Fine tuning H-transfer and β-scission reactions in VGO FCC using metal promoted dual functional ZSM-5
[Display omitted] •Metal promoted ZSM-5 additives demonstrated dual functional activity.•Propylene increased and cracked naphtha olefins decreased.•High total acidity promoted hydride transfer reactions.•Strong acid sites increased β-scission reactions.•Protolytic cracking was enhanced on metal prom...
Gespeichert in:
Veröffentlicht in: | Fuel (Guildford) 2019-04, Vol.242, p.487-495 |
---|---|
Hauptverfasser: | , , , , , |
Format: | Artikel |
Sprache: | eng |
Schlagworte: | |
Online-Zugang: | Volltext |
Tags: |
Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
|
container_end_page | 495 |
---|---|
container_issue | |
container_start_page | 487 |
container_title | Fuel (Guildford) |
container_volume | 242 |
creator | Mehla, Sunil Kukade, Somanath Kumar, Pramod Rao, P.V.C. Sriganesh, G. Ravishankar, R. |
description | [Display omitted]
•Metal promoted ZSM-5 additives demonstrated dual functional activity.•Propylene increased and cracked naphtha olefins decreased.•High total acidity promoted hydride transfer reactions.•Strong acid sites increased β-scission reactions.•Protolytic cracking was enhanced on metal promoted ZSM-5.
Recently the importance of Petroleum Refining Industries has gradually shifted from a supplier of nonrenewable fuels to a supplier of petrochemical feed stocks such as olefins and aromatics (BTX). Zeolite ZSM-5 still remains a zeolite of tremendous importance due to its application as a FCC additive among other applications. New cracking technologies such as deep catalytic cracking, which also use ZSM-5 catalyst to increase gas yields, are also being developed and commercialized. ZSM-5 increases the yields of gaseous fractions at the expense of gasoline and is a good source of Ethylene, Propylene, Butenes and Pentenes because of high alkene/alkane ratios in the gas fraction.
Conventionally catalyst manufacturers have independently marketed propylene maximization and olefin reduction additives for the benefit of petroleum refiners. In this article, the use of metal promoted ZSM-5 based FCC additives for the increase of propylene yields along with simultaneous reduction of olefins in gasoline fraction is elaborated. A Dual Functional Index was proposed to compare the effectiveness of additives towards this objective. The effect of metal modification in same proportions on cracking ratios and product distribution over additives was analyzed and it was demonstrated that the extent of H-transfer, β-scission, protolytic cracking and dehydrogenation reactions could be fine-tuned by metal modifications. It was observed that an excess of H-transfer reactions led to high aromatics and high coke deposit on the additive whereas a balance between β-scission reactions and H-transfer reactions lead to high propylene yields along with a great reduction in cracked naphtha olefin content and minimum carbon loss as dry gas. |
doi_str_mv | 10.1016/j.fuel.2019.01.065 |
format | Article |
fullrecord | <record><control><sourceid>proquest_cross</sourceid><recordid>TN_cdi_proquest_journals_2197881339</recordid><sourceformat>XML</sourceformat><sourcesystem>PC</sourcesystem><els_id>S0016236119300663</els_id><sourcerecordid>2197881339</sourcerecordid><originalsourceid>FETCH-LOGICAL-c328t-9bfbd489e1dff3ac1a77a9a91433c82a03fd257fc280931f9eaadf09c2b96063</originalsourceid><addsrcrecordid>eNp9kMtKAzEUhoMoWKsv4CrgesZcOjMJuJHBtkKlC4sLNyHNRTK0mZpkBF_LB_GZzFjXrs458P2Hnw-Aa4xKjHB925V2MLuSIMxLhEtUVydggllDiwZX9BRMUKYKQmt8Di5i7BBCDatmE2DnzhuYBu_8G1wWKUgfrQlQeg2_v4qoXIyu9zAYqVJeInQevizWcN62cIhjam-S3MFD6Pd9MhrqIV928L94Xl-fn4rqEpxZuYvm6m9OwWb-sGmXxWq9eGzvV4WihKWCb-1Wzxg3WFtLpcKyaSSXHM8oVYxIRK0mVWMVYYhTbLmRUlvEFdnyGtV0Cm6Ob3Ob98HEJLp-CLlFFATzhjFMKc8UOVIq9DEGY8UhuL0MnwIjMeoUnRh1ilGnQFhknTl0dwyZXP_DmSCyG-OV0S4YlYTu3X_xHz5Rft4</addsrcrecordid><sourcetype>Aggregation Database</sourcetype><iscdi>true</iscdi><recordtype>article</recordtype><pqid>2197881339</pqid></control><display><type>article</type><title>Fine tuning H-transfer and β-scission reactions in VGO FCC using metal promoted dual functional ZSM-5</title><source>Elsevier ScienceDirect Journals</source><creator>Mehla, Sunil ; Kukade, Somanath ; Kumar, Pramod ; Rao, P.V.C. ; Sriganesh, G. ; Ravishankar, R.</creator><creatorcontrib>Mehla, Sunil ; Kukade, Somanath ; Kumar, Pramod ; Rao, P.V.C. ; Sriganesh, G. ; Ravishankar, R.</creatorcontrib><description>[Display omitted]
•Metal promoted ZSM-5 additives demonstrated dual functional activity.•Propylene increased and cracked naphtha olefins decreased.•High total acidity promoted hydride transfer reactions.•Strong acid sites increased β-scission reactions.•Protolytic cracking was enhanced on metal promoted ZSM-5.
