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Is a monolithic loop reactor a viable option for Fischer–Tropsch synthesis?
A Monolithic Loop Reactor design for Fischer–Tropsch synthesis with a production capacity of 5000 ton middle distillates per day (about 40 000 bbl/ day ) is presented. The required volume, 3350 m 3 , is competitive with conventional reactors, while eliminating disadvantages of existing reactor types...
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| Published in: | Chemical engineering science 2003-02, Vol.58 (3), p.583-591 |
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| Main Authors: | , , , , , , |
| Format: | Article |
| Language: | English |
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| cited_by | cdi_FETCH-LOGICAL-c434t-dd9100f2f1b8a8dae85382d8fa2f204c5db0c169a40629ed6d2b4ea8e2a488683 |
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| cites | cdi_FETCH-LOGICAL-c434t-dd9100f2f1b8a8dae85382d8fa2f204c5db0c169a40629ed6d2b4ea8e2a488683 |
| container_end_page | 591 |
| container_issue | 3 |
| container_start_page | 583 |
| container_title | Chemical engineering science |
| container_volume | 58 |
| creator | de Deugd, Ronald M. Chougule, Rahul B. Kreutzer, Michiel T. Meeuse, F.Michiel Grievink, Johan Kapteijn, Freek Moulijn, Jacob A. |
| description | A Monolithic Loop Reactor design for Fischer–Tropsch synthesis with a production capacity of
5000
ton
middle distillates per day (about
40
000
bbl/
day
) is presented. The required volume,
3350
m
3
, is competitive with conventional reactors, while eliminating disadvantages of existing reactor types such as catalyst attrition and separation, backmixing and large diffusion distances. Although the kinetic expressions used in this study do not allow calculating the selectivity precisely, all important conditions, low temperature rise and constant H
2/CO ratios, are met to ensure high selectivity towards heavy hydrocarbons. |
| doi_str_mv | 10.1016/S0009-2509(02)00583-3 |
| format | article |
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5000
ton
middle distillates per day (about
40
000
bbl/
day
) is presented. The required volume,
3350
m
3
, is competitive with conventional reactors, while eliminating disadvantages of existing reactor types such as catalyst attrition and separation, backmixing and large diffusion distances. Although the kinetic expressions used in this study do not allow calculating the selectivity precisely, all important conditions, low temperature rise and constant H
2/CO ratios, are met to ensure high selectivity towards heavy hydrocarbons.</description><identifier>ISSN: 0009-2509</identifier><identifier>EISSN: 1873-4405</identifier><identifier>DOI: 10.1016/S0009-2509(02)00583-3</identifier><identifier>CODEN: CESCAC</identifier><language>eng</language><publisher>Oxford: Elsevier Ltd</publisher><subject>Applied sciences ; Chemical engineering ; Energy ; Exact sciences and technology ; Fischer–Tropsch synthesis ; Fuel processing. Carbochemistry and petrochemistry ; Fuels ; Gas processing ; Modeling ; Monolithic catalysts ; Multiphase reactors ; Reactors</subject><ispartof>Chemical engineering science, 2003-02, Vol.58 (3), p.583-591</ispartof><rights>2003 Elsevier Science Ltd</rights><rights>2003 INIST-CNRS</rights><lds50>peer_reviewed</lds50><woscitedreferencessubscribed>false</woscitedreferencessubscribed><citedby>FETCH-LOGICAL-c434t-dd9100f2f1b8a8dae85382d8fa2f204c5db0c169a40629ed6d2b4ea8e2a488683</citedby><cites>FETCH-LOGICAL-c434t-dd9100f2f1b8a8dae85382d8fa2f204c5db0c169a40629ed6d2b4ea8e2a488683</cites></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><link.rule.ids>309,310,314,780,784,789,790,23930,23931,25140,27924,27925</link.rule.ids><backlink>$$Uhttp://pascal-francis.inist.fr/vibad/index.php?action=getRecordDetail&idt=14598759$$DView record in Pascal Francis$$Hfree_for_read</backlink></links><search><creatorcontrib>de Deugd, Ronald M.