对苯二酚催化加氢制备1,4-环己二醇的研究

对Pt/C、Pd/C、Ru/C、Rh/C和Raney Ni几种催化剂,以及以钌为活性组分的催化剂载体如活性碳、SiO2、Al-MCM-41、ZSM-5、MgO、TiO2在对苯二酚加氢反应中的催化活性进行了比较.结果表明Ru/C催化剂的催化活性和对目的产物的选择性最好.对Ru/C催化剂催化对苯二酚加氢反应的反应条件如反应温度,氢气压力,反应溶剂,反应时间等对反应转化率和产物选择性的影响进行了讨论.反应的适宜条件为:反应物和催化剂的物质量比为367∶1,温度为150℃、氢气压力5 MPa,乙醇为溶剂,反应时间2 h.在此反应条件下,对苯二酚的转化率为98.8%,目的产物1,4-环己二醇的选择性为77.7%.并根据产物随时间的变化规律对该反应路径进行了分析.     

非晶态合金作催化材料的研究IV. 超细非晶态Ni-B催化剂的制备及催化性能研究

采用化学还原法制备了非晶态Ni-B超细粒子催化剂, 所含两种粒子的粒径分别为5~20nm和150nm左右。对环戊二烯常压液相加氢反应的活性测试结果表明, 该催化剂具有很高的活性和选择性, 并且在加氢反应中具有替代Raney Ni和Pd/C催化剂的工业应用潜力。动力学测量表明, 在该催化剂上, 环戊二烯选择加氢生成环戊烯的反应为零级, 环戊烯生成环戊烷的反应为近似一级。     

非晶态合金作催化材料的研究IV. 超细非晶态Ni-B催化剂的制备及催化性能研究

采用化学还原法制备了非晶态Ni-B超细粒子催化剂, 所含两种粒子的粒径分别为5~20nm和150nm左右。对环戊二烯常压液相加氢反应的活性测试结果表明, 该催化剂具有很高的活性和选择性, 并且在加氢反应中具有替代Raney Ni和Pd/C催化剂的工业应用潜力。动力学测量表明, 在该催化剂上, 环戊二烯选择加氢生成环戊烯的反应为零级, 环戊烯生成环戊烷的反应为近似一级。     

一种催化降解有机废水制氢的资源化技术

提出了一种催化化学法降解有机废水制氢的资源化技术,特别是为生物难降解高毒性的有机废水的净化处理和制氢资源化利用提供了一条途径。在Raney Ni、Sn修饰的Raney Ni（Sn-Raney-Ni）或Pd／C等催化剂的作用下和比较温和的条件下,利用水相重整反应技术将废水中的有机物（如,苯酚、苯胺、硝基苯、四氢呋喃、甲苯、DMF和环己醇等）高选择性地降解为H2和CO2等无机分子。分别在连续固定床和间歇釜式反应器中的实验结果表明,在优化的反应条件下,有机废水的降解率和H2选择性均达到100％。Sn修饰的Raney Ni（Sn／Ni=0.06）和Pd／C催化剂比Raney Ni催化剂具有更好的降解有机废水制氢的性能。     

非晶态合金作催化材料的研究 Ⅳ.超细非晶态Ni-B催化剂的制备及催化性能研究

采用化学还原法制备了非晶态Ni-B超细粒子催化剂,所含两种粒子的粒径分别为5～20nm和150nm左右.对环戊二烯常压液相加氢反应的活性测试结果表明,该催化剂具有很高的活性和选择性,并且在加氢反应中具有替代Raney Ni和Pd/C 催化剂的工业应用潜力.动力学测量表明,在该催化剂上,环戊二烯选择加氢生成环戊烯的反应为零级,环戊烯生成环戊烷的反应为近似一级.     

