Loading…

Production of 1,3-propanediol via in situ glycerol hydrogenolysis in aqueous phase reforming using bimetallic W-Ni/CeO 2

The production of 1,3-propanediol via in situ glycerol hydrogenolysis and aqueous phase reforming is a promising technique to ensure high product yield with shorter reaction times and lower costs, as demonstrated in this study by investigating the effect of tungsten (W) doping on Ni/CeO catalysts. P...

Full description

Saved in:
Bibliographic Details
Published in:Environmental science and pollution research international 2024-10
Main Authors: Md Radzi, Mohamad Razlan, Rosli, Siti Nor Amira, Yusoff, Mohd Hizami Mohd, Abidin, Sumaiya Zainal
Format: Article
Language:English
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by
cites
container_end_page
container_issue
container_start_page
container_title Environmental science and pollution research international
container_volume
creator Md Radzi, Mohamad Razlan
Rosli, Siti Nor Amira
Yusoff, Mohd Hizami Mohd
Abidin, Sumaiya Zainal
description The production of 1,3-propanediol via in situ glycerol hydrogenolysis and aqueous phase reforming is a promising technique to ensure high product yield with shorter reaction times and lower costs, as demonstrated in this study by investigating the effect of tungsten (W) doping on Ni/CeO catalysts. Physicochemical properties of catalyst were determined using XRD, H -TPR, NH -TPD, BET, and FESEM-EDX techniques, and the catalytic performance was investigated at 230 °C, 20 bar, and 5 wt.% glycerol in an autoclave batch reactor. W doping ranging from 1-7% improved the catalyst's performance, with 3% W in 10% Ni/CeO₂ (3W10NC) achieving the highest yield (2.4%), selectivity (33.3%), and a good conversion rate (72.18%). The effect of reaction parameter on the 3W10NC catalyst showed that increasing pressure and temperature from the initial parameters had a detrimental effect on 1,3-propanediol attributed to the phenomenon called over-hydrogenolysis. Increasing the glycerol concentration to 20 wt.% also had a positive effect, resulting in the highest 1,3-propanediol yield of 22.27%. The effect of reaction time study revealed that the yield of 1,3-propanediol continued to increase steadily, reaching 38.29% after 4 h of reaction under the optimal conditions of 230 °C, 20 bar, and 20 wt.% glycerol. The kinetic study confirmed that the reaction follows first-order reaction with activation energy of 20.104 kJ mol . The catalyst reusability test revealed a decrease in the yield of 1,3-propanediol to 32.55%, likely due to deactivation caused by sintering and leaching, as indicated by the FESEM micrograph, EDX spectra, and NH -TPD.
doi_str_mv 10.1007/s11356-024-35262-x
format article
fullrecord <record><control><sourceid>pubmed</sourceid><recordid>TN_cdi_pubmed_primary_39397235</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>39397235</sourcerecordid><originalsourceid>FETCH-pubmed_primary_393972353</originalsourceid><addsrcrecordid>eNqFjstOwzAURC0kREvLD7BA9wMw9SMPZV2BWFEWSCwrN7lJL3JsY8eo-XuoBGs2M9KZsxjGbqV4kELUmySlLisuVMF1qSrFTxdsKStZ8LpomgW7TulDCCUaVV-xhW50UytdLtnpNfoutxN5B74Hea95iD4Yhx15C19kgBwkmjIMdm4x_sDj3EU_oPN2TpTOu_nM6HOCcDQJIWLv40hugJzOeaARJ2MttfDOX2izxR2oNbvsjU1489srdvf0-LZ95iEfRuz2IdJo4rz_u6r_Fb4B8pZQcw</addsrcrecordid><sourcetype>Index Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>Production of 1,3-propanediol via in situ glycerol hydrogenolysis in aqueous phase reforming using bimetallic W-Ni/CeO 2</title><source>Springer Nature</source><creator>Md Radzi, Mohamad Razlan ; Rosli, Siti Nor Amira ; Yusoff, Mohd Hizami Mohd ; Abidin, Sumaiya Zainal</creator><creatorcontrib>Md Radzi, Mohamad Razlan ; Rosli, Siti Nor Amira ; Yusoff, Mohd Hizami Mohd ; Abidin, Sumaiya Zainal</creatorcontrib><description>The production of 1,3-propanediol via in situ glycerol hydrogenolysis and aqueous phase reforming is a promising technique to ensure high product yield with shorter reaction times and lower costs, as demonstrated in this study by investigating the effect of tungsten (W) doping on Ni/CeO catalysts. Physicochemical properties of catalyst were determined using XRD, H -TPR, NH -TPD, BET, and FESEM-EDX techniques, and the catalytic performance was investigated at 230 °C, 20 bar, and 5 wt.