Optimization of hydrogen distribution systems with pressure constraints

被引:42
作者
Ding, Ye [2 ]
Feng, Xiao [1 ]
Chu, Khim H. [2 ]
机构
[1] China Univ Petr, Coll Chem Engn, Beijing 102249, Peoples R China
[2] Xi An Jiao Tong Univ, Dept Chem Engn, Xian 710049, Peoples R China
基金
中国国家自然科学基金;
关键词
Hydrogen network; Compressor; Pressure drop; Impurity; Cost equation; REFINERY; INTEGRATION; MANAGEMENT; NETWORKS;
D O I
10.1016/j.jclepro.2010.09.013
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Hydrogenation units are often operated at high pressure, requiring the use of compressors which are one of the most expensive chemical processing equipment. Optimizing a hydrogen network should therefore take into consideration not only purity and flowrate constraints but also pressure requirements. In this paper, based on the hydrogen surplus diagram approach, the average pressure profiles of hydrogen sources and sinks are proposed through the introduction of a system's minimum pressure drop Delta p. Combined with the traditional purity profiles, whether a source can meet a sink either for hydrogen concentration or for pressure requirements can be determined intuitively. In cases where the pressure of a source is not sufficient for a sink, installing a hydrogen compressor or using another source with higher purity and pressure could be potential solutions. A cost equation is established to determine which of the two solutions is economically more viable. For different matching situations between sources and sinks, strategies for optimum placement of compression equipment within a given hydrogen network are proposed. A case study is used to illustrate the application and effectiveness of the proposed method. (C) 2010 Elsevier Ltd. All rights reserved.
引用
收藏
页码:204 / 211
页数:8
相关论文
共 13 条
[1]   Modelling and optimisation for design of hydrogen networks for multi-period operation [J].
Ahmad, Muhammad Imran ;
Zhang, Nan ;
Jobson, Megan .
JOURNAL OF CLEANER PRODUCTION, 2010, 18 (09) :889-899
[2]   Analysis of refinery hydrogen distribution systems [J].
Alves, JJ ;
Towler, GP .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2002, 41 (23) :5759-5769
[3]   Rigorous graphical targeting for resource conservation via material recycle/reuse networks [J].
El-Halwagi, MM ;
Gabriel, F ;
Harell, D .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2003, 42 (19) :4319-4328
[4]   Hydrogen distribution network optimization: a refinery case study [J].
Fonseca, Andre ;
Sa, Vitor ;
Bento, Hugo ;
Tavares, Manuel L. C. ;
Pinto, Gilberto ;
Gomes, Luisa A. C. N. .
JOURNAL OF CLEANER PRODUCTION, 2008, 16 (16) :1755-1763
[5]   Process Integration, Modelling and Optimisation for Energy Saving and Pollution Reduction [J].
Friedler, Ferenc .
PRES'09: 12TH INTERNATIONAL CONFERENCE ON PROCESS INTEGRATION, MODELLING AND OPTIMISATION FOR ENERGY SAVING AND POLLUTION REDUCTION, PTS 1 AND 2, 2009, 18 :1-26
[6]   Refinery hydrogen management for clean fuels production [J].
Hallale, N ;
Liu, F .
ADVANCES IN ENVIRONMENTAL RESEARCH, 2001, 6 (01) :81-98
[7]   Minimising emissions and energy wastage by improved industrial processes and integration of renewable energy [J].
Klemes, Jiri Jaromir ;
Varbanov, Petar Sabev ;
Pierucci, Sauro ;
Huisingh, Donald .
JOURNAL OF CLEANER PRODUCTION, 2010, 18 (09) :843-847
[8]   Integrating purifiers in refinery hydrogen networks: a retrofit case study [J].
Liao, Zuwei ;
Wang, Jingdai ;
Yang, Yongrong ;
Rong, Gang .
JOURNAL OF CLEANER PRODUCTION, 2010, 18 (03) :233-241
[9]   Strategy of purifier selection and integration in hydrogen networks [J].
Liu, F ;
Zhang, N .
CHEMICAL ENGINEERING RESEARCH & DESIGN, 2004, 82 (A10) :1315-1330
[10]  
Peters M.S., 1990, McGraw-Hill Chemical Engineering Series, Vfourth