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Optimization of a crude distillation unit using a combination of wavelet neural network and line-up competition algorithm 被引量:3
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作者 Bin Shi Xu Yang Liexiang Yan 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2017年第8期1013-1021,共9页
The modeling and optimization of an industrial-scale crude distillation unit (CDU) are addressed. The main spec- ifications and base conditions of CDU are taken from a crude oil refinery in Wuhan, China. For modelin... The modeling and optimization of an industrial-scale crude distillation unit (CDU) are addressed. The main spec- ifications and base conditions of CDU are taken from a crude oil refinery in Wuhan, China. For modeling of a com- plicated CDU, an improved wavelet neural network (WNN) is presented to model the complicated CDU, in which novel parametric updating laws are developed to precisely capture the characteristics of CDU. To address CDU in an economically optimal manner, an economic optimization algorithm under prescribed constraints is presented. By using a combination of WNN-based optimization model and line-up competition algorithm (LCA), the supe- rior performance of the proposed approach is verified. Compared with the base operating condition, it is validat- ed that the increments of products including kerosene and diesel are up to 20% at least by increasing less than 5% duties of intermediate coolers such as second pump-around (PA2) and third Dump-around (PA3). 展开更多
关键词 crude oil distillation Wavelet neural network Line-up competition algorithm optimization
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Simultaneous optimization of heat-integrated crude oil distillation systems 被引量:1
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作者 罗祎青 王丽雯 +1 位作者 王赫 袁希钢 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2015年第9期1518-1522,共5页
Crude oil distillation is important in refining industry. Operating variables of distillation process have a critical effect on product output value and energy consumption. However, the objectives of minimum energy co... Crude oil distillation is important in refining industry. Operating variables of distillation process have a critical effect on product output value and energy consumption. However, the objectives of minimum energy consumption and maximum product output value do not coordinate with each other and do not lead to the maximum economic benefit of a refinery. In this paper, a systematic optimization approach is proposed for the maximum annual economic benefit of an existing crude oil distillation system, considering product output value and energy consumption simultaneously. A shortcut model in Aspen Plus is used to describe the crude oil distillation and the pinch analysis is adopted to identify the target of energy recovery. The optimization is a nonlinear programming problem and solved by stochastic algorithm of particle warm optimization. 展开更多
关键词 crude oil distillation Annual economic benefit Energy optimization Particle warm optimization System engineering
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