Recently the importance of Petroleum Refining Industries has gradually shifted from a supplier of nonrenewable fuels to a supplier of petrochemical feed stocks such as olefins and aromatics (BTX). Zeolite ZSM-5 still remains a zeolite of tremendous importance due to its application as a FCC additive among other applications. New cracking technologies such as deep catalytic cracking, which also use ZSM-5 catalyst to increase gas yields, are also being developed and commercialized. ZSM-5 increases the yields of gaseous fractions at the expense of gasoline and is a good source of Ethylene, Propylene, Butenes and Pentenes because of high alkene/alkane ratios in the gas fraction.
Conventionally catalyst manufacturers have independently marketed propylene maximization and olefin reduction additives for the benefit of petroleum refiners. In this article, the use of metal promoted ZSM-5 based FCC additives for the increase of propylene yields along with simultaneous reduction of olefins in gasoline fraction is elaborated. A Dual Functional Index was proposed to compare the effectiveness of additives towards this objective. The effect of metal modification in same proportions on cracking ratios and product distribution over additives was analyzed and it was demonstrated that the extent of H-transfer, β-scission, protolytic cracking and dehydrogenation reactions could be fine-tuned by metal modifications. It was observed that an excess of H-transfer reactions led to high aromatics and high coke deposit on the additive whereas a balance between β-scission reactions and H-transfer reactions lead to high propylene yields along with a great reduction in cracked naphtha olefin content and minimum carbon loss as dry gas.</description><identifier>ISSN: 0016-2361</identifier><identifier>EISSN: 1873-7153</identifier><identifier>DOI: 10.1016/j.fuel.2019.01.065</identifier><language>eng</language><publisher>Kidlington: Elsevier Ltd</publisher><subject>Additives ; Alkanes ; Alkenes ; Aromatic compounds ; Butenes ; Catalysts ; Catalytic cracking ; Cleavage ; Commercialization ; Dehydrogenation ; FCC dual functional additive ; Fluid catalytic cracking ; Gasoline ; Hydride transfer reactions ; Metals ; Naphtha ; Petrochemicals industry ; Petroleum ; Petroleum industry ; Petroleum refining ; Propylene ; Protolytic cracking ; Reduction ; Refining ; Yield ; Zeolite ZSM-5 ; Zeolites ; β-Scission</subject><ispartof>Fuel (Guildford), 2019-04, Vol.242, p.487-495</ispartof><rights>2019 Elsevier Ltd</rights><rights>Copyright Elsevier BV Apr 15, 2019</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c328t-9bfbd489e1dff3ac1a77a9a91433c82a03fd257fc280931f9eaadf09c2b96063</citedby><cites>FETCH-LOGICAL-c328t-9bfbd489e1dff3ac1a77a9a91433c82a03fd257fc280931f9eaadf09c2b96063</cites><orcidid>0000-0002-8657-2354</orcidid></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://www.sciencedirect.com/science/article/pii/S0016236119300663$$EHTML$$P50$$Gelsevier$$H</linktohtml><link.rule.ids>314,776,780,3537,27901,27902,65306</link.rule.ids></links><search><creatorcontrib>Mehla, Sunil</creatorcontrib><creatorcontrib>Kukade, Somanath</creatorcontrib><creatorcontrib>Kumar, Pramod</creatorcontrib><creatorcontrib>Rao, P.V.C.</creatorcontrib><creatorcontrib>Sriganesh, G.</creatorcontrib><creatorcontrib>Ravishankar, R.</creatorcontrib><title>Fine tuning H-transfer and β-scission reactions in VGO FCC using metal promoted dual functional ZSM-5</title><title>Fuel (Guildford)</title><description>[Display omitted]
•Metal promoted ZSM-5 additives demonstrated dual functional activity.•Propylene increased and cracked naphtha olefins decreased.•High total acidity promoted hydride transfer reactions.•Strong acid sites increased β-scission reactions.•Protolytic cracking was enhanced on metal promoted ZSM-5.
