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...

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Main Authors: Ahmed Najeeb Hammadi, Ibtehal K. Shakir
Format: Article
Language:English
Published: University of Baghdad/College of Engineering 2019-12-01
Series:Iraqi Journal of Chemical and Petroleum Engineering
Subjects:
Online Access:http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/525
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spelling doaj-033f607286464456800667cb96caf2e62020-11-25T01:46:57ZengUniversity of Baghdad/College of EngineeringIraqi Journal of Chemical and Petroleum Engineering1997-48842618-07072019-12-0120410.31699/IJCPE.2019.4.5525Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated CarbonAhmed Najeeb Hammadi0Ibtehal K. Shakircollege of engineering- university of baghdad 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. http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/525Light naphtha , Zeolite (5A) , Activated carbon , Adsorption process .
collection DOAJ
language English
format Article
sources DOAJ
author Ahmed Najeeb Hammadi
Ibtehal K. Shakir
spellingShingle Ahmed Najeeb Hammadi
Ibtehal K. Shakir
Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated Carbon
Iraqi Journal of Chemical and Petroleum Engineering
Light naphtha , Zeolite (5A) , Activated carbon , Adsorption process .
author_facet Ahmed Najeeb Hammadi
Ibtehal K. Shakir
author_sort Ahmed Najeeb Hammadi
title Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated Carbon
title_short Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated Carbon
title_full Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated Carbon
title_fullStr Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated Carbon
title_full_unstemmed Adsorption Behavior of Light Naphtha Components on Zeolite (5A) and Activated Carbon
title_sort adsorption behavior of light naphtha components on zeolite (5a) and activated carbon
publisher University of Baghdad/College of Engineering
series Iraqi Journal of Chemical and Petroleum Engineering
issn 1997-4884
2618-0707
publishDate 2019-12-01
description 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.
topic Light naphtha , Zeolite (5A) , Activated carbon , Adsorption process .
url http://ijcpe.uobaghdad.edu.iq/index.php/ijcpe/article/view/525
work_keys_str_mv AT ahmednajeebhammadi adsorptionbehavioroflightnaphthacomponentsonzeolite5aandactivatedcarbon
AT ibtehalkshakir adsorptionbehavioroflightnaphthacomponentsonzeolite5aandactivatedcarbon
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