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首页> 外文期刊>American Chemical Society, Division of Fuel Chemistry, Preprints >DESIGN OF THE CATALYSTS CONTAINING BOTH MICROPOROUS ZEOLITE AND MESOPOROUS MATERIALS FOR THE HYDROREFINING OF GASOLINE AND DIESEL FUEL
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DESIGN OF THE CATALYSTS CONTAINING BOTH MICROPOROUS ZEOLITE AND MESOPOROUS MATERIALS FOR THE HYDROREFINING OF GASOLINE AND DIESEL FUEL

机译:汽油和柴油加氢精制同时包含微孔沸石和中孔材料的催化剂的设计

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摘要

(1) Several novel micro-mesoporous composite materialsrnincluding L(M-L), L-MC[3], L-KIT-6 (LK)[4] were synthesized byrnthe self-assembly of zeolite L nanocrystal clusters in the presence ofrnmesoporous template Triton X 100,CTAB and P123, respectively.rnThe characterization results demonstrated that these materialsrnpossessed relatively high acid amount and acid strength, appropriaternacid types, and a composite pore structure with micropores andrnmesopores.rn(2) The above as-prepared meso-microporous materials werernused as supports to prepare the catalysts for the refining of gasoline.rnCompared with the catalysts introduced conventional microporousrnzeolite L or mesoporous Al-MSU-2 and used bare alumina asrnsupport, the catalysts containing mesoporous zeolite L showed thernexcellent performances of deep desulfurization, aromatization, isomerization and preserving RON value for the hydrodesulfurizationrnreaction of full-range FCC gasoline.rn(3) Micro-mesoporous composite material Beta-KIT-6 (BK) withrnthe BEA microporous structure and cubic Ia3d mesoporous structurernwas synthesized, and used as the catalyst support for thernhydrodesulfurization (HDS) of dibenzothiophene (DBT). Therncomposite material possessed both KIT-6 and Beta structures.rnNiMo/BK had similar acidity as NiMo/Beta, and possessed morernacid sites and stronger acidity than NiMo/KIT-6 and NiMo/SBA-15.rnNiMo/BK showed the highest DBT HDS activity among all therncatalysts that were studied, and the DBT conversion on NiMo/BKrnwas about 2 to 3 times that of NiMo/Al_2O_3. The acidity of NiMo/BKrnenhanced the activity of direct desulfurization (DDS) morernsignificantly than that of the hydrogenation (HYD) pathway.rnCyclohexen-1-yl-benzene was detected as the necessary intermediaternof the HYD pathway[5].rn(4) A new composite material ZSM-5/KIT-6 (ZK-W) wasrnsynthesized by enwrapping nano-sized ZSM-5 zeolite crystals withrnmesoporous KIT-6 silica. This composite was used as catalystrnsupport for NiMo sulfide in the hydrodesulfurization (HDS) of 4,6-rndimethyldibenzothiophene (4,6-DMDBT). The NiMo/ZK-W catalystrngave the highest HDS activity and its 4,6-DMDBT conversion wasrnabout double that of a conventional NiMo/Al_2O_3. The two isomers ofrn4,6-DMDBT (3,6-DMDBT and 3,7-DMDBT), were identifiedrnsimultaneously for the first time in the HDS products of 4,6-DMDBTrnover the NiMo/ZK-W catalyst. The NiMo/ZK-W catalyst exhibited arnsuperior isomerization ability, and 4,4’-dimethylbiphenyl was thernmain product. A new reaction network of 4,6-DMDBT HDS overrnNiMo/ZK-W catalyst was proposed[6].
机译:(1)在中孔模板Triton存在下,通过分子筛L纳米晶簇的自组装合成了几种新型的中微孔复合材料,包括L(ML),L-MC [3],L-KIT-6(LK)[4]。表征结果表明,这些材料具有较高的酸量和酸强度,合适的酸类型以及具有微孔和中孔的复合孔结构.rn(2)使用上述制备的中微孔材料与制备传统的微孔沸石L或介孔Al-MSU-2和使用裸露的氧化铝作为载体的催化剂相比,含中孔沸石L的催化剂表现出优异的深脱硫,芳构化,异构化和异构化性能。保持全系列FCC汽油加氢脱硫反应的RON值。(3)微介孔复合材料Be合成了具有BEA微孔结构和立方Ia3d介孔结构的ta-KIT-6(BK),并用作二苯并噻吩(DBT)的加氢脱硫(HDS)的催化剂载体。复合材料具有KIT-6和Beta结构.rnNiMo / BK与NiMo / Beta具有相似的酸度,比NiMo / KIT-6和NiMo / SBA-15具有更多的酸位和更强的酸度.rnNiMo / BK具有最高的DBT HDS所研究的所有催化剂均具有活性,NiMo / BKrn上的DBT转化率约为NiMo / Al_2O_3的2至3倍。 NiMo / BK的酸度比氢化(HYD)途径增强了直接脱硫(DDS)的活性。环己烯-1-基苯被检测为HYD途径的必要中间体[5]。rn(4)A通过用介孔的KIT-6二氧化硅包裹纳米尺寸的ZSM-5沸石晶体来合成新型复合材料ZSM-5 / KIT-6(ZK-W)。该复合物在4,6-甲基二甲基二苯并噻吩(4,6-DMDBT)的加氢脱硫(HDS)中用作NiMo硫化物的催化剂载体。 NiMo / ZK-W催化剂具有最高的HDS活性,其4,6-DMDBT转化率约为传统NiMo / Al_2O_3的两倍。首次在NiMo / ZK-W催化剂的4,6-DMDBTr的HDS产物中同时鉴定了4,4,6-DMDBT的两个异构体(3,6-DMDBT和3,7-DMDBT)。 NiMo / ZK-W催化剂具有极好的异构化能力,其主要产物是4,4′-二甲基联苯。提出了4,6-DMDBT HDS在NiMo / ZK-W催化剂上的新反应网络[6]。

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    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, P. R. China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, P. R. China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, P. R. China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, P. R. China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, P. R. China;

    State Key Laboratory of Heavy Oil Processing, China University of Petroleum, Beijing 102249, P. R. China;

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