Adsorption Desulfurization Of Iraqi Heavy Naphtha Using Zeolite 13x
Author(s) -
Muwafaq Mohammed Yahya,
Hussein Qasim Hussein
Publication year - 2019
Publication title -
association of arab universities journal of engineering sciences
Language(s) - English
Resource type - Journals
eISSN - 2616-9401
pISSN - 1726-4081
DOI - 10.33261/jaaru.2019.26.2.003
Subject(s) - naphtha , zeolite , adsorption , flue gas desulfurization , molecular sieve , sulfur , chemistry , desorption , space velocity , raw material , refinery , chromatography , organic chemistry , catalysis , selectivity
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 25C and 40C. The best operating conditions for removing sulfur compounds was 3.0 h-1 LHSV, 20 gr molecular sieve bed weight and 25C 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 200–350C, the best desorption conditions for (85.8%) weight percent removing was at 16.66 liter / min air flow and 350 C. Keywords— Adsorption, heavy naphtha, molecular sieve 13X; fixed bed, regeneration.
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