Abstract
Combined with the backfill mining, the heat collection tube group (HCTG) in the backfill body can extract geothermal energy, which can effectively alleviate heat damage caused by high ground temperature. This paper takes the HCTG as research object, the temperature, velocity and pressure distribution of the heat transfer fluid (HTF) during the heat release process of the backfill body were analyzed, and the influences of Re, tube diameter, tube spacing and tube arrangement on the performance of the HCTG were discussed. The results show that the heat transfer capacity increases from 2.24×103 kJ to 16.78×103 kJ and the comprehensive evaluation factor increases from 0.087 to 1.31 for Re from 100 to 5000. The heat transfer capacity increases from 15.07×103 kJ to 17.11×103 kJ and the comprehensive evaluation factor increases from 1.157 to 1.388 for tube diameter from 4 mm to 6 mm. The heat transfer capacity increases from 14.24>103 kJ to 16.25>103 kJ and the comprehensive evaluation factor increases from 1.013 to 1.263 for tube spacing from 130 mm to 170 mm. In addition, the four-way parallel arrangement can ensure higher heat transfer capacity and lower pressure drop, and obtain a higher comprehensive evaluation factor. The research provides a theoretical reference for the design and optimization of HCTG in the backfill body.
摘要
通过将采热管群与充填采矿技术相结合可提取矿井中的地热能,有效缓解高地热带来的热害问 题。本文以采热管群为研究对象,分析了充填体放热过程中传热流体的温度、速度和压力分布,讨论 了雷诺数、管径、管间距和管排方式对采热管群性能的影响。结果表明:当雷诺数从100 增加到5000 时,换热量从2.24×103 kJ 增加到16.78×103 kJ,综合评价因子从0.087 增加到1.31。当管径从4 mm增加 到 6 mm时,换热量从15.07×103 kJ 增加到17.11×103 kJ,综合评价因子从1.157 增加到1.388。当管间距 从130 mm增加到170 mm时,换热量从14.24×103 kJ 增加到16.25×103 kJ,综合评价因子从1.013 增加到 1.263。此外,四路并联布置可以保证较高的换热量和较低的压降,从而获得较高的综合评价因子。该 研究为充填体中采热管群的设计和优化提供了理论参考。
Abbreviations
- A m :
-
Mushy zone constant
- C :
-
Inertial coefficient (m−1)
- C P :
-
Specific heat capacity (J/(kg·K))
- \({\vec K}\) :
-
Body force in the momentum equation
- \({\vec g}\) :
-
Acceleration of gravity (m/s2)
- k :
-
Effective thermal conductivity (W/(m·K))
- T :
-
Temperature (K)
- N :
-
Permeability of porous foam (m−2)
- PCM :
-
phase change material
- d :
-
Diameter (m)
- B :
-
Thermal expansion coefficient (K−1)
- L :
-
Latent heat capacity
- Nu :
-
Nusselt number
- Q :
-
Heat transfer capacity (kJ)
- q :
-
Heat flux (W/m2)
- Re :
-
Reynolds number
- \({\vec V}\) :
-
Velocity vector (m/s)
- V :
-
Volume (m3)
- β :
-
Liquid fraction
- ρ :
-
Density (kg/m3)
- γ :
-
Thermal conductivity (W/(m·K))
- α :
-
Thermal diffusivity (m2/s)
- ε :
-
Porosity
- τ :
-
Dynamic viscosity (kg/(m·s))
- τ :
-
Time (s)
- f:
-
Reference
- b:
-
Backfill body
- mp:
-
Microcapsule PCM
- in:
-
Inlet
- out:
-
Outlet
- l:
-
Liquid
- s:
-
Solid
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Foundation item: Projects(51974225, 52274063, 52304154, 52104148) supported by the National Natural Science Foundation of China; Project(2022JQ-401) supported by the Natural Science Basic Research Program of Shaanxi Province of China; Project (21JP077) supported by Scientific Research Project of Youth Innovation Team Construction of Shaanxi Provincial Department of Education
Contributors
ZHANG Xiao-yan: Writing-review & editing. DU Qiang-qiang: Writing original draft, Results analysis. LIU Lang: Conceptualization, methodology. XU Mu-yan: Supervision, Data Curation. KE Ya-ping: Supervision, Data Curation. WANG Xue-li: Review & Editing.
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The authors declare that there is no conflict of interests regarding the publication of the article titled “Study on the thermal and pressure performance of heat collection tube group in the backfill body added with phase change material”.
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Zhang, Xy., Du, Qq., Liu, L. et al. Thermal and pressure performance of heat collection tube group in backfill body added with phase change material. J. Cent. South Univ. 31, 649–669 (2024). https://doi.org/10.1007/s11771-024-5588-5
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DOI: https://doi.org/10.1007/s11771-024-5588-5