负载型Ni-Co-P/CNFs催化剂的制备及释氢性能

以纳米碳纤维(CNFs)为基体材料,采用化学镀法在CNFs表面沉积了Ni-Co-P催化剂。研究了催化剂用量,硼氢化钠、氢氧化钠浓度,温度等对碱性硼氢化钠溶液水解释氢的影响。电感耦合等离子体原子发射光谱法(ICP-AES)测试得出负载型Ni-Co-P催化剂含镍13.30%(质量分数,下同)、钴82.25%、磷4.45%。硼氢化钠水解释氢实验结果表明,产氢速率与催化剂用量呈线性关系。当温度为45 ℃、催化剂浓度为7.5 g/L、氢氧化钠浓度为5%、硼氢化钠浓度为2.5%时,氢气释放速率达到最大值18.044 L/(g·min)。通过对负载型催化剂Ni-Co-P/CNFs催化碱性硼氢化钠溶液释放氢气动力学研究表明,该催化剂的活化能E_a为51.57 kJ/mol。     

Effect of support on activity of palladium catalysts in nitrobenzene hydrogenation

The effect of two types of catalysts on the activity of the catalytic hydrogenation of nitrobenzene was studied. Catalysts were prepared by the surface deposition of palladium hydroxide with a simultaneous reduction with formaldehyde in a basic environment and were characterised by X-ray powder diffraction, transmission electron microscopy, adsorption-desorption, and catalytic tests — hydrogenation of nitrobenzene in methanol. The influence of the supports’ (activated carbon and a mixture of activated carbon and multi-walled carbon nanotubes) surface area is discussed. Despite having a size comparable (4–5 nm) to crystallites of metallic palladium, the catalyst prepared on a mixture of activated carbon and nanotubes (Pd/C/CNT) was significantly less active than the catalyst prepared on pure activated carbon (Pd/C); the rate of this reaction was approximately 30 % lower than the initial reaction rate. This feature could be attributed to the lower specific surface area of the Pd/C/CNT (531 m² g^?1) in comparison with the Pd/C (692 m² g^?1).     

高灰煤小型流化床混合气催化气化研究

在内径28mm流化床中,对阳泉高灰煤在碱性催化剂（固碱和黏胶废碱液）作用下进行了混合气（空气/水蒸气）催化气化研究,两种碱性催化剂的适宜添加量均为6％。不加催化剂,气化温度830℃~900℃与900℃～920℃下,气化反应的表观反应级数n分别约为2/3与1/3;有催化剂（3％固碱）时,表观反应级数有两个明显的温度段,在830℃~860℃,催化气化的表观反应级数n=1;在860℃~920℃,催化气化的表观反应级数为n=1/3。     

碱金属沉积对Mn-Ce/TiO_2低温SCR催化剂性能影响

采用溶胶凝胶法制备了Mn-Ce/TiO_2低温SCR催化剂,考察了碱金属浓度与种类对催化剂活性的影响,探究了不同反应条件下钠盐沉积对活性保留分率的影响,利用SEM、BET、XRD和FT-IR对催化剂碱金属中毒原因进行了分析。结果表明,碱金属毒化后催化剂脱硝活性下降,钾中毒催化剂失活程度高于钠中毒的催化剂,2%钾中毒催化剂在160℃时NO去除率为62.0%,较新鲜催化剂下降29.2%。这主要因为碱金属毒化造成催化剂比表面积明显减小,且催化剂载体锐钛矿型TiO_2部分转化为金红石型,BET和SEM表征均说明碱金属沉积堵塞了催化剂表面的微孔。碱金属对Mn-Ce/TiO_2催化剂活性保留分率的影响表明,催化剂的颗粒粒径对其活性保留分率影响不大,碱金属含量减小、温度升高,Mn-Ce/TiO_2催化剂的活性保留分率增加,Na_2SO_4和NaCl对Mn-Ce/TiO_2催化剂的脱硝活性抑制作用大于KNO_3。     

Understanding phase-transfer catalytic synthesis of fullerenol and its interference from carbon dioxide and ozone

Research on Chemical Intermediates - Phase-transfer catalytic reaction involving the use of tetrabutylammonium hydroxide (TBAH) as catalyst and sodium hydroxide (NaOH) solution as the source of...     

