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Oligomerization of C_4 Fraction from FCCU on ZSM-5

Oligomerization of C_4 Fraction from FCCU on ZSM-5
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摘要 In order to make more liquid products like gasoline, the oligomerition of a C4 feedstock taking placeon catalyst containing ZSM-5 was studied in a pressurized reactor. The products were C5- gas, liquid hydro-carbons and coke. During the reaction on the catalyst BO-1, when the WHSV was 0.71h-1 and total pressurewas 4.0MPa, the C5+ product yield reached a maximum at a temperature around 320℃. As oligomerizationreaction was the dominating one, there were minor C9 hydrocarbons in liquid products and the main productswere C7 and C8 olefins and n- C10 paraffins. When the temperature was higher than 286℃, 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. In order to make more liquid products like gasoline, the oligomerition of aC_4 feedstock taking place on catalyst containing ZSM-5 was studied in a pressurized reactor. Theproducts were C_5^- gas, liquid hydrocarbons and coke. During the reaction on the catalyst BO-1,when the WHSV was 0.71h^(-1) and total pressure was 4.0MPa, the C_5^+ product yield reached amaximum at a temperature around 32℃. As oligomerization reaction was the dominating one, there wereminor C_9 hydrocarbons in liquid products and the main products were C_7 and C_8 olefins and n-C_(10) paraffins. When the temperature was higher than 286℃, a small amount of C_9 hydrocarbons wasformed and more normal and isomeric paraffins other than olefins were formed in products. Gasolineyield increased linearly with a rising total pressure under the same operating conditions.
出处 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2004年第4期31-36,共6页 中国炼油与石油化工(英文版)
关键词 OLIGOMERIZATION C4 FRACTION CATALYST liquid product oligomerization C_4 fraction catalyst liquid product
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参考文献4

  • 1[1]Givens et al. USP 3960978, Converting low molecular weight olefins over zeolites.
  • 2[2]John S Magee, Maurice M Mitchell. Fluid Catalytic Cracking: Science and Technology. 1995.
  • 3[3]Garwood et al. USP 4,413,153, Integrated process for making transportation fuels and lubes from wet natural gas.
  • 4[4]Miller. USP 4417088, Oligomerization of liquid olefins.

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