Kinetic study of liquid-phase hydrodechlorination of hexachlorobenzene on Ni/C and 2%PdNi/C

Liquid-phase hydrodechlorination of hexachlorobenzene was kinetically studied in the presence of both nickel (Ni/C) and palladium-promoted nickel (2%PdNi/C) catalysts under different reaction conditions. Molecular hydrogen (at 1 and 20 atm) and sodium borohydride (NaBH₄) were used as reducing agents. In the presence of the nickel catalyst, the hydrodechlorination of C₆Cl₆ occurs via a consecutive mechanism (removal of one chlorine atom from the substrate at each stage), whereas with the 2%PdNi/C catalyst, the transformation of C₆Cl₆ occurs via both consecutive and multiplet mechanism (with the elimination of several chlorine atoms without desorption of the chloroaromatic substrate from the catalyst surface). The promotion of the nickel catalysts with palladium substantially changes the selectivity of formation of intermediate products of C₆C1₆ dechlorination. The mechanism of hydrodechlorination of hexachlorobenzene was suggested that explained the presence of only certain products of partial dechlorination of hexachlorobenzene in the reaction medium.     

镍负载量对乙醇水蒸气重整制氢催化性能和催化剂的影响

采用稳态实验对镍负载量对Ni/MgO催化剂在乙醇水蒸气重整反应的影响进行了研究。结果表明，在101.3kPa下，镍负载量越高，催化剂的活性越高。对于催化剂的选择性，存在一个最佳镍负载量为10%Ni/MgO。按选择性从大到小排序，不同镍负载量的催化剂为：10Ni/MgO>15Ni/MgO>12.5Ni/MgO>7.5Ni/MgO≈5Ni/MgO。热分析表明，焙烧过程中不同镍负载量的催化剂镍前体与载体前体之间发生的相互作用不同。XRD和TPR 表征结果显示，催化剂的晶体结构和还原特性也与催化剂上镍的负载量有关。焙烧过程中样品10Ni/MgO上镍前体与载体前体发生了两种相互作用, 并且其氧化态与其他催化剂相比具有特殊的结构和还原性。说明催化剂的选择性不仅受活性相Ni的影响而且受Ni活性相周围环境的影响。     

TiO2纳米管负载Pd-Ag催化1,2-二氯乙烷的选择性加氢脱氯

以二氧化钛纳米管为载体,分别采用光沉积法和浸渍法制备负载Pd和Ag的双金属催化剂,并考察它们对1,2-二氯乙烷选择性加氢脱氯的行为。催化剂的UV-Vis,XRD,XPS等表征结果显示,在Ag负载量相近的情况下,光沉积法制备的催化剂较浸渍法制备的催化剂具备更显著的Ag富集现象。催化剂对1,2-二氯乙烷活性评价的结果表明,在Ag负载量相近时,光沉积法制备的催化剂对乙烯具有更高的选择性,且随着Ag负载量的提高,催化剂对乙烯选择性也逐渐增强。     

1,2-二氯丙烷加氢脱氯制丙烯Ni/活化炭化树脂催化剂

镍催化剂;1;2-二氯丙烷加氢脱氯制丙烯Ni/活化炭化树脂催化剂     

TiO_2纳米管负载Pd-Ag催化1,2-二氯乙烷的选择性加氢脱氯

以二氧化钛纳米管为载体,分别采用光沉积法和浸渍法制备负载Pd和Ag的双金属催化剂,并考察它们对1,2-二氯乙烷选择性加氢脱氯的行为。催化剂的UV-Vis,XRD,XPS等表征结果显示,在Ag负载量相近的情况下,光沉积法制备的催化剂较浸渍法制备的催化剂具备更显著的Ag富集现象。催化剂对1,2-二氯乙烷活性评价的结果表明,在Ag负载量相近时,光沉积法制备的催化剂对乙烯具有更高的选择性,且随着Ag负载量的提高,催化剂对乙烯选择性也逐渐增强。     

Preparation of nickel-mesoporous materials and their application to the hydrodechlorination of chlorinated organic compounds

Mesoporous materials have attracted considerable attention for use as a catalyst or a catalyst support due to their remarkable textural properties such as high surface area and large pore volume with a narrow pore size distribution. Many efforts have been made to design mesoporous materials for use in heterogeneous catalyst systems. Recent progress and results regarding the preparation of nickel-mesoporous materials and their application to the hydrodechlorination of chlorinated organic compounds were discussed in this review. Mesoporous materials were used as a support for nickel catalyst or a nickel-incorporated mesoporous catalytic material in this work. Two research areas were described and discussed in this review. One is the preparation of mesoporous alumina-supported nickel catalysts and their application to the hydrodechlorination of 1,2-dichloropropane and o-dichlorobenzene. The other is the preparation of mesoporous silica-supported nickel catalysts and their application to the hydrodechlorination of 1,1,2-trichloroethane and chlorobenzene.     

