作者:迟克彬;赵震;田志坚;胡胜;阎立军;孟祥彬;高善彬; 时间:2013-01-01 点击数:
迟克彬;赵震;田志坚;胡胜;阎立军;孟祥彬;高善彬;
1:中国石油大学(北京)重质油国家重点实验室
2:中国石油石油化工研究院
3:中国科学院大连化学物理研究所
摘要(Abstract):
采用常规水热法合成SAPO-11和ZSM-22分子筛,制备分别含有分子筛的催化剂,借助XRD、SEM和NH3-TPD表征2种催化剂的结构和酸性,并以加氢预精制溶剂脱蜡油为原料,采用固定床反应器研究Pt/SAPO-11和Pt/ZSM-22催化剂的加氢异构反应性能.结果表明:催化剂的反应活性和选择性主要取决于催化剂的酸量和酸强度,相对而言,由于SAPO-11分子筛催化剂弱酸含量较高,具有更佳的异构化选择性.利用1 H NMR和13 C NMR核磁共振研究加氢异构反应前后基础油的化学结构变化,Pt/SAPO-11催化剂有较高的加氢异构选择性.
关键词(KeyWords):Pt/SAPO-11催化剂;Pt/ZSM-22催化剂;溶剂脱蜡油;加氢异构反应;润滑油基础油
Abstract:
Keywords:
基金项目(Foundation):国家“863”高技术研究发展计划项目(2009AA064201);; 国家科技支撑计划项目(2012BAE05B02);; 中国石油天然气集团公司科技项目(2009A-3801-04)
作者(Author):迟克彬;赵震;田志坚;胡胜;阎立军;孟祥彬;高善彬;
Email:
参考文献(References):
[1]孔劲媛.国内外润滑油基础油市场分析及展望[J].国际石油经济,2009(10):49-53.Kong Jinyuan.Analysis and outlook for the domestic and international lubricating oil and base oil mairkets[J].International Petrole-um Economics,2009(10):49-53.
[2]高辉,马爽,孙忠镭.2009中国润滑油行业报告[J].润滑油,2010,25(6):1-8.Gao Hui,Ma Shuang,Sun Zhonglei.Chinese lubricant industry report,2009[J].Lubricating Oil,2010,25(6):1-8.
[3]邴国强,陈建,田然,等.润滑油异构化脱蜡催化剂——Pt/H-SAPO-11的初探[J].大庆石油学院学报,2004,28(4)52-54.Bing Guoqiang,Chen Jian,Tian Ran,et al.Investigation of the catalyzing trasformation of Pt/H-SAPO-11catalyst applied to heav-y oil[J].Journal of Daqing Petroleum Institute,2004,28(4):52-54.
[4]Marcilly C.Present status and future trends in catalysis for refining and petrochemicals[J].Journal of Catalysis,2003,216(1-2):47-62.
[5]Eswaramoorthi I,Lingappan N.Hydroisomerisation of n-hexane over bimetallic bifunctional silicoaluminophosphate based molecularsieves[J].Applied Catalysis A:General,2003,245(1):119-135.
[6]Fang K G,Wei W,Ren J,et al.n-Dodecane hydroconversion over Ni/AlMCM-41catalysts[J].Catalysis Letters,2004,93(3-4):235-242.
[7]Hu Y F,Wang X S,Guo X W,et al.Effects of channel structure and acidity of molecular sieves in hydroisomerization of n-octane o-ver bi-functional catalysts[J].Catalysis Letters,2005,100(1-2):59-65.
[8]童广明,廖士纲.正构烷烃在分子筛催化剂上的加氢异构化(上)[J].抚顺烃加工技术,2002,1:1-16.Tong Guangming,Liao Shigang.N-alkanes hydrogenation isomerization on the molecular sieve catalyst(I)[J].Fushun hydrocarbonprocessing technology,2002,1:1-16.
[9]Deldari H.Suitable catalysts for hydroisomerization of long-chain normal paraffins[J].Applied Catalysis A:General,2005,293:1-10.
[10]黄卫国,李大东,石亚华,等.分子筛催化剂上正十六烷的临氢异构化反应[J].催化学报,2003,24(9):651-657.Huang Weiguo,Li Dadong,Shi Yahua,et al.Hydroisomerization of n-Hexadecane on Zeolite Catalysts[J].Chinese Journal of Ca-..talysis,2003,24(9):651-657.
[11]刘全杰,徐会青,贾立明.正十二烷在分子筛催化剂上的反应研究[J].南阳师范学院学报,2008,7(6):43-46.Liu Quanjie,Xu Huiqing,Jia Liming.Investigation of n-dodecane reaction over the zeolite catalysts[J].Journal of Nanyang Nor-mal University,2008,7(6):43-46.
[12]Murphy W J,Soled S L,Cody I A,et al.Lube basestocks manufacturing process using improved hydrodewaxing catalysts[P].US:7662273,2010.
[13]Miller S J,Rosenbaum J M.Method for producing aplurality of lubricant base oils from paraffinic feedstock[P].US:6962651,2005.
[14]Lok B M,Messina C A,Patton R L,et al.Crystalline silicoaluminophosphates[P].US:4440871,1984.
[15]Valyocsik E W.Synthesis of zeolite ZSM-22[P].US:4902406,1990.
[16]陆婉珍,汪燮卿.近代物理分析方法及其在石油工业中的应用[M].北京:石油工业出版社,1984.Lu Wanzhen,Wang Xieqing.Modern physics analysis method and its applications in the oil industry[M].Beijing:Petroleum Indus-try Press,1984.
[17]Sarpal A S,Kapur G S,Mukherjee S,et al.Characterization by 13C N M R spectroscopy of base oils produced by different processes[J].Fuel,1997,76(10):931-937.
[18]Sarpal A S,Kapur G S,Chopra A,et al.Hydrocarbon characterization of hydrocracked base stocks by one-and two-dimensional N MR spectroscopy[J].Fuel,1996,75(4):483-490.
[19]Park K C,Ihm S K.Comparison of Pt/zeolite catalysts for n-hexadecane hydroisomerization[J].Applied Catalysis A:General,2000,203(2):201-209.
[20]Thybaut J W,Narasimhan C S L,Denayer J F,et al.Acid metal balance of a hydrocracking catalyst:ideal versus nonideal behavior[J].Industrial&Engineering Chemistry Research,2005,44(14):
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