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Experimental And Numerical Study Of Convection Heat Transfer Of Co_2 At Supercritical Pressures In Vertical Porous Tubes

机译:垂直多孔管中超临界压力下Co_2对流换热的实验与数值研究

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Convection heat transfer of CO_2 at supercritical pressures in vertical sintered porous tubes with particle diameters of 0.1-0.12 mm and 0.2-0.28 mm was investigated experimentally and numerically. The study investigated the influence of the inlet fluid temperature, mass flow rate, pressure, particle diameter, heat flux, flow direction and buoyancy on convection heat transfer in porous tubes. The results show that the inlet temperature, pressure, mass flow rate, particle diameter and heat flux all strongly influence the convection heat transfer at supercritical pressures. When the inlet temperature is much larger than the pseudocritical temperature, T_(pc), the local heat transfer coefficients in porous tubes are much less than when the inlet temperature is less than T_(pc). For T_o < T_(pc) and wall temperatures not much larger than T_(pc), the local heat transfer coefficients have a maximum for both upward flow and downward flow along the porous tube when the fluid bulk temperatures are near T_(pc). Buoyancy caused the different variations in the local heat transfer coefficients along the porous tube for upward and downward flows. The results also show that the heat transfer coefficients increase as the particle diameter decrease. The numerical simulations were performed using the local thermal equilibrium model with consideration of the effects of variable porosity, thermal dispersion and area-of-contact stagnant effective thermal conductivity. The experimental and numerical results for the friction factor of CO_2 at supercritical pressures flowing in sintered porous tubes at constant temperature (without heating) corresponded very well with the known correlation. However, the predicted results for the friction factor of CO_2 at supercritical pressures flowing in the heated sintered porous tube differ from those measured in the experiments both for upward and downward flows. The calculated wall temperatures corresponded well with the measured wall temperatures.
机译:实验和数值研究了粒径为0.1-0.12mm和0.2-0.28mm的垂直烧结多孔管中CO_2在超临界压力下的对流换热。该研究调查了入口流体温度,质量流量,压力,粒径,热通量,流向和浮力对多孔管中对流传热的影响。结果表明,入口温度,压力,质量流量,粒径和热通量均对超临界压力下的对流换热有很大影响。当入口温度远大于假临界温度T_(pc)时,多孔管中的局部传热系数要比入口温度小于T_(pc)时小得多。对于T_o

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