bio(oh)-nabh4还原法制备氧化偶氮苯类化合物

以NaOH溶液快速沉淀BiCI3溶液制备了BiO(OH),研究了BiO(OH)对NaBH4还原芳香族硝基化合物的催化性能,考察了NaBH4用量对反应的影响.结果表明,在温和条件下BiO(OH)具有很高的催化活性和选择性.NaBH4和芳香族硝基化合物的摩尔比为1.04:1,在甲醇中室温反应2 h,芳香族硝基化合物主要被还原为氧化偶氮苯类化合物,收率80.4%～96.9%.该催化剂重复使用5次后活性没有明显下降.于120℃再生后,其活性与新制备催化剂相当.     

Co(acac)2催化过氧叔丁醇烯丙位与苄位氧化

以烯烃为原料,Co(acac)2为催化剂,过氧叔丁醇(t-BuO2H)为氧化剂,分别进行烯丙位与卞位氧化合成了相应的α,β-不饱和酮,其结构经1H NMR,13C NMR和Ms表征.较适宜的反应条件为:烯烃5 mmol,Co(acac)2 0.375 mmol,r-Bu0OH 25 mmol,在10 mL乙腈中,于60℃反应2 h～3 h,收率35%～96%.     

反应控制相转移催化合成环氧大豆油

以磷钨杂多酸盐作为反应控制相转移催化剂,1,2-二氯乙烷为溶剂,30%H2O2为氧源,研究了中性条件下大豆油的环氧化反应,并考察了各反应条件对环氧化反应的影响。结果表明,在催化剂质量分数为3%,n(H2O2)∶n(双键)=1.2∶1,m(溶剂)/m(大豆油)=3.2,反应温度70℃,反应时间4h时,生成环氧大豆油中的碘值小于0.04g(I)/g,环氧值大于6%,催化剂循环使用5次后不降低催化活性。整个反应过程中,催化剂显示出良好的反应控制相转移催化性能。     

N,P掺杂型C@Mo_2C催化剂的制备及其催化CO_2加氢反应研究

以三聚氰胺苯甲酸盐为碳源和氮源、以三聚氰胺磷钼酸盐为钼源、磷源和氮源,采用程序升温的方法制备了系列N,P掺杂型C@Mo_2C催化剂。采用XRD、SEM、TEM和XPS等对催化剂的结构、形貌和表面特性进行了表征,研究了三聚氰胺苯甲酸盐中n(三聚氰胺)/n(苯甲酸)、前驱体中n(C)/n(Mo)等因素对所制备催化剂的结构及其在二氧化碳加氢反应中催化性能的影响。在反应温度为220℃、反应压力为3.0 MPa、空速为3 600 m L/(g·h)的条件下,在N,P掺杂型C@Mo_2C的催化作用下,CO_2转化率可以达到12.2%,此时产物中CH_3OH的选择性达到52.2%。     

载体对Pt/WO_3-ZrO_2催化临氢异构反应性能的影响

以平衡吸附过氧钨酸的水合氧化锆为前驱体,经焙烧得到WO_3-ZrO_2固体酸,并采用XRD、UV-vis、NH_3-TPD等手段考察了过氧钨酸吸附液浓度及焙烧温度对WO_3-ZrO_2固体酸组成、结构及酸性的影响。通过BET、H_2-TPR、H_2-TPD等表征手段和正戊烷临氢异构反应,考察了负载铂后相应催化剂的结构、还原与氢吸附性质及其催化正戊烷临氢异构反应的性能。结果表明,焙烧温度为700℃时,随着吸附液浓度的增加,所得载体酸度及相应催化剂比表面积均先增加后减小,且在吸附液浓度为82 mmol W/L时达到最大值。吸附液浓度为59 mmol W/L时,随着焙烧温度的升高,所得载体四方相氧化锆含量、酸度及相应催化剂比表面积均降低。吸附液浓度为82 mmol W/L、焙烧温度为700℃所得载体负载0.5%(质量分数)铂后催化活性最高。该催化剂在250℃常压临氢操作、n(H_2)/n(n-C_5H_(12))为3、WHSV为1.0 h~(-1)的条件下,催化正戊烷异构反应中异戊烷收率可达57.7%。     