聚苯胺对钯催化甲酸电氧化反应的促进作用

钯基纳米材料是甲酸电氧化反应的优良催化剂.本工作制备了两个系列钯基催化剂,并考察了聚苯胺对钯上甲酸电氧化反应的助催化作用.一种是以聚苯胺为基底,在其表面电沉积钯纳米粒子,制得nPANI/Pd催化剂(n表示聚合苯胺的循环数);另一种是直接在商业Pd/C催化剂表面电聚合苯胺,制得Pd/C/nPANI催化剂.结果显示,聚苯胺单独存在时对甲酸电氧化反应没有催化活性,但其可对钯上甲酸电氧化反应呈现明显的促进作用,且促进作用与聚苯胺的厚度(聚合循环数)密切相关.在两个系列催化剂中,15PANI/Pd和Pd/C/20PANI显示出最高的催化性能.15PANI/Pd中钯的质量比催化活性是纯钯催化剂的7.5倍; Pd/C/20PANI中钯的质量比催化活性和本征催化活性分别是商业Pd/C催化剂的2.3和3.3倍.钯催化性能的提升与聚苯胺和钯纳米粒子间的电子效应有关.     

聚苯胺对钯催化甲酸电氧化反应的促进作用（英文）

钯基纳米材料是甲酸电氧化反应的优良催化剂.本工作制备了两个系列钯基催化剂,并考察了聚苯胺对钯上甲酸电氧化反应的助催化作用.一种是以聚苯胺为基底,在其表面电沉积钯纳米粒子,制得n PANI/Pd催化剂(n表示聚合苯胺的循环数);另一种是直接在商业Pd/C催化剂表面电聚合苯胺,制得Pd/C/n PANI催化剂.结果显示,聚苯胺单独存在时对甲酸电氧化反应没有催化活性,但其可对钯上甲酸电氧化反应呈现明显的促进作用,且促进作用与聚苯胺的厚度(聚合循环数)密切相关.在两个系列催化剂中,15PANI/Pd和Pd/C/20PANI显示出最高的催化性能.15PANI/Pd中钯的质量比催化活性是纯钯催化剂的7.5倍;Pd/C/20PANI中钯的质量比催化活性和本征催化活性分别是商业Pd/C催化剂的2.3和3.3倍.钯催化性能的提升与聚苯胺和钯纳米粒子间的电子效应有关.     

用超声波技术制备的Raney Ni催化剂及其催化加氢活性

 将超声波技术与碱抽滤方法相结合制备出一种Raney Ni催化剂. 以苯饱和加氢为探针反应,测定了超声处理时间对Raney Ni催化剂催化活性(包括吸氢速率和苯转化率)的影响. 结果表明,超声处理对催化剂的活性有明显的促进作用. 随着超声处理时间的延长,催化剂的活性先逐渐升高,后慢慢降低,超声处理15 min时可获得最高的催化活性. 通过ICP,XRD,XPS,BET和SEM等手段对Raney Ni催化剂的表面电子态、比表面积、孔体积、孔径、粒径及表面形貌等进行了表征,并对超声波的作用进行了初步讨论.     

PdNiO/C在碱性介质中对甲醇的电氧化

应用循环伏安,计时电流,计时电位和XRD等方法研究了碱性介质中甲醇在自制PdNiO/C和Pd/C催化剂上的电化学氧化以及高温热处理对催化剂结构和性能的影响.结果表明,还原温度为70℃,Pd、Ni原子比为8∶2时,PdNiO/C催化剂对甲醇电化学氧化具有较好的催化活性.热处理可增大催化剂粒径,升高结晶度,降低分散度和催化活性,并且可使NiO从Pd的晶格中脱离出来.与Pd/C催化剂相比,优选的PdNiO/C催化剂有更高的催化活性和更好的抗毒化能力.     

高分散的炭载Au纳米催化剂的制备、表征和催化活性

采用柠檬酸钠还原-胶体负载法, 制备了高分散的炭载Au纳米催化剂, 并以液相催化氧化葡萄糖为葡萄糖酸钠的反应评价了Au/C催化剂的活性. 研究结果表明, 金溶胶制备过程中柠檬酸钠的用量对粒子尺寸以及所获催化剂的催化活性有重要影响; 催化剂在多次使用之后活性的降低可能是由于在活性炭表面金粒子活性位点上形成的Au^δ＋-O^δ－化合态减少的缘故. 同时比较了制备的Au/C和商业Pd/C催化剂对葡萄糖的液相催化氧化反应, 证明Au/C催化剂明显优于Pd/C催化剂.     

