Adsorption Desulfurization Of Iraqi Heavy Naphtha Using Zeolite 13x

M. M. Yahya, H. Hussein
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引用次数: 2

Abstract

This work was conducted to study the effect of selective adsorption on removal of sulfur  compounds  from  Iraqi  heavy  naphtha  from  Al-Dura refinery  by using  molecular  sieve (13X)  in a fixed-bed column and  it was be run out at 1.5–6.0h-1 LHSV, 15–30 gr  weight of molecular sieve (13X), 600–1650ppm sulfur concentration in the feedstock ,  the adsorption  temperature  was  25oC and 40oC.  The best operating conditions for removing sulfur compounds was 3.0 h-1 LHSV, 20 gr molecular sieve bed weight and 25oC temperature, where the sulfur content in heavy naphtha was reduced from nearly 600 ppm to less than 1 ppm (by weight). Regeneration steps was thermally took place by hot air flow in a range from 16.66 – 25 liter / min and temperature range from 200–350oC, the best desorption conditions for (85.8%) weight percent removing was at 16.66 liter / min air flow and 350 oC.
沸石13x吸附脱硫伊拉克重质石脑油
本研究采用分子筛(13X)在固定床塔中选择性吸附Al-Dura炼油厂伊拉克重质石脑油中含硫化合物,在1.5 ~ 6.0h-1 LHSV、分子筛重量15 ~ 30 g (13X)、原料硫浓度600 ~ 1650ppm、吸附温度为25℃和40℃的条件下运行。在3.0 h-1 LHSV、20 g分子筛床重、25℃温度条件下,重质石脑油中硫含量由近600 ppm降至1 ppm以下(重量计)。在16.66 ~ 25 l / min的热风流量和200 ~ 350℃的温度下进行再生,在350℃和16.66 l / min的空气流量条件下脱附效果最佳,脱附率为85.8%。
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