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Heat transfer characteristics of the metal hydride vessel based on the plate-fin type heat exchanger

机译:基于板翅式热交换器的金属氢化物容器的传热特性

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Heat transfer characteristics of the metal hydride vessel based on the plate-fin type heat exchanger were investigated. Metal hydride beds were filled with AB_2 type hydrogen-storage alloy's particles, Ti_(0.42)Zr_(0.58)Cr_(0.78)Fe_(0.57)Ni_(0.2)Mn_(0.39)Cu_(0.03), with a storage capacity of 0.92 wt.%. Heat transfer model in the metal hydride bed based on the heat transfer mechanism for packed bed proposed by Kunii and co-workers is presented. The time-dependent hydrogen absorption/desorption rate and pressure in the metal hydride vessel calculated by the model were compared with the experimental results. During the hydriding, calculated hydrogen absorption rates agreed with measured ones. Calculated thermal equilibrium hydrogen pressures were slightly lower than the measured hydrogen pressures at the inlet of metal hydride vessel. Taking account of the pressure gradient between the inlet of metal hydride vessel and the metal hydride bed, it is considered that this discrepancy is reasonable. During the dehydriding, there were big differences between the calculated hydrogen desorption rates and measured ones. As calculated hydrogen desorption rates were lower than measured ones, there were big differences between the calculated thermal equilibrium hydrogen pressures and the measured hydrogen pressures at the inlet of metal hydride vessel. It is considered that those differences are due to the differences of the heat transfer characteristics such as thermal conductivity of metal hydride particles and porosity between the assumed and actual ones. It is important to obtain the heat transfer characteristics such as thermal conductivity of metal hydride particles and porosity both during the hydriding and dehydriding to design a metal hydride vessel.
机译:研究了基于板翅式热交换器的金属氢化物容器的传热特性。金属氢化物床填充AB_2型储氢合金颗粒Ti_(0.42)Zr_(0.58)Cr_(0.78)Fe_(0.57)Ni_(0.2)Mn_(0.39)Cu_(0.03),存储容量为0.92 wt 。%。基于Kunii及其同事提出的基于填充床传热机理的金属氢化物传热模型。将模型计算出的金属氢化物容器中随时间变化的氢吸收/解吸速率和压力与实验结果进行了比较。在氢化过程中,计算出的氢吸收率与实测值一致。计算得出的热平衡氢气压力略低于金属氢化物容器进口处的氢气压力。考虑到金属氢化物容器入口与金属氢化物床之间的压力梯度,认为这种差异是合理的。在脱水过程中,计算出的氢解吸速率与测得的氢解吸速率之间存在很大差异。由于计算出的氢解吸速率低于实测值,因此在金属氢化物容器进口处计算出的热平衡氢气压力与实测氢气压力之间存在较大差异。认为这些差异是由于传热特性(例如金属氢化物颗粒的导热率和假定的和实际的之间的孔隙率)的不同引起的。重要的是在氢化和脱水期间获得热传递特性,例如金属氢化物颗粒的导热性和孔隙率,以设计金属氢化物容器。

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