V_2O_5/C催化乙二醛氧化为乙醛酸的研究

选用V2O5作为催化剂,活性炭为载体,偏钒酸铵的草酸溶液为浸渍前驱体,采用等体积浸渍法制备了V2O5/C催化剂,将其应用于乙二醛的液相氧化.并对反应液用液相色谱进行了定性,在确定了催化体系中氧化产物的基础上,考察了V2O5含量和焙烧温度对催化剂催化性能的影响,利用XRD和TEM等手段对催化剂进行了表征.结果显示,V2O5含量较低时(w(V2O5)<3%),催化剂的活性组分分散度较高,乙二醛转化率和乙醛酸的选择性都随着V2O5的含量提高而逐渐增加;当负载量为3%时,催化效果最佳,乙二醛转化率和乙醛酸的选择性分别达到16.16%和76.75%;当V2O5的质量分数大于3%时,V2O5颗粒在活性炭表面发生明显聚集,V2O5开始出现多层吸附,导致乙二醛转化率和乙醛酸得率略有下降.而焙烧温度是制备负载型催化剂的一个重要影响因素.焙烧温度的作用不仅在于使活性组分的前驱体充分分解,同时也影响着活性组分的分散状态.我们考察了经不同温度焙烧后的催化剂的活性,从表征结果来看,在473K以下焙烧时,可能活性组分的前驱体未能充分分解,活性中心数目较少,反应效果较差;当V2O5负载量为3%、焙烧温度为573K时,催化剂具有较高的催化活...     

V2O5／C催化乙二醛氧化为乙醛酸的研究

选用V2O5作为催化剂,活性炭为载体,偏钒酸铵的草酸溶液为浸溃前驱体,采用等体积浸渍法制备了V2O5/C催化剂,将其应用于乙二醛的液相氧化．并对反应液用液相色谱进行了定性,在确定了催化体系中氧化产物的基础上,考察了V2O5含量和焙烧温度对催化剂催化性能的影响,利用XRD和TEM等手段对催化剂进行了表征．结果显示,V2O5含量较低时（w（V2O5）〈3％）,催化剂的活性组分分散度较高,乙二醛转化率和乙醛酸的选择性都随着V2O5的含量提高而逐渐增加;当负载量为3％时,催化效果最佳,乙二醛转化率和乙醛酸的选择性分别达到16．16％和76．75％;     

乙二醛在Pd4团簇吸附、解离以及选择氧化

采用第一性原理密度泛函理论,我们研究了乙二醛在具有四面体结构的Pd4团簇上吸附、解离以及氧化反应历程.研究表明:乙二醛中C-H键是最容易断裂的,断裂后形成的HCOOC基团分别和O或OH反应形成乙醛酸,也就是说乙二醛经过脱氢,选择氧化形成产物乙醛酸.在整个反应过程中,所需要的能垒均小于11.53 Kcal/mol.我们的研究不仅有助于理解乙二醛氧化的反应机理,而且对于今后设计更好的乙二醛选择氧化催化剂有一定的帮助作用.     

Adsorption,Dissociation and Selective Oxidation of Glyoxal over Pd_4 Cluster

采用第一性原理密度泛函理论,我们研究了乙二醛在具有四面体结构的Pd4团簇上吸附、解离以及氧化反应历程.研究表明：乙二醛中C-H键是最容易断裂的,断裂后形成的HCOOC基团分别和O或OH反应形成乙醛酸,也就是说乙二醛经过脱氢,选择氧化形成产物乙醛酸.在整个反应过程中,所需要的能垒均小于11.53 Kcal/mol.我们的研究不仅有助于理解乙二醛氧化的反应机理,而且对于今后设计更好的乙二醛选择氧化催化剂有一定的帮助作用.     

V_2O_5/CeO_2催化剂上甲醇氧化一步法合成二甲氧基甲烷

采用溶胶-凝胶法制备了V2O5/CeO2催化剂,并用于甲醇氧化一步法合成二甲氧基甲烷(DMM)反应中.考察了V2O5含量对钒氧化物的存在状态、催化剂表面酸性、氧化-还原性及其催化甲醇氧化反应性能的影响.结果表明,V2O5含量为15%时钒氧化物呈单层分散,小于15%时以孤立或聚合态存在,大于20%时出现V2O5晶体,达到30%时出现CeVO4.当V2O5含量为15%时,较高的钒氧化物分散度使催化剂具有较强的氧化还原能力和较多的酸性中心,从而使催化剂具有较高的活性和DMM选择性.     

