Loading…

Direct Gas–Solid Carbonation Kinetics of Steel Slag and the Contribution to In situ Sequestration of Flue Gas CO 2 in Steel‐Making Plants

Direct gas–solid carbonation of steel slag under various operational conditions was investigated to determine the sequestration of the flue gas CO 2 . X‐ray diffraction analysis of steel slag revealed the existence of portlandite, which provided a maximum theoretical CO 2 sequestration potential of...

Full description

Saved in:
Bibliographic Details
Published in:ChemSusChem 2013-12, Vol.6 (12), p.2348-2355
Main Authors: Tian, Sicong, Jiang, Jianguo, Chen, Xuejing, Yan, Feng, Li, Kaimin
Format: Article
Language:English
Citations: Items that this one cites
Items that cite this one
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
cited_by cdi_FETCH-LOGICAL-c846-5d6eb053386ff92d2faf8bb35aa7e0a34eb104a06ce83d3560e9a062ed8e873f3
cites cdi_FETCH-LOGICAL-c846-5d6eb053386ff92d2faf8bb35aa7e0a34eb104a06ce83d3560e9a062ed8e873f3
container_end_page 2355
container_issue 12
container_start_page 2348
container_title ChemSusChem
container_volume 6
creator Tian, Sicong
Jiang, Jianguo
Chen, Xuejing
Yan, Feng
Li, Kaimin
description Direct gas–solid carbonation of steel slag under various operational conditions was investigated to determine the sequestration of the flue gas CO 2 . X‐ray diffraction analysis of steel slag revealed the existence of portlandite, which provided a maximum theoretical CO 2 sequestration potential of 159.4 kg  t slag −1 as calculated by the reference intensity ratio method. The carbonation reaction occurred through a fast kinetically controlled stage with an activation energy of 21.29 kJ mol −1 , followed by 10 3 orders of magnitude slower diffusion‐controlled stage with an activation energy of 49.54 kJ mol −1 , which could be represented by a first‐order reaction kinetic equation and the Ginstling equation, respectively. Temperature, CO 2 concentration, and the presence of SO 2 impacted on the carbonation conversion of steel slag through their direct and definite influence on the rate constants. Temperature was the most important factor influencing the direct gas–solid carbonation of steel slag in terms of both the carbonation conversion and reaction rate. CO 2 concentration had a definite influence on the carbonation rate during the kinetically controlled stage, and the presence of SO 2 at typical flue gas concentrations enhanced the direct gas–solid carbonation of steel slag. Carbonation conversions between 49.5 % and 55.5 % were achieved in a typical flue gas at 600 °C, with the maximum CO 2 sequestration amount generating 88.5 kg  t slag −1 . Direct gas–solid carbonation of steel slag showed a rapid CO 2 sequestration rate, high CO 2 sequestration amounts, low raw‐material costs, and a large potential for waste heat utilization, which is promising for in situ carbon capture and sequestration in the steel industry.
doi_str_mv 10.1002/cssc.201300436
format article
fullrecord <record><control><sourceid>crossref</sourceid><recordid>TN_cdi_crossref_primary_10_1002_cssc_201300436</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>10_1002_cssc_201300436</sourcerecordid><originalsourceid>FETCH-LOGICAL-c846-5d6eb053386ff92d2faf8bb35aa7e0a34eb104a06ce83d3560e9a062ed8e873f3</originalsourceid><addsrcrecordid>eNo9kLFOwzAQhi0EEqWwMt8LpFzixE1HFGipKCpSOrBFTnIuhuCA7QzdujCDxBv2SWgp6nT_SXffL32MXYY4CBGjq8q5ahBhyBFjLo5YL0xFHCQifjo-ZB6esjPnXhAFjoTosa8bbanyMJFus_7J20bXkElbtkZ63Rq414a8rhy0CnJP1EDeyCVIU4N_Jsha460uu79b38LUbNafTvsOcvroyHm7x2y_x01HuxrI5hCBNnvcZv39IF-1WcJjI4135-xEycbRxf_ss8X4dpHdBbP5ZJpdz4IqjUWQ1IJKTDhPhVKjqI6UVGlZ8kTKIaHkMZUhxhJFRSmveSKQRtstojqldMgV77PBHlvZ1jlLqni3-k3aVRFisbNZ7GwWB5v8F45hbQk</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>Direct Gas–Solid Carbonation Kinetics of Steel Slag and the Contribution to In situ Sequestration of Flue Gas CO 2 in Steel‐Making Plants</title><source>Wiley-Blackwell Read &amp; Publish Collection</source><creator>Tian, Sicong ; Jiang, Jianguo ; Chen, Xuejing ; Yan, Feng ; Li, Kaimin</creator><creatorcontrib>Tian, Sicong ; Jiang, Jianguo ; Chen, Xuejing ; Yan, Feng ; Li, Kaimin</creatorcontrib><description>Direct gas–solid carbonation of steel slag under various operational conditions was investigated to determine the sequestration of the flue gas CO 2 . X‐ray diffraction analysis of steel slag revealed the existence of portlandite, which provided a maximum theoretical CO 2 sequestration potential of 159.4 kg  t slag −1 as calculated by the reference intensity ratio method. The carbonation reaction occurred through a fast kinetically controlled stage with an activation