Activation of Hydrogen on Zeolites: Kinetics and Mechanism of n-Heptane Cracking on H-ZSM-5 Zeolites Under High Hydrogen Pressure
The cracking of n-heptane on H-ZSM-5 zeolite was studied using a tubular reactor at 543 K, 2.4 MPa total pressure and varying hydrogen and n-heptane partial pressures. The rate of reaction was determined at times on stream ranging from 0.5 to 62 min. Under the above experimental conditions H-ZSM-5 d...
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Veröffentlicht in: | Journal of Catalysis 1995-03, Vol.152 (1), p.189-197 |
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description | The cracking of
n-heptane on H-ZSM-5 zeolite was studied using a tubular reactor at 543 K, 2.4 MPa total pressure and varying hydrogen and
n-heptane partial pressures. The rate of reaction was determined at times on stream ranging from 0.5 to 62 min. Under the above experimental conditions H-ZSM-5 deactivates rapidly during the first 10 min of reaction time. The initial rate of
n-heptane cracking is independent of the
n-heptane partial pressure between 0.25 and 0.47 MPa, while it increases linearly with increasing hydrogen partial pressure. This is interpreted with the assumption that under these reaction conditions the desorption of adsorbed intermediates is the rate determining step and that the rate of desorption can be increased by hydrogen via hydride transfer from molecular hydrogen, producing a high paraffin/olefin ratio in the reaction products. In addition to this effect, hydrogen diminishes the rate of catalyst coking. |
doi_str_mv | 10.1006/jcat.1995.1072 |
format | Article |
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n-heptane on H-ZSM-5 zeolite was studied using a tubular reactor at 543 K, 2.4 MPa total pressure and varying hydrogen and
n-heptane partial pressures. The rate of reaction was determined at times on stream ranging from 0.5 to 62 min. Under the above experimental conditions H-ZSM-5 deactivates rapidly during the first 10 min of reaction time. The initial rate of
n-heptane cracking is independent of the
n-heptane partial pressure between 0.25 and 0.47 MPa, while it increases linearly with increasing hydrogen partial pressure. This is interpreted with the assumption that under these reaction conditions the desorption of adsorbed intermediates is the rate determining step and that the rate of desorption can be increased by hydrogen via hydride transfer from molecular hydrogen, producing a high paraffin/olefin ratio in the reaction products. In addition to this effect, hydrogen diminishes the rate of catalyst coking.</description><identifier>ISSN: 0021-9517</identifier><identifier>EISSN: 1090-2694</identifier><identifier>DOI: 10.1006/jcat.1995.1072</identifier><identifier>CODEN: JCTLA5</identifier><language>eng</language><publisher>Amsterdam: Elsevier Inc</publisher><subject>02 PETROLEUM ; 40 CHEMISTRY ; Applied sciences ; CATALYTIC CRACKING ; CATALYTIC EFFECTS ; CHEMICAL REACTION KINETICS ; COKING ; Energy ; Exact sciences and technology ; Fuel processing. Carbochemistry and petrochemistry ; Fuels ; HEPTANE ; HETEROGENEOUS CATALYSIS ; HYDROGEN ; Liquid petroleum product processing ; ZEOLITES</subject><ispartof>Journal of Catalysis, 1995-03, Vol.152 (1), p.189-197</ispartof><rights>1995 Academic Press</rights><rights>1995 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c443t-a1013790fab509571c7adce12bf1959d57e1a6966e3c47fd911dab36b2bd13403</citedby></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://dx.doi.org/10.1006/jcat.1995.1072$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,780,784,885,3548,27923,27924,45994</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=3441870$$DView record in Pascal Francis$$Hfree_for_read</backlink><backlink>$$Uhttps://www.osti.gov/biblio/525940$$D View this record in Osti.gov$$Hfree_for_read</backlink></links><search><creatorcontrib>Meusinger, J.</creatorcontrib><creatorcontrib>Corma, A.</creatorcontrib><title>Activation of Hydrogen on Zeolites: Kinetics and Mechanism of n-Heptane Cracking on H-ZSM-5 Zeolites Under High Hydrogen Pressure</title><title>Journal of Catalysis</title><description>The cracking of
n-heptane on H-ZSM-5 zeolite was studied using a tubular reactor at 543 K, 2.4 MPa total pressure and varying hydrogen and
n-heptane partial pressures. The rate of reaction was determined at times on stream ranging from 0.5 to 62 min. Under the above experimental conditions H-ZSM-5 deactivates rapidly during the first 10 min of reaction time. The initial rate of
n-heptane cracking is independent of the
