z-logo
open-access-imgOpen Access
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.

The content you want is available to Zendy users.

Already have an account? Click here to sign in.
Having issues? You can contact us here
Accelerating Research

Address

John Eccles House
Robert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom