Chlorine Production by HCl Oxidation in a Molten Chloride Salt Catalyst
A molten salt mixture containing 45 mol % KCl and 55 mol % CuCl2 was investigated as a catalyst for the reaction of HCl with O2 to produce Cl2. The HCl conversion for an HCl:O2 molar feed ratio of 1:2 at 450 °C and a total pressure of 1 atm was 80% at a residence time of less than 1 s in a lab scale...
Gespeichert in:
Veröffentlicht in: | Industrial & engineering chemistry research 2018-06, Vol.57 (23), p.7795-7801 |
---|---|
Hauptverfasser: | , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 7801 |
---|---|
container_issue | 23 |
container_start_page | 7795 |
container_title | Industrial & engineering chemistry research |
container_volume | 57 |
creator | Su, Shizhao Mannini, Davide Metiu, Horia Gordon, Michael J McFarland, Eric W |
description | A molten salt mixture containing 45 mol % KCl and 55 mol % CuCl2 was investigated as a catalyst for the reaction of HCl with O2 to produce Cl2. The HCl conversion for an HCl:O2 molar feed ratio of 1:2 at 450 °C and a total pressure of 1 atm was 80% at a residence time of less than 1 s in a lab scale bubble column reactor. The equilibrium conversion at this temperature and pressure is 84%. The catalyst system was found to remain stable throughout a continuous 24-h experiment. The use of a mixed transition metal/alkali metal molten salt catalyst for HCl oxidation reduces the volatility of supported chlorides and may avoid the mechanical stability limitations of solid catalysts caused by volume changes between the halide and the oxide. |
doi_str_mv | 10.1021/acs.iecr.8b01141 |
format | Article |
fullrecord | <record><control><sourceid>acs_osti_</sourceid><recordid>TN_cdi_osti_scitechconnect_1539074</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><sourcerecordid>b02606855</sourcerecordid><originalsourceid>FETCH-LOGICAL-a344t-d21c11f708a24000533298dc02e7cc5d4ce48ba2c3d4481c0aecc00d47d1de653</originalsourceid><addsrcrecordid>eNp1kEFLAzEQRoMoWKt3j8GzWyfZxE2PsmgrVCqo55BOUpqyJpKkYP-9u65XTwMz3xtmHiHXDGYMOLszmGfeYZqpDTAm2AmZMMmhkiDkKZmAUqqSSslzcpHzHgCkFGJCFu2ui8kHR19TtAcsPga6OdJl29H1t7fmt-EDNfQldsUFOgLW0TfTFdqaYrpjLpfkbGu67K7-6pR8PD2-t8tqtV48tw-rytRClMpyhoxtG1CGi-GIuuZzZRG4axClFeiE2hiOtRVCMQTjEAGsaCyz7l7WU3Iz7o25eJ3RF4c7jCE4LJrJeg6N6EMwhjDFnJPb6q_kP006agZ6sKV7W3qwpf9s9cjtiAyTfTyk0H_xf_wH3wRs_w</addsrcrecordid><sourcetype>Open Access Repository</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype></control><display><type>article</type><title>Chlorine Production by HCl Oxidation in a Molten Chloride Salt Catalyst</title><source>American Chemical Society Journals</source><creator>Su, Shizhao ; Mannini, Davide ; Metiu, Horia ; Gordon, Michael J ; McFarland, Eric W</creator><creatorcontrib>Su, Shizhao ; Mannini, Davide ; Metiu, Horia ; Gordon, Michael J ; McFarland, Eric W ; Univ. of California, San Diego, CA (United States)</creatorcontrib><description>A molten salt mixture containing 45 mol % KCl and 55 mol % CuCl2 was investigated as a catalyst for the reaction of HCl with O2 to produce Cl2. The HCl conversion for an HCl:O2 molar feed ratio of 1:2 at 450 °C and a total pressure of 1 atm was 80% at a residence time of less than 1 s in a lab scale bubble column reactor. The equilibrium conversion at this temperature and pressure is 84%. The catalyst system was found to remain stable throughout a continuous 24-h experiment. The use of a mixed transition metal/alkali metal molten salt catalyst for HCl oxidation reduces the volatility of supported chlorides and may avoid the mechanical stability limitations of solid catalysts caused by volume changes between the halide and the oxide.