Ni基催化剂在邻甲酚原位加氢反应中的催化性能

采用等体积浸渍法制备了一系列负载型Ni基催化剂,利用XRD、H₂-TPR、NH₃-TPD 等技术表征了催化剂的理化特性,考察了载体(CMK-3、SiO₂ZrO₂、MgO、Al₂O₃)、助剂(Cu、Ce、Fe)对Ni基催化剂理化特性的影响,测试了230 oC、0.1 MPa冷压下催化剂对邻甲酚原位加氢反应的性能．结果表明,在负载型镍基催化剂作用下,甲醇水相重整制氢反应可以与邻甲酚的原位加氢反应相耦合;以CMK-3为载体的催化剂活性明显优于其他三种载体,邻甲酚的转化率为45.35%;助剂的添加对催化剂性能影响显著,Fe 的引入使原位加氢体系的转化率降至40.49%,助剂Ce、Cu的加入提高了Ni/CMK-3催化剂的原位加氢反应性能,转化率分别提高至64.6%、66.8%,Cu的添加改变了产物的分布,在产物中出现了新产物甲苯;同时探讨原位加氢反应路径及反应机理．     

固-液-气三相环境下非均相苯加氢反应的原位核磁共振研究

本文使用原位核磁共振（NMR）方法成功实现了对固-液-气三相环境下加氢反应的在线监测.在反应过程中,无需分离产物.以Pd纳米颗粒粉末及不同晶面形貌的Pd催化剂作为研究对象,我们研究了反应压强、反应时间,以及催化剂表面性质对加氢反应的影响.结果表明,压强和反应时间都可以影响加氢反应产物的产率,使用暴露不同晶面的Pd共催化剂时,苯加氢产物不同.该原位NMR方法为研究固-液-气三相催化环境下的加氢反应机理提供了可能.     

基于Pt／C／FN疏水催化剂的常温氢氧复合反应

常温氢氧复合是指在室温或略高于室温温度将H2化合成水，可用于装置设备故障及泄漏时产生大量H2时的应急处理，也可用于火药爆炸气体、含氚废气等的处理。国内常温氢氧复合研究主要选择Pt／SDB和Pt／PTFE为催化剂，由于氢氧复合为强放热反应，热量在高分子载体SDB，PTFE上不容易散失，Pt在反应过程中容易因热迁移而发生团聚，SDB载体在氧化条件下还容易因氧化而老化，使催化剂活性下降。文中选择具有高传热系数的泡沫镍（FN）为惰性载体，制备疏水催化剂，催化氢氧复合反应，并研究了CO和水直接冷却对疏水催化剂活性的影响。     

铈基催化剂催化氧化燃煤烟气中汞的实验及机理研究

采用超声波增强的浸渍法合成了CeO₂-TiO₂催化剂,并采用BET,XRD,XPS等分析手段对催化剂进行了表征。利用固定床反应器,在模拟燃煤烟气条件下研究了CeO₂-TiO₂催化剂对单质汞的催化氧化行为及机理。结果表明:CeO₂-TiO₂催化剂在低温范围（150～250°）具有很强的催化氧化汞的能力;最佳的CeO₂/TiO₂质量比在1.5左右,此时汞的氧化效率可高达90%以上;P25,Evonik TiO₂比锐钛矿TiO₂更适合做铈基催化剂载体;CeO₂-TiO₂催化剂上汞的催化氧化符合Langmuir-Hinshelwood机理,即吸附态的汞与其邻近的活性物质反应生成氧化态汞。     

光促进温和条件非贵金属催化下卤代烃与二氧化碳的羰基化反应及ESR谱研究

研究了卤代烃在光促进温和条件（常温常压）非贵金属[Co(acac)₂,Co(OAc)₂或CoCl₂]催化下与二氧化碳的羰基化反应；同时对反应过程中的ESR谱进行了研究. ESR谱研究表明，在光促进下二氧化碳参与的羰基化反应中有二氧化碳游离基负离子（CO^·-₂）[用DMPO（5,5-二甲基-1-吡咯啉-N-氧化物）捕获］生成.     

