Optimizing Renewable Injection in Integrated Natural Gas Pipeline Networks Using a Multi-Period Programming Approach

被引:4
作者
Ogbe, Emmanuel [1 ,2 ]
Almansoori, Ali [2 ]
Fowler, Michael [1 ]
Elkamel, Ali [1 ,2 ]
机构
[1] Univ Waterloo, Dept Chem Engn, 200 Univ Ave West, Waterloo, ON N2L 3G1, Canada
[2] Khalifa Univ Sci Technol & Res KUSTAR, Dept Chem Engn, POB 2533, Abu Dhabi, U Arab Emirates
基金
加拿大自然科学与工程研究理事会;
关键词
power-to-gas; methanation; multi-period optimization; pipeline optimization; renewable integration; mixed-integer non-linear programming (MINLP); POWER-TO-GAS; OPTIMIZATION MODEL; HYDROGEN; DESIGN; ENERGY; SYSTEMS; DECOMPOSITION; ELECTRICITY; OPERATION; CAPTURE;
D O I
10.3390/en16062631
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
In this paper, we propose an optimization model that considers two pathways for injecting renewable content into natural gas pipeline networks. The pathways include (1) power-to-hydrogen or PtH, where off-peak electricity is converted to hydrogen via electrolysis, and (2) power-to-methane, or PtM, where carbon dioxide from different source locations is converted into renewable methane (also known as synthetic natural gas, SNG). The above pathways result in green hydrogen and methane, which can be injected into an existing natural gas pipeline network. Based on these pathways, a multi-period network optimization model that integrates the design and operation of hydrogen from PtH and renewable methane is proposed. The multi-period model is a mixed-integer non-linear programming (MINLP) model that determines (1) the optimal concentration of hydrogen and carbon dioxide in the natural gas pipelines, (2) the optimal location of PtH and carbon dioxide units, while minimizing the overall system cost. We show, using a case study in Ontario, the optimal network structure for injecting renewable hydrogen and methane within an integrated natural gas network system provides a $12M cost reduction. The optimal concentration of hydrogen ranges from 0.2 vol % to a maximum limit of 15.1 vol % across the network, while reaching a 2.5 vol % at the distribution point. This is well below the maximum limit of 5 vol % specification. Furthermore, the optimizer realized a CO2 concentration ranging from 0.2 vol % to 0.7 vol %. This is well below the target of 1% specified in the model. The study is essential to understanding the practical implication of hydrogen penetration in natural gas systems in terms of constraints on hydrogen concentration and network system costs.
引用
收藏
页数:24
相关论文
共 68 条
  • [1] Strong formulations for the pooling problem
    Alfaki, Mohammed
    Haugland, Dag
    [J]. JOURNAL OF GLOBAL OPTIMIZATION, 2013, 56 (03) : 897 - 916
  • [2] Altfeld K., 2013, GAS ENERGY, V3, P2013
  • [3] Multi-objective design optimization of natural gas transmission networks
    Alves, Felipe da Silva
    Miranda de Souza, Jame Neiva
    Hemerly Costa, Andre Luiz
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2016, 93 : 212 - 220
  • [4] [Anonymous], 2013, Deterministic Global Optimization: Theory, Methods and Applications
  • [5] [Anonymous], Natural gas explained: where our natural gas comes from
  • [6] [Anonymous], 2021, GLOBAL HYDROGEN REV
  • [7] Aruna C., 2022, THESIS U COLL DUBLIN
  • [8] Energy efficient water utilization systems in process plants
    Bagajewicz, M
    Rodera, H
    Savelski, M
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2002, 26 (01) : 59 - 79
  • [9] A review of recent design procedures for water networks in refineries and process plants
    Bagajewicz, M
    [J]. COMPUTERS & CHEMICAL ENGINEERING, 2000, 24 (9-10) : 2093 - 2113
  • [10] GLOBAL MINIMIZATION BY REDUCING THE DUALITY GAP
    BENTAL, A
    EIGER, G
    GERSHOVITZ, V
    [J]. MATHEMATICAL PROGRAMMING, 1994, 63 (02) : 193 - 212