Recently the importance of Petroleum Refining Industries has gradually shifted from a supplier of nonrenewable fuels to a supplier of petrochemical feed stocks such as olefins and aromatics (BTX). Zeolite ZSM-5 still remains a zeolite of tremendous importance due to its application as a FCC additive among other applications. New cracking technologies such as deep catalytic cracking, which also use ZSM-5 catalyst to increase gas yields, are also being developed and commercialized. ZSM-5 increases the yields of gaseous fractions at the expense of gasoline and is a good source of Ethylene, Propylene, Butenes and Pentenes because of high alkene/alkane ratios in the gas fraction.
Conventionally catalyst manufacturers have independently marketed propylene maximization and olefin reduction additives for the benefit of petroleum refiners. In this article, the use of metal promoted ZSM-5 based FCC additives for the increase of propylene yields along with simultaneous reduction of olefins in gasoline fraction is elaborated. A Dual Functional Index was proposed to compare the effectiveness of additives towards this objective. The effect of metal modification in same proportions on cracking ratios and product distribution over additives was analyzed and it was demonstrated that the extent of H-transfer, β-scission, protolytic cracking and dehydrogenation reactions could be fine-tuned by metal modifications. It was observed that an excess of H-transfer reactions led to high aromatics and high coke deposit on the additive whereas a balance between β-scission reactions and H-transfer reactions lead to high propylene yields along with a great reduction in cracked naphtha olefin content and minimum carbon loss as dry gas.</description><subject>Additives</subject><subject>Alkanes</subject><subject>Alkenes</subject><subject>Aromatic compounds</subject><subject>Butenes</subject><subject>Catalysts</subject><subject>Catalytic cracking</subject><subject>Cleavage</subject><subject>Commercialization</subject><subject>Dehydrogenation</subject><subject>FCC dual functional additive</subject><subject>Fluid catalytic cracking</subject><subject>Gasoline</subject><subject>Hydride transfer reactions</subject><subject>Metals</subject><subject>Naphtha</subject><subject>Petrochemicals industry</subject><subject>Petroleum</subject><subject>Petroleum industry</subject><subject>Petroleum refining</subject><subject>Propylene</subject><subject>Protolytic cracking</subject><subject>Reduction</subject><subject>Refining</subject><subject>Yield</subject><subject>Zeolite ZSM-5</subject><subject>Zeolites</subject><subject>β-Scission</subject><issn>0016-2361</issn><issn>1873-7153</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2019</creationdate><recordtype>article</recordtype><recordid>eNp9kMtKAzEUhoMoWKsv4CrgesZcOjMJuJHBtkKlC4sLNyHNRTK0mZpkBF_LB_GZzFjXrs458P2Hnw-Aa4xKjHB925V2MLuSIMxLhEtUVydggllDiwZX9BRMUKYKQmt8Di5i7BBCDatmE2DnzhuYBu_8G1wWKUgfrQlQeg2_v4qoXIyu9zAYqVJeInQevizWcN62cIhjam-S3MFD6Pd9MhrqIV928L94Xl-fn4rqEpxZuYvm6m9OwWb-sGmXxWq9eGzvV4WihKWCb-1Wzxg3WFtLpcKyaSSXHM8oVYxIRK0mVWMVYYhTbLmRUlvEFdnyGtV0Cm6Ob3Ob98HEJLp-CLlFFATzhjFMKc8UOVIq9DEGY8UhuL0MnwIjMeoUnRh1ilGnQFhknTl0dwyZXP_DmSCyG-OV0S4YlYTu3X_xHz5Rft4</recordid><startdate>20190415</startdate><enddate>20190415</enddate><creator>Mehla, Sunil</creator><creator>Kukade, Somanath</creator><creator>Kumar, Pramod</creator><creator>Rao, P.V.C.</creator><creator>Sriganesh, G.</creator><creator>Ravishankar, R.</creator><general>Elsevier Ltd</general><general>Elsevier BV</general><scope>AAYXX</scope><scope>CITATION</scope><scope>7QF</scope><scope>7QO</scope><scope>7QQ</scope><scope>7SC</scope><scope>7SE</scope><scope>7SP</scope><scope>7SR</scope><scope>7T7</scope><scope>7TA</scope><scope>7TB</scope><scope>7U5</scope><scope>8BQ</scope><scope>8FD</scope><scope>C1K</scope><scope>F28</scope><scope>FR3</scope><scope>H8D</scope><scope>H8G</scope><scope>JG9</scope><scope>JQ2</scope><scope>KR7</scope><scope>L7M</scope><scope>L~C</scope><scope>L~D</scope><scope>P64</scope><orcidid>https://orcid.org/0000-0002-8657-2354</orcidid></search><sort><creationdate>20190415</creationdate><title>Fine tuning H-transfer and β-scission reactions in VGO FCC using metal promoted dual functional ZSM-5</title><author>Mehla, Sunil ; Kukade, Somanath ; Kumar, Pramod ; Rao, P.V.C. ; Sriganesh, G. ; Ravishankar, R.