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Numerical Modeling Of High-temperature Shell-and-tube Heat Exchanger And Chemical Decomposer For Hydrogen Production

机译:制氢用高温管壳式换热器及化学分解器的数值模拟

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Numerical simulations of shell-and-tube heat exchanger and chemical decomposer with straight tube configuration and porous media were performed using FLUENT6.2.16 to examine the percentage decomposition of sulfur trioxide. The decomposition process can be a part of sulfur-iodine (S-I) thermochemical water splitting cycle, which is one of the most studied cycles for hydrogen production. A steady-state, laminar, two-dimensional axisymmetric shell-and-tube model with counter flow and parallel flow arrangements and simple uniform cubical packing was developed using porous medium approach to investigate the fluid flow, heat transfer and chemical reactions in the decomposer. As per the investigation, the decomposition percentage of sulfur trioxide for counter flow arrangement was found to be 93% and that of parallel flow was 92%. Also, a high pressure drop was observed in counter flow arrangement compared to parallel flow. The effects of inlet velocity, temperature and the porous medium properties on the pressure drop across the porous medium were studied. The influence of geometric parameters mainly the diameter of the tube, diameter of the shell and the length of the porous zone on the percentage decomposition of sulfur trioxide in the tube was investigated as well. A preliminary parametric study of the mentioned configuration is conducted to explore effects of varying parameters on the decomposition of sulfur trioxide. From the performed calculations, it was found that the Reynolds number played a significant role in affecting the sulfur trioxide decomposition. The percentage decomposition decreases with an increase in Reynolds number. Surface-to-volume area ratio and activation energy were also the important parameters that influenced the decomposition percentage. A high surface-to-volume area ratio enhances the rate of the chemical reaction and high activation energy decreases the decomposition percentage. The decomposition of sulfur trioxide is calculated and compared for both counter and parallel flow arrangements.
机译:使用FLUENT6.2.16进行了具有直管结构和多孔介质的管壳式换热器和化学分解器的数值模拟,以检查三氧化硫的分解百分数。分解过程可能是硫碘(S-I)热化学水分解循环的一部分,这是研究最多的制氢循环之一。利用多孔介质方法研究了具有逆流和平行流布置以及简单均匀的立方堆积的稳态层流二维轴对称壳管模型,以研究分解器中的流体流动,传热和化学反应。根据研究,发现用于逆流布置的三氧化硫的分解百分数为93%,而平行流的分解百分数为92%。另外,与平行流相比,在逆流布置中观察到高的压降。研究了入口速度,温度和多孔介质特性对穿过多孔介质的压降的影响。还研究了几何参数,主要是管的直径,壳的直径和多孔区域的长度对管中三氧化硫分解百分比的影响。进行了上述配置的初步参数研究,以探索各种参数对三氧化硫分解的影响。从进行的计算中发现,雷诺数在影响三氧化硫分解中起重要作用。分解百分数随着雷诺数的增加而降低。表面积体积比和活化能也是影响分解百分数的重要参数。高的表面积体积比提高了化学反应的速率,高的活化能降低了分解百分数。计算并比较了逆流和并流布置的三氧化硫分解情况。

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