铈改性NaZSM-5分子筛担载Pd催化剂上CO氧化性能研究

以浸渍法制备了一系列添加CeO2的Pd-Ce/NaZSM-5负载型催化剂．以C0氧化为 模型反应，考察了反应温度、Ce含量、预还原、空速及水蒸气等对C0氧化性能的影 响，并利用XIlD和朋等手段对催化剂体相及表面结构进行了表征．结果表明：加入 CeO2作助剂可明显提高催化剂的活性，且催化转化率随着反应温度及Ce含量的增加 而增加；随着空速的增加而降低；催化剂对水蒸气不敏感，在水蒸气存在的条件下 反应可连续进行720h以上保持C0完全转化；H2预还原作用使催化剂活性有所提高． XRD测试结果表明，催化剂中Pd组分处于高分散状态，Ceob的引入促进了N物种在 NaZSM—5载体上的分散．表面XPS分析证实催化剂表面Pd物种处于较高的氧化状态 ，且CeO2与Pd物种间存在协同作用．Pd的高分散及其与CeO2的相互作用是催化剂具 有高活性的关键．     

改进型甲醇合成催化剂NC208的催化特性

采用ＴＰＤ、ＸＲＤ、ＢＥＴ和Ｈ２Ｓ中毒试验等方法，对比研究三组份（Ｃｕ－Ｚｎ－Ａｌ）甲醇合成催化剂Ｃ２０７和添加少量金属氧化物的改进型催化剂ＮＣ２０８．结果表明，工作态ＮＣ２０８催化剂表面Ｃｕ＋／Ｃｕ０的比值和价态稳定性大于Ｃ２０７．     

高分子负载加氢催化剂中钯流失的研究——Ⅰ.高分子载体的影响

高分子催化剂由于同时具有多相催化剂和均相催化剂的优点,已引起了广泛的重视.然而表面活性组份贵金属的流失直接影响了此类高活性催化剂的推广应用.作者合成了不同载体的几类负载钯催化剂,探讨其在1,5,9-环十二碳三烯的选择加氢反应过程中钯的流失规律.从改变高分子配位体入手,通过调整聚合物载体的物理性能、配位原     

对硝基氯苄与活性亚甲基化合物的反应

对硝基苄基衍生物可以与许多阴离子起单电子转移的亲核取代反应。Kornblum等以对硝基氯苄为底物,2-乙氧羰基香豆满-3-酮的钠盐为阴离子,作了深入的研究,得出对硝基氯苄与2-乙氧羰基香豆满-3-酮钠盐的C-烷化反应机理为自由基链式亲核取代反应。同时,Russell等提出对硝基氯苄与2-     

金属－助剂相互作用对SiO_2载铑催化剂化学吸附的影响──Ⅱ．Rh－V／SiO_2催化剂

由ＲｈＣｌ_３·ｘＨ_２Ｏ制备了不同Ｒｈ含量的Ｒｈ／ＳｉＯ_２和Ｒｈ－Ｖ／ＳｉＯ_２催化剂，采用化学吸附和原位ＴＰＤ－ＩＲ方法考察钒助剂对Ｒｈ／ＳｉＯ_２催化剂在常温和高温的Ｈ_２和ＣＯ化学吸附的影响。结果再次表明：１）不同Ｒｈ中心对Ｈ_２和ＣＯ的化学吸附性能不同，钒助剂对不同Ｒｈ中心的Ｈ_２和ＣＯ吸附的影响也不同。Ｈ_２主要吸附在Ｒｈ~Ⅱ和Ｒｈ~Ⅲ中心上，而在Ｒｈ~Ⅰ中心上的吸附弱。２）Ｒｈ－钒助剂的强相互作用主要是Ｒｈ~Ⅱ和Ｒｈ~Ⅲ与钒助剂之间的相互作用，Ｈ_２吸附受到比ＣＯ吸附更强烈的抑制。钒助剂对Ｒｈ／ＳｉＯ_２的Ｈ_２和ＣＯ吸附性能的影响可用覆盖模型解释。     

丁氧基氯化钛载体型催化体系用于乙烯/丁烯-1共聚合的研究

<正> 近十几年来有关载体型高效齐格勒-纳塔催化体系用于乙烯共聚合反应有了不少报道,其中尤以氯化镁为载体的体系居多。本文系统地研究了以氯化镁为载体的一系列正丁氧基氯化钛催化体系,在催化乙烯与丁烯-1共聚合反应的动力学行为,以及催化剂     

烯烃氢甲酰化催化剂活性物种的原位1H NMR研究

The rhodium-phosphine complex catalyst Rh(CO)(acac)(PPh3)(Ⅰ) for 1-hexene hydroformylation was studied under the following reaction conditions: CO/H2=1(mole rate), pressure 1.0 MPa, temperature 25-120℃, by using the pressurized in-situ 1H NMR technique. Experimental results indicated that the formation of a rhodium hydride complex from (Ⅰ) began at room temperature and its amount increased with increasing of reaction temperature. This intermediate complex began to decompose at 100℃ and disapeared completely at 120℃. The intensity change of the proton signal was parallel to catalytical activity in hydroformylation of olefins. Under pure CO pressure the proton signal of Ph-H bond was not observed. There was a 0.2 ppm difference in proton chemical shifts of Rh-H bond under pure H2 pressure and under H2+CO pressure. The results showed that the rhodium-hydride carbonyl complex is the active intermediate in the industrial hydroformylation process.     

A New Reaction-controlled Phase-transfer Catalyst System

A new reaction-controlled phase-transfer catalyst system was designed and synthesized.In this system, heteropolytungstate [C7H7N(CH3)3]9PW9O34 was used for catalytic epoxidation of cyclohexene with H2O2 as the oxidant. The conversion of H2O2 was 100% and the yield of cyclohexene oxide was 87.1% based on cyclohexene. Infrared spectra showed that both fresh catalyst and the recovered catalyst do have completely same absorption peak, indicating the structure of catalyst is very stability and can be recycled.     

NETWORK CROWN ETHER POLYMERS WITH CENTRIC FUNCTIONAL GROUP (Ⅳ) SYNTHESIS OF NETWORK CROWN ETHER POLYMER WITH PENDANT DIETHYLAMINO THIAALKYL GROUP AND ITS PLATINUM COMPLEX*

The title polymer was prepared from 5-diethylamino-3-thia-pentyl glycidyl ether anddiethylene glycol bisglycidyl ether via ring-opening copolymerization. It was found that thisreaction could be catalyzed by sodium, but not Lewis acid. The obtained polymer can coordinatewith platinum compound, and the platinum complex is a new kind of catalyst for thehydrosilylation of olefins with triethoxysilane.     

Large scale Biginelli reaction via water-based biphasic media: a green chemistry strategy

An important stage in process development is kilo scale preparation of the target compound. For this reason, a procedure involving water-based biphasic reaction media has been developed for conducting some exothermic reactions on a large scale. This protocol is illustrated by the energy-efficient and rapid preparation of dihydropyrimidinones by a solvent-free, green chemistry procedure applied to the Biginelli reaction using p-toluenesulfonic acid as catalyst.