</creatorcontrib><creatorcontrib>Chougule, Rahul B.</creatorcontrib><creatorcontrib>Kreutzer, Michiel T.</creatorcontrib><creatorcontrib>Meeuse, F.Michiel</creatorcontrib><creatorcontrib>Grievink, Johan</creatorcontrib><creatorcontrib>Kapteijn, Freek</creatorcontrib><creatorcontrib>Moulijn, Jacob A.</creatorcontrib><title>Is a monolithic loop reactor a viable option for Fischer–Tropsch synthesis?</title><title>Chemical engineering science</title><description>A Monolithic Loop Reactor design for Fischer–Tropsch synthesis with a production capacity of
5000
ton
middle distillates per day (about
40
000
bbl/
day
) is presented. The required volume,
3350
m
3
, is competitive with conventional reactors, while eliminating disadvantages of existing reactor types such as catalyst attrition and separation, backmixing and large diffusion distances. Although the kinetic expressions used in this study do not allow calculating the selectivity precisely, all important conditions, low temperature rise and constant H
2/CO ratios, are met to ensure high selectivity towards heavy hydrocarbons.</description><subject>Applied sciences</subject><subject>Chemical engineering</subject><subject>Energy</subject><subject>Exact sciences and technology</subject><subject>Fischer–Tropsch synthesis</subject><subject>Fuel processing. Carbochemistry and petrochemistry</subject><subject>Fuels</subject><subject>Gas processing</subject><subject>Modeling</subject><subject>Monolithic catalysts</subject><subject>Multiphase reactors</subject><subject>Reactors</subject><issn>0009-2509</issn><issn>1873-4405</issn><fulltext>true</fulltext><rsrctype>article</rsrctype><creationdate>2003</creationdate><recordtype>article</recordtype><recordid>eNqFkEtOwzAQhi0EEqVwBKRsQLAIjB07cVYVqigggVhQ1pZrT1SjNA52qNQdd-CGnIT0IViymtc3r5-QUwpXFGh-_QIAZcoElBfALgGEzNJsjwyoLLKUcxD7ZPCLHJKjGN_6sCgoDMjTQ0x0svCNr103dyapvW-TgNp0PvSVpdOzGhPfds43SdXnJi6aOYbvz69p8G3vJ3HVdHOMLo6OyUGl64gnOzskr5Pb6fg-fXy-exjfPKaGZ7xLrS0pQMUqOpNaWo1SZJJZWWlWMeBG2BkYmpeaQ85KtLllM45aItNcylxmQ3K-ndsG__6BsVOL_iqsa92g_4iKFWXOmFiDYgua4GMMWKk2uIUOK0VBrcVTG_HUWhkFTG3EU1nfd7ZboKPRdRV0Y1z8a-ailIUoe2605bD_dukwqGgcNgatC2g6Zb37Z9MPtSOEkA</recordid><startdate>20030201</startdate><enddate>20030201</enddate><creator>de Deugd, Ronald M.</creator><creator>Chougule, Rahul B.</creator><creator>Kreutzer, Michiel T.</creator><creator>Meeuse, F.Michiel</creator><creator>Grievink, Johan</creator><creator>Kapteijn, Freek</creator><creator>Moulijn, Jacob A.</creator><general>Elsevier Ltd</general><general>Elsevier</general><scope>IQODW</scope><scope>AAYXX</scope><scope>CITATION</scope><scope>8FD</scope><scope>F28</scope><scope>FR3</scope></search><sort><creationdate>20030201</creationdate><title>Is a monolithic loop reactor a viable option for Fischer–Tropsch synthesis?</title><author>de Deugd, Ronald M. ; Chougule, Rahul B. ; Kreutzer, Michiel T. ; Meeuse, F.Michiel ; Grievink, Johan ; Kapteijn, Freek ; Moulijn, Jacob A.