Synthesis of Acetic Acid on Pd—H4SiW12O40—Based Catalysts by Direct Oxidation of Ethylene

Synthesis of acetic acid by direct oxidation of ethylene on Pd-H4SiW12O40-based catalysts was studied in a fixed-bed integral reactor and a pulse differential reactor,From the performance of the catalysts with different compositions and configurations,it is proposed that acetic acid is predominantly produced via an intermediate of acetaldehyde ,This can be easily confirmed by comparing the product distributions in the integral and the differential reactors,The active sites for acetic acid formation are considered to exist mainly at the boundaries between the H2SiW12O40 and the Pd particles,The Pd-based catalysts reduced by H2/N2 have higher activities than those reduced by hydrazine,as explained by the degree of Pd dispersion obtained from the characteristics of hydrogen chemical adsorption It was found that the Pd-Se-SiW12/SiO2 catalyst with selenium tetrachloride as a precursor was more active than that with potassium selenite ,and that the acetic acid yield can be greatly increased by adding a suitable amount of dichloroethane (C2H4Cl2/C2H4 mole ratio=0.03) to the reactants.     

Direct Oxidation of Ethene to Acetic Acid

Compared with the chemical processes of naphtha oxidation, n-butane oxidation, methanol carbonylation and acetaldehyde oxidation currently used in the manufacture of acetic acid, direct selective oxidation of ethene to acetic acid is a very attractive process1,2. Uchida et al.3,5 and Denko4 have reported a highly active catalyst system which produces acetic acid with 240 g/h(L of the STY and 86.4% of selectivity. The catalyst system consisted of 2% of Pd by weight, 0.02 of the mole ratio of …     

MnCl2-H4SiW12O40/SiO2催化氧化二甲醚制取甲缩醛

 采用浸渍法制备了H4SiW12O40/SiO2杂多酸催化剂,分别使用MnCl2, SnCl4和CuCl2对其进行修饰,并在常压连续流动固定床反应器中考察了催化剂对二甲醚选择氧化制取甲缩醛的催化活性. 结果表明, MnCl2修饰的H4SiW12O40/SiO2催化剂的活性和甲缩醛选择性均高于SnCl4和CuCl2修饰的催化剂. 进一步考察了不同MnCl2含量及反应温度对反应的影响. 在MnCl2含量为5%, 反应温度为593 K时, MnCl2-H4SiW12O40/SiO2催化剂的活性和甲缩醛选择性最佳,二甲醚转化率为8.6%, 甲缩醛选择性为36.3%. X射线衍射结果显示, MnCl2与H4SiW12O40相互作用并均匀地分散在载体上. 用红外光谱研究了MnCl2-H4SiW12O40/SiO2催化剂的结构,发现改性后的催化剂基本保持了杂多酸的Keggin结构. NH3程序升温脱附结果显示, MnCl2的加入较明显地降低了催化剂的酸强度和酸中心数目.     

乙烯直接氧化制乙酸的研究Ⅱ．助剂对Pd－Se／H4SiW12O40／SiO2催化性能的影响

 研究了不同助剂促进的负载型Pd－Se／H4SiW12O40／SiO2催化剂对乙烯直接氧化制乙酸反应的影响．采用固定床微反装置评价了催化剂的性能，并采用C2H4和O2吸附量测定、吸附C2H4的TPD－MS和TPSR－MS等技术对催化剂进行了表征．结果表明，以SiO2为载体，以硅钨酸为助剂，Pd－Se－Na－Ru组成的催化剂体系其催化性能比文献报道的结果明显提高．在原料气配比n（C2H4）∶n（N2）∶n（O2）∶n（H2O）＝55∶14∶9∶22，反应物空速GHSV＝3844h－1，反应压力p＝1．4MPa，反应温度θ＝155℃条件下，乙烯的转化率和乙酸的选择性分别为8．0％和87．4％，乙酸的单程时空产率达372．0g／（L·h）．吸附量测定表明，吸附在催化剂表面上的C2H4／O2比值高对于提高乙酸的选择性是有利的．     

Synthesis of Acetic Acid on Pd-H_4SiW_(12)O_(40)-Based Catalysts by Direct Oxidation of Ethylene

Synthesis of acetic acid by direct oxidation of ethylene on Pd-H4SiW12O40-based catalysts was studied in a fixed-bed integral reactor and a pulse differential reactor. From the performance of the catalysts with different compositions and configurations, it is proposed that acetic acid is predominantly produced via an intermediate of acetaldehyde. This can be easily confirmed by comparing the product distributions in the integral and the differential reactors. The active sites for acetic acid formation are considered to exist mainly at the boundaries between the H4SiW12O40 and the Pd particles. The Pd-based catalysts reduced by H2/N2 have higher activities than those reduced by hydrazine, as explained by the degree of Pd dispersion obtained from the characteristics of hydrogen chemical adsorption. It was found that the Pd-Se-SiW12/SiO2 catalyst with selenium tetrachloride as a precursor was more active than that with potassium selenite, and that the acetic acid yield can be greatly increased by adding a s     