energy of 21.29 kJ mol −1 , followed by 10 3 orders of magnitude slower diffusion‐controlled stage with an activation energy of 49.54 kJ mol −1 , which could be represented by a first‐order reaction kinetic equation and the Ginstling equation, respectively. Temperature, CO 2 concentration, and the presence of SO 2 impacted on the carbonation conversion of steel slag through their direct and definite influence on the rate constants. Temperature was the most important factor influencing the direct gas–solid carbonation of steel slag in terms of both the carbonation conversion and reaction rate. CO 2 concentration had a definite influence on the carbonation rate during the kinetically controlled stage, and the presence of SO 2 at typical flue gas concentrations enhanced the direct gas–solid carbonation of steel slag. Carbonation conversions between 49.5 % and 55.5 % were achieved in a typical flue gas at 600 °C, with the maximum CO 2 sequestration amount generating 88.5 kg  t slag −1 . Direct gas–solid carbonation of steel slag showed a rapid CO 2 sequestration rate, high CO 2 sequestration amounts, low raw‐material costs, and a large potential for waste heat utilization, which is promising for in situ carbon capture and sequestration in the steel industry.</description><identifier>ISSN: 1864-5631</identifier><identifier>EISSN: 1864-564X</identifier><identifier>DOI: 10.1002/cssc.201300436</identifier><language>eng</language><ispartof>ChemSusChem, 2013-12, Vol.6 (12), p.2348-2355</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c846-5d6eb053386ff92d2faf8bb35aa7e0a34eb104a06ce83d3560e9a062ed8e873f3</citedby><cites>FETCH-LOGICAL-c846-5d6eb053386ff92d2faf8bb35aa7e0a34eb104a06ce83d3560e9a062ed8e873f3</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>314,776,780,27901,27902</link.rule.ids></links><search><creatorcontrib>Tian, Sicong</creatorcontrib><creatorcontrib>Jiang, Jianguo</creatorcontrib><creatorcontrib>Chen, Xuejing</creatorcontrib><creatorcontrib>Yan, Feng</creatorcontrib><creatorcontrib>Li, Kaimin</creatorcontrib><title>Direct Gas–Solid Carbonation Kinetics of Steel Slag and the Contribution to In situ Sequestration of Flue Gas CO 2 in Steel‐Making Plants</title><title>ChemSusChem</title><description>Direct gas–solid carbonation of steel slag under various operational conditions was investigated to determine the sequestration of the flue gas CO 2 . X‐ray diffraction analysis of steel slag revealed the existence of portlandite, which provided a maximum theoretical CO 2 sequestration potential of 159.4 kg  t slag −1 as calculated by the reference intensity ratio method. The carbonation reaction occurred through a fast kinetically controlled stage with an activation energy of 21.29 kJ mol −1 , followed by 10 3 orders of magnitude slower diffusion‐controlled stage with an activation energy of 49.54 kJ mol −1 , which could be represented by a first‐order reaction kinetic equation and the Ginstling equation, respectively. Temperature, CO 2 concentration, and the presence of SO 2 impacted on the carbonation conversion of steel slag through their direct and definite influence on the rate constants. Temperature was the most important factor influencing the direct gas–solid carbonation of steel slag in terms of both the carbonation conversion and reaction rate. CO 2 concentration had a definite influence on the carbonation rate during the kinetically controlled stage, and the presence of SO 2 at typical flue gas concentrations enhanced the direct gas–solid carbonation of steel slag. Carbonation conversions between 49.5 % and 55.5 % were achieved in a typical flue gas at 600 °C, with the maximum CO 2 sequestration amount generating 88.5 kg  t slag −1 . Direct gas–solid carbonation of steel slag showed a rapid CO 2 sequestration rate, high CO 2 sequestration amounts, low raw‐material costs, and a large potential for waste heat utilization, which is promising for in situ carbon capture and sequestration in the steel industry.