One-step synthesis of phenol by O- and OH- emission material

A novel approach to the direct synthesis of phenol from benzene was obtained with high benzene conversion (30%) and phenol selectivity (approximately 90%) by using a microporous material [Ca24Al28O64]4+.4O-(C12A7-O-) as catalyst with oxygen and water; active O- and OH- anions are proposed to play important roles in the formation of phenol by hydroxylating the aromatic ring of benzene.     

Reduction features of NO over a potassium-doped C12A7-O- catalyst

The NO reduction features over a noble-metal-free NO(x) storage/reduction catalyst ([Ca24Al28O64](4+*)4O-/K, defined as C12A7-O-/K), including the NO conversion, the N2 selectivity, and sulfur tolerance, were investigated with hydrogen and C3H6 as the reducing agents in a fixed-bed continuous flow reactor. The NO conversion and the N2 selectivity on the C12A7-O-/K catalyst mainly depends on the sample temperature, the percentage of potassium, the reducing agents, and the composition of the mixture of gases. The C12A7-O-/10%K catalyst possessed the highest selective reduction ability (to N2) among the catalysts C12A7-O-/x%K. Over 50% of NO can be reduced to N2 with H2 as the reduction agent at 550-700 degrees C. The C12A7-O-/K catalyst also shows higher NO(x) storage capacity (183.9 micromol/g at about 550 degrees C) as well as sulfur tolerance for both the NO(x) storage and the reduction processes. The catalyst characteristics and the intermediate species formed in the NO storage and reduction processes were investigated by the X-ray diffraction, X-ray photoelectron spectroscopy, Fourier transform infrared spectroscopy, and time-of-flight mass spectrometry. The mechanism of NO(x) reduction was addressed according to the above investigations.     

Features and mechanism of H- anion emission from 12 CaO x 7 Al2O3 surface

The hydrogen anion (H-) and other anionic species (O-, OH-, e-) in the gas phase, emitted from the synthesized crystal surface of 12 CaO x 7 Al2O3-H- (C12A7-H-), have been observed. The emission intensity of all the anionic species strongly depends on the sample surface temperature and the extraction field. H- has the highest emission branch ratio, and the extraction field can reduce its apparent activation energy. H- emission current at a microA/cm2-level has been achieved, which is about 4 orders of magnitude higher than that obtained from the thermal desorption process of CaH2. The observed anions of H- and OH- are attributed to their migration from the C12A7-H- cages onto the surface [i.e., Y-(cages) --> Y-(surface) --> Y-(gas phase) (Y = H, OH)]. The weak O- and electron emission would both arise from the dissociation of O2-: O2-(surface) --> O-(surface) + e-(surface) --> O-(gas phase) + e-(space).     

固体酸催化烯烃改性生物油酚类化合物研究

选取生物油中含量较高的愈创木酚、儿茶酚和苯酚为酚类模型化合物,以蒙脱土K-10负载的Cs2.5H0.5PW12O40为固体超强酸催化剂,苯酚/1-辛烯烷基化反应为探针,考察了催化剂负载量,反应温度及物料摩尔比等因素对酚类烷基化反应的影响.结果表明,在60～100℃范围内,30%Cs2.5H0.5PW12O40/K-10对苯酚烷基化反应具有很好的催化活性和选择性,原料摩尔比为1时苯酚氧烷基化产物的选择性最好.愈创木酚中甲氧基的位阻效应使其转化率在相同条件下比苯酚低很多,相应氧烷基化产物的选择性也很低.儿茶酚与1-辛烯反应主要生成单羟基氧烷基化产物,100℃时选择性仍高达96%.升高温度有利于烷基化改性反应的进行,但产物中氧烷基化产物的选择性随着温度升高而降低.     

Low energy electron and O- reactions in films of O2 coadsorbed with benzene or toluene

A detailed understanding of nascent reactive events leading to DNA damage is required to describe ionizing radiation effects on living cells. These early, sub-picosecond events involve mainly low energy (E < 20 eV) secondary electrons (SE), and low energy (E < 5 eV) secondary ion (and neutral) fragments; the latter are created either by the primary radiation, or by SE via dissociative electron attachment (DEA). While recent work has shown that SE initiate DNA strand break formation via DEA, the subsequent damage induced by the DEA ion fragments in DNA, or its basic components is unknown. Here, we report 0-20 eV electron impact measurements of anion desorption from condensed films containing O2 and either benzene (C6H6), or toluene (C6H5CH3); these molecules represent the most fundamental structural analogs of pyrimidine bases. Our experiments show that all of the observed OH- yields are the result of reactive scattering of 1-5 eV O- fragments produced initially by DEA to O2. These O- reactions involve hydrogen abstraction from benzene or toluene, and result in the formation of benzyl radicals, or toluene radicals centered on either the ring or exocyclic methyl group. O- scatters over nm distances comparable to DNA dimensions, and reactions involve a transient anion collision complex. Anion desorption is found to depend on both, the temperature of hydrocarbon film formation (morphology), and the order of overlayer adsorption, e.g. O2 on benzene, or benzene on O2. Our measurements support the notion that in irradiated DNA similar secondary-ion reactions can be initiated by the abundant secondary electrons, and may lead to clustered damage.     