金催化剂上乙二醛氧气氧化合成乙醛酸的研究

利用沉积-沉淀法和溶液相还原法制备了系列金催化剂,以氧气氧化乙二醛合成乙醛酸为探针反应,进行了反应条件的优化,并通过对催化剂进行XRD、AAS、UV-Vis和XPS表征,分析了影响催化剂活性的因素.结果显示:与沉积-沉淀法相比,采用溶液相还原法制备的催化剂Au/ZrO2(L),金的实际负载量较高,表现出较高的催化活性,当溶液pH为7.7,反应温度为323 K时,乙醛酸收率达到6.2%.     

The Research of Oxidation of Glyoxal to Glyoxylic Acid over Gold Catalyst

利用沉积-沉淀法和溶液相还原法制备了系列金催化剂,以氧气氧化乙二醛合成乙醛酸为探针反应,进行了反应条件的优化,并通过对催化剂进行XRD、AAS、UV-Vis和XPS表征,分析了影响催化剂活性的因素.结果显示：与沉积-沉淀法相比,采用溶液相还原法制备的催化剂Au/ZrO2（L）,金的实际负载量较高,表现出较高的催化活性,当溶液pH为7.7,反应温度为323 K时,乙醛酸收率达到6.2%.     

V2O5/MO-Al2O3（M = Mg，Ca，Sr，Ba）催化剂用于正丁烷催化氧化脱氢反应

采用浸渍法制备了不同V2O5担载量的V2O5/MO-Al2O3(M = Mg, Ca, Sr, Ba)催化剂,钒物种的前驱体为偏钒酸铵.对制备的催化剂进行了一系列表征,并对催化剂上正丁烷选择性氧化脱氢制取丁烯进行了反应研究.表征结果(包括比表面积、X射线衍射、傅里叶红外光谱、氢气程序升温还原和拉曼光谱)显示,不同碱土金属元素掺杂的催化剂显示不同的钒价态信息和催化性能.其中掺杂Ca, Sr, Ba的催化剂,正钒酸盐相很难被还原,因此催化剂的氧化还原循环难以建立,导致以上三种催化剂在正丁烷氧化脱氢反应中活性较低.然而, Mg掺杂的催化剂却显示出较高的催化活性和选择性.实验结果表明：在Mg掺杂的载体上担载5% V2O5的催化剂上600°C时可获得高达30.3%的正丁烷转化率和64.3%的烯烃总选择性.这与V2O5担载量为5%时,在获得高度分散的钒氧化合物物种时可使MgO晶相稳定存在密切相关.     

固相球磨法制备丙烷氧化脱氢V2O5/NiO催化剂

以不同温度焙烧制备的NiO和V2O5为前驱物,采用固相球磨法制备了V2O5/NiO催化剂,考察了前驱物的焙烧温度对该催化剂丙烷氧化脱氢制丙烯反应性能的影响,并采用x射线衍射、N2物理吸附、电感耦合等离子体原子发射光谱、透射电子显微镜、H2程序升温还原和x射线光电子能谱等对催化剂进行了表征.结果表明,固相球磨法制备的V2O5/NiO催化剂表现出较好的丙烷氧化脱氢制丙烯催化性能,当以400℃焙烧的氧化物为前驱体时,V2O5/NiO催化剂表面含有较多的未完全还原氧物种Oδ-,因而表现出了较高的丙烯选择性.在475℃反应时,丙烷转化率可达20.1%,丙烯选择性达到71.2%.     

高效液相色谱法测定乙醛溶液中的乙二醛和乙醛酸

利用醛基与2,4-二硝基苯肼(DNPH)反应得到的腙产物对紫外-可见光有吸收的特性,采用高效液相色谱法(HPLC)测定乙醛溶液中乙二醛和乙醛酸的含量。结果表明,DNPH衍生乙二醛成腙反应的适宜条件为: 反应温度70 ℃, pH 1.75, DNPH与羰基的物质的量比为6,反应时间150 min。在20 ℃、pH 1.75的乙腈溶液中,乙二醛二腙的溶解度为20.2 mg/L。乙二醛质量浓度在2～20 mg/L范围内,乙二醛二腙的峰面积与乙二醛的质量浓度之间呈良好的线性关系;乙醛酸质量浓度在10～100 mg/L范围内,乙醛酸腙的峰面积与乙醛酸的质量浓度之间呈良好的线性关系。用HPLC测定乙醛硝酸氧化法制乙二醛反应液中乙二醛和乙醛酸的含量,结果的重复性好;对乙二醛的测定结果与应用化学分析法测定结果的平均相对误差为1.77%;对反应液中乙二醛、乙醛酸含量的测定有着较高的加标回收率,分别为99.6%～103.3%和98.1%～102.4%。所建立的方法为醛及二羰基化合物的测定提供了准确、便捷的方法。     