</description><issn>1864-5631</issn><issn>1864-564X</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2013</creationdate><recordtype>article</recordtype><recordid>eNo9kLFOwzAQhi0EEqWwMt8LpFzixE1HFGipKCpSOrBFTnIuhuCA7QzdujCDxBv2SWgp6nT_SXffL32MXYY4CBGjq8q5ahBhyBFjLo5YL0xFHCQifjo-ZB6esjPnXhAFjoTosa8bbanyMJFus_7J20bXkElbtkZ63Rq414a8rhy0CnJP1EDeyCVIU4N_Jsha460uu79b38LUbNafTvsOcvroyHm7x2y_x01HuxrI5hCBNnvcZv39IF-1WcJjI4135-xEycbRxf_ss8X4dpHdBbP5ZJpdz4IqjUWQ1IJKTDhPhVKjqI6UVGlZ8kTKIaHkMZUhxhJFRSmveSKQRtstojqldMgV77PBHlvZ1jlLqni3-k3aVRFisbNZ7GwWB5v8F45hbQk</recordid><startdate>201312</startdate><enddate>201312</enddate><creator>Tian, Sicong</creator><creator>Jiang, Jianguo</creator><creator>Chen, Xuejing</creator><creator>Yan, Feng</creator><creator>Li, Kaimin</creator><scope>AAYXX</scope><scope>CITATION</scope></search><sort><creationdate>201312</creationdate><title>Direct Gas–Solid Carbonation Kinetics of Steel Slag and the Contribution to In situ Sequestration of Flue Gas CO 2 in Steel‐Making Plants</title><author>Tian, Sicong ; Jiang, Jianguo ; Chen, Xuejing ; Yan, Feng ; Li, Kaimin</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c846-5d6eb053386ff92d2faf8bb35aa7e0a34eb104a06ce83d3560e9a062ed8e873f3</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2013</creationdate><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Tian, Sicong</creatorcontrib><creatorcontrib>Jiang, Jianguo</creatorcontrib><creatorcontrib>Chen, Xuejing</creatorcontrib><creatorcontrib>Yan, Feng</creatorcontrib><creatorcontrib>Li, Kaimin</creatorcontrib><collection>CrossRef</collection><jtitle>ChemSusChem</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Tian, Sicong</au><au>Jiang, Jianguo</au><au>Chen, Xuejing</au><au>Yan, Feng</au><au>Li, Kaimin</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Direct Gas–Solid Carbonation Kinetics of Steel Slag and the Contribution to In situ Sequestration of Flue Gas CO 2 in Steel‐Making Plants</atitle><jtitle>ChemSusChem</jtitle><date>2013-12</date><risdate>2013</risdate><volume>6</volume><issue>12</issue><spage>2348</spage><epage>2355</epage><pages>2348-2355</pages><issn>1864-5631</issn><eissn>1864-564X</eissn><abstract>Direct gas–solid carbonation of steel slag under various operational conditions was investigated to determine the sequestration of the flue gas CO 2 . X‐ray diffraction analysis of steel slag revealed the existence of portlandite, which provided a maximum theoretical CO 2 sequestration potential of 159.4 kg  t slag −1 as calculated by the reference intensity ratio method. The carbonation reaction occurred through a fast kinetically controlled stage with an activation energy of 21.29 kJ mol −1 , followed by 10 3 orders of magnitude slower diffusion‐controlled stage with an activation energy of 49.54 kJ mol −1 , which could be represented by a first‐order reaction kinetic equation and the Ginstling equation, respectively. Temperature, CO 2 concentration, and the presence of SO 2 impacted on the carbonation conversion of steel slag through their direct and definite influence on the rate constants. Temperature was the most important factor influencing the direct gas–solid carbonation of steel slag in terms of both the carbonation conversion and reaction rate. CO 2 concentration had a definite influence on the carbonation rate during the kinetically controlled stage, and the presence of SO 2 at typical flue gas concentrations enhanced the direct gas–solid carbonation of steel slag. Carbonation conversions between 49.5 % and 55.5 % were achieved in a typical flue gas at 600 °C, with the maximum CO 2 sequestration amount generating 88.5 kg  t slag −1 . Direct gas–solid carbonation of steel slag showed a rapid CO 2 sequestration rate, high CO 2 sequestration amounts, low raw‐material costs, and a large potential for waste heat utilization, which is promising for in situ carbon capture and sequestration in the steel industry.</abstract><doi>10.1002/cssc.201300436</doi><tpages>8</tpages></addata></record>
fulltext fulltext
identifier ISSN: 1864-5631
ispartof ChemSusChem, 2013-12, Vol.6 (12), p.2348-2355
issn 1864-5631
1864-564X
language eng
recordid cdi_crossref_primary_10_1002_cssc_201300436
source Wiley-Blackwell Read & Publish Collection
title Direct Gas–Solid Carbonation Kinetics of Steel Slag and the Contribution to In situ Sequestration of Flue Gas CO 2 in Steel‐Making Plants
url http://sfxeu10.hosted.exlibrisgroup.com/loughborough?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-03T08%3A30%3A22IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-crossref&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Direct%20Gas%E2%80%93Solid%20Carbonation%20Kinetics%20of%20Steel%20Slag%20and%20the%20Contribution%20to%20In%E2%80%85situ%20Sequestration%20of%20Flue%20Gas%20CO%202%20in%20Steel%E2%80%90Making%20Plants&rft.jtitle=ChemSusChem&rft.au=Tian,%20Sicong&rft.date=2013-12&rft.volume=6&rft.issue=12&rft.spage=2348&rft.epage=2355&rft.pages=2348-2355&rft.issn=1864-5631&rft.eissn=1864-564X&rft_id=info:doi/10.1002/cssc.201300436&rft_dat=%3Ccrossref%3E10_1002_cssc_201300436%3C/crossref%3E%3Cgrp_id%3Ecdi_FETCH-LOGICAL-c846-5d6eb053386ff92d2faf8bb35aa7e0a34eb104a06ce83d3560e9a062ed8e873f3%3C/grp_id%3E%3Coa%3E%3C/oa%3E%3Curl%3E%3C/url%3E&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true