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CaO/Al2O3复合催化剂催化裂解大豆油制备烃类燃料的研究

CATALYTIC PERFORMANCES OF CaO/Al_2O_3 COMPOSITE IN CATALYTIC CRACKING OF SOYBEAN OIL FOR HYDROCARBON FUEL
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摘要 以物理混合法制备复合催化剂CaO/Al_2O_3,采用单因素实验法,在固定床反应器以大豆油为原料进行CaO/Al_2O_3复合催化剂催化裂解大豆油制备烃类燃料的研究,考察裂解温度、空速、m(CaO)/m(Al_2O_3)对裂解产物的影响。结果表明:在裂解温度为510℃、质量空速为10.00h^(-1)、m(CaO)/m(Al_2O_3)为2∶8的条件下,裂解液收率为71.00%;裂解油组成中烃类质量分数高达80.96%,裂解油的运动黏度(20℃)为3.1 mm^2/s,酸值为4.1 mg KOH/g,氧质量分数为2.37%,热值达44.79kJ/g。 The physical mixing catalyst CaO/Al2O3 was applied in soybean oil by catalytic pyrolysis for hydrocarbon fuel production.The single factor experimental method was used to investigate the effect of cracking temperature,mass space velocity,m(CaO)/m(Al2O3)on cracking products in a fixed bed reactor.The results indicated that the optimum reaction conditions are cracking temperature of 510℃,space velocity of 10.00 h-1,and m(CaO)/m(Al2O3)of 2∶8.Under the optimal conditions,the liquid yield reaches 71.00%.The content of hydrocarbon in pyrolysis oil is over 80.96%with kinetic viscosity(20℃)of 3.1 mm 2/s,the acid value of 4.1 mgKOH/g,and the oxygen content of 2.37%,resulting in calorific value of 44.79 kJ/g.
作者 韦一 刘兵 于凤文 计建炳 Wei Yi;Liu Bing;Yu Fengwen;Ji Jianbing(College of Chemical Engineering,Zhejiang University of Technology,Zhejiang Province Key Laboratory of Biofuel,Hangzhou 310014)
出处 《石油炼制与化工》 CAS CSCD 北大核心 2018年第4期45-50,共6页 Petroleum Processing and Petrochemicals
关键词 催化裂解 复合催化剂 大豆油 燃料油 catalytic cracking composite catalyst soybean oil fuel oil
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  • 1闵恩泽.利用可再生油料资源发展生物炼油化工厂[J].化工学报,2006,57(8):1739-1745. 被引量:39
  • 2EMIRBAS A. Biodiesel fuels from vegetable oils via catalytic and non-catalytic supercritical alcohol transesterifications and other methods: A survey [J]. Energy Convers Manage, 2003, 44 (13) : 2093-2109.
  • 3MAHER K D, BRESSLER D C. Pyrolysis of triglyceride materials for the production of renewable fuels and chemicals [ J ]. Bioresour Teehnol, 2007, 98(12) : 2351-2368.
  • 4VONGHIA E, BOOCOCK D G B, KONAR S K, LEUNG A. Pathways for the deoxygenation of triglyeerides to aliphatie-hydrocarbons over activated alumina[ J ]. Energy Fuels, 1995, 9 (6) : 1090-1096.
  • 5PRASAD Y S, BAKHSHI N N, MATHEWS J F, EAGER R L. Catalytic conversion of eanola oil to fuels and chemical feedstocks : 2 Effect of cofeeding steam on the performance of HZSM-5 catalyst[J]. Can J Chem Eng, 1986, 64(2) : 285-292.
  • 6TWAIQ F A, MOHAMED A R, BHATIA S. Liquid hydrocarbon fuels from palm oil by catalytic cracking over aluminosilicate mesoporous catalysts with various Si/AI ratios [ J ]. Microporous Mesoporous Mater, 2003, 64 ( 1/3 ) : 95-107.
  • 7TWAIQ F A, ZABIDI N A M, MOHAMED A R, BHATIA S. Catalytic conversion of palm oil over mesoporous aluminosilicate MCM-41 for the production of liquid hydrocarbon fuels[ J]. Fuel Process Technol, 2003, 84(1/3) , 105-120.
  • 8LIMAA D G, SOARES V C D, RIBEIRO E B, CARVALHO D A, CARDOSO E C V, MONDIM K C, RUBIM J C, SUAREZ P A Z. Diesel-like fuel obtained by pyrolysis of vegetable oils[ J]. J Anal Appl Pyrolysis, 2004, 71 (2) : 987-996.
  • 9Maher K D, Bressler D C. Cracking of triglyceride materials for the production of renewable fuels and chemicals [J]. Bioresource Technology, 2007, 98(12): 2351-2368.
  • 10Demirbas A. Biodiesel fuels from vegetable oils via catalytic and non-catalytic supercritical alcohol transesterifications and other methods: A survey [J]. Energy Conversion and Management, 2003, 44(13) : 2093-2109.

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