Nickel Complexes Catalyzed Hydrodechlorination of Aryl Chlorides in Ionic Liquid

The hydrodechlorination performance of nickel complex catalysts, Ni[phen]₂(PF₆)₂ and Ni[bpy]₃(PF₆)₂, were investigated with [Bmim]Br as the ionic liquid solvent. It is proved that Ni[phen]₂(PF₆)₂ is efficient for the hydrodechlorination of aryl chlorides under mild conditions with water as the hydrogen source. The hydrogen source of reaction is from the water which was confirmed by the deuterium incorporation experiments. Recycling experiments showed a decreasing activity of this catalyst due to a small leaching of nickel complex from the ionic liquid phase during the recycling process where n‐heptane was used as the extractant. A plausible reaction route has been suggested.     

氯代苯胺液相催化加氢合成环己酮

提出了一种催化降解氯代苯胺高选择性合成环己酮的技术.在La修饰Pd/Al2O3催化剂作用下,通过催化加氢的方法实现了由多氯代苯胺(2,4,6-三氯苯胺和2,4,-二氯苯胺)高选择性地合成环己酮(不含环己醇).在优化的反应条件下,2,4,6-三氯苯胺加氢生成环己酮的转化率和选择性分别为100%和98.6%(没有检测到环己醇);2,4,-二氯苯胺加氢生成环己酮的转化率和选择性均为100%.氯代苯胺在Pd/La-Al2O3催化剂表面首先发生加氢脱氯/N-甲基化等反应生成苯胺、N-甲基苯胺和N,N-二甲基苯胺等中间产物,随后这些中间产物发生苯环加氢、氨基水解/醇解等反应得到环己酮;氯代苯胺上Cl元素的存在和体系中水的含量是影响环己酮选择性的重要因素.     

不同载体Ni基催化剂生物质热解气甲烷化反应性能

采用浸渍法制备了Ni金属负载在不同载体(SiO2、ZrO2、CeO2、Al2O3和Al2O3-CeO2)表面形成的催化剂,研究了水蒸气和载体对生物质热解气甲烷化反应性能的影响。结果表明,随着水蒸气量的增加CO转化率逐渐增大,而甲烷选择性呈现先增加后降低的变化趋势,当nw ater/ngas比值为0.26时达到最大。载体Al2O3相比SiO2、ZrO2和CeO2具有更大的比表面积和Ni金属分散度,促进了生物质热解气甲烷化反应活性和选择性。相比于Ni-Al2O3催化剂,Al2O3-CeO2复合载体具有更多的镍金属负载量活性金属分散度,以及最好的低温甲烷化反应性能。在300℃的低温条件下,Ni-Al2O3-CeO2催化剂的CO转化率达到97%,CH4增长率达到110%。     

Preparation of Uniform Ni-B Amorphous Alloy Catalyst on CNTs and its Performance for Acetylene Selective Hydrogenation

Carbon nanotubes (CNTs) are severely bundled and essentially insoluble in solvent. These properties are generally considered as a significant barrier toward the practical uses of CNTs. Therefore, the functionalization and solubilization of CNTs have recei…     

负载Ni催化剂用于乙二醇蒸汽重整制氢催化性能研究

采用等体积浸渍法和共沉淀法制备了Ni催化剂,在固定床反应器上考察了Ni负载量、焙烧温度、反应温度等因素对乙二醇低温重整制氢反应活性和选择性的影响。应用X射线衍射、氮物理吸附、H₂程序升温还原等技术对负载型Ni催化剂进行了表征。结果表明,共沉淀法制备的Ni/CeO₂催化剂具有较小的NiO颗粒与CeO₂载体颗粒粒径,催化活性较高。添加少量氧化钴到Ni/CeO₂催化剂中可使H₂收率达72.6%,EG转化率达93.1%。在CeO₂中添加Al₂O₃能提高负载Ni催化剂的活性,乙二醇转化率达94.0%,H₂收率达67.0%;但添加SiO₂则使其活性明显变差。     