The hydrodechlorination of chloroaromatic and unsaturated chloroaliphatic compounds using a nickel boride reagent

A nickel boride reagent, prepared in situ by the reaction of nickel chloride with sodium borohydride, has been used to hydrodechlorinate and hydrogenate chloroaromatic compounds. The same reagent can also dechlorinate chloro-olefinic compounds but chloroalkanes do not react. The reactions can be sustained by addition of hydrogen gas and the ratio of the aromatic to aliphatic hydrocarbons produced can be varied by addition of sodium hydroxide to the reaction mixture and by the duration of the reaction. The reactivity of polychlorinated biphenyls (PCBs), polychlorinated naphthalenes (PCNs), chlorobenzene and tetrachloroethylene have been studied. Capillary gas chromatography was used to follow the course of reactions and gas chromatography-mass spectroscopy (GC–MS) was used for product identification.     

The activity of NaOH buffered by silicate solids in molten sodium acetate-water at 317°C

Silica and sodium acetate are present in the steam generator tube sheet crevices of many nuclear power plants. Trace solutes in the condensate are tremendously concentrated in the crevices by boiling. Sparingly soluble sodium silicates and other solids precipitate from the crevice liquid leaving an extremely concentrated molten mixture of water, sodium acetate and other salts. The precipitates buffer the activity of sodium hydroxide in the superheated liquid that remains. The activity of NaOH corresponding to the buffers quartz/sodium disilicate and sodium disilicate/sodium metasilicate at 317°C has been determined experimentally. The sodium hydroxide content of a sodium acetate-water melt buffered by these reactions was determined bychemical analysis, and the corresponding activity of NaOH at temperature was calculated using the recently published Pitzer-Simonson Model of molten salt-water mixtures. The molten mixture of sodium acetate and water plays the role of solvent in these experiments and calculations. The free energies of formation of solid sodium silicates at 317°C were also determined. The activity of NaOH corresponding to other silicate and phosphate buffers was calculated using published thermodynamic data and estimated from phase diagrams.     

2-甲硫基-4-羟基-5-嘧啶甲酸乙酯的工艺优化

以S-甲基异硫脲半硫酸盐和乙氧基亚甲基丙二酸二乙酯为主要原料,乙醇为溶剂,合成出2-甲硫基-4-羟基-5-嘧啶甲酸乙酯,研究了2-甲硫基-4-羟基-5-嘧啶甲酸乙酯的工艺优化,考察了投料比、反应温度、反应时间等因素对产率的影响。 获得较好的反应条件:n(C₂H₆N₂S·1/2H₂SO₄):n(C₁₀H₁₆O₅):n(NaOH)=1.2:1:1.8,在室温下缓慢滴加NaOH溶液,搅拌反应6 h,酸化得白色固体产物,产率为81.1%。产物结构经熔点测定仪、¹H NMR、ESI-MS、FT-IR等技术手段得到验证。     

Kinetics of catalytic hydrogenation of 4-nitroaniline in aqueous solutions of propan-2-ol with acid or base additives

The effect of addition of acetic acid and sodium hydroxide to an aqueous azeotropic solution of propan-2-ol on the rate of 4-nitroaniline hydrogenation is studied. The base additive accelerates the apparent rate of nitro group reduction, while the presence of acetic acid slows the reaction rate. It is experimentally established that the rate of nitro group conversion calculated from the amount of reacted 4-nitroaniline exceeds the rate of hydrogen uptake from the gas phase in all of the studied solvents. Hydrogen bound by active sites of the catalyst surface is found to participate notably in the reactions. It is proved both experimentally and theoretically that strongly bound atomic forms of adsorbed hydrogen are most active in the reduction of the nitro group.     

Stereochemistry and mechanism of catalytic hydrogenation of substituted cyclohexanones

Substituted alkylcyclohexanones were hydrogenated over several transition metal catalysts. The hydrogenation with freshly prepared Raney Ni gave predominantly the axial alcohols but catalyst to which sodium hydroxide was added or aged catalyst increased the stereoselectivity. In contrast to the PtO₂ hydrogenation in which the equatorial alcohols were favoured, more axial alcohols were obtained than the equatorial counterparts on Pt-black. On Pd catalyst the isomeric ratios of the cyclohexanols changed as the reaction progressed. This may be due to a decrease in the amount of hydrogen available caused by the strong adsorption of ketones on the catalyst. Rh catalyst gave more of the axial alcohols than any other catalyst used in the present study.     