催化剂对碳纳米管产率及质量的影响

本文研究了添加钴/二茂铁、镍/二茂铁、钴、镍/钴不同催化剂对高温热解法制备碳纳米管质量、产率等的影响。高分辨率透射电镜图象显示在800℃左右,镍/二茂铁、钴/二茂铁和钴催化条件下,有多壁碳纳米管生成,而用镍/钴作催化剂时,只有直径在0 5μm左右,长度十几个微米的非晶态棒状物生成。通过对生成碳纳米管的质量和产量进行比较,催化剂的催化活性满足二茂铁>钴>镍。简单分析了在碳源高温热解环境下不同金属催化剂的性能差异,并对不同催化条件下生成物的拉曼光谱进行了分析。     

改性镍基催化剂催化甲苯重整与积碳特性研究

通过添加不同比例铁对镍基催化剂进行改性制备得到Fe-Ni/Al_2O_3(FNA)催化剂,在鼓泡流化床上完成焦油模型化合物(甲苯)水蒸气催化重整性能实验,并对反应前后催化剂进行XRD、TPR、BET、XPS和TPO-MS等表征。结果表明:添加铁能够显著提高镍基催化剂催化活性,并有效抑制积碳的生成。F2N1A催化剂(铁镍摩尔比为2)相同条件下甲苯转化率达到90.2%,而未添加助剂的NA催化剂只有44.7%。相应积碳减少了40%左右,其中石墨型等难去除积碳只有NA催化剂的1/3。镍铁合金是Fe-Ni/Al_2O_3催化剂的活性组分,甲苯反应过程中合金中的铁容易被氧化,为镍颗粒表面提供充足的氧。     

生物质基活性炭负载镍对CrⅥ的催化吸附性能研究

为了有效处理污水中的重金属铬,本文利用废弃物甘蔗渣负载镍和氮,制备出一种高催化性能的活性炭用于降解吸附污染水体中的Cr~Ⅵ.利用BET、SEM、Raman、XRD、XPS等手段对负载镍生物质基活性炭进行理化性质表征,对其催化吸附Cr~Ⅵ的性能进行评估并探究了其催化吸附机理。结果表明,在甲酸作为辅助催化剂时,负载镍生物质基活性炭对Cr~Ⅵ的最大降解量高达824.38mg/g,并且循环性能优良,活性位点有较高稳定性。而其催化吸附过程涉及到含氧官能团与Cr的络合作用、单质镍与Cr~Ⅵ氧化还原反应、Ni~(3+)和Cr~(3+)共沉淀等作用。     

Pt_(10)团簇催化肉桂醛选择性加氢反应机理的研究

本文以Pt_(10)团簇作为催化剂模型,采用密度泛函理论(DFT)中的B3LYP方法,在6-31+G(d)(Pt采用贗势基组Lanl2dz)基组水平上,探讨了Pt_(10)团簇催化肉桂醛选择性加氢反应的微观反应历程.研究结果表明,Pt_(10)团簇催化肉桂醛选择性加氢反应可生成3种不同的产物,分别是3-苯基丙醛(P1)、3-苯基丙烯醇(P2)和肉桂醇(P3),每种产物分别通过两条不同的反应通道而得到.Pt_(10)团簇催化有利于肉桂醛分子中C=O键活化加氢.这点与实验结果一致.     

镍改性ZSM-5催化剂及其SCR催化性能

采用液态离子交换法制备了不同负载量的镍改性ZSM-5分子筛催化剂,并考察了上述催化剂的微观结构和物理化学特性及其在NH3-SCR反应中的催化性能。结果表明:在负载量<10.9%时镍在分子筛中具有高度的分散性,而随着镍负载量的进一步增加,分子筛表面开始出现较大的NiO颗粒;镍元素只以+2价存在于分子筛催化剂中;在NH₃-SCR反应中,镍负载量低于14.9%时,增加镍负载量将提高催化剂的低温活性;当反应温度超过300℃时,高温催化中心开始起作用,但随镍负载量的增加,高温活性开始下降时的温度逐渐降低。     

Homogeneous and heterogeneous asymmetric reactions: Part 11. Sonochemical enantioselective hydrogenation of trifluoromethyl ketones over platinum catalysts

Enantioselective sonochemical hydrogenation of alpha,alpha,alpha-trifluoromethyl ketones, namely, 1,1,1-trifluoroacetophenone and 1,1,1-trifluoro-phenylacetone was carried out over various platinum catalysts modified by cinchonidine in different solvents. Both compounds yielded the (R)-alcohol as major product. The reaction rates and the enantiomeric excesses were determined over Pt/C, Pt/SiO2, Pt/K-10 and Pt/Al2O3 catalysts under conventional conditions. Since Pt/Al2O3 exhibited the best catalytic performance the effect of ultrasound on the catalytic activity and enantioselectivity was tested using this catalyst applying different sonochemical pretreatments. These methods included a pretreatment before the reaction in hydrogen and oxygen or both. The ultrasonic irradiation was found to be highly advantageous in the case of trifluoroacetophenone, whereas only moderate changes were observed using trifluoro-phenylacetone. After insonation of the catalyst, the enantioselectivity was considerably improved. Both the aerobic and anaerobic sonochemical pretreatments resulted in significant improvement in optical yield (up to 49% and 17% ee, at room temperature under 10 bar in 1,2-dichlorobenzene). In parallel, the hydrogenation rates increased to a small extent (1.1-1.2-fold increase) after hydrogenative ultrasonic pretreatment, whereas the rates decreased by a factor of 1.5-2 after aerobic insonation. To obtain more insight into the process, the effect of insonation time on the activity and enantioselectivity and actual changes of the catalyst were also studied.     