The hydrodechlorination of chlorobenzene in the vapor phase in the presence of metal-carbon nanocomposites based on nickel,palladium, and iron

Metal-carbon nanocomposites based on nickel, palladium, and iron and bimetallic palladium-nickel-carbon nanocomposites were for the first time used as catalysts of hydrodechlorination of chlorobenzene in the vapor phase in the atmosphere of hydrogen. Nickel and Pd-Ni nanoparticles completely coated by a carbon layer not only were stable to oxidation and agglomeration but also exhibited considerable activity in hydrodechlorination of chlorobenzene at temperatures much lower than those at which dechlorination on carbon carriers occurred. The dependence of catalytic properties (activity, selectivity, and stability) on temperature and nanocomposite composition was studied. Depending on the nature of the metal, the composition of bimetallic particles and temperature the selectivity could be changed, and the reaction could be directed toward the formation of benzene or cyclohexane. Carbon coating was stable under reaction conditions at least up to 350°C and did not hinder hydrodechlorination. Substrate adsorption likely occurred on the outside carbon surface of composite particles. The activity and structure of Ni@C composite remained almost unchanged after triple cycling over the temperature range from 50 to 350°C in a flow system.     

还原条件对Ni2P/SiO2催化剂催化氯苯气相加氢脱氯反应性能的影响

采用程序升温还原方法制备了Ni2P/SiO2催化剂,考察了还原条件对催化剂结构及其催化氯苯加氢脱氯反应性能的影响.结果表明,还原条件(氢气流速、还原温度及时间)对Ni2P/SiO2催化剂的比表面积、孔结构及Ni2P晶粒大小没有明显的影响,但催化剂表面的磷含量差异较大.Ni2P/SiO2催化剂在氯苯加氢脱氯反应过程中存在一定的诱导期,而采用提高还原温度和H2空速以及延长还原时间等方法制备的催化剂可以缩短反应诱导期.初步分析认为磷覆盖催化剂活性中心是产生诱导期的主要原因,而还原条件会影响催化剂的表面性质.Ni2P/SiO2催化剂具有良好的加氢脱氯活性及稳定性,在573K,H2流量75ml/min及氯苯流量3ml/h的条件下,该催化剂上氯苯转化率在130h内保持在99%以上.     

镍盐前驱体对Ni/C催化剂乙醇气相羰化活性的影响

采用等体积浸渍法制备了分别以乙酰丙酮镍、氯化镍、硝酸镍和醋酸镍为前驱体负载在活性炭上的四种催化剂。用BET、金属分散度、H2-TPR、CO-TPD和XRD等方法研究了四种催化剂的结构特点和乙醇气相羰化活性。结果表明,以醋酸镍制备的Ni/C催化剂的羰化活性最高,乙醇转化率和丙酸选择性分别为96.1%和95.7%,而以乙酰丙酮镍制备的Ni/C催化剂的羰化活性最低,乙醇转化率和丙酸选择性分别为68.9%和27.1%。这种活性的差异与镍盐前驱体和活性炭之间的相互作用强弱有着密切关系。醋酸镍组分与活性炭之间的相互作用较强,浸渍组分易在活性炭表面充分吸附,活性中心Ni0在240－340 ℃温度范围内对CO吸附量最大,还原后金属镍的分散度较好且晶粒较小。     

嫁接法制备Ni/SBA-15催化剂的催化氯苯加氢脱氯

SBA-15表面经嫁接方式引入氨基官能团,与Ni络合制备了SBA-15负载的Ni催化剂(Ni/SBA-15N)。同时,采用传统的浸渍法制备了具有相似Ni负载量的催化剂(Ni/SBA-15)。在负载量相近条件下,Ni/SBA-15N的Ni颗粒分散性均高于Ni/SBA-15。XRD和TPR结果表明,催化剂焙烧后,在氨化SBA-15表面,Ni以硅酸镍形式存在,而在SBA-15表面,Ni以NiO形式存在。Ni/SBA-15对氯苯催化加氢脱氯活性不随Ni负载量的变化而变化;而在Ni/SBA-15N中,Ni负载量增加,催化剂活性增加。     