TS－1分子筛催化苯羟基化反应

ＴＳ－１分子筛对苯羟基化反应有着较高的催化活性及选择性．在反应体系中加入适量的无机酸，可提高反应的选择性；增加催化剂ＴＳ－１及Ｈ２Ｏ２的加入量，由于转化率的提高，反应选择性略有下降，而产物分布中苯酚的含量减少，苯醌的含量增大．ＴＳ－１催化苯羟基化反应是一个复杂的串连反应过程，即首先是苯氧化为苯酚，然后苯酚进一步氧化为苯二酚（对苯二酚为主），苯二酚再进一步氧化为醌．提高反应温度，Ｈ２Ｏ２的转化率和选择性随之提高，并且产物分布中苯酚的含量增大，醌的含量减少，这可能是热力学因素所致     

中孔氧化硅负载铬催化剂上苯高选择性生成苯酚：响应曲面分析法用于反应条件优化

以硝酸铬为前驱体,中孔氧化硅SBA-16为载体,采用简单浸渍法制备了Cr/SBA-16催化剂,并采用广角和小角X射线衍射、N2吸附-脱附、透射电镜和紫外-可见光谱等技术对其进行了表征.同时将该催化剂用于以H2O2为氧化剂的苯直接羟基化制苯酚反应以考察其催化性能.将中心组合设计与响应曲面分析法(RSM)相结合,对影响反应性能的操作变量如反应温度、反应时间及H2O2和催化剂用量进行了优化.结果表明,独立变量和苯酚产率之间的关系可用二阶多项式模型来表达,其相关系数(R2)高达0.985,表明用RSM预测的数值与实验值吻合较好.得到的苯酚选择性较高时的操作条件为：反应温度324 K,反应时间8 h, H2O2和催化剂用量分别为3.28 mL和0.09 g.由此可见,将RSM法用于苯羟基化制苯酚反应条件优化是可靠的.     

Kinetics and reaction mechanism of phenol hydroxylation catalyzed by La-Cu_4FeAlCO_3

Phenol hydroxylation is an industrially important reaction, whose main products are catechol and hy-droquinone being diverse applications which are im-portant intermediates for perfumes, drugs, and phar-maceuticals and so on[1]. The processes using H2O2 a…     

二乙醇胺作添加剂Ru-Zn催化剂上苯选择加氢制环己烯

采用共沉淀法制备了Ru-Zn催化剂,考察了二乙醇胺的添加对Ru-Zn催化剂上苯选择加氢制环己烯性能的影响,并采用N2物理吸附、透射电镜、X射线衍射、X射线荧光、傅里叶变换红外和程序升温还原等手段对催化剂进行了表征.结果表明,二乙醇胺可以与浆液中ZnSO4反应生成(Zn(OH)2)3(ZnSO4)(H2O)3和硫酸二乙醇胺盐.随着二乙醇胺用量的增加,化学吸附在催化剂表面的(Zn(OH)2)3(ZnSO4)(H2O)3增多,它与硫酸二乙醇胺盐的协同作用提高了Ru-Zn(4.9%)催化剂上苯选择加氢生成环己烯的选择性.当二乙醇胺用量为0.3g时,(Zn(OH)2)3(ZnSO4)(H2O)3在Ru-Zn(4.9%)催化剂加氢后样品的表面高度分散,反应性能最佳,循环使用第3次时苯转化率为84.3%,环己烯选择性和收率分别达75.5%和63.6%;使用至第4次时,反应25min时苯转化率和环己烯选择性仍可达75%以上,环己烯收率为58%以上.     

