Removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.

Adsorption technology has led to the development of promising techniques to purify biogas, i.e., biomethane or biohydrogen. Such techniques mainly depend on the adsorbent ability and operating parameters. This research focused on adsorption technology for upgrading biogas technique by developing a n...

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Main Authors: Nurul Noramelya Zulkefli, Mohd Shahbudin Masdar, Wan Nor Roslam Wan Isahak, Jamaliah Md Jahim, Syahril Anuar Md Rejab, Chew Chien Lye
Format: Article
Language:English
Published: Public Library of Science (PLoS) 2019-01-01
Series:PLoS ONE
Online Access:https://doi.org/10.1371/journal.pone.0211713
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spelling doaj-325445b3f3854c268e4ef05e2731d4c72021-03-03T20:53:26ZengPublic Library of Science (PLoS)PLoS ONE1932-62032019-01-01142e021171310.1371/journal.pone.0211713Removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.Nurul Noramelya ZulkefliMohd Shahbudin MasdarWan Nor Roslam Wan IsahakJamaliah Md JahimSyahril Anuar Md RejabChew Chien LyeAdsorption technology has led to the development of promising techniques to purify biogas, i.e., biomethane or biohydrogen. Such techniques mainly depend on the adsorbent ability and operating parameters. This research focused on adsorption technology for upgrading biogas technique by developing a novel adsorbent. The commercial coconut shell activated carbon (CAC) and two types of gases (H2S/N2 and H2S/N2/CO2) were used. CAC was modified by copper sulfate (CuSO4), zinc acetate (ZnAc2), potassium hydroxide (KOH), potassium iodide (KI), and sodium carbonate (Na2CO3) on their surface to increase the selectivity of H2S removal. Commercial H2S adsorbents were soaked in 7 wt.% of impregnated solution for 30 min before drying at 120°C for 24 h. The synthesized adsorbent's physical and chemical properties, including surface morphology, porosity, and structures, were characterized by SEM-EDX, FTIR, XRD, TGA, and BET analyses. For real applications, the modified adsorbents were used in a real-time 0.85 L single-column adsorber unit. The operating parameters for the H2S adsorption in the adsorber unit varied in L/D ratio (0.5-2.5) and feed flow rate (1.5-5.5 L/min) where, also equivalent with a gas hourly space velocity, GHSV (212.4-780.0 hour-1) used. The performances of H2S adsorption were then compared with those of the best adsorbent that can be used for further investigation. Characterization results revealed that the impregnated solution homogeneously covered the adsorbent surface, morphology, and properties (i.e., crystallinity and surface area). BET analysis further shows that the modified adsorbents surface area decreased by up to 96%. Hence, ZnAc2-CAC clarify as the best adsorption capacity ranging within 1.3-1.7 mg H2S/g, whereby the studied extended to adsorption-desorption cycle.https://doi.org/10.1371/journal.pone.0211713
collection DOAJ
language English
format Article
sources DOAJ
author Nurul Noramelya Zulkefli
Mohd Shahbudin Masdar
Wan Nor Roslam Wan Isahak
Jamaliah Md Jahim
Syahril Anuar Md Rejab
Chew Chien Lye
spellingShingle Nurul Noramelya Zulkefli
Mohd Shahbudin Masdar
Wan Nor Roslam Wan Isahak
Jamaliah Md Jahim
Syahril Anuar Md Rejab
Chew Chien Lye
Removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.
PLoS ONE
author_facet Nurul Noramelya Zulkefli
Mohd Shahbudin Masdar
Wan Nor Roslam Wan Isahak
Jamaliah Md Jahim
Syahril Anuar Md Rejab
Chew Chien Lye
author_sort Nurul Noramelya Zulkefli
title Removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.
title_short Removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.
title_full Removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.
title_fullStr Removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.
title_full_unstemmed Removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.
title_sort removal of hydrogen sulfide from a biogas mimic by using impregnated activated carbon adsorbent.
publisher Public Library of Science (PLoS)
series PLoS ONE
issn 1932-6203
publishDate 2019-01-01
description Adsorption technology has led to the development of promising techniques to purify biogas, i.e., biomethane or biohydrogen. Such techniques mainly depend on the adsorbent ability and operating parameters. This research focused on adsorption technology for upgrading biogas technique by developing a novel adsorbent. The commercial coconut shell activated carbon (CAC) and two types of gases (H2S/N2 and H2S/N2/CO2) were used. CAC was modified by copper sulfate (CuSO4), zinc acetate (ZnAc2), potassium hydroxide (KOH), potassium iodide (KI), and sodium carbonate (Na2CO3) on their surface to increase the selectivity of H2S removal. Commercial H2S adsorbents were soaked in 7 wt.% of impregnated solution for 30 min before drying at 120°C for 24 h. The synthesized adsorbent's physical and chemical properties, including surface morphology, porosity, and structures, were characterized by SEM-EDX, FTIR, XRD, TGA, and BET analyses. For real applications, the modified adsorbents were used in a real-time 0.85 L single-column adsorber unit. The operating parameters for the H2S adsorption in the adsorber unit varied in L/D ratio (0.5-2.5) and feed flow rate (1.5-5.5 L/min) where, also equivalent with a gas hourly space velocity, GHSV (212.4-780.0 hour-1) used. The performances of H2S adsorption were then compared with those of the best adsorbent that can be used for further investigation. Characterization results revealed that the impregnated solution homogeneously covered the adsorbent surface, morphology, and properties (i.e., crystallinity and surface area). BET analysis further shows that the modified adsorbents surface area decreased by up to 96%. Hence, ZnAc2-CAC clarify as the best adsorption capacity ranging within 1.3-1.7 mg H2S/g, whereby the studied extended to adsorption-desorption cycle.
url https://doi.org/10.1371/journal.pone.0211713
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