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c328t-9bfbd489e1dff3ac1a77a9a91433c82a03fd257fc280931f9eaadf09c2b96063</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2019</creationdate><topic>Additives</topic><topic>Alkanes</topic><topic>Alkenes</topic><topic>Aromatic compounds</topic><topic>Butenes</topic><topic>Catalysts</topic><topic>Catalytic cracking</topic><topic>Cleavage</topic><topic>Commercialization</topic><topic>Dehydrogenation</topic><topic>FCC dual functional additive</topic><topic>Fluid catalytic cracking</topic><topic>Gasoline</topic><topic>Hydride transfer reactions</topic><topic>Metals</topic><topic>Naphtha</topic><topic>Petrochemicals industry</topic><topic>Petroleum</topic><topic>Petroleum industry</topic><topic>Petroleum refining</topic><topic>Propylene</topic><topic>Protolytic cracking</topic><topic>Reduction</topic><topic>Refining</topic><topic>Yield</topic><topic>Zeolite ZSM-5</topic><topic>Zeolites</topic><topic>β-Scission</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>Mehla, Sunil</creatorcontrib><creatorcontrib>Kukade, Somanath</creatorcontrib><creatorcontrib>Kumar, Pramod</creatorcontrib><creatorcontrib>Rao, P.V.C.</creatorcontrib><creatorcontrib>Sriganesh, G.</creatorcontrib><creatorcontrib>Ravishankar, R.</creatorcontrib><collection>CrossRef</collection><collection>Aluminium Industry Abstracts</collection><collection>Biotechnology Research Abstracts</collection><collection>Ceramic Abstracts</collection><collection>Computer and Information Systems Abstracts</collection><collection>Corrosion Abstracts</collection><collection>Electronics & Communications Abstracts</collection><collection>Engineered Materials Abstracts</collection><collection>Industrial and Applied Microbiology Abstracts (Microbiology A)</collection><collection>Materials Business File</collection><collection>Mechanical & Transportation Engineering Abstracts</collection><collection>Solid State and Superconductivity Abstracts</collection><collection>METADEX</collection><collection>Technology Research Database</collection><collection>Environmental Sciences and Pollution Management</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><collection>Aerospace Database</collection><collection>Copper Technical Reference Library</collection><collection>Materials Research Database</collection><collection>ProQuest Computer Science Collection</collection><collection>Civil Engineering Abstracts</collection><collection>Advanced Technologies Database with Aerospace</collection><collection>Computer and Information Systems Abstracts Academic</collection><collection>Computer and Information Systems Abstracts Professional</collection><collection>Biotechnology and BioEngineering Abstracts</collection><jtitle>Fuel (Guildford)</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>Mehla, Sunil</au><au>Kukade, Somanath</au><au>Kumar, Pramod</au><au>Rao, P.V.C.</au><au>Sriganesh, G.</au><au>Ravishankar, R.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Fine tuning H-transfer and β-scission reactions in VGO FCC using metal promoted dual functional ZSM-5</atitle><jtitle>Fuel (Guildford)</jtitle><date>2019-04-15</date><risdate>2019</risdate><volume>242</volume><spage>487</spage><epage>495</epage><pages>487-495</pages><issn>0016-2361</issn><eissn>1873-7153</eissn><abstract>[Display omitted]
•Metal promoted ZSM-5 additives demonstrated dual functional activity.•Propylene increased and cracked naphtha olefins decreased.•High total acidity promoted hydride transfer reactions.•Strong acid sites increased β-scission reactions.•Protolytic cracking was enhanced on metal promoted ZSM-5.
