固体颗粒油馏分加氢处理催化剂的防护:实验研究与计算

I. Mik, O. P. Klenov, M. O. Kazakov, K. Nadeina, O. Klimov, S. I. Reshetnikov, A. Noskov
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引用次数: 0

摘要

对柴油中含有的固体微颗粒的捕集效率进行了研究,以便进行催化剂装填--这是对水处理过程中的防护床工业包的模拟。该催化剂包由催化剂颗粒组成,颗粒的形状和大小依次为:分段环形、两种标准尺寸的空心圆柱形和三叶形。实验是在涓流状态下进行的,在催化剂装填入口处有 5 至 150 μm 大小的微粒子--铁鳞的恒定组合。实验发现,在实验过程中,防护床催化剂负载的渗透系数没有明显变化(K ≈ 0.985)。同时,在高度为 17 厘米的防护床上,由于催化剂颗粒对固体微颗粒的截留作用,催化剂负载的压降呈线性上升趋势,从 220 Pa 上升到 408 Pa。初始压降的理论估计值(228 帕)与实验数据(220 帕)非常吻合。
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Guard of hydrotreating catalysts of oil fractions from solid particulates: experimental studies and calculation
A study was made of the efficiency of trapping solid microparticulates contained in diesel fuel for catalyst loading – an analogue of an industrial package of guard beds of hydroprocesses. The package of catalysts consisted of catalyst granules ranked by shape and size: segmented rings, hollow cylinders of two standard sizes and trilobe shape. The experiments were carried out in the trickle flow regime with a constant ensemble of microparticulates – iron scale with a size of 5 to 150 μm at the inlet of the catalysts loading. It was found that the penetration coefficient of the catalysts loading of the guard beds did not change significantly (K ≈ 0.985) during the experiment. At the same time, a linear increase in the pressure drop on the catalysts loading of the guard beds with a height of 17 cm from 220 to 408 Pa was observed which occurred as a result of the trapping of solid microparticulates by the catalyst granules. The theoretical estimate of the initial pressure drop (228 Pa) coincides with the experimental data (220 Pa) with good accuracy.
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