Influence of lanthanum on the performance of Zr-Co/activated carbon catalysts in Fischer-Tropsch synthesis

The influence of La loading on Zr-Co/activated carbon （AC） catalysts has been studied for Fischer-Tropsch synthesis. The catalyst samples were characterized by XRD, TPR, CO-TPD, and temperature programmed CO hydrogenation. The catalytic property was evaluated in a fixed bed reactor. The experimental results showed that CO conversion increased from 86.4% to 92.3% and the selectivity to methane decreased from 14.2% to 11.5% and C5＋ selectivity increased from 71.0% to 74.7% when low La loading （La = 0.2wt%） was added into the Zr-Co/AC catalyst. However, high loadings of La （La = 0.3-1.0 wt%） would decrease catalyst activity as well as the C5＋ selectivity and increase methane selectivity. XRD results displayed that La-modified Zr-Co/AC catalyst had little effect on the dispersion of Co catalyst. But, the results of TPR, CO-TPD, and temperature programmed CO hydrogenation techniques indicated that the extent of cobalt reduction was found to greatly influence the activity and selectivity of the catalyst. The addition of a small amount of La increased the reducibility of the Zr-Co/AC catalyst and restrained the formation of methane and improved the selectivity to long chain hydrocarbons. However, excess of La led to the decrease of the reducibility of Co catalyst thus resulted in higher methanation activity.     

Effect of group VIII elements on the behavior of Li/CaO catalyst in the oxidative dehydrogenation of ethane

The effect of addition of group VIII elements to Li/CaO on the oxidative dehydrogenation of ethane has been investigated in the range of 550–650°c. Iron, cobalt and nickel promote the reaction. The experiments show that iron and cobalt additives in Li/CaO catalysts mainly increase the catalytic activity. Li/Ni/CaO catalyst gives a high ethane conversion and excellent ethylene selectivity. The results on the catalyst are probably due to coordinative interaction between lithium and nickel. The characteristics of the catalysts revealed by XRD also give evidence that the promotion for both catalytic activity and ethylene selectivity is directly related to the formation of favorable crystal phases.     

Effect of decomposition of catalyst precursor on Ni/CeO2 activity for CO methanation

CO methanation on Ni/CeO₂ has recently received increasing attention. However, the low-temperature activity and carbon resistance of Ni/CeO₂ still need to be improved. In this study, plasma decomposition of nickel nitrate was performed at ca. 150°C and atmospheric pressure. This was followed by hydrogen reduction at 500 °C in the absence of plasma, and a highly dispersed Ni/CeO₂ catalyst was obtained with improved CO adsorption and enhanced metal-support interaction. The plasma-decomposed catalyst showed significantly improved low-temperature activity with high methane selectivity (up to 100%) and enhanced carbon resistance for CO methanation. For example, at 250°C, the plasma-decomposed catalyst showed a CO conversion of 96.8% with high methane selectivity (almost 100%), whereas the CO conversion was only 14.7% for a thermally decomposed catalyst.     

Vapor-phase synthesis of N-butylaniline from aniline and 1-butanol over Cu/SiO2 catalyst

The Cu/SiO2 catalyst prepared by incipient wetness method exhibited very high activity and selectivity for the vapor-phase synthesis of N-butylaniline from aniline and 1-butanol. When Cu loading was 0.70 mmol/g-SiO2 and the catalyst precursor was calcined at 500 ℃, 1-butanol conversion reached 99%, and the selectivity of N-butylaniline exceeded 97%.     

Mo对Ni/ZnO催化乙醇水蒸气重整制氢性能的影响

考察了Mo及温度对Ni/ZnO催化乙醇水蒸气重整制氢的活性、选择性和抗积炭性能的影响。结果表明,773K适量添加Mo能提高Ni/ZnO催化剂的活性和氢气选择性;Ni/ZnO及Ni-Mo/ZnO催化剂的活性随着温度的升高而提高,823K乙醇完全转化;873K时,Mo质量分数为0.83%的Ni-Mo/ZnO催化剂对氢气的选择性最高;添加Mo可以提高Ni/ZnO催化剂的抗积炭能力,从而提高该催化剂的稳定性。程序升温还原（TPR）和X射线衍射（XRD）结果表明,添加Mo有利于Ni氧化物在载体上的分散;减弱氧化态镍物种与载体之间的作用,从而提高了催化剂的活性、选择性和稳定性。