The leaching and re-deposition of metal species from and onto conventional supported palladium catalysts in the Heck reaction of iodobenzene and methyl acrylate in N-methylpyrrolidone

When supported palladium catalysts are used for Heck vinylation of iodobenzene with methyl acrylate in N-methylpyrrolidone (NMP) in the presence of triethylamine and sodium carbonate bases, the reaction proceeds homogeneously with dissolved active palladium species that are formed through coordination of NMP and triethylamine with palladium. These active species easily react with iodobenzene (oxidative addition), beginning the catalytic cycle of Heck coupling. The last step of catalyst regeneration takes place with the action of sodium carbonate. The active palladium species are not stable and deposit the metal to support when they cannot find iodobenzene to react in the reaction mixture after this substrate is completely consumed. The re-deposition of palladium occurs on the surfaces of bare support and/or palladium particles remaining on it, depending on the nature of support surface and the number and size of residual metal particles. The growth of palladium particles has been observed after the reuse of catalyst in some case. However, the supported catalysts are recyclable without loss of activity.     

Synthesis and catalytic application of Pd/PdO/Fe3O4@polymer-like graphene quantum dots

A novel approach was achieved for growing citric acid towards polymer-like graphene quantum dots (PGQD) with high efficiency in the presence of sodium hydroxide as a base catalyst. This protocol is completely safe, simple, fast, and efficient by a bottom up strategy. Thermal treatment of a mixture containing citric acid with NaOH at 300 °C gave PGQD during 5 min. The reaction afforded a new heterogeneous catalyst, Pd/PdO/Fe₃O₄@PGQD, in the presence of Pd and Fe₃O₄. The magnetically recoverable catalyst showed high activity in the oxidation of alkylarenes and alcohols using H₂O₂ as a green oxidant at room temperature. Comparison of the results with previous reports showed the efficiency of the catalyst to have high turnover numbers in mild reaction conditions.     

FePO<Subscript>4</Subscript>/SiO<Subscript>2</Subscript> Catalysts for Propylene Glycol Oxidation

FePО₄/SiO₂ supported catalysts with a different content of iron phosphate are prepared. The properties of the catalyst are changed by the introduction of alkali metal compounds (Na or Cs) on its surface. The samples obtained are characterized by X-ray diffraction, low-temperature nitrogen adsorption, temperatureprogrammed reduction by hydrogen, and temperature-programmed desorption of ammonia. The catalytic properties are investigated in the reaction of gas-phase propylene glycol oxidation. It is shown that the selectivity of methylglyoxal formation on the unmodified catalysts is determined by the state of the supported active component and by its reduction–oxidation ability under the action of a reaction mixture.     

Selective synthesis of isobutanol by means of the Guerbet reaction: Part 2. Reaction of methanol/ethanol and methanol/ethanol/n-propanol mixtures over copper based/MeONa catalytic systems

The synthesis of isobutanol via the Guerbet condensation between methanol and ethanol was studied by using sodium methoxide (MeONa) as soluble basic component and copper-based catalysts as heterogeneous dehydrogenating/hydrogenating metal species. The effect of the nature of the catalyst and the relative amount of its individual components with respect to the reacting alcohols as well as of temperature on productivity and selectivity of the process was investigated. The collected data indicated that the copper chromite/MeONa was more active than Cu-Raney/MeONa system. The reaction was shown to proceed with the formation only of n-propanol and isobutanol. Ethanol conversion up to 61% with selectivity to isobutanol up to 98.4% was obtained. The same catalytic systems were also employed in the reaction of the methanol/ethanol/n-propanol ternary mixture. Again copper chromite/MeONa resulted more active than the Cu-Raney/MeONa system. Finally, experiments were carried out on methanol/n-propanol mixtures in the presence of the copper chromite/MeONa catalytic system by recycling both the recovered solid copper component and the liquid reaction mixture for evidencing eventual copper leaching by MeONa. On the basis of the obtained results it was concluded that in the Guerbet reaction copper chromite works as heterogeneous catalyst.     

