期刊文献+

正癸烷在不同酸性Y型分子筛催化剂上的加氢裂化反应 被引量:2

HYDROCRACKING OF DECANE ON DIFFERENT ACIDITY Y ZEOLITE CATALYSTS
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摘要 用3种酸性不同的Y型分子筛,采用孔饱和共浸渍法制备了NiW/Y-Al2O3双功能加氢裂化催化剂,以正癸烷为模型化合物,考察了硫化态NiW/Y-Al2O3催化剂上的活性、异构癸烷收率和二次裂化与Y型分子筛酸性的关系。结果表明,增加Y型分子筛上的中强酸量,能够提高NiW/Y-Al2O3催化剂的活性。反应温度较低(330℃)时,Y型分子筛中的中强B酸量和二次裂化相关;而反应温度较高(380℃)时,Y型分子筛的总酸量与二次裂化相关。反应温度升高,正癸烷转化率增加,异构选择性降低,异构癸烷收率先增加后降低,出现1个峰值。 Three catalysts of NiW supported on different Y-A12 03 were prepared and their catalytic properties were evaluated for the hydrocracking of n-decane. The results showed that amount increase of medium and strong acidic sites on catalyst led to higher activity of the catalyst in n decane hydrocracking. Over the catalyst with higher medium and strong acidity severe secondary cracking of n decane occurred at low temperature, while the total acidic sites of catalyst were related to secondary cracking at higher temperature. The conversion of n-decane increased with temperature rising, while the selectivity of i-decane decreased and the yield of i decane went through a maximum.
出处 《石油学报(石油加工)》 EI CAS CSCD 北大核心 2009年第1期31-35,共5页 Acta Petrolei Sinica(Petroleum Processing Section)
基金 国家重点基础研究发展规划"973"项目(2006CB202506)资助
关键词 加氢裂化 酸性 催化剂 正癸烷 分子筛 hydrocraeking acidity catalyst decane zeolite
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参考文献10

  • 1李大东主编..加氢处理工艺与工程[M].北京:中国石化出版社,2004:1408.
  • 2聂红,胡志海,石亚华,李大东.RIPP加氢裂化技术新进展[J].石油炼制与化工,2006,37(6):9-13. 被引量:22
  • 3毛以朝,聂红,李毅,熊震霖.高活性中间馏分油型加氢裂化催化剂RT-30的研制[J].石油炼制与化工,2005,36(6):1-4. 被引量:1
  • 4韩崇仁主编..加氢裂化工艺与工程[M].北京:中国石化出版社,2001:935.
  • 5ALVAREZ F, RIBEIRO F R, PEROT G, et al. Hydroisomerization and hydrocracking of alkane 7 Influence of balance between acid and hydrogenating functions on transformation of n-decane on PtHY catalysts[J].Journal of Catalysis, 1996, 162(2):179- 189. 被引量:1
  • 6DECANIO S J, SOHN J R, FRITZ P O, et al. Acid catalysis by dealuminated zeolite-Y I Methanol dehydration and cumene dealkylation[J].Journal of Catalysis,1986,101(1):132-141. 被引量:1
  • 7FRITZ P O, LUNSFORD J H. The effect of sodium poisoning on dealuminated Y-type zeolites[J]. Journal of Catalysis, 1989, 118(1): 85-98. 被引量:1
  • 8GATES B C, KATZER J R, SCHUIT G C A. Chemistry of Catalytic Processes[M]. New York: McGraw Hill Book Company. 1979: 68-78. 被引量:1
  • 9SCHERZER J, GRUIA A J. Hydrocracking Science and Technology[M]. Hong Kong :Marcel Dekker Inc, New York Basel. 1996: 73-75. 被引量:1
  • 10何奕工,舒兴田,龙军.正碳离子和相关的反应机理[J].石油学报(石油加工),2007,23(4):1-7. 被引量:36

二级参考文献28

  • 1吴越.催化化学[M].北京:科学出版社,2000.162-470. 被引量:21
  • 2Mark VanWees, Vinayan Nair, Hemant B Gala. UNICRACK INGTM innovations maximize your ROA for low-sulfur fuels.In: Annual Meeting Technical Papers, San Antonio TX: National Petrochemical&Refiners Association, 2002. AM-02 36. 被引量:1
  • 3Leiras Gomes A C, Falabella S-Aguiar E, Cabral Menezes S, et al. Influence of combined acid treatment on physico-chemical characteristics of ultrastable zeolite Y and on its catalytic properties in the disproportionation of ethylbenzene. Applied Catal ysis A : General, 1997,148(2) : 373~385. 被引量:1
  • 4Thi Chang. New JV markets one-stop GTL package. Oil and Gas Journal,2000,98(51):45-52 被引量:1
  • 5Xiong Zhenlin, Wang Yiguan, Zhang Maoying, et al. Commercial application of RMC technology in the 1.5 Mt/a hydrocracking unit at Shetroanghai pchemical company. China Petroleum & Petrochemical Processing Technology, 2003, (3): 33 - 37 被引量:1
  • 6Anne K Rhodes. World crude capacity, conversion capability Inch upward. Oil and Gas Journal,1994,92(51):56-64 被引量:1
  • 7华东石油学院炼油工程教研室.石油炼制工程[M].北京:石油工业出版社,1981. 被引量:1
  • 8MEERWEIN H,EMSTER V K.Carbocation[J].Chem Ber,1922,55:2500-2505. 被引量:1
  • 9MEERWEIN H.Methodenb der Organischen Chemie[M].Houben-Weyl Company,4th ed.,Vol Ⅵ/3,Germany:Thieme Stuttgart,1965. 被引量:1
  • 10INGOLD C K.Structure and Mechanisms in Organic Chemistry[M].New York:Cornell Univ Press,Ithaca,1953. 被引量:1

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