% glycerol in an autoclave batch reactor. W doping ranging from 1-7% improved the catalyst's performance, with 3% W in 10% Ni/CeO₂ (3W10NC) achieving the highest yield (2.4%), selectivity (33.3%), and a good conversion rate (72.18%). The effect of reaction parameter on the 3W10NC catalyst showed that increasing pressure and temperature from the initial parameters had a detrimental effect on 1,3-propanediol attributed to the phenomenon called over-hydrogenolysis. Increasing the glycerol concentration to 20 wt.% also had a positive effect, resulting in the highest 1,3-propanediol yield of 22.27%. The effect of reaction time study revealed that the yield of 1,3-propanediol continued to increase steadily, reaching 38.29% after 4 h of reaction under the optimal conditions of 230 °C, 20 bar, and 20 wt.% glycerol. The kinetic study confirmed that the reaction follows first-order reaction with activation energy of 20.104 kJ mol . The catalyst reusability test revealed a decrease in the yield of 1,3-propanediol to 32.55%, likely due to deactivation caused by sintering and leaching, as indicated by the FESEM micrograph, EDX spectra, and NH -TPD.</description><identifier>EISSN: 1614-7499</identifier><identifier>DOI: 10.1007/s11356-024-35262-x</identifier><identifier>PMID: 39397235</identifier><language>eng</language><publisher>Germany</publisher><ispartof>Environmental science and pollution research international, 2024-10</ispartof><rights>2024. The Author(s), under exclusive licence to Springer-Verlag GmbH Germany, part of Springer Nature.</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,777,781,27905,27906</link.rule.ids><backlink>$$Uhttps://www.ncbi.nlm.nih.gov/pubmed/39397235$$D View this record in MEDLINE/PubMed$$Hfree_for_read</backlink></links><search><creatorcontrib>Md Radzi, Mohamad Razlan</creatorcontrib><creatorcontrib>Rosli, Siti Nor Amira</creatorcontrib><creatorcontrib>Yusoff, Mohd Hizami Mohd</creatorcontrib><creatorcontrib>Abidin, Sumaiya Zainal</creatorcontrib><title>Production of 1,3-propanediol via in situ glycerol hydrogenolysis in aqueous phase reforming using bimetallic W-Ni/CeO 2</title><title>Environmental science and pollution research international</title><addtitle>Environ Sci Pollut Res Int</addtitle><description>The production of 1,3-propanediol via in situ glycerol hydrogenolysis and aqueous phase reforming is a promising technique to ensure high product yield with shorter reaction times and lower costs, as demonstrated in this study by investigating the effect of tungsten (W) doping on Ni/CeO catalysts. Physicochemical properties of catalyst were determined using XRD, H -TPR, NH -TPD, BET, and FESEM-EDX techniques, and the catalytic performance was investigated at 230 °C, 20 bar, and 5 wt.% glycerol in an autoclave batch reactor. W doping ranging from 1-7% improved the catalyst's performance, with 3% W in 10% Ni/CeO₂ (3W10NC) achieving the highest yield (2.4%), selectivity (33.3%), and a good conversion rate (72.18%). The effect of reaction parameter on the 3W10NC catalyst showed that increasing pressure and temperature from the initial parameters had a detrimental effect on 1,3-propanediol attributed to the phenomenon called over-hydrogenolysis. Increasing the glycerol concentration to 20 wt.% also had a positive effect, resulting in the highest 1,3-propanediol yield of 22.27%. The effect of reaction time study revealed that the yield of 1,3-propanediol continued to increase steadily, reaching 38.29% after 4 h of reaction under the optimal conditions of 230 °C, 20 bar, and 20 wt.% glycerol. The kinetic study confirmed that the reaction follows first-order reaction with activation energy of 20.104 kJ mol . The catalyst reusability test revealed a decrease in the yield of 1,3-propanediol to 32.55%, likely due to deactivation caused by sintering and leaching, as indicated by the FESEM micrograph, EDX spectra, and NH -TPD.