The effect of iron nanocrystallites’ size in catalysts for ammonia synthesis on nitriding reaction and catalytic ammonia decomposition

Iron catalyst for ammonia synthesis of various mean sizes of iron nanocrystallites were nitrided with ammonia in a differential reactor equipped with systems that made it possible to conduct both thermogravimetric measurements and hydrogen concentration analyses in the reacting gas mixture. The nitriding process was investigated under atmospheric pressure at the temperature of 475°C. It was found that along with an increase of mean size of iron nanocrystallites, with a decrease of specific surface area of the samples, nitriding degree of solid samples increased. At the same time the rate of surface reaction of catalytic ammonia decomposition decreased. Along with an increase of the samples’ specific surface area an increase of the catalyst’s activity was observed. However, it was also observed that the concentration of active sites on the catalysts’ surface decreased along with an increase of specific surface area.     

NaOH浓度对Cu_2O结构及甲醛乙炔化性能的影响

以CuCl_2·2H_2O为铜源,NaOH为沉淀剂,L-抗坏血酸钠为还原剂,采用液相还原法制备了Cu_2O,并将其应用于甲醛乙炔化反应制1,4-丁炔二醇.借助傅里叶变换红外光谱(FT-IR)、拉曼光谱(Raman)、X射线粉末衍射(XRD)、X射线光电子能谱(XPS)、扫描电子显微镜(SEM)和H_2程序升温还原(H2-TPR)等手段研究了NaOH浓度对Cu_2O结构、性质及催化性能的影响.结果表明,调变NaOH浓度改变了Cu2O的结晶度与粒径,从而使Cu_2O表现出不同的炔化性能.低NaOH浓度时,Cu_2O结晶度低,粒径小,易被还原为非活性的金属Cu;高浓度时,Cu_2O结晶度过高,粒径大,难以转化为活性物种炔化亚铜,两者均造成催化剂活性较低.而中等浓度的NaOH使Cu_2O具有了适宜的结晶度与粒径大小,Cu_2O可高效转化为炔化亚铜活性物种,表现出最优的炔化性能.     

复合氧化物催化剂(Cu)CeO2上硝基苯加氢反应的研究

 基于用FT－IR表征H2与硝基苯在催化剂（Cu）CeO2上的吸附和反\r\n应行为，对硝基苯加氢反应进行了研究．结果表明，氢在催化剂表面的\r\n吸附主要为解离吸附，硝基苯的吸附也主要为化学吸附；两种吸附物种\r\n在催化剂上进行表面反应生成易脱附的苯胺，避免了产物与反应物间的\r\n竞争吸附，有利于反应物完全转化．在（Cu）CeO2催化剂上，硝基苯加\r\n氢反应机理为朗格缪尔－欣谢伍德型，即表面反应为控制步骤．     

等级孔微孔-介孔Fe2O3/ZSM-5中空分子筛催化材料的制备及催化苄基化性能

ZSM-5分子筛具有极其均匀的孔道结构、 良好的形状选择性和催化活性及耐水热稳定性, 是一种高效、 绿色的固体催化剂, 被广泛应用于石油催化裂化、 精细化工和环境保护等领域. 但其单一的微孔结构大大降低了客体分子的流通扩散性, 导致由大分子参与的芳烃烷基化反应受到极大限制. 本文采用NaOH/四丙基氢氧化铵(TPAOH)混合碱处理微孔ZSM-5, 制备了具备高结晶度、 高比表面积的等级孔微孔-介孔ZSM-5中空分子筛材料, 该材料在保持微孔孔道良好水热稳定性和大量活性中心的同时, 还通过介孔的引入进一步促进反应物及产物的扩散, 使间三甲苯苄基化反应的转化率提高了3.8倍. 通过在等级孔微孔-介孔ZSM-5中空材料上负载Fe, 开发出了具有双功能的等级孔微孔-介孔Fe₂O₃/ZSM-5中空催化剂, 该催化剂在苯的苄基化反应中表现出优异的催化性能, 当Fe负载量(质量分数)为6.67%, 反应温度为75 ℃, 反应时间为15 min时, 转化率高达98.3%, 选择性为81.6%, 最终收率达到80.2%.     