丙烯选择氧化反应中钼基催化剂动态结构的研究

 用原位共焦显微拉曼光谱技术考察了丙烷选择氧化反应中Ag－M\r\no－P－O催化剂的结构，讨论了催化剂动态结构的成因及其对催化剂性\r\n能的影响．实验结果表明，在773K和n（C3H8）∶n（O2）∶n（N2）＝\r\n3∶1∶4的反应条件下，Ag－Mo－P－O催化剂中的Mo－O物种可转化为A\r\ngMoO2PO4中的Mo－O物种（多钼酸根），此时催化剂对丙烷选择氧化具\r\n有较高的催化活性．催化剂中Mo－O物种的转化是由MoO3中Mo－O物种和\r\nAgMoO2PO4中Mo－O物种的结构特性决定的．AgMoO2PO4中的Mo－O物种具\r\n有较强的参与MarsvanKrevelen氧化－还原循环的能力，可能是丙烷选\r\n择氧化反应的活性物种．     

镍-钒催化剂作用下由苯直接氧化氨化合成苯胺

设计并制备了Ni-V/γ-Al2O3催化剂, 研究了其上苯用过氧化氢氧化氨化一步直接合成苯胺的性能和不同氨基源对合成苯胺的影响. 实验结果显示：在本文条件下, Ni/γ-Al2O3和V/γ-Al2O3催化剂均能活化苯环上C—H键, 使苯一步氧化羟基化为苯酚. Ni、V双组分催化剂则表现出较好的合成苯胺活性和选择性, 催化剂中Ni/V摩尔比在5.5时催化活性和选择性最好,目标产物苯胺的选择性达到85％, 远远高于主要副产物苯酚的选择性. 反应时间宜控制在2 h左右, 反应最佳温度为333 K. 尿素在碱性条件下可作为氨基化试剂, 在Ni-V/γ-Al2O3催化剂作用下使苯直接氧化氨化为苯胺, 尿素和氨水作为共氨化剂表现出对生成苯胺有利的协同效应.     

Nanoporous crystal 12CaO.7Al2O3: a playground for studies of ultraviolet optical absorption of negative ions

A novel nanoporous material 12CaO.7Al2O3 (C12A7) offers a possibility of incorporating large concentrations (>1021 cm-3) of a wide range of extraframework anions inside its nanopores. We have investigated, both experimentally and theoretically, optical absorption associated with several types of such anions, including F-, OH-, O-, O2-, O2-, and O22-, and assigned their optical absorption bands. It is demonstrated that the chemical identity and concentration of extraframework anions can be controlled by an appropriate treatment of "as grown" C12A7. We also show that the position of the adsorption edge is, in turn, determined by the chemical identity of the extraframework species and can be varied in the range of approximately 4-6 eV. We suggest that C12A7 is a unique host material, which can be used as a playground for studying negatively charged species that are unstable in other environments.     

Ni-Cu/Al_2O_3催化剂上顺酐液相选择加氢制丁二酸酐反应性能

以Al2O3为载体,采用等体积浸渍法制备了一系列Ni-Cu/Al2O3催化剂,用于顺酐液相加氢反应,并结合低温N2物理吸-脱附、H2程序升温还原、H2程序升温脱附、X射线衍射、CO程序升温表面反应等表征结果,详细考察了催化剂中Cu含量对其催化性能的影响.结果表明,Cu的引入提高了活性组分Ni的分散度,促进了催化剂上C=C的加氢活性;同时,由于Ni-Cu双金属间的相互作用,明显抑制了催化剂表面C=O的加氢.当Cu含量为7%时,催化剂上顺酐加氢定向合成丁二酸酐的活性最高.在210oC,H2压力5.0MPa的条件下反应40min时,顺酐转化率与丁二酸酐选择性均达100%.     

C12A7-O-纳米材料的制备及抗菌活性

利用溶胶-凝胶法制备了C12A7-O-{[Ca24Al28O64]4+·4(O-)}纳米材料. 采用X射线衍射、电子顺磁共振及透射电子显微镜等手段对制备的材料进行了表征. 结果表明, 在最佳焙烧条件(1150 ℃, 6 h)下制备的材料平均粒径为74 nm, 并具有晶胞参数为(1.199±0.004) nm的C12A7(Ca12Al14O33)笼状结构, 材料内包含浓度高达1.2×1020 cm-3的氧负离子(O-). 初步研究结果表明, 合成的C12A7-O-纳米材料具有良好的广谱抗菌作用.     

Ru/ZrO2·xH2O催化剂催化肉桂醛选择性加氢制肉桂醇

采用共沉淀法制备了7.5%Ru/ZrO2·xH2O催化剂,运用N2物理吸附-脱附法、X射线衍射、X射线光电子能谱和高分辨透射电子显微镜等技术对催化剂进行了表征,并用于催化肉桂醛选择加氢制肉桂醇反应中,考察了温度、H2压力和溶剂对肉桂醛转化率和肉桂醇选择性的影响.结果表明,肉桂醛转化率随着温度或H2压力的升高而升高,而肉...     