NiO/LaMnO3催化剂用于乙醇水蒸气重整反应

采用柠檬酸络合-浸渍法制备了NiO/LaMnO3钙钛矿型复合氧化物催化剂并将其应用于乙醇水蒸汽重整制氢反应, 考察了NiO含量、焙烧温度对催化剂性能的影响, 采用XRD、TPR和热分析等手段对催化剂进行了表征. 结果表明, 该催化剂具有高活性、高选择性和良好的稳定性. 催化剂中的NiO含量和焙烧温度对催化性能有显著影响. 在原料气体积组成为20%(体积分数, φ) C2H5OH 和水以及80%(φ)N2, 其中水醇摩尔比为3:1, 空速为80000 mL·h-1·g-1 cat, 反应温度为400 ℃时, 15%(质量分数, w)的NiO/LaMnO3上, 乙醇转化率接近100%. 关联催化剂活性和TPR及XRD实验结果, 发现催化剂的高活性源于由催化剂前驱体中进入钙钛矿型复合氧化物晶格中的镍离子被还原所得的金属镍.     

Ni/C催化剂上山梨醇氢解反应中碱对乳酸形成的影响（英文）

山梨醇是重要的生物基平台化合物,其选择加氢裂解制备乙二醇和1,2-丙二醇等低碳二元醇,是一个具有重要科学意义和应用前景的催化过程.山梨醇氢解反应涉及C-C键和C-O键等化学键的裂解,裂解选择性尤为关键.通常情况下,添加NaOH,KOH,Ca(OH)_2,CaO和Ba(OH)_2等碱性物质可增加糖醇转化率和二元醇选择性,但也会生成大量乳酸等副产物.研究乳酸的生成途径,探索抑制乳酸生成的方法,对于提高山梨醇加氢裂解制备低碳二元醇的选择性具有重要意义.本文以Ni/C催化剂上山梨醇加氢裂解反应为模型反应,研究了碱性化合物添加剂类型及其用量对乳酸生成的影响.根据加氢裂解机理分析可知,糖醇氢解主要涉及以下关键步骤:在碱的存在下,多元醇在金属催化剂上发生脱氢反应生成相应的羰基中间体;然后,羰基中间体在碱性介质中通过逆羟醛缩合反应,发生C-C键断裂.因此,在糖醇氢解反应和C-C键断裂中,添加碱性化合物将会不可避免地生成乳酸.结果表明,以NaOH和Ca(OH)_2为添加剂时,山梨醇加氢裂解生成乳酸的选择性分别为15.1%和8.9%.而以La(OH)_3为添加剂时,生成乳酸的选择性仅为0.1%.以Ca(OH)_2和La(OH)_3为添加剂时反应具有高活性,山梨醇转化率均可达到99%以上.分别以Ca(OH)_2和La(OH)_3为添加剂,研究了碱性添加剂用量对山梨醇氢解反应的影响.结果表明,以Ca(OH)_2为添加剂时,山梨醇转化率和乳酸选择性均随着Ca(OH)_2用量增加而增加;当OH~-投料量为11.06 mmol时,乳酸选择性可达11.7%.而以La(OH)_3为添加剂时,即使La(OH)_3用量仅为0.08 mmol时,山梨醇转化率也可高达99%;继续增加La(OH)_3用量,对乳酸的选择性影响不大;当OH~-投料量为11.06 mmol时,乳酸选择性也只有0.3%.对山梨醇加氢裂解反应分析可知,与Ca(OH)_2相比,La(OH)_3添加剂可使C2和C4产物的总选择性从20.0%增加到24.5%.上述结果表明La(OH)_3可高效促进山梨醇加氢转化.为了探索Ca(OH)_2或La(OH)_3为添加剂时山梨醇加氢裂解产物分布不同的本质原因,以Ni/C催化剂催化的丙酮醛加氢转化为探针反应,探讨了乳酸形成的可能路径.结果表明,丙酮醛可能是山梨醇氢解反应的关键中间体之一.在仅以Ni/C催化加氢时,丙酮醛容易被转化为1,2-丙二醇;当只存在碱性添加剂时,丙酮醛可发生重排并被转化为乳酸主产物,这可能是乳酸生成的主要原因.进一步研究表明,以Ca(OH)_2为添加剂时,乳酸选择性是以La(OH)_3为添加剂时的1.9倍.在Ni/C催化剂和碱性添加剂共存时,由于碱性添加剂的区别,则会得到不同选择性的1,2-丙二醇和乳酸.结果表明,通过丙酮醛催化加氢可得到1,2-丙二醇,也可以通过重排反应生成乳酸;这两类反应是竞争性的.在山梨醇氢解反应中,以Ca(OH)_2为添加剂时,加氢反应和重排反应均可发生,而以La(OH)_3为添加剂时,丙酮醛加氢反应占主导,仅生成微量乳酸.该研究对提高山梨醇催化加氢裂解选择性具有参考意义.     