高分散Fe-N-C氧还原反应电催化剂及其在直接甲醇燃料电池中的应用

氧还原反应(ORR)是燃料电池和金属空气电池等洁净发电装置中阴极的主要反应,该反应动力学过程慢,电化学极化严重. Pt基电催化剂具有较好的ORR活性,然而Pt资源有限、价格昂贵,研制高活性、低成本的代Pt电催化剂意义重大.经过几十年的探索,研究者发现将含有C, N和Fe等元素的前体进行高温热处理得到的Fe-N-C电催化剂对ORR具有良好的活性,然而在高温热解过程中Fe容易发生聚集而形成大块颗粒,导致Fe的利用率不高,影响了电催化剂的ORR活性.
　　本文分别以聚吡咯和乙二胺四乙酸二钠(EDTA-2Na)为C和N的前驱体,利用高温热解形成的富含微孔的碳材料对铁前体的吸附及锚定作用,获得了一种Fe高度分散的Fe-N-C电催化剂.采用物理吸脱附技术、高分辨透射电镜(HRTEM)和扫描电镜对Fe-N-C及其制备过程中相关电催化剂的孔结构及表面形貌进行了表征.结果表明,在第一步热解过程中, EDTA-2Na的Na对碳材料起到了活化作用,形成富含微孔的N掺杂碳材料(N-C-1),其BET比表面积达到1227 m2/g,孔径约1.1 nm.在第二步热解过程中, N-C-1有效地抑制了Fe的聚集,产物Fe-N-C中的Fe元素均匀地分布在碳材料中,其比表面积高达1501 m2/g.
　　电化学测试结果表明,在碱性介质(0.1 mol/L NaOH)中, Fe-N-C电催化剂对ORR具有良好的催化活性, ORR起始电位(Eo)为1.08 V (vs. RHE),半波电位(E1/2)0.88 V,电子转移数n接近4, H2O2产率<3%,与商品20%Pt/C(Johnson Matthey)接近.电化学加速老化测试结果表明, Fe-N-C的E1/2未发生明显变化,而Pt的负移45 mV,表明Fe-N-C具有很好的稳定性;在酸性介质(0.1 mol/L HClO4)中, Fe-N-C的Eo为0.85 V, E1/2为0.75 V,其E1/2比Pt/C负移约0.15 V,表明在酸性介质中Fe-N-C对ORR的催化活性还有待提高.采用TEM、X射线衍射、X射线光电子能谱以及穆斯堡尔谱等方法研究了电催化剂构效关系.结果表明, Fe-N-C较好的ORR活性主要来自于高分散的Fe-N4结构,此外, N(吡啶N和石墨N)掺杂的C也对反应具有一定的催化活性.
　　与Pt/C相比, Fe-N-C电催化剂具有很好的耐甲醇性能.本文对比了Fe-N-C和Pt/C作为阴极催化剂的直接醇类燃料电池(DMFC)性能,采用质子交换膜的DMFC最大功率密度分别为47(Fe-N-C)和79 mW/cm2(Pt/C),而采用碱性电解质膜的则分别为33(Fe-N-C)和8 mW/cm2(Pt/C).结合半电池结果表明, Fe-N-C电催化剂在碱性介质中具有比Pt更为优秀的催化活性和稳定性,有望用作DMFC阴极代Pt催化剂.     

Y_2O_3负载金属Cu在催化甲醛水溶液制氢反应中的Y_2O_3载体效应

采用NaBH_4还原法将纳米金属Cu负载在Y_2O_3上.通过X射线衍射(XRD)、X射线光电子能谱(XPS)、透射电子显微镜(TEM)和测定氢氧根在Y_2O_3和Cu上的吸附等手段对样品进行了表征.结果表明,Y_2O_3表面存在一层薄的Y(OH)3,能优先吸附OH-使其在Y_2O_3表面"富集";金属Cu以纳米粒子形式负载在Y_2O_3上.在碱性甲醛溶液中考察了Y_2O_3负载Cu(Cu/Y_2O_3)的催化性能.结果表明,在低碱度条件下,相对于未负载纳米Cu的Y_2O_3,Cu/Y_2O_3具有较高的产氢活性.当氢氧化钠浓度为0.050 mol/L时,在氮气气氛下Cu/Y_2O_3产氢量约为未负载纳米Cu的7.8倍;而在空气气氛下约为4.3倍.在2种气氛下,Cu/Y_2O_3产氢的最佳氢氧化钠浓度均为0.25 mol/L.这可归结为Y_2O_3表面对OH-的"富集"效应,使其表面产生更多的活性物种CH2(OH)O-(甲二醇负离子).相对于未负载纳米Cu的Y_2O_3,Y_2O_3负载Cu提高了催化剂的稳定性,其原因是Y_2O_3负载阻止了Cu粒子在反应过程的生长.