轻石脑油组分在沸石(5A)和活性炭上的吸附行为

Q4 Chemical Engineering
A. Hammadi, I. Shakir
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引用次数: 2

摘要

轻石脑油:炼油厂精馏塔的一种产品,用作生产汽油的原料。轻石脑油的主要成分有(正石蜡、异石蜡、环烷烃和芳烃)。本文采用孔径均匀(5Ao)的沸石(5A)对轻石脑油进行分离,由于其孔径适合该工艺,并与孔径范围广(微孔和介孔)、比表面积大的活性炭进行吸附行为比较。该工艺在连续系统-固定床反应器-气相中进行,恒定条件为流量5 ml/min,温度180℃,压力1.6 bar,每种吸附剂重量100克。我们注意到分子筛(5A)将正石蜡(C4 - C8)从轻石脑油原料中分离出来,直到平衡(饱和)。活性炭分离了环烷和芳烃,此外,正烷烃的另一组分为C6(正己烷)、C7(正庚烷)和C8(正辛烷)。C4(正丁烷)、C5(正戊烷)的质量百分比和异石蜡的质量百分比依次增加,直至达到平衡(饱和)。研究结果表明,不同的孔隙大小对不同的吸附过程有不同的影响。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated Carbon
Light naphtha one of the products from distillation column in oil refineries used as feedstock for gasoline production. The major constituents of light naphtha are (Normal Paraffin, Isoparaffin, Naphthene, and Aromatic). In this paper, we used zeolite (5A) with uniform pores size (5Ao) to separate normal paraffin from light naphtha, due to suitable pore size for this process and compare the behavior of adsorption with activated carbon which has a wide range of pores size (micropores and mesopores) and high surface area. The process is done in a continuous system - Fixed bed reactor- at the vapor phase with the constant conditions of flow rate 5 ml/min, temperature 180oC, pressure 1.6 bar and 100-gram weight of each adsorbents. We notice that the molecular sieve (5A) separated the normal paraffin (C4 – C8) from light naphtha feed until equilibrium (saturation). Activated carbon separated naphthene and aromatics, in addition, the other component of normal paraffin C6 (n-hexane), C7 (n-heptane) and C8 (n-octane). And there is increasing in weight percentage of C4 (n-butane), C5 (n-pentane) and the weight percentage of isoparaffin until equilibrium (Saturation). The study showed the difference in physical adsorption behavior and the effect of pore size on these processes.
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来源期刊
CiteScore
1.20
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