Fast Design and Numerical Simulation of a Metal Hydride Reactor Embedded in a Conventional Shell-and-Tube Heat Exchanger

被引:0
作者
Ran, Ruizhe [1 ,2 ]
Wang, Jing [2 ]
Yang, Fusheng [2 ]
Imin, Rahmatjan [3 ]
机构
[1] Xinjiang Univ, Sch Mech Engn, Urumqi 830017, Peoples R China
[2] Xi An Jiao Tong Univ, Sch Chem Engn & Technol, Xian 710049, Peoples R China
[3] Xinjiang Univ, Sch Math & Syst Sci, Urumqi 830017, Peoples R China
关键词
metal hydride; reactor; design; bed thickness; HYDROGEN STORAGE PERFORMANCE; SCALE; ENERGY; TECHNOLOGIES;
D O I
10.3390/en17030712
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
The purpose of this work is to present a convenient design approach for metal hydride reactors that meet the specific requirements for hydrogen storage. Three methods from the literature, the time scale, the acceptable envelope, and the reaction front, are used to estimate the maximum thickness of the bed allowing for sufficient heat transfer. Further heat transfer calculations are performed within the framework of standardized heat exchanger via the homemade design software, to generate the complete geometry and dimensions of the reactor. LaNi5 material packed in tubular units based on conventional shell-and-tube heat exchanger is selected for analysis for an expected charging time of 500 s, 1000 s, and 1500 s. Apparently, the smaller the expected charging time, the smaller the bed thickness and hence the diameter of the tubular units. After comparison, the method of reaction front was adopted to output standard tube diameters and calculate the weight of the reactor. Significant weight differences were found to result from the varying wall thickness and number of tubes. In general, the shorter the expected charging time, the more tubular units with a small diameter will be built and the heavier the reactor. Fluent 2022 R2 was used to solve the reactor model with a tube diameter of 50 mm supposed to fulfill a charging time of 1500 s. The simulation results revealed that the reaction fraction reaches its maximum and the hydrogen storage process is completed at 500 s. However, because the calculation is conducted on meeting the heat exchange requirements, the average temperature of the bed layer is close to the initial temperature of 290 K and stops changing at 1500 s. The applicability of the method to the design of metal hydride reactors is thus confirmed by the temperature and reaction fraction judgment criteria.
引用
收藏
页数:18
相关论文
共 50 条
  • [11] Design optimization of shell-and-tube heat exchangers
    Costa, Andre L. H.
    Queiroz, Eduardo M.
    APPLIED THERMAL ENGINEERING, 2008, 28 (14-15) : 1798 - 1805
  • [12] Complete and reduced models for metal hydride reactor with coiled-tube heat exchanger
    Tong, Liang
    Xiao, Jinsheng
    Yang, Tianqi
    Benard, Pierre
    Chahine, Richard
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2019, 44 (30) : 15907 - 15916
  • [13] An optimization study on the finned tube heat exchanger used in hydride hydrogen storage system - analytical method and numerical simulation
    Nyamsi, Serge Nyallang
    Yang, Fusheng
    Zhang, Zaoxiao
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (21) : 16078 - 16092
  • [14] Experimental investigation of shell-and-tube heat exchanger with a new type of baffles
    Wang, Yingshuang
    Liu, Zhichun
    Huang, Suyi
    Liu, Wei
    Li, Weiwei
    HEAT AND MASS TRANSFER, 2011, 47 (07) : 833 - 839
  • [15] Performance Degradation of a Shell-and-Tube Heat Exchanger Due to Tar Deposition
    Aldi, Nicola
    Casari, Nicola
    Pinelli, Michele
    Suman, Alessio
    Vulpio, Alessandro
    ENERGIES, 2022, 15 (04)
  • [16] Effectiveness improvement and optimization of shell-and-tube heat exchanger with entransy method
    Chahartaghi, Mahmood
    Eslami, Pouya
    Naminezhad, Alireza
    HEAT AND MASS TRANSFER, 2018, 54 (12) : 3771 - 3784
  • [17] Design and analysis of shell and tube heat exchanger
    Fernandes E.J.
    Krishanmurthy S.H.
    International Journal for Simulation and Multidisciplinary Design Optimization, 2022, 13
  • [18] Flow mechanism and heat transfer enhancement in longitudinal-flow tube bundle of shell-and-tube heat exchanger
    Liu Wei
    Liu ZhiChun
    Wang YingShuang
    Huang SuYi
    SCIENCE IN CHINA SERIES E-TECHNOLOGICAL SCIENCES, 2009, 52 (10): : 2952 - 2959
  • [19] Performance simulation of metal hydride hydrogen storage device with embedded filters and heat exchanger tubes
    Mohan, G.
    Maiya, M. Prakash
    Murthy, S. Srinivasa
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2007, 32 (18) : 4978 - 4987
  • [20] Study on the heat transfer characteristics of a shell-and-tube phase change energy storage heat exchanger
    Zheng, Yuxin
    Wang, Zhihua
    INNOVATIVE SOLUTIONS FOR ENERGY TRANSITIONS, 2019, 158 : 4402 - 4409