title_full Superstructure-based MINLP Formualtion for Design of Multi-effect Distillation Arrangements
title_fullStr Superstructure-based MINLP Formualtion for Design of Multi-effect Distillation Arrangements
title_full_unstemmed Superstructure-based MINLP Formualtion for Design of Multi-effect Distillation Arrangements
title_sort superstructure-based minlp formualtion for design of multi-effect distillation arrangements
publishDate 2008
url http://ndltd.ncl.edu.tw/handle/69950109238032081701
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