包覆Y(OH)3的球形Ni(OH)2的电化学性能

利用软嵌式粉末电极技术研究了Y(OH)3包覆对球形Ni(OH)2电化学性能的影响. 循环伏安结果表明, 在球形Ni(OH)2的氧化过程中存在Ni(Ⅲ)和Ni(Ⅳ)的两步氧化反应, 产生的Ni(Ⅳ)不稳定, 能分解产生NiOOH和氧气, 所以可将Ni(Ⅲ)→Ni(Ⅳ)看作副反应. Y(OH)3包覆层对Ni(OH)2氧化过程后期的副反应, 特别是Ni(Ⅲ)→Ni(Ⅳ)具有较好的抑制作用. 由包覆后的Ni(OH)2制成的模拟电池表现出很好的高温性能, 在1C充放电条件下, 当Y的摩尔分数为1.61%时, 在60 ℃时所对应的容量保持率可达到25 ℃的92.7％; 当Y的摩尔分数仅为0.55 %时, 在60 ℃时所对应的质量比容量也可达到241.3 mA·h/g.     

硒催化3,4-二氯苯胺和甲醇氧化羰基化合成灭草灵

报道了一种绿色、简易的合成灭草灵的方法,首次以廉价易得且能循环使用的非金属硒作催化剂,以CO替代剧毒光气作羰基化试剂,通过3,4-二氯苯胺和甲醇经"一锅法"的硒催化氧化羰基化反应来直接合成灭草灵。考察了压力、3,4-二氯苯胺和甲醇用量比、催化剂硒粉用量、溶剂种类、时间、温度及助催化剂种类对反应的影响规律,获得了实施该反应的较优条件。即,在100 mL高压反应釜中:压力3 MPa(n(CO)∶n(O2)=9∶1),3,4-二氯苯胺5 mmol,CH3OH 75 mmol,Se 0.25 mmol,乙酸乙酯10 mL,时间5 h,温度130℃,三乙胺10 mmol。在此条件下,目标产物灭草灵的收率为67%。该方法具有步骤简短、方法绿色和操作方便等优点。     

负载型金基催化剂Au/Fe(OH)3催化苯乙烯环氧化反应

用共沉淀法制备了Au/Fe(OH)3催化剂, 以叔丁基过氧化氢为氧化剂, 考察焙烧温度和金担载量等对苯乙烯环氧化反应的影响. 结果表明, 催化剂的焙烧温度、金担载量对苯乙烯环氧化反应有较大影响. 在室温下直接合成的质量分数为4.67%的Au/Fe(OH)3催化剂对苯乙烯环氧化反应显示了很好的催化活性, 于80 ℃反应3 h苯乙烯的转化率达到84.1%, 环氧苯乙烷的选择性达到71.5%. 通过X射线粉末衍射(XRD)、X射线光电子能谱(XPS)和Mössbauer分析, 发现催化剂的催化活性与金的价态及铁的化学存在状态有很大关系. 离子态Au3+与载体Fe(OH)3的协同作用对苯乙烯环氧化反应显示出很好的催化活性.     