n-heptane partial pressure between 0.25 and 0.47 MPa, while it increases linearly with increasing hydrogen partial pressure. This is interpreted with the assumption that under these reaction conditions the desorption of adsorbed intermediates is the rate determining step and that the rate of desorption can be increased by hydrogen via hydride transfer from molecular hydrogen, producing a high paraffin/olefin ratio in the reaction products. In addition to this effect, hydrogen diminishes the rate of catalyst coking.</description><subject>02 PETROLEUM</subject><subject>40 CHEMISTRY</subject><subject>Applied sciences</subject><subject>CATALYTIC CRACKING</subject><subject>CATALYTIC EFFECTS</subject><subject>CHEMICAL REACTION KINETICS</subject><subject>COKING</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fuel processing. Carbochemistry and petrochemistry</subject><subject>Fuels</subject><subject>HEPTANE</subject><subject>HETEROGENEOUS CATALYSIS</subject><subject>HYDROGEN</subject><subject>Liquid petroleum product processing</subject><subject>ZEOLITES</subject><issn>0021-9517</issn><issn>1090-2694</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>1995</creationdate><recordtype>article</recordtype><recordid>eNp1kDFP5DAQhS10SOwBLbWRaLN4kjhZ06HVQRAgkICGJnLGk13D4qxsg0TJPydmEVdRjUf63nvjx9gBiCkIUR0_oY5TUEqOa51vsQkIJbK8UuUfNhEih0xJqHfY3xCehACQcjZhH6cY7ZuOdnB86HnzbvywoPHt-CMNKxspnPBL6yhaDFw7w68Jl9rZ8JJ4lzW0jtoRn3uNz9YtkrLJHu-uM_njwB-cIc8bu1j-T7j1FMKrpz223etVoP3vucsezv7dz5vs6ub8Yn56lWFZFjHTIKColeh1J4WSNWCtDRLkXQ9KKiNrAl2pqqICy7o3CsDorqi6vDNQlKLYZYcb3yFE2wYcD8MlDs4RxlbmUn0x0w2DfgjBU9-uvX3R_r0F0aaS21Rym0puU8mj4GgjWOuAetV77dCGH1VRljCrk-9sg9H4wTdLPuWTQzLWp3gz2N8SPgHx4I_8</recordid><startdate>19950301</startdate><enddate>19950301</enddate><creator>Meusinger, J.</creator><creator>Corma, A.</creator><general>Elsevier Inc</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>OTOTI</scope></search><sort><creationdate>19950301</creationdate><title>Activation of Hydrogen on Zeolites: Kinetics and Mechanism of n-Heptane Cracking on H-ZSM-5 Zeolites Under High Hydrogen Pressure</title><author>Meusinger, J. ; Corma, A.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c443t-a1013790fab509571c7adce12bf1959d57e1a6966e3c47fd911dab36b2bd13403</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>1995</creationdate><topic>02 PETROLEUM</topic><topic>40 CHEMISTRY</topic><topic>Applied sciences</topic><topic>CATALYTIC CRACKING</topic><topic>CATALYTIC EFFECTS</topic><topic>CHEMICAL REACTION KINETICS</topic><topic>COKING</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>Fuel processing. Carbochemistry and petrochemistry</topic><topic>Fuels</topic><topic>HEPTANE</topic><topic>HETEROGENEOUS CATALYSIS</topic><topic>HYDROGEN</topic><topic>Liquid petroleum product processing</topic><topic>ZEOLITES</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Meusinger, J.</creatorcontrib><creatorcontrib>Corma, A.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>OSTI.GOV</collection><jtitle>Journal of Catalysis</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Meusinger, J.</au><au>Corma, A.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Activation of Hydrogen on Zeolites: Kinetics and Mechanism of n-Heptane Cracking on H-ZSM-5 Zeolites Under High Hydrogen Pressure</atitle><jtitle>Journal of Catalysis</jtitle><date>1995-03-01</date><risdate>1995</risdate><volume>152</volume><issue>1</issue><spage>189</spage><epage>197</epage><pages>189-197</pages><issn>0021-9517</issn><eissn>1090-2694</eissn><coden>JCTLA5</coden><abstract>The cracking of
n-heptane on H-ZSM-5 zeolite was studied using a tubular reactor at 543 K, 2.4 MPa total pressure and varying hydrogen and
n-heptane partial pressures. The rate of reaction was determined at times on stream ranging from 0.5 to 62 min. Under the above experimental conditions H-ZSM-5 deactivates rapidly during the first 10 min of reaction time. The initial rate of
n-heptane cracking is independent of the
n-heptane partial pressure between 0.25 and 0.47 MPa, while it increases linearly with increasing hydrogen partial pressure. This is interpreted with the assumption that under these reaction conditions the desorption of adsorbed intermediates is the rate determining step and that the rate of desorption can be increased by hydrogen via hydride transfer from molecular hydrogen, producing a high paraffin/olefin ratio in the reaction products. In addition to this effect, hydrogen diminishes the rate of catalyst coking.</abstract><cop>Amsterdam</cop><pub>Elsevier Inc</pub><doi>10.1006/jcat.1995.1072</doi><tpages>9</tpages></addata></record> |
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source | ScienceDirect Journals (5 years ago - present) |
subjects | 02 PETROLEUM 40 CHEMISTRY Applied sciences CATALYTIC CRACKING CATALYTIC EFFECTS CHEMICAL REACTION KINETICS COKING Energy Exact sciences and technology Fuel processing. Carbochemistry and petrochemistry Fuels HEPTANE HETEROGENEOUS CATALYSIS HYDROGEN Liquid petroleum product processing ZEOLITES |
title | Activation of Hydrogen on Zeolites: Kinetics and Mechanism of n-Heptane Cracking on H-ZSM-5 Zeolites Under High Hydrogen Pressure |
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