</author></sort><facets><frbrtype>5</frbrtype><frbrgroupid>cdi_FETCH-LOGICAL-c434t-dd9100f2f1b8a8dae85382d8fa2f204c5db0c169a40629ed6d2b4ea8e2a488683</frbrgroupid><rsrctype>articles</rsrctype><prefilter>articles</prefilter><language>eng</language><creationdate>2003</creationdate><topic>Applied sciences</topic><topic>Chemical engineering</topic><topic>Energy</topic><topic>Exact sciences and technology</topic><topic>Fischer–Tropsch synthesis</topic><topic>Fuel processing. Carbochemistry and petrochemistry</topic><topic>Fuels</topic><topic>Gas processing</topic><topic>Modeling</topic><topic>Monolithic catalysts</topic><topic>Multiphase reactors</topic><topic>Reactors</topic><toplevel>peer_reviewed</toplevel><toplevel>online_resources</toplevel><creatorcontrib>de Deugd, Ronald M.</creatorcontrib><creatorcontrib>Chougule, Rahul B.</creatorcontrib><creatorcontrib>Kreutzer, Michiel T.</creatorcontrib><creatorcontrib>Meeuse, F.Michiel</creatorcontrib><creatorcontrib>Grievink, Johan</creatorcontrib><creatorcontrib>Kapteijn, Freek</creatorcontrib><creatorcontrib>Moulijn, Jacob A.</creatorcontrib><collection>Pascal-Francis</collection><collection>CrossRef</collection><collection>Technology Research Database</collection><collection>ANTE: Abstracts in New Technology & Engineering</collection><collection>Engineering Research Database</collection><jtitle>Chemical engineering science</jtitle></facets><delivery><delcategory>Remote Search Resource</delcategory><fulltext>fulltext</fulltext></delivery><addata><au>de Deugd, Ronald M.</au><au>Chougule, Rahul B.</au><au>Kreutzer, Michiel T.</au><au>Meeuse, F.Michiel</au><au>Grievink, Johan</au><au>Kapteijn, Freek</au><au>Moulijn, Jacob A.</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Is a monolithic loop reactor a viable option for Fischer–Tropsch synthesis?</atitle><jtitle>Chemical engineering science</jtitle><date>2003-02-01</date><risdate>2003</risdate><volume>58</volume><issue>3</issue><spage>583</spage><epage>591</epage><pages>583-591</pages><issn>0009-2509</issn><eissn>1873-4405</eissn><coden>CESCAC</coden><abstract>A Monolithic Loop Reactor design for Fischer–Tropsch synthesis with a production capacity of
5000
ton
middle distillates per day (about
40
000
bbl/
day
) is presented. The required volume,
3350
m
3
, is competitive with conventional reactors, while eliminating disadvantages of existing reactor types such as catalyst attrition and separation, backmixing and large diffusion distances. Although the kinetic expressions used in this study do not allow calculating the selectivity precisely, all important conditions, low temperature rise and constant H
2/CO ratios, are met to ensure high selectivity towards heavy hydrocarbons.</abstract><cop>Oxford</cop><pub>Elsevier Ltd</pub><doi>10.1016/S0009-2509(02)00583-3</doi><tpages>9</tpages></addata></record> |
| fulltext | fulltext |
| identifier | ISSN: 0009-2509 |
| ispartof | Chemical engineering science, 2003-02, Vol.58 (3), p.583-591 |
| issn | 0009-2509 1873-4405 |
| language | eng |
| recordid | cdi_proquest_miscellaneous_27962258 |
| source | ScienceDirect Freedom Collection 2022-2024 |
| subjects | Applied sciences Chemical engineering Energy Exact sciences and technology Fischer–Tropsch synthesis Fuel processing. Carbochemistry and petrochemistry Fuels Gas processing Modeling Monolithic catalysts Multiphase reactors Reactors |
| title | Is a monolithic loop reactor a viable option for Fischer–Tropsch synthesis? |
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