Oxidation of glyoxal to glyoxylic acid by oxygen over V2O5/C catalyst

A novel vanadium oxide catalyst supported on active carbon was prepared by an incipient wetness impregnation method, and the precursor was obtained from oxalic acid aqueous solutions of NH4VO3. The catalyst was applied liquid phase oxidation of glyoxal to glyoxylic acid. It was found that V2O5/C catalyst exhibited obvious activity for glyoxal oxidation. Glyoxylic acid could be obtained without pH regulation during the reaction. By using this catalyst, the conversion of glyoxal and the yield of glyoxalic acid were 29.2% and 13.6%, respectively at 313 K and oxygen flow 0.1 L/rain after reaction for 10 h.     

V2O5/C catalyst for liquid phase oxidation of glyoxal to glyoxylic acid

A study of the catalytic activity of V₂O₅/C catalyst for the oxygen oxidation of glyoxal has been made, showing that glyoxylic acid can be formed without control of pH value and there is little oxalic acid from the excessive oxidation of glyoxylic acid. The studies of XRD and TEM have shown that V₂O₅ diffraction peaks gradually strengthen with the increase of the content of V₂O₅. With the content of 3% V₂O₅ and the calcination temperature of 573 K, V₂O₅/C catalyst displayed the best activity and selectivity. The conversion of glyoxal and the selectivity of glyoxylic acid reached 18.76% and 77.70% after 5 h, respectively. Moreover, V₂O₅/C catalyst showed small deactivation after recycling three times, which indicates that V₂O₅/C has a higher stability than noble metal catalysts in the reaction medium. Supported by the Technology Research and Development Project for University of Shanxi Province of China (Grant No. 20051272)     

V2O5/C catalyst for liquid phase oxidation of glyoxal to glyoxylic acid

Science China Chemistry - A study of the catalytic activity of V2O5/C catalyst for the oxygen oxidation of glyoxal has been made, showing that glyoxylic acid can be formed without control of pH...     

Selective oxidation of propane to acrylic acid over mixed metal oxide catalysts

The effects of metal atomic ratio, water content, oxygen content, and calcination temperature on the catalytic performances of MoVTeNbO mixed oxide catalyst system for the selective oxidation of propane to acrylic acid have been investigated and discussed. Among the catalysts studied, it was found that the MoVTeNbO catalyst calcined at a temperature of 600 ℃ showed the best performance in terms of propane conversion and selectivity for acrylic acid under an atmosphere of nitrogen. An effective MoVTeNbO oxide catalyst for propane selective oxidation to acrylic acid was obtained with a combination of a preferred metal atomic ratio （Mo1V0.31Te0.23Nb0.12）. The optimum reaction condition for the selective oxidation of propane was the molar ratio of C3H8 ：O2 ： H2O ： N2 = 4.4： 12.8 ： 15.3 ： 36.9. Under such conditions, the conversion of propane and the maximum yield of acrylic acid reached about 50% and 21%, respectively.     

Heterogeneous glyoxal oxidation: a potential source of secondary organic aerosol

Laboratory studies are described that suggest reactive uptake of glyoxal on particulate containing HNO(3) could contribute to the formation of secondary organic aerosol (SOA) in the upper troposphere (UT). Using a Knudsen cell flow reactor, glyoxal is observed to react on supercooled H(2)O/HNO(3) surfaces to form condensed-phase glyoxylic acid. This product was verified by derivatization and GC-MS analysis. The reactive uptake coefficient, γ, of glyoxal varies only slightly with the pressure of nitric acid, from γ = 0.5 to 3.0 × 10(-3) for nitric acid pressures between 10(-8) and 10(-6) Torr. The data do not show any dependence on temperature (181-201 K) or pressure of glyoxal (10(-7) to 10(-5) Torr). Using the determined reactive uptake kinetics in a simple model shows that glyoxal uptake to supercooled H(2)O/HNO(3) may account for 4-53% of the total organic mass fraction of aerosol in the UT.     

Ozonocatalytic decomposition of glyoxal and glyoxylic and formic acids in the presence of iron(III) ions

Rate constants of reactions of ozone with glyoxal, glyoxylic and formic acid in aqueous solutions at pH 1.5 were determined. It was shown that iron(III) in the form of ions accelerates oxidation of glyoxal and glyoxylic acid, but does not influence reaction between ozone and formic acid. It was established that the catalyst acts effectively if its concentration is comparable to the concentration of the oxidized substrate, the optimal stoichiometric ratio (Fe³⁺/substrate) being close to 1/3. The catalytic reaction mechanism was studied using a competitive chelate ligand, oxalic acid. We concluded that the catalytic activity of iron(III) in the investigated reaction was due to its ability to form chelate complexes in which the substrate was more easily oxidized by molecular ozone.     

