Development of an Optimization-Based Framework for Simultaneous Process Synthesis and Heat Integration

被引:9
|
作者
Kong, Qingyuan [1 ]
Shah, Nilay [1 ]
机构
[1] Imperial Coll London, Dept Chem Engn, London SW7 2AZ, England
基金
英国工程与自然科学研究理事会;
关键词
IN-PROCESS SYNTHESIS; CONCEPTUAL DESIGN; POWER INTEGRATION; PINCH ANALYSIS; BIOMASS; CHEMICALS; BIOREFINERIES; PATHWAYS; LIMONENE; FEEDSTOCKS;
D O I
10.1021/acs.iecr.7b00549
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
With the increasing attention toward renewable platform chemicals, a considerable amount of reaction pathways are being investigated for the potential of scale-up and industrialization. Heat integration, as a key feature in the field of process engineering, needs to be taken into consideration when developing preliminary reaction networks producing value-added products. In this study, we introduce an optimization-based framework for the simultaneous process synthesis and heat integration with the goal of finding the most profitable biobased platform chemical and its production pathways from a number of alternatives. A process superstructure that consists of master reaction stages and lower-level separation stages is introduced to demonstrate the theory. With a novel variable discretization approach, the problem is formulated as a mixed integer linear programming model to determine the optimal reaction pathways and separation sequences along with the heat integration cascade using simple data. The solutions to the problem reveal key information of the optimal flowsheet such as the maximum economic performance the process can achieve and the minimum cooling and heating duties required resulting from the heat integration analysis. A case study is presented to illustrate the applicability of the proposed approach.
引用
收藏
页码:5000 / 5013
页数:14
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