Simultaneous optimization of heat-integrated crude oil distillation systems
摘要
Abstract
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 minimumenergy 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.
关键词
Keywords
references
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相关作者
Zheng Wang
Cheng Shao
Li Zhu
Bin Shi
Xu Yang
Liexiang Yan
Liang Kong
Ignacio E. Grossmann
相关机构
Institute of Advanced Control Technology, Dalian University of Technology
Department of Chemical Engineering, Wuhan University of Technology
Center for Advanced Process Decision-making, Department of Chemical Engineering, Carnegie Mellon University