</description><identifier>ISSN: 0888-5885</identifier><identifier>EISSN: 1520-5045</identifier><identifier>DOI: 10.1021/acs.iecr.8b01141</identifier><language>eng</language><publisher>United States: American Chemical Society</publisher><subject>Engineering</subject><ispartof>Industrial & engineering chemistry research, 2018-06, Vol.57 (23), p.7795-7801</ispartof><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-a344t-d21c11f708a24000533298dc02e7cc5d4ce48ba2c3d4481c0aecc00d47d1de653</citedby><cites>FETCH-LOGICAL-a344t-d21c11f708a24000533298dc02e7cc5d4ce48ba2c3d4481c0aecc00d47d1de653</cites><orcidid>0000-0002-3134-4493 ; 0000-0002-0697-4207 ; 0000000231344493 ; 0000000206974207</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktopdf>$$Uhttps://pubs.acs.org/doi/pdf/10.1021/acs.iecr.8b01141$$EPDF$$P50$$Gacs$$H</linktopdf><linktohtml>$$Uhttps://pubs.acs.org/doi/10.1021/acs.iecr.8b01141$$EHTML$$P50$$Gacs$$H</linktohtml><link.rule.ids>230,315,781,785,886,2766,27078,27926,27927,56740,56790</link.rule.ids><backlink>$$Uhttps://www.osti.gov/biblio/1539074$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Su, Shizhao</creatorcontrib><creatorcontrib>Mannini, Davide</creatorcontrib><creatorcontrib>Metiu, Horia</creatorcontrib><creatorcontrib>Gordon, Michael J</creatorcontrib><creatorcontrib>McFarland, Eric W</creatorcontrib><creatorcontrib>Univ. of California, San Diego, CA (United States)</creatorcontrib><title>Chlorine Production by HCl Oxidation in a Molten Chloride Salt Catalyst</title><title>Industrial & engineering chemistry research</title><addtitle>Ind. Eng. Chem. Res</addtitle><description>A molten salt mixture containing 45 mol % KCl and 55 mol % CuCl2 was investigated as a catalyst for the reaction of HCl with O2 to produce Cl2. The HCl conversion for an HCl:O2 molar feed ratio of 1:2 at 450 °C and a total pressure of 1 atm was 80% at a residence time of less than 1 s in a lab scale bubble column reactor. The equilibrium conversion at this temperature and pressure is 84%. The catalyst system was found to remain stable throughout a continuous 24-h experiment. The use of a mixed transition metal/alkali metal molten salt catalyst for HCl oxidation reduces the volatility of supported chlorides and may avoid the mechanical stability limitations of solid catalysts caused by volume changes between the halide and the oxide.</description><subject>Engineering</subject><issn>0888-5885</issn><issn>1520-5045</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2018</creationdate><recordtype>article</recordtype><recordid>eNp1kEFLAzEQRoMoWKt3j8GzWyfZxE2PsmgrVCqo55BOUpqyJpKkYP-9u65XTwMz3xtmHiHXDGYMOLszmGfeYZqpDTAm2AmZMMmhkiDkKZmAUqqSSslzcpHzHgCkFGJCFu2ui8kHR19TtAcsPga6OdJl29H1t7fmt-EDNfQldsUFOgLW0TfTFdqaYrpjLpfkbGu67K7-6pR8PD2-t8tqtV48tw-rytRClMpyhoxtG1CGi-GIuuZzZRG4axClFeiE2hiOtRVCMQTjEAGsaCyz7l7WU3Iz7o25eJ3RF4c7jCE4LJrJeg6N6EMwhjDFnJPb6q_kP006agZ6sKV7W3qwpf9s9cjtiAyTfTyk0H_xf_wH3wRs_w</recordid><startdate>20180613</startdate><enddate>20180613</enddate><creator>Su, Shizhao</creator><creator>Mannini, Davide</creator><creator>Metiu, Horia</creator><creator>Gordon, Michael J</creator><creator>McFarland, Eric W</creator><general>American Chemical Society</general><general>American Chemical Society (ACS)</general><scope>AAYXX</scope><scope>CITATION</scope><scope>OTOTI</scope><orcidid>https://orcid.org/0000-0002-3134-4493</orcidid><orcidid>https://orcid.org/0000-0002-0697-4207</orcidid><orcidid>https://orcid.org/0000000231344493</orcidid><orcidid>https://orcid.org/0000000206974207</orcidid></search><sort><creationdate>20180613</creationdate><title>Chlorine Production by HCl Oxidation in a Molten Chloride Salt Catalyst</title><author>Su, Shizhao ; Mannini, Davide ; Metiu, Horia ; Gordon, Michael J ; McFarland, Eric W</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-a344t-d21c11f708a24000533298dc02e7cc5d4ce48ba2c3d4481c0aecc00d47d1de653</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2018</creationdate><topic>Engineering</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Su, Shizhao</creatorcontrib><creatorcontrib>Mannini, Davide</creatorcontrib><creatorcontrib>Metiu, Horia</creatorcontrib><creatorcontrib>Gordon, Michael J</creatorcontrib><creatorcontrib>McFarland, Eric W</creatorcontrib><creatorcontrib>Univ. of California, San Diego, CA (United States)</creatorcontrib><collection>CrossRef</collection><collection>OSTI.GOV</collection><jtitle>Industrial & engineering chemistry research</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Su, Shizhao</au><au>Mannini, Davide</au><au>Metiu, Horia</au><au>Gordon, Michael J</au><au>McFarland, Eric W</au><aucorp>Univ. of California, San Diego, CA (United States)</aucorp><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Chlorine Production by HCl Oxidation in a Molten Chloride Salt Catalyst</atitle><jtitle>Industrial & engineering chemistry research</jtitle><addtitle>Ind. Eng. Chem. Res</addtitle><date>2018-06-13</date><risdate>2018</risdate><volume>57</volume><issue>23</issue><spage>7795</spage><epage>7801</epage><pages>7795-7801</pages><issn>0888-5885</issn><eissn>1520-5045</eissn><abstract>A molten salt mixture containing 45 mol % KCl and 55 mol % CuCl2 was investigated as a catalyst for the reaction of HCl with O2 to produce Cl2. The HCl conversion for an HCl:O2 molar feed ratio of 1:2 at 450 °C and a total pressure of 1 atm was 80% at a residence time of less than 1 s in a lab scale bubble column reactor. The equilibrium conversion at this temperature and pressure is 84%. The catalyst system was found to remain stable throughout a continuous 24-h experiment. The use of a mixed transition metal/alkali metal molten salt catalyst for HCl oxidation reduces the volatility of supported chlorides and may avoid the mechanical stability limitations of solid catalysts caused by volume changes between the halide and the oxide.</abstract><cop>United States</cop><pub>American Chemical Society</pub><doi>10.1021/acs.iecr.8b01141</doi><tpages>7</tpages><orcidid>https://orcid.org/0000-0002-3134-4493</orcidid><orcidid>https://orcid.org/0000-0002-0697-4207</orcidid><orcidid>https://orcid.org/0000000231344493</orcidid><orcidid>https://orcid.org/0000000206974207</orcidid></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0888-5885 |
ispartof | Industrial & engineering chemistry research, 2018-06, Vol.57 (23), p.7795-7801 |
issn | 0888-5885 1520-5045 |
language | eng |
recordid | cdi_osti_scitechconnect_1539074 |
source | American Chemical Society Journals |
subjects | Engineering |
title | Chlorine Production by HCl Oxidation in a Molten Chloride Salt Catalyst |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2024-12-18T04%3A47%3A04IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-acs_osti_&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Chlorine%20Production%20by%20HCl%20Oxidation%20in%20a%20Molten%20Chloride%20Salt%20Catalyst&rft.jtitle=Industrial%20&%20engineering%20chemistry%20research&rft.au=Su,%20Shizhao&rft.aucorp=Univ.%20of%20California,%20San%20Diego,%20CA%20(United%20States)&rft.date=2018-06-13&rft.volume=57&rft.issue=23&rft.spage=7795&rft.epage=7801&rft.pages=7795-7801&rft.issn=0888-5885&rft.eissn=1520-5045&rft_id=info:doi/10.1021/acs.iecr.8b01141&rft_dat=%3Cacs_osti_%3Eb02606855%3C/acs_osti_%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_id=info:pmid/&rfr_iscdi=true |