GC/ITMS measurement of carbonyls and multifunctional carbonyls in PM2.5 particles emitted from motor vehicles.

A method was developed and tested to identify and quantitate carbonyls and multifunctional carbonyls in fine particulate matter (PM2.5; <2.5 microm aerodynamic diameter). The method relies on ultrasonic extraction of particulate matter on filters at -8 degrees C; derivatization with O-(2,3,4,5,6-pentafluorobenzyl) hydroxylamine (PFBHA), and PFBHA along with bis (trimethylsilyl) trifluoroacetamide (BSTFA); and detection of the derivatives by gas chromatography/ion trap mass spectrometry. Ultrasonic extraction of model compounds from enriched particles was affected by solvent polarity (water > methylene chloride > toluene-isopropanol (2 + 1, v/v). Water provided the highest recovery for dihydroxy acetone, pyruvic acid, and hydroxy acetone, compared to methylene chloride, and toluene-isopropanol. Lowering the ultrasonication bath temperature from 0 degrees to -8 degrees C improved the recoveries of the less water soluble and more volatile species-methacrolein, methyl vinyl ketone, 2,3-butanedione, and tolualdehyde. The power of the method was demonstrated by identification and quantitation of carbonyls and multifunctional carbonyls in sample extracts of fine particulate matter (PM2.5) collected in the Caldecott tunnel, CA. The identities of crotonaldehyde, 2,3-butanedione, glyoxal, 9H-fluoren-9-one, glycolaldehyde, glyoxylic acid, levulinic acid, and 3-hydroxybenzaldehyde were confirmed by comparing the relative retention time and mass spectra of the analyte in the sample extract with an authentic standard. Quantitation of crotonaldehyde, glyoxal, 2,3-butanedione, glyoxylic acid, and levulinic acid was accomplished. This is the first report of glyoxylic acid, levulinic acid, and 3-hydroxybenzaldheyde in PM2.5 particles sampled in a roadway tunnel. It is also the first report of a C10 carbonyl with the molecular formula of C10H16O2, a hydroxy carbonyl with the molecular formula of C17H21NO2, and a hydroxy or dihydroxy carbonyl with the molecular formula of C16H14O2 or C9H10O3. The high-molecular weight hydroxy carbonyls, which were found only in the heavy-duty (diesel) bore, may be tracers of diesel emissions in air.     

硅藻土负载H6PMo9V2Nb1O40催化剂上乙烷氧化制乙酸和乙醛的反应性能

采用浸渍法制备了硅藻土负载的杂多化合物催化剂PMo9V2Nb1/K，利用TPR、IR、TPD和微反技术研究了催化剂的表面酸性、乙烷化学吸附和氧化反应性能。结果表明，含铌的PMo9V2Nb1/K催化剂仍保持着Keggin形杂多酸的化学构造，晶格氧的活泼性明显提高，B酸强度和酸量均有所降低；乙烷分子主要通过H原子吸附在Lewis碱位V—O—Mo和Nb—O—Mo的桥氧上，吸附在Nb—O—Mo桥氧上的乙烷易发生解离吸附，并与邻近的表面氧发生反应生成乙酸或乙醛；在240 ℃，0.4 MPa和2 000 h-1下，乙烷的摩尔转化率为22.5%，产物乙酸和乙醛的总选择性达90.8%。     

A new method of ion chromatography technology for speedy determination and analysis in organic electrosynthesis of glyoxylic acid

Based on ion chromatography (IC) technology, we have developed a new method that combines ion chromatography with a conductivity detector to separate and determine the substances of glyoxal, glycolic acid, oxalic acid and glyoxylic acid. The ion chromatography was applied for the first time in quantitative determination of substances involved in electrosynthesis of glyoxylic acid. The method has been applied to separate and analyze simultaneously either glyoxylic acid and glyoxal in electroxidation of glyoxal, or glyoxylic acid and oxalic acid in electroreduction of oxalic acid. An aqueous Na2CO3-NaHCO3 or NaOH-Na2CO3 solution was confirmed to be the most desirable eluent. The experimental results demonstrated that the detection sensitivity is ahead of ppm grade, and the variation coefficients such as the retention time, the peak height and the peak area outperform 2%. All the recoveries of the detected substances are ranged between 97 and 103%. The method exhibits advantages of high selectivity, high sensitivity, speediness and simple apparatus requirement. Furthermore, simultaneous determination of a mixture of several substances can be achieved by the developed method, and even a neutral molecule of glyoxal can be also determined by choosing an appropriate composition and concentration of eluent.