柠檬酸络合法制备的Co/CeO2催化剂上中温乙醇水蒸气重整性能（英文）

采用柠檬酸络合法制备了Co/CeO2及其钙掺杂系列催化剂,并对催化剂进行了低温N2物理吸附、X射线衍射、H2程序升温还原、傅里叶变换红外光谱、高分辨透射电镜表征以及乙醇水蒸气重整催化性能测试.结果表明,所制Co/CeO2催化剂具有良好的乙醇水蒸气重整催化性能,500oC时乙醇能全部转化为C1,氢气产率高达85%以上.Ca掺杂减小了载体CeO2纳米颗粒尺寸,但对还原后Co0尺寸的影响较小.当Ca掺杂量大于5.0%时,催化剂氧化还原性能和乙醇水蒸气重整催化性能下降.较高的还原温度有利于体相Ce4+还原为Ce3+,并且提高了催化活性,认为金属-氧化物边界的增加提高了催化活性.初步稳定性考察结果表明,5%钙掺杂后的催化剂具有更好的抗积炭性能.     

Preparation and characterization of ultrafine Fe-Cu-based catalysts for CO hydrogenation

The ultrafine particles of a new style Fe-Cu-based catalysts for CO hydrogenation were prepared by impregnating the organic sol of Fe（OH）3 and Cu（OH）2 onto the activated Al2O3, in which the organic sol of Fe（OH）3 and Cu（OH）2 were prepared in the microemulsion of dodecylbenzenesulfonic acid sodium（S）/n-butanol（A）/toluene（O）/water with V（A）/V（O） = 0.25 and W（A）/W（S） = 1.50. This catalyst was characterized by particle size analysis, XRD and TG. The results of particle size analysis showed that Fe（OH）3 particles with a mean size of 17.1 nm and Cu（OH）2 particles with an average size of 6.65 um were obtained. TG analysis and XRD patterns suggested that 673 K is the optimal calcination temperature. CO hydrogenation produced C＋OH with a high selectivity above 58 wt% by using the ultrafine particles as catalyst, and the total alcohol yield of 0.250 g·ml^-1 ·h^-1 was obtained when the contents of Al2O3 and K were 88.61 wt% and 1.60 wt%, respectively.     

OMS-2/堇青石整体式催化剂的制备及其对二甲醚燃烧的催化性能

 以有机物为粘合剂, 采用涂覆法制备了氧化锰八面体分子筛 (OMS-2)/堇青石整体式催化剂, 采用热重-差热分析、扫描电镜、X 射线衍射、H2 程序升温还原和 O2 程序升温脱附等技术对催化剂进行了表征, 考察了有机粘合剂种类及其用量对二甲醚 (DME) 催化燃烧性能的影响. 结果表明, 在有机粘合剂聚乙烯醇 1799 (其质量含量为 3%) 的作用下, OMS-2 以相互交织的簇体均匀分布于堇青石表面, 且粘附力较强, 制备的整体式催化剂在 DME 催化燃烧中表现出最优的催化性能, 起燃温度 T10 = 169 oC, 完全转化温度 T90 = 243 oC; 催化剂使用后再经高温焙烧其活性仍能保持稳定, 表现出较高的重复使用性.     

