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Some studies on wall-to-bed heat transfer in a pressurized circulating fluidized bed unit

机译:关于加压循环流化床单元中壁上床传热的研究

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In the present work, a pressurized circulating fluidized bed (PCFB) unit of 54 mm inner diameter and riser height Of 2000 mm has been fabricated to investigate the effect of pressure on suspension density and heat transfer. The effects of blending of biomass in sand, and superficial velocity on bed hydrodynamics and heat transfer has also been studied. Experiments have been conducted at four different percentage blending of biomass such as 2.5 %, 7.5 %, 15 % and 20 % in sand with two different weight composition ratios and at a superficial velocity of 5 m/s. Operating pressure is varied from 1 to 5 bar in a step of 2 bar. Results show that, the axial heat transfer coefficient increases from the bottom to the top of heat transfer probe with the increase in operating pressure. The radial variation of heat transfer coefficient decreases from the wall to the core of the heat transfer probe. The heat transfer coefficient is also found to be higher in between the 7.5 to 15 % biomass blending in sand. The overall uncertainty in calculating heat transfer coefficient is found to be 3.90 %.
机译:在本作工作中,已经制造了一个54mm内径的加压流化床(PCFB)单元和2000mM的提升管高度,以研究压力对悬浮密度和传热的影响。还研究了沙子中生物质混合的影响,以及床流体动力学和热传递的浅表速度。实验已经以四种不同的百分比对生物质混合进行,如2.5%,7.5%,15%和20%,砂中具有两种不同的重量组成比,并且在浅刻速度为5m / s。在2巴的步骤中,操作压力在1到5巴中变化。结果表明,轴向传热系数从热传递探针的底部增加到顶部,随着操作压力的增加。传热系数的径向变化从壁到传热探针的核心减小。在沙子中混合的7.5至15%生物质中也发现传热系数较高。计算传热系数的总体不确定性是3.90%。

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