Ultrasonics in heterogeneous metal catalysis: sonochemical chemo- and enantioselective hydrogenations over supported platinum catalysts

Sonochemical chemo- and enantioselective hydrogenations over supported platinum catalysts are described. We disclose our results with respect to a sonochemical modification of the chemoselective hydrogenation of cinnamaldehyde over supported platinum catalysts, and the asymmetric hydrogenation of ethyl pyruvate promoted by various ultrasonic pretreatments. The ultrasonic pretreatment of the supported platinum catalysts was found to be highly beneficial in almost every case, improving both the catalytic activity and selectivity. The effect of additional experimental variables, such as hydrogen pressure, catalyst support, temperature and the ultrasonic insonation time were also studied. The enantioselectivity of the hydrogenation of ethyl pyruvate increased up to 97.1% ee. In the case of cinnamaldehyde hydrogenation, the selective preparation of cinnamyl alcohol became possible. The theoretical aspects of the working mechanisms in comparison with 'silent' reactions will also be provided.     

Phase-transfer catalysis and ultrasonic waves. I. Cannizzaro reaction

The aim of this work is to study the effect of an ultrasonic wave on the Cannizzaro reaction catalyzed by a phase-transfer catalyst. The reaction of benzaldehyde with potassium hydroxide was chosen as the reference reaction. The kinetics of the reaction was followed by the amount of benzoic acid which is well characterized and easily isolatable. Investigations were made on variables such as the kind of aldehyde, the phase-transfer catalyst, the temperature and the frequency of ultrasonic wave. As the phase-transfer catalyst depends strongly on mass transfer between two phases, it is well understood that ultrasonic waves have a greater efficiency of interface mixing than conventional agitation. The results showed that an ultrasonic wave of 20 kHz dramatically accelerates on the reaction.     

Sonochemical enantioselective hydrogenation of ethyl pyruvate over platinum catalysts

Chiral sonochemical hydrogenation of an aliphatic -ketoester, ethyl pyruvate to ethyl lactate was carried out over various platinum catalysts in different solvents under atmospheric hydrogen pressure. The reaction rates and the enantiomeric excesses were determined over Pt/C, Pt/SiO₂ and Pt/K-10 catalysts both under conventional and sonochemical conditions. The effect of ultrasounds on the catalytic activity and enantioselectivity was tested applying sonochemical pretreatment before the reaction. The ultrasonic irradiation was found to be highly advantageous in these hydrogenations. After insonation of the catalysts, the enantioselectivity was highly improved over Pt/SiO₂ and Pt/K-10 catalysts. In addition, the reactions took place in quantitative yield and with complete chemoselectivity and the hydrogenation rates increased with one order of magnitude despite the very mild (atmospheric hydrogen pressure, room temperature) experimental conditions.     

Ultrasonically improved semi-hydrogenation of alkynes to (Z-)alkenes over novel lead-free Pd/Boehmite catalysts

This paper reports the application of ultrasound in the semi-hydrogenation of alkynes over two novel Pd/Boehmite catalysts. The semi-hydrogenations of phenylacetylene, diphenylacetylene and 2-butyne-1,4-diol have either been investigated in an ultrasonic bath under atmospheric hydrogen pressure, or in an ultrasonic horn reactor under 0.1–0.5 MPa hydrogen pressure. Alkyne hydrogenation was suppressed by sonication under atmospheric hydrogen pressure, but promoted by sonication under 0.1 MPa of hydrogen pressure. Sonication increased selectivity towards the semi-hydrogenated products in both cases. Catalyst loading, hydrogen pressure, temperature and the presence of quinoline, all impacted on hydrogenation rate, activity and selectivity to semi-hydrogenated products. Palladium leaching from the catalyst was evaluated in ethanol and hexane both under plain stirring and sonication.     

Effect of ultrasound in enantioselective hydrogenation of 1-phenyl-1,2-propanedione: comparison of catalyst activation, solvents and supports

The enantioselective hydrogenation of 1-phenyl-1,2-propanedione was carried out over Pt/Al2O3, Pt/SiO2, Pt/SF (silica fiber), Pt/C catalysts modified with cinchonidine under ultrasonic irradiation. The initial rate, regioselectivity and enantioselectivity were investigated for different catalyst pretreatments, solvents and ultrasonic powers. The ultrasound effects were very catalyst dependent. The sonication significantly enhanced enantioselectivity and activity of the Pt/SF (silica fiber) catalyst. For the other Pt supported catalysts the reaction rate, enantioselectivity and regioselectivity increased moderately. The choice of solvent influenced the impact of ultrasound effect, namely in mesitylene, which has the lowest vapor pressure, the highest ultrasound enhancement was observed. The effect of sonication on catalysts surface was studied by transmission electron microscopy and scanning electron microscopy (SEM). No significant change in the metal particle size distribution due to sonication was observed. However, in the case of the Pt/SF catalyst, acoustic irradiation induced morphological changes on the catalyst particle surface (SEM), which might be the cause for enhancement of the initial reaction rate and enantioselectivity.     