钒改性六方介孔硅分子筛催化苯羟基化制苯酚

以偏钒酸铵为钒源,采用溶胶-凝胶法合成了不同钒含量的六方介孔硅（V-HMS）分子筛,利用X射线衍射、N2吸附-脱附和程序升温还原(H2-TPR)对合成的催化剂进行了表征,考察了V-HMS对苯羟基化反应的影响。 结果表明,钒进入了分子筛骨架,并且在HMS分子筛上具有较好的分散性。 V-HMS对苯羟基化反应具有良好的催化活性;高分散的钒氧物种有利于提高苯的羟基化反应性能,溶剂乙腈对反应促进作用明显。 乙腈为溶剂,w(V(5.8)-HMS)=2%,60 ℃反应5 h,苯酚收率达到18.55%,选择性达到100%。     

Effect of CO_2 on the structural variation of Na_2WO_4/Mn/SiO_2 catalyst for oxidative coupling of methane to ethylene

In this work,the influence of CO2 on the structural variation and catalytic performance of Na2WO4/Mn/Si O2 for oxidative coupling of methane to ethylene was investigated. The catalyst was prepared by impregnation method and characterized by XRD,Raman and XPS techniques. Appropriate amount of CO2 in the reactant gases enhanced the formation of surface tetrahedral Na2WO4 species and promoted the migration of O in MOx,Na,W from the catalyst bulk to surface,which were favorable for oxidative coupling of methane. When the molar ratio of CH4/O2/CO2 was 3/1/2,enriched surface tetrahedral Na2WO4 species and high surface concentration of O in MOx,Na,W were detected,and then high CH4 conversion of 33.1% and high C2H4 selectivity of 56.2% were obtained. With further increase of CO2 in the reagent gases,the content of active surface tetrahedral Na2WO4 species and surface concentration of O in MOx,Na,W decreased,while that of inactive species(Mn WO4 and Mn2O3) increased dramatically,leading to low CH4 conversion and low C2H4 selectivity. It could be speculated that Na2WO4 crystal was transformed into Mn WO4 crystal with excessive CO2 added under the reaction conditions. Pretreatment of Na2WO4/Mn/Si O2 catalyst by moderate amount of CO2 before OCM also promoted the formation of Na2WO4 species.     

Effects of pretreatment and reduction on the Co/Al2O3 catalyst for CO hydrogenation

The purpose of this study was to investigate the effect of preadsorbed CO at different temperatures, calcination temperatures, the combined influence of reduction temperature and time, and pretreatment using hydrogen or syngas as reduction agents on the F-T synthesis （FTS） activity and selectivity of Co/Al2O3 catalyst. The reactivity of the carbon species at higher preadsorption temperature with H2 in TPSR decreased, whereas the carbon-containing species showed higher reactivity over Co/Al2O3 catalyst with low calcination temperature. This agreed well with the order of catalytic activity for F-T synthesis on this catalyst. The catalytic activity of the catalyst varied with reduction temperature and time remarkably. CODEX optimization gave an optimum reduction temperature of 756 K and reduction time of 6.2 h and estimated C5＋ yield perfectly. The pretreatment of Co/Al2O3 catalyst with different reduction agents （hydrogen or syngas） showed important influences on the catalytic performance. A high CO conversion and C5＋ yield were obtained on the catalyst reduced by hydrogen, whereas methane selectivity on the catalyst reduced by syngas was much higher than that on the catalyst reduced by hydrogen.     

改性L石催化苯酚羟基化反应的应用

以L沸石为载体,分别采用浸渍法和离子交换法制备了Cu/L催化剂,并应用于苯酚羟基化反应.在苯酚与双氧水摩尔比等于3的条件下详细考察了反应时间、反应温度、L沸石酸碱性以及Cu的负载量和负载方法等因素对反应的影响.结果表明:采用浸渍法制备的催化剂比离子交换法制备的催化剂具有更高的活性,而且增加催化剂酸量或者升高反应温度均有利于提高苯酚转化.在最佳反应条件下,反应2h苯酚转化率为24.0%,苯二酚选择性为71.4%,其中n(邻苯二酚)/n(对苯二酚)为1.22.     

纳米孔碳负载Fe3O4催化剂上苯直接羟基化制苯酚

Fe3O4/CMK-3 was prepared by impregnation and used as a catalyst for the direct hydroxylation of benzene to phenol with hydro-gen peroxide. The iron species in the prepared catalyst was Fe3O4 because of the partial reduction of iron(III) to iron(II) on the surface of CMK-3. The high catalytic activity of the catalyst arises from the formation of Fe3O4 on the surface of CMK-3 and the high selectivity for phenol is attributed to the consumption of excess hydroxyl radicals by CMK-3. The effect of temperature,re...