Rational Design of Pt−Pd−Ni Trimetallic Nanocatalysts for Room-Temperature Benzaldehyde and Styrene Hydrogenation

Nanostructures of the multimetallic catalysts offer great scope for fine tuning of heterogeneous catalysis, but clear understanding of the surface chemistry and structures is important to enhance their selectivity and efficiency. Focussing on a typical Pt−Pd−Ni trimetallic system, we comparatively examined the Ni/C, Pt/Ni/C, Pd/Ni/C and Pt−Pd/Ni/C catalysts synthesized by impregnation and galvanic replacement reaction. To clarify surface chemical/structural effect, the Pt−Pd/Ni/C catalyst was thermally treated at X=200, 400 or 600 °C in a H₂ reducing atmosphere, respectively termed as Pt−Pd/Ni/C−X. The as-prepared catalysts were characterized complementarily by XRD, XPS, TEM, HRTEM, HS-LEIS and STEM-EDS elemental mapping and line-scanning. All the catalysts were comparatively evaluated for benzaldehyde and styrene hydrogenation. It is shown that the “PtPd alloy nanoclusters on Ni nanoparticles” (PtPd/Ni) and the synergistic effect of the trimetallic Pt−Pd−Ni, lead to much improved catalytic performance, compared with the mono- or bi- metallic counterparts. However, with the increase of the treatment temperature of the Pt−Pd/Ni/C, the catalytic performance was gradually degraded, which was likely due to that the favourable nanostructure of fine “PtPd/Ni” was gradually transformed to relatively large “PtPdNi alloy on Ni” (PtPdNi/Ni) particles, thus decreasing the number of noble metal (Pt and Pd) active sites on the surface of the catalyst. The optimum trimetallic structure is thus the as synthesised Pt−Pd/Ni/C. This work provides a novel strategy for the design and development of highly efficient and low-cost multimetallic catalysts, e. g. for hydrogenation reactions.     

Ni,Pd／Al2O3对丙酮加氢一步合成甲基异丁基酮性能比较

研究了Ａｌ２Ｏ３负载Ｎｉ、Ｐｄ催化剂上丙酮加氢一步合成甲基异丁基酮的反应活性。考察了不同Ｎｉ含量和不同Ｐｄ含量对活性的影响。结果表明，在载体Ａｌ２Ｏ３中加入不同含量的ＳｉＯ２后，会改善载体的性能，Ｎｉ／Ａｌ２Ｏ３催化剂中添加稀土元素Ｌａ或Ｃｅ后可改善催化剂的稳定性。     

Butane Dehydrogenation Reaction on Sulfur Poisoned Group 10 Metal/SiO2 Catalysts

Butane cracking and dehydrogenation reactions on silica supported Ni, Pt, Pd, and S, Pb modified Ni, Pt, Pd catalysts were studied via a fixed bed reaction system. Cracking reaction path prevailed when butane reaction was catalyzed by clean Ni, Pt, Pd and sulfur poisoned Ni catalysts. The addition of sulfur into Pt and Pd catalytic systems can shift the reaction path to dehydrogenation reaction. However, the deactivation problem due to carbonaceous deposit is not improved by the addition of sulfur into the catalytic system. The origin of the sulfur effect on the change of butane reaction pathway is discussed on the basis of the concentrations of Ph and S additives, oxygen perturbation effect, metal loading, carbonaceous deposit and reaction temperatures.     

Pd-Co/C催化剂上葡萄糖的催化氧化反应

Pd-Co/C催化剂上葡萄糖的催化氧化反应     

Pt，Pd助剂对Ni基催化剂中Ni的分散度及抗积碳性能的影响

研究了添加少量贵金属(Pt,Pd)的Ni/Al2O3催化剂对甲烷水蒸汽重整反应抗积碳能力和催化性能的影响.催化活性实验表明,添加少量Pt的样品显著提高了Ni/Al2O3催化剂的活性,稳定性,抗积碳和抗氧化能力,而添加Pd的样品对Ni/Al2O3催化剂的催化性能提高并不明显.利用氢气程序升温还原(H2-TPR),X射线晶体衍射(XRD),热重-差热分析(TG-DTA)等手段对反应前后的催化剂进行了表征,研究发现在Ni-Pt/Al2O3催化剂中Ni与Pt之间存在较强的相互作用力,在主要由Ni覆盖的表面形成了Ni-Pt双金属簇,提高了Ni的分散度,在催化剂的表面易于形成较小的Ni颗粒,抑制了Ni的烧结,改善了Ni基催化剂的抗积碳能力;贵金属Pt通过H2的溢流效应促进了Ni的还原,抑制了催化剂的氧化.而在Ni-Pd/Al2O3中,Ni和Pd存在着一定的偏析效应,不能有效的形成Ni-Pd双金属簇,在还原过程中分别被还原.     