Study on ultrasound-assisted precipitation for preparing Ni/Al2O3 catalyst

With the rapid development of oil hydrogenation industry, the development of oil hydrogenation catalyst has also become a research hotspot. In this paper, ultrasound-assisted precipitation technique is used to prepare Ni/Al₂O₃ catalyst. The effect of ultrasonic output power on catalyst performance is investigated. The prepared catalyst is applied to the hydrogenation reaction of castor oil. It is found that the prepared catalyst shows the best hydrogenation performance when ultrasonic output power, frequency and ultrasonic treatment time are 80 W, 40 kHz and 600 min respectively. It also indicates that ultrasound-assisted precipitation technique can reduce the particle size and increase the specific surface area of Ni/Al₂O₃ catalyst so that its activity is improved. In addition, six important elements that should be considered in the development of industrial oil refining catalysts are discussed, and the effects of these factors on the catalyst performance are discussed. Finally, new way for improving catalyst performance is given, and the application of some new materials and methods in oil refining is introduced.     

Carbon nanotubes supported Pt-Ni catalysts and their properties for the liquid phase hydrogenation of cinnamaldehyde to hydrocinnamaldehyde

The Pt-Ni catalysts supported on CNTs have been prepared by wet impregnation and the selective hydrogenation of cinnamaldehyde (CMA) to the corresponding hydrocinnamaldehyde (HCMA) over the catalysts has been studied in ethanol at different reaction conditions. The results show that Pt-0.34 wt% Ni/CNTs catalyst exhibits the highest activity and selectivity at a reaction temperature of 70 °C under a pressure of around 2.0 MPa, and 98.6% for the conversion of CMA and 88.2% for the selectivity of CMA to HCMA, respectively. The selective hydrogenation for the CC bond in CMA would be improved as increasing the reaction temperature, and the hydrogenation for the CO bond in CMA is enhanced as increasing the H₂ pressure. In addition, these catalysts have also been characterized using TEM-EDS, XPS, H₂-TPR and H₂-TPD techniques. The results show that Pt particles are dispersed more homogeneously on the outer surface of the nanotubes, while the strong interaction between Pt and Ni would improve the increasing of activated hydrogen number because of the hydrogen spillover from reduced Pt⁰ onto CNTs and increase the catalytic activity and selectivity of CMA to HCMA.     

不同制备工艺钒系SCR催化剂理化及催化性能研究

本文研究了制备工艺对 TiO2-WO3-V2O5- 载体型催化剂理化特性及其在 NH3-SCR 反应中催化性能的影响.通过 XRD、TG/DTA 等分析方法考察了煅烧温度等对催化剂中各组分晶体结构的影响,确定了制备负载型催化剂的最佳煅烧温度为 500℃.不同制备工艺催化剂理化性能的对比表明,多步浸渍法不仅提高了锐钛矿型 TiO2 向金红石型 TiO2 的转变温度,而且使更多的钒氧化物处于较低的价态,有利于提高还原反应的催化性能;催化活性评价试验也表明使用多步浸渍法制备的 SCR 催化剂具有较高的催化活性和更宽的高活性反应温度窗口.最后考察了反应空速对多步浸渍法所制备催化剂 NOx 转化效率的影响,结果表明:随空速的增加,NOx 转化效率逐渐降低.     

Ultrasound-assisted sequentially precipitated nickel-silica catalysts and its application in the partial hydrogenation of edible oil

Sequentially precipitated Mg-promoted nickel-silica catalysts with ageing performed under various ultrasonic intensities were employed to study the catalyst performance in the partial hydrogenation of sunflower oil. Results from various characterisation studies showed that increasing ultrasonic intensity caused a higher degree of hydroxycarbonate erosion and suppressed the formation of Ni silicates and silica support, which improved Ni dispersion, BET surface area and catalyst reducibility. Growth of silica clusters on the catalyst aggregates were observed in the absence of ultrasonication, which explained the higher silica and nickel silicate content on the outer surface of the catalyst particle. Application of ultrasound also altered the electron density of the Ni species, which led to higher activity and enhanced product selectivity for sonicated catalysts. The catalyst synthesised with ultrasonic intensity of 20.78 Wcm⁻² achieved 22.6% increase in hydrogenation activity, along with 28.5% decrease in trans-C18:1 yield at IV = 70, thus supporting the feasibility of such technique.