Thermal Science and Engineering Progress · 2019 · 13 citations · 8 references
EngineeringChemical EngineeringMaterials EngineeringHeat TransferThermodynamicsTransport PhenomenaHeat ConductionHeat Transfer AnalysisHeat Transfer In ReactorsHeat Transfer ModelingRefrigerationThermal Properties Of MaterialsContact Heat TransferDensityHeat Transfer Coefficient EstimationHeat Transfer In Packed BedsThermal ConductivityThermal Conductivity EstimationThermal Conductivity ModelingWall Heat Transfer
This paper investigates the heat transfer coefficient of the wall to packed carbon contact (h) and the thermal conductivity of the packed bed (λ) by using parameters estimation method. A numerical heat conduction method was used in conjunction with an iterative process of minimizing the Mean Square Error (MSE) between both experimentally measured and model predicted temperatures in order to estimate h and λ parameters simultaneously. Experimental work was carried out by measuring the wall and centre temperatures of the sample reactor when suddenly submerged in a temperature controlled water bath at around 90 °C. Four samples with packed bed density ranging from 600 kg m−3 to 750 kg m−3 were tested. The results for the GAC-R723 refrigerant pair show a quasi-linear increase in both thermal conductivity (λ) and wall contact heat transfer coefficient (h) with packed bed density. The thermal conductivity of GAC-R723 refrigerant varies between 0.77 W m−1 K−1 and 1.36 W m−1 K−1 (about three times the values without R723 refrigerant) while the wall contact heat transfer coefficient varied between 390 W m−2 K−1 and 735 W m−2 K−1 (up to 30% better than values without R723).
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Studies on effective thermal conductivities in packed beds
Sakae Yagi, Daizō Kunii · AIChE Journal · 1957 · 738 citations
Engineering, Chemical Engineering, Materials Engineering +16
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Thermal conductivity of porous systems
A.V. Luikov, A. G. Shashkov, L. L. Vasiliev et al. · International Journal of Heat and Mass Transfer · 1968 · 201 citations