</description><issn>1614-7499</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2024</creationdate><recordtype>article</recordtype><recordid>eNqFjstOwzAURC0kREvLD7BA9wMw9SMPZV2BWFEWSCwrN7lJL3JsY8eo-XuoBGs2M9KZsxjGbqV4kELUmySlLisuVMF1qSrFTxdsKStZ8LpomgW7TulDCCUaVV-xhW50UytdLtnpNfoutxN5B74Hea95iD4Yhx15C19kgBwkmjIMdm4x_sDj3EU_oPN2TpTOu_nM6HOCcDQJIWLv40hugJzOeaARJ2MttfDOX2izxR2oNbvsjU1489srdvf0-LZ95iEfRuz2IdJo4rz_u6r_Fb4B8pZQcw</recordid><startdate>20241013</startdate><enddate>20241013</enddate><creator>Md Radzi, Mohamad Razlan</creator><creator>Rosli, Siti Nor Amira</creator><creator>Yusoff, Mohd Hizami Mohd</creator><creator>Abidin, Sumaiya Zainal</creator><scope>NPM</scope></search><sort><creationdate>20241013</creationdate><title>Production of 1,3-propanediol via in situ glycerol hydrogenolysis in aqueous phase reforming using bimetallic W-Ni/CeO 2</title><author>Md Radzi, Mohamad Razlan ; Rosli, Siti Nor Amira ; Yusoff, Mohd Hizami Mohd ; Abidin, Sumaiya Zainal</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-pubmed_primary_393972353</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2024</creationdate><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Md Radzi, Mohamad Razlan</creatorcontrib><creatorcontrib>Rosli, Siti Nor Amira</creatorcontrib><creatorcontrib>Yusoff, Mohd Hizami Mohd</creatorcontrib><creatorcontrib>Abidin, Sumaiya Zainal</creatorcontrib><collection>PubMed</collection><jtitle>Environmental science and pollution research international</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Md Radzi, Mohamad Razlan</au><au>Rosli, Siti Nor Amira</au><au>Yusoff, Mohd Hizami Mohd</au><au>Abidin, Sumaiya Zainal</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Production of 1,3-propanediol via in situ glycerol hydrogenolysis in aqueous phase reforming using bimetallic W-Ni/CeO 2</atitle><jtitle>Environmental science and pollution research international</jtitle><addtitle>Environ Sci Pollut Res Int</addtitle><date>2024-10-13</date><risdate>2024</risdate><eissn>1614-7499</eissn><abstract>The production of 1,3-propanediol via in situ glycerol hydrogenolysis and aqueous phase reforming is a promising technique to ensure high product yield with shorter reaction times and lower costs, as demonstrated in this study by investigating the effect of tungsten (W) doping on Ni/CeO catalysts. Physicochemical properties of catalyst were determined using XRD, H -TPR, NH -TPD, BET, and FESEM-EDX techniques, and the catalytic performance was investigated at 230 °C, 20 bar, and 5 wt.% glycerol in an autoclave batch reactor. W doping ranging from 1-7% improved the catalyst's performance, with 3% W in 10% Ni/CeO₂ (3W10NC) achieving the highest yield (2.4%), selectivity (33.3%), and a good conversion rate (72.18%). The effect of reaction parameter on the 3W10NC catalyst showed that increasing pressure and temperature from the initial parameters had a detrimental effect on 1,3-propanediol attributed to the phenomenon called over-hydrogenolysis. Increasing the glycerol concentration to 20 wt.% also had a positive effect, resulting in the highest 1,3-propanediol yield of 22.27%. The effect of reaction time study revealed that the yield of 1,3-propanediol continued to increase steadily, reaching 38.29% after 4 h of reaction under the optimal conditions of 230 °C, 20 bar, and 20 wt.% glycerol. The kinetic study confirmed that the reaction follows first-order reaction with activation energy of 20.104 kJ mol . The catalyst reusability test revealed a decrease in the yield of 1,3-propanediol to 32.55%, likely due to deactivation caused by sintering and leaching, as indicated by the FESEM micrograph, EDX spectra, and NH -TPD.</abstract><cop>Germany</cop><pmid>39397235</pmid><doi>10.1007/s11356-024-35262-x</doi></addata></record>
fulltext fulltext
identifier EISSN: 1614-7499
ispartof Environmental science and pollution research international, 2024-10
issn 1614-7499
language eng
recordid cdi_pubmed_primary_39397235
source Springer Nature
title Production of 1,3-propanediol via in situ glycerol hydrogenolysis in aqueous phase reforming using bimetallic W-Ni/CeO 2
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-01-19T16%3A52%3A35IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-pubmed&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Production%20of%201,3-propanediol%20via%20in%20situ%20glycerol%20hydrogenolysis%20in%20aqueous%20phase%20reforming%20using%20bimetallic%20W-Ni/CeO%202&rft.jtitle=Environmental%20science%20and%20pollution%20research%20international&rft.au=Md%20Radzi,%20Mohamad%20Razlan&rft.date=2024-10-13&rft.eissn=1614-7499&rft_id=info:doi/10.1007/s11356-024-35262-x&rft_dat=%3Cpubmed%3E39397235%3C/pubmed%3E%3Cgrp_id%3Ecdi_FETCH-pubmed_primary_393972353%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_id=info:pmid/39397235&rfr_iscdi=true