Influence of the Charge Transfer Capacity of Alkali and Alkaline Earth Metals as Promoters in Thehydrogenation of Phenol over Palladium and Nickel Catalysts

The gas phase hydrogenation (523-573 K) of phenol has been studied over 1 wt.% Pd/Al₂O₃ and 1 wt.% Ni/SiO₂ catalysts doped with Group I and II promoter oxides. A direct correlation between catalytic activity and the charge transfer capacity of the promoters is presented where hydrogenation is favored by increasing electron donation from the promoter. The Pd catalysts generated cyclohexanone (selectivity > 97%) as the predominant product; selectivity was unaffected by the presence of the alkali or alkaline earth dopants. The Ni system exhibited appreciable hydrogenolysis behavior and charge transfer from the dopants limited the degree of hydrodeoxygenation to favor complete hydrogenation to cyclohexanol.     

A resource recycling technique of hydrogen production from the catalytic degradation of organics in wastewater

A resource recycling technique of hydrogen production from the catalytic degradation of organics in wastewater by aqueous phase reforming (APR) has been proposed. It is worthy of noting that this technique may be a potential way for the purification of refractory and highly toxic organics in water for hydrogen production. Hazardous organics (such as phenol, aniline, nitrobenzene, tetrahydrofuran (THF), toluene, N,N-dimethylformamide (DMF) and cyclohexanol) in water could be completely de-graded into H2 and CO2 with high selectivity over Raney Ni, and Sn-modified Raney Ni (Sn-Raney-Ni) or Pd/C catalyst under mild conditions. The experimental results operated in tubular and autoclave reactors, indicated that the degradation degree of organics and H2 selectivity could reach 100% under the optimal reaction conditions. The Sn-Raney-Ni (Sn/Ni=0.06) and Pd/C catalysts show better catalytic performances than the Raney Ni catalyst for the degradation of organics in water into H2 and CO2 by the aqueous phase reforming process.     

Pd/Ni异结构纳米催化剂的制备及其对甲酸氧化的电催化

通过两步还原法制备了Pd/Ni双金属催化剂.由于金属Pd原子在先行还原的Ni纳米粒子表面的外延生长以及其在Ni表面及Pd表面生长表现出的吉布斯自由能差异,最终导致了异结构Pd/Ni纳米粒子的形成.高分辨电子透射显微镜结果证实了异结构的存在,然而X射线衍射测量表明Pd/Ni纳米粒子具有类似于Pd的面心立方结构.制备的Pd/Ni纳米粒子与同等条件下合成的Pd纳米粒子相比对甲酸氧化呈现了更高的电催化活性,而且电催化稳定性也要明显优于纯Pd纳米粒子,证明Pd/Ni双金属催化剂是可选的直接甲酸燃料电池阳极催化剂.双金属催化剂对甲酸氧化电催化活性和稳定性增强可能是Ni原子的修饰改变了Pd粒子表面配位不饱和原子的电子结构所致.     

Catalytic reduction of aromatic polynitro compounds

The liquid-phase catalytic hydrogenation of 3,5-dinitrophenyl phenyl ether to give 3,5-diaminophenyl phenyl ether in the presence of Group VIII metals as catalysts has been investigated. The main kinetic characteristics of the process have been established. The reduction occursvia the formation of 5-amino-3-nitrophenyl phenyl ether. In terms of their activity, the catalysts studied can be arranged in the following sequence: 1% Pd/Sibunit> 2 % Pd/C > Lindlare Pd > 5% Ru/Sibunit > Raney Ni. The selectivity of the process with respect to intermediate 5-amino-3-nitrophenyl phenyl ether depends on the relative adsorption abilities of mono- and dinitro compounds. A promoting effect of water during hydrogenation of 3,5-dinitrophenyl phenyl ether in isopropanol or 1,4-dioxane has been noted. Catalytic synthesis of 3,5-diaminophenyl phenyl ether has been carried out for the first time.Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 9, pp. 1716–1719, September, 1995.