Recently the importance of Petroleum Refining Industries has gradually shifted from a supplier of nonrenewable fuels to a supplier of petrochemical feed stocks such as olefins and aromatics (BTX). Zeolite ZSM-5 still remains a zeolite of tremendous importance due to its application as a FCC additive among other applications. New cracking technologies such as deep catalytic cracking, which also use ZSM-5 catalyst to increase gas yields, are also being developed and commercialized. ZSM-5 increases the yields of gaseous fractions at the expense of gasoline and is a good source of Ethylene, Propylene, Butenes and Pentenes because of high alkene/alkane ratios in the gas fraction.
Conventionally catalyst manufacturers have independently marketed propylene maximization and olefin reduction additives for the benefit of petroleum refiners. In this article, the use of metal promoted ZSM-5 based FCC additives for the increase of propylene yields along with simultaneous reduction of olefins in gasoline fraction is elaborated. A Dual Functional Index was proposed to compare the effectiveness of additives towards this objective. The effect of metal modification in same proportions on cracking ratios and product distribution over additives was analyzed and it was demonstrated that the extent of H-transfer, β-scission, protolytic cracking and dehydrogenation reactions could be fine-tuned by metal modifications. It was observed that an excess of H-transfer reactions led to high aromatics and high coke deposit on the additive whereas a balance between β-scission reactions and H-transfer reactions lead to high propylene yields along with a great reduction in cracked naphtha olefin content and minimum carbon loss as dry gas.</abstract><cop>Kidlington</cop><pub>Elsevier Ltd</pub><doi>10.1016/j.fuel.2019.01.065</doi><tpages>9</tpages><orcidid>https://orcid.org/0000-0002-8657-2354</orcidid></addata></record> |
fulltext | fulltext |
identifier | ISSN: 0016-2361 |
ispartof | Fuel (Guildford), 2019-04, Vol.242, p.487-495 |
issn | 0016-2361 1873-7153 |
language | eng |
recordid | cdi_proquest_journals_2197881339 |
source | Elsevier ScienceDirect Journals |
subjects | Additives Alkanes Alkenes Aromatic compounds Butenes Catalysts Catalytic cracking Cleavage Commercialization Dehydrogenation FCC dual functional additive Fluid catalytic cracking Gasoline Hydride transfer reactions Metals Naphtha Petrochemicals industry Petroleum Petroleum industry Petroleum refining Propylene Protolytic cracking Reduction Refining Yield Zeolite ZSM-5 Zeolites β-Scission |
title | Fine tuning H-transfer and β-scission reactions in VGO FCC using metal promoted dual functional ZSM-5 |
url | https://sfx.bib-bvb.de/sfx_tum?ctx_ver=Z39.88-2004&ctx_enc=info:ofi/enc:UTF-8&ctx_tim=2025-02-01T01%3A20%3A16IST&url_ver=Z39.88-2004&url_ctx_fmt=infofi/fmt:kev:mtx:ctx&rfr_id=info:sid/primo.exlibrisgroup.com:primo3-Article-proquest_cross&rft_val_fmt=info:ofi/fmt:kev:mtx:journal&rft.genre=article&rft.atitle=Fine%20tuning%20H-transfer%20and%20%CE%B2-scission%20reactions%20in%20VGO%20FCC%20using%20metal%20promoted%20dual%20functional%20ZSM-5&rft.jtitle=Fuel%20(Guildford)&rft.au=Mehla,%20Sunil&rft.date=2019-04-15&rft.volume=242&rft.spage=487&rft.epage=495&rft.pages=487-495&rft.issn=0016-2361&rft.eissn=1873-7153&rft_id=info:doi/10.1016/j.fuel.2019.01.065&rft_dat=%3Cproquest_cross%3E2197881339%3C/proquest_cross%3E%3Curl%3E%3C/url%3E&disable_directlink=true&sfx.directlink=off&sfx.report_link=0&rft_id=info:oai/&rft_pqid=2197881339&rft_id=info:pmid/&rft_els_id=S0016236119300663&rfr_iscdi=true |