Oligomerization of C4 Fraction from FCCU on ZSM-5
In order to make more liquid products like gasoline, the oligomerition of a C4 feedstock taking place on catalyst containing ZSM-5 was studied in a pressurized reactor. The products were C5- gas, liquid hydrocarbons and coke. During the reaction on the catalyst BO-l, when the WHSV was 0.71h-1 and to...
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Veröffentlicht in: | China petroleum processing & petrochemical technology 2004-12 (4), p.31-36 |
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description | In order to make more liquid products like gasoline, the oligomerition of a C4 feedstock taking place on catalyst containing ZSM-5 was studied in a pressurized reactor. The products were C5- gas, liquid hydrocarbons and coke. During the reaction on the catalyst BO-l, when the WHSV was 0.71h-1 and total pressure was 4.0MPa, the C5+ product yield reached a maximum at a temperature around 320℃. As oligomerization reaction was the dominating one, there were minor C9 hydrocarbons in liquid products and the main products were C7 and C8 olefins and n- C10 paraffins. When the temperature was higher than 286C, a small amount of C9hydrocarbons was formed and more normal and isomeric paraffins other than olefins were formed in products.Gasoline yield increased linearly with a rising total pressure under the same operating conditions. |
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The products were C5- gas, liquid hydrocarbons and coke. During the reaction on the catalyst BO-l, when the WHSV was 0.71h-1 and total pressure was 4.0MPa, the C5+ product yield reached a maximum at a temperature around 320℃. As oligomerization reaction was the dominating one, there were minor C9 hydrocarbons in liquid products and the main products were C7 and C8 olefins and n- C10 paraffins. When the temperature was higher than 286C, a small amount of C9hydrocarbons was formed and more normal and isomeric paraffins other than olefins were formed in products.Gasoline yield increased linearly with a rising total pressure under the same operating conditions.</description><identifier>ISSN: 1008-6234</identifier><language>eng</language><publisher>Research Institute of Petroleum Processing,SINOPEC,Beijing,100083</publisher><subject>catalyst ; fraction ; liquid ; oligomerization ; product</subject><ispartof>China petroleum processing & petrochemical technology, 2004-12 (4), p.31-36</ispartof><rights>Copyright © Wanfang Data Co. Ltd. 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During the reaction on the catalyst BO-l, when the WHSV was 0.71h-1 and total pressure was 4.0MPa, the C5+ product yield reached a maximum at a temperature around 320℃. As oligomerization reaction was the dominating one, there were minor C9 hydrocarbons in liquid products and the main products were C7 and C8 olefins and n- C10 paraffins. 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The products were C5- gas, liquid hydrocarbons and coke. During the reaction on the catalyst BO-l, when the WHSV was 0.71h-1 and total pressure was 4.0MPa, the C5+ product yield reached a maximum at a temperature around 320℃. As oligomerization reaction was the dominating one, there were minor C9 hydrocarbons in liquid products and the main products were C7 and C8 olefins and n- C10 paraffins. When the temperature was higher than 286C, a small amount of C9hydrocarbons was formed and more normal and isomeric paraffins other than olefins were formed in products.Gasoline yield increased linearly with a rising total pressure under the same operating conditions.</abstract><pub>Research Institute of Petroleum Processing,SINOPEC,Beijing,100083</pub><tpages>6</tpages></addata></record> |
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title | Oligomerization of C4 Fraction from FCCU on ZSM-5 |
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