Robust optimization of hydrogen network

被引:66
作者
Lou, Junyi [1 ]
Liao, Zuwei [1 ]
Jiang, Binbo [1 ]
Wang, Jingdai [1 ]
Yang, Yongrong [1 ]
机构
[1] Zhejiang Univ, Dept Chem & Biol Engn, State Key Lab Chem Engn, Hangzhou 310027, Zhejiang, Peoples R China
基金
中国国家自然科学基金;
关键词
Hydrogen network; Robustness; Robust optimization; Stochastic programming; FEED FLOW-RATE; DISTRIBUTION-SYSTEMS; REFINERY; INTEGRATION; MANAGEMENT; DESIGN; MODEL; CONSTRAINTS; UNCERTAINTY; DIAGRAM;
D O I
10.1016/j.ijhydene.2013.11.024
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
Process integration is an effective way to reduce hydrogen utility consumption in refineries. A number of graphical and mathematical programming approaches have been proposed to synthesis the optimal network. However, as the operation of refineries encounters uncertainty with the rapidly changing market and deteriorating crude oil, existing approaches are inadequate to achieve robust hydrogen network distribution due to the uncertain factors. In this paper, robust optimization is introduced as a framework to optimize hydrogen network of refineries under uncertainty. In this framework, a number of scenarios representing possible future environments are considered. Both model robust and solution robust are explicitly incorporated into the objective function. A possible optimal network distribution which is less sensitive to the change of scenarios and has the minimum total annual cost is achieved by the tradeoff between the total annual cost and the expected error. Case studies indicate that this method is effective in dealing with hydrogen network design and planning under uncertainty in comparison to the deterministic approach and the stochastic programming method. Copyright (C) 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:1210 / 1219
页数:10
相关论文
共 44 条
[11]   Setting the minimum utility gas flowrate targets using cascade analysis technique [J].
Foo, Dominic Chwan Yee ;
Manan, Zainuddin Abdul .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (17) :5986-5995
[12]  
Grossmann IE., 2002, GAMS DICOPT DISCRETE
[13]   Refinery hydrogen management for clean fuels production [J].
Hallale, N ;
Liu, F .
ADVANCES IN ENVIRONMENTAL RESEARCH, 2001, 6 (01) :81-98
[14]   Byproduct Hydrogen Network Design Using Pressure Swing Adsorption and Recycling Unit for the Petrochemical Complex [J].
Jeong, Changhyun ;
Han, Chonghun .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2011, 50 (06) :3304-3311
[15]   Multi-component optimisation for refinery hydrogen networks [J].
Jia, Nan ;
Zhang, Nan .
ENERGY, 2011, 36 (08) :4663-4670
[16]   Design and Optimization of Flexible Hydrogen Systems in Refineries [J].
Jiao, Yunqiang ;
Su, Hongye ;
Hou, Weifeng ;
Li, Pu .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2013, 52 (11) :4113-4131
[17]   Optimization of refinery hydrogen network based on chance constrained programming [J].
Jiao, Yunqiang ;
Su, Hongye ;
Hou, Weifeng ;
Liao, Zuwei .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2012, 90 (10) :1553-1567
[18]   A Multiperiod Optimization Model for Hydrogen System Scheduling in Refinery [J].
Jiao, Yunqiang ;
Su, Hongye ;
Hou, Weifeng ;
Liao, Zuwei .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (17) :6085-6098
[19]  
Khajehpour M, INT J HYDROGEN ENERG
[20]   Hydrogen distribution in the refinery using mathematical modeling [J].
Kumar, A. ;
Gautami, G. ;
Khanam, S. .
ENERGY, 2010, 35 (09) :3763-3772