Numerical modeling and experimental validation of fractional heat transfer induced by gas adsorption in heterogeneous coal matrix

被引:25
|
作者
Kang, Jianhong [1 ,2 ]
Zhang, Di [2 ]
Zhou, Fubao [1 ,2 ]
Li, Haijian [2 ]
Xia, Tongqiang [3 ]
机构
[1] China Univ Min & Technol, Jiangsu Key Lab Fire Safety Urban Underground Spa, Xuzhou 221116, Jiangsu, Peoples R China
[2] China Univ Min & Technol, Sch Safety Engn, Xuzhou 221116, Jiangsu, Peoples R China
[3] China Univ Min & Technol, Sch Elect & Power Engn, Xuzhou 221008, Jiangsu, Peoples R China
关键词
Fractional derivative; Heat transfer; Gas adsorption; Coal matrix; CONDUCTION EQUATION; DIFFUSION-MODEL; CARBON-DIOXIDE; SORPTION; METHANE; CO2; FLOW; IMPACT; TIME; SUBDIFFUSION;
D O I
10.1016/j.ijheatmasstransfer.2018.08.087
中图分类号
O414.1 [热力学];
学科分类号
摘要
Despite one fundamental issue in the adsorption theory of coalbed methane, little is known about the thermodynamic properties of gas adsorption in a porous coal matrix. In this work, considering the heterogeneity of pore structure and the exothermic characteristics of gas adsorption, a fractional heat conduction model with an unsteady volumetric heat source is proposed to study the heat transfer process induced by gas adsorption in a heterogeneous coal matrix. The heat conduction equation with a fractional time derivative is discretized by using an implicit numerical method based on the generalization of a standard finite-difference scheme. First, to validate the fractional heat conduction model, gas adsorption experiments on a microcalorimeter were carried out on 5 g coal samples of 0.3 mm diameter at 25 degrees C. The experimental heat flux with initial adsorption pressures of 3.23 bar, 5.83 bar and 9.77 bar increases rapidly from zero to peak values of 7.17 mW, 12.05 mW and 16.81 mW in less than 7 min (i.e., fast thermal diffusion stage) and then decreases slowly to zero again in approximately 2 h (i.e., slow thermal diffusion stage). It is revealed that for all tested gas pressures the fractional heat conduction model with a fractional order alpha = 0.86 can reproduce the experimental process of heat flux with better accuracy than the Fourier law-based model (i.e., alpha = 1), suggesting that anomalous thermal diffusion is the governing heat transfer process of gas adsorption in the coal matrix. Second, the spatial distribution and temporal evolution of temperature patterns with different model parameters are numerically simulated. It is found that the time to reach the peak temperature decreases from 760 s at the center of the coal particles to 490 s at the boundary. Finally, the parametric sensitivity of the thermodynamic properties of gas adsorption such as temperature, heat flux and integral adsorption heat is discussed in detail. Particularly, it is shown that as one of the most important thermodynamic parameters, the integral heat is very sensitive to the fractional order a. In the case of 3.23 bar, if a increases from 0.75 to 1, while other model parameters remain unchanged, the integral heat could be enhanced from 1.1 J/g to 8.5 J/g. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:492 / 503
页数:12
相关论文
共 50 条
  • [41] Experimental study and numerical modeling of heat and mass transfer in rubberwood during kiln drying
    Santi Khamtree
    Thanate Ratanawilai
    Chayut Nuntadusit
    Hormoz Marzbani
    Heat and Mass Transfer, 2021, 57 : 453 - 464
  • [42] Numerical investigation on heat transfer characteristics of the plate air heater with variable channels and experimental validation
    Li, Haowen
    Wu, Lijun
    Yuan, Zhicheng
    Yuan, Zhaokuo
    APPLIED THERMAL ENGINEERING, 2017, 122 : 546 - 554
  • [43] Numerical Simulation and Experimental Validation of Coupled Flow, Heat Transfer and Electromagnetic Problems in Electrical Transformers
    Jacek Smolka
    Oszkár Bíró
    Andrzej J. Nowak
    Archives of Computational Methods in Engineering, 2009, 16 : 319 - 355
  • [44] Experimental study and numerical modeling of heat and mass transfer in rubberwood during kiln drying
    Khamtree, Santi
    Ratanawilai, Thanate
    Nuntadusit, Chayut
    Marzbani, Hormoz
    HEAT AND MASS TRANSFER, 2021, 57 (03) : 453 - 464
  • [45] Comprehensive numerical modeling analysis and experimental validation of a multi-turn pulsating heat pipe
    Opalski, Marcin
    Czajkowski, Cezary
    Blasiak, Przemyslaw
    Nowak, Andrzej Ireneusz
    Ishimoto, Jun
    Pietrowicz, Slawomir
    INTERNATIONAL COMMUNICATIONS IN HEAT AND MASS TRANSFER, 2024, 159
  • [46] Experimental Modeling of Gas-Solid Heat Transfer in a Pipe with Various Inclination Angles
    Mokhtarifar, Naser
    Saffaraval, Farhad
    Saffar-Avval, Majid
    Mansoori, Zohreh
    Siamie, Alireza
    HEAT TRANSFER ENGINEERING, 2015, 36 (01) : 113 - 122
  • [47] Modeling a Porous Region for Natural Convection Heat Transfer and Experimental Validation in Slender Cylindrical Geometries
    Noah, Olugbenga O.
    Slabber, Johan F.
    Meyer, Josua P.
    NUCLEAR TECHNOLOGY, 2016, 193 (03) : 375 - 390
  • [48] Numerical Investigation with Experimental Validation of Heat and Mass Transfer during Evaporation in the Porous Wick within a Loop Heat Pipe
    Zheng, Suzheng
    Lin, Binyao
    Zhao, Chenyang
    Zhou, Xue
    Li, Nanxi
    Dong, Deping
    ENERGIES, 2023, 16 (05)
  • [49] Numerical simulation and experimental studies on heat and mass transfer using sweeping gas membrane distillation
    Charfi, K.
    Khayet, M.
    Safi, M. J.
    DESALINATION, 2010, 259 (1-3) : 84 - 96
  • [50] Numerical and experimental study of the heat transfer and fluid flow by thermocapillary convection around gas bubbles
    J. Betz
    J. Straub
    Heat and Mass Transfer, 2001, 37 : 215 - 227