手性修饰的介孔碳材料MPC-61负载铂催化剂上α-酮酸酯的不对称氢化反应

采用氯铂酸乙醇溶液和氯铂酸水溶液为前体,通过浸渍法制备了介孔碳材料MPC-61负载Pt质量分数分别为4%和10%的Pt/MPC-61催化剂,并利用XRD,TEM,N2吸附-脱附和CO化学吸附等手段对催化剂进行了表征.考察了经过手性分子辛可尼定修饰后的Pt/MPC-61催化剂在丙酮酸乙酯不对称氢化反应中的催化性能.以氯铂...     

碱性条件下Pt-M(Ni,Fe,Mo)/C电催化氧化甲醇的性能对比研究

采用溶胶法制备了碳载Pt-M(M为Ni, Fe, Mo)电催化剂, 并用TEM和XRD技术表征活性物微观结构, 实验结果表明, Pt基合金微粒在碳黑表面分布均匀, 粒径约为2~4 nm. 用循环伏安法测定催化剂在不同碱性条件下的活性, 研究结果表明, 不同掺杂元素催化剂的活性大小顺序为Pt75Ni25/C>Pt75Fe25/C>Pt50Mo50/C, 掺杂Ni可明显地促进纳米Pt的催化活性, Pt75Ni25/C在1.0 mol/L NaOH+1.0 mol/L CH3OH溶液中的峰电流密度可以达到726.9 mA/mg.     

UNSUPPORTED PRECIPITATED Fe-Cu-K CATALYSTS USED FOR THE SLURRY FISCHER-TROPSCH SYNTHESIS

lntroducti0nInordertodeveloptheslurn'Fischcr-Tropsch(SFT)technolog}',thccatalystsusedforslunyFischer-TroPschs}vithesisshouldnotonl}'havehighactivity',goodselectivityandlonglife,butalsosatisfy'therequiremcntofliquidphascprocess,suchasthelowviscosityofslunyandacehainamountoft`axformaintainingstead}'operationanddecreasingmasstransferresisboce.Recently,althoughthcrchasbeenrenct"edinterestintheuseofCoasacommercialFTcatalyst,objcctivcofdcvclopingcobaIt-bascdFTcatalystisformethane-dcrivcds\'ngas…     

E?ect of Thermal Treatment on Structure and Catalytic Activity of Supported Fischer-Tropsch Nano-Cobalt Catalysts for Clean Fuels

"A series of 15%Co/Al2O3 catalysts were prepared by incipient wetness impregnation under various calcination conditions (90-500 oC), and were characterized by X-ray diffraction (XRD), X-ray photoelectron spectroscopy experiments (XPS), temperature programmed reduction, and catalytic measurements of hydrogenation of carbon monoxide to long-chained hydrocarbons leading to clean fuels (Fischer-Tropsch synthesis). The results of XPS show the presence of incompletely decomposed cobalt nitrate for catalysts calcined at 90-200 oC, and the presence of Co3O4 for catalysts calcined at 200-500 oC. For the four alumina-supported nano cobalt catalysts with different thermal treatment (200-500 oC), XRD and XPS results illustrated that there were mainly nano Co3O4 crystalite phases of 9-10 nm and the size of cobalt nano-particles did almost not change with the different temperature of thermal treatment. This was different from that of silica-supported cobalt catalysts. The supported cobalt catalyst (CoAp340 sample) calcinated at 340 oC presented a better activity for Fischer Tropsch synthesis to clean fuels, at mild conditions like atmospheric pressure (100 kPa), 1800 mL/g/h and 190 oC; rather than high pressure (2 MPa or more)."     

Synthesis of dimethyl carbonate by vapor phase oxidative carbonylation of methanol over Cu-based catalysts

Dimethyl carbonate (DMC) synthesis reaction by oxidative carbonylation of methanol has been studied using vapor phase flow reaction system in the presence of Cu-based catalysts. A series of Cu-based catalysts were prepared by the conventional impregnation method using activated carbon (AC) as support. The effect of various promoters and reaction conditions on the catalytic reactivities were intensively evaluated in terms of methanol conversion and DMC selectivity. The morphological analysis by X-ray diffraction and SEM was also conducted in order to characterize the emloyed catalysts. Regardless of catalyst compositions, the optimal reaction temperature for oxidative carbonylation of methanol was found to be around 120–130°C. The reaction rate was too slow below 100°C, while too much by-products was produced above 150°C. Among the various catalysts employed, CuCl₂/NaOH/AC catalyst with the molar ratio of OH/Cu=0.5–1.0, has shown the best catalytic performance, which appears to have a strong relationship with the formation of intermediate species, Cu₂(OH)₃Cl.     

Properties of anodic RuNiO<Subscript><Emphasis Type="Italic">x</Emphasis></Subscript>(OH)<Subscript><Emphasis Type="Italic">y</Emphasis></Subscript> catalysts synthesized on carbon supports with various dispersion degree

A number of catalysts of the (Ru-Ni)/C system is synthesized and studied for application in anodes of alkaline ethanol-air fuel cells. The carbon supports used are carbon blacks with different specific surface area and graphite powders. The X-ray photoelectron spectroscopy technique allowed detecting on the catalyst surface metallic ruthenium and nickel in the form of Ni(OH)2 hydroxide and possibly oxyhydroxide NiOOH. It is shown that the catalyst activity in the reaction of ethanol electrochemical oxidation grows at an increase in the specific surface area of the carbon support. The method of carbon monoxide oxidative desorption was used to determine the values of the specific surface area of the catalyst metallic phase. It is shown that at an increase in the relative ruthenium content from (1Ru3Ni)/C to Ru/C, the specific catalytic activity in the catalysts of the (Ru-Ni)/C system reaches the maximum value near the composition of (2Ru1Ni)/C. It is shown that the found optimum catalyst composition is independent of the carbon support dispersion degree. Activity in ethanol electrooxidation of the (2Ru1Ni)/C catalyst supported on the Ketjenblack EC-600 carbon black is 18 ± 3 A/g of the catalyst (>120 A/g of Ru) at 40°C and potential E = 0.5 V in the 2MKOH + 1 M C₂H₅OH electrolyte.     

Characterization of carbon-supported AuPt nanoparticles for electrocatalytic methanol oxidation reaction

In view of the recent finding that the bimetallic AuPt nanoparticles prepared by molecular-capping-based colloidal synthesis and subsequent assembly on carbon black support and thermal activation treatment exhibit alloy properties, which is in sharp contrast to the bimetallic miscibility gap known for the bulk counterparts in a wide composition range, there is a clear need to assess the electrocatalytic properties of the catalysts prepared with different bimetallic composition and different thermal treatment temperatures. This paper reports recent results of such an investigation of the electrocatalytic methanol oxidation reaction (MOR) activities of the carbon-supported AuPt nanoparticle catalysts with different bimetallic composition and thermal treatment temperatures. Au(m)Pt(100)(-)(m) nanoparticles of 2-3 nm core sizes with different atomic compositions ranging from 10% to 90% Au (m = 10 approximately 90) have been synthesized by controlling the feeding of the metal precursors used in the synthesis. The electrocatalytic MOR activities of the carbon-supported AuPt bimetallic catalysts were characterized in alkaline electrolytes. The catalysts with 65% to 85% Au and treated at 500 degrees C were found to exhibit maximum electrocatalytic activities in the alkaline electrolytes. The findings, together with a comparison with some well-documented catalysts as well as recent experimental and theoretical modeling results, have revealed important insights into the participation of CO(ad) and OH(ad) on Au sites in the catalytic reaction of Pt in the AuPt alloys with approximately 75% Au. The insights are useful for understanding the correlation of the bifunctional electrocatalytic activity of the bimetallic nanoparticle catalysts with the bimetallic composition and the thermal treatment temperatures.