SiO2包裹的杂多酸催化剂Cu-H4SiW12O40瞬间催化四氢吡喃化反应

以微乳化法制备的二氧化硅担载的的杂多酸催化剂Cu—H4SiW12O40在室温下能瞬间催化四氢吡喃化反应。且催化剂在至少重复使用四次而未见明显的失活。     

硅钨酸催化合成苯甲醛1,2-丙二醇缩醛

以硅钨酸为催化剂,通过苯甲醛和1,2-丙二醇反应合成了苯甲醛1,2-丙二醇缩醛。实验结果表明,硅钨酸对缩醛反应具有较高的催化活性,反应的最佳条件为：苯甲醛150mmol,n(苯甲醛)：n(1,2-丙二醇)：1.0：1.5,催化剂0.7％(反应物料总质量),带水剂环己烷8mL,反应温度85℃～125℃,反应时间1．0h,收率达88．9％．     

Catalytic Synthesis of n-Butyraldehyde 1,2-propanediol Acetal over H4SiW12O40-PAn

A new environmentally friendly catalyst, H₄SiW₁₂O₄₀-polyaniline (PAn), was prepared, and n-butyraldehyde 1,2-propanediol acetal was synthesized from n-butyraldehyde and 1,2-propanediol in the presence of H₄SiW₁₂O₄₀-PAn. The influence factors of the synthesis were discussed, and the best reaction conditions were found: the molar ratio of n-butyraldehyde to 1,2-propanediol is 1:1.5, the amount of catalyst used is 1.2% of feed stock, and the reaction time is 1.0 h. H₄SiW₁₂O₄₀-PAn is an excellent catalyst for synthesizing n-butyraldehyde 1,2-propanediol acetal, and the yield can reach more than 95.2%. *Translated from Journal of Central China Normal University (Natural Sciences Edition), 2005, 39(9) (in Chinese), 2004, 28(4) (in Chinese)     

Pd-SiW12/SiO2催化剂上乙烯直接氧化制乙酸的反应机理

 利用积分反应器和微分反应器对Pd－SiW12／SiO2催化剂上乙烯直接氧化生成乙酸的反应机理进行了探讨．乙烯在积分反应中氧化的主要产物为乙酸（选择性为77．6％），很少生成乙醛（选择性仅为8．1％）；而在微分反应中氧化的主要产物是乙醛（选择性为98．4％）．在微分反应中分别以乙醛和乙醇为主反应物时，乙醛氧化完全生成乙酸，选择性为100％，而乙醇氧化生成乙酸的选择性低于0．15％．可以认为，在Pd－SiW12／SiO2催化剂上，水蒸气存在下乙烯主要经由中间物乙醛而生成乙酸．通过对含有不同组分和不同还原条件处理的催化剂活性的比较，认为目的反应主要发生在Pd与SiW12相互接触的部位，催化剂中的Pd0是活性Pd物种的主要形态．     

Effect of Support and Acidity of Catalyst on the Direct Oxidation of Ethylene to Acetic Acid

The selective oxidation of ethylene to acetic acid was investigated on Pd-acid/ support catalyst system. The catalytic activity is influenced strongly by the acidity of the catalyst. The stronger the catalyst acidity the higher the catalytic activity. The nature of the support also influences the activity of the catalyst substantially. The catalyst has highest activity when it exhibits highest acidity on silica.     

Cr2O3-Co3O4／SiO2对十八醇氧化生成十八酸反应的催化性能

 制备了一系列不同Cr／Co比例的Cr2O3－Co3O4／SiO2催化剂，并用XRD，FT－IR和BET等手段对催化剂进行了表征；考察了催化剂对十八醇氧化生成十八酸反应的催化性能，及反应条件（反应温度和反应时间）对催化性能的影响，确定了最佳反应条件．结果表明，金属硝酸盐在773K焙烧后转变成相应的氧化物并负载于二氧化硅上．Cr2O3－Co3O4／SiO2催化剂对十八醇氧化反应有很高的催化活性，十八酸选择性最高可达99．93％，收率可达52．44％．Cr2O3－Co3O4／SiO2催化剂的活性明显高于单一的Cr2O3／SiO2或Co3O4／SiO2催化剂     

乙酸存在下磷酸铁催化对甲酚气相选择性氧化

 在乙酸存在和空气气氛下,以磷酸铁为催化剂进行了对甲酚气相选择氧化生成对羟基苯甲醛和对羟基苯甲醇的反应. 考察了不同乙酸/对甲酚比和反应温度对反应产物分布的影响. 结果表明,加入乙酸可抑制目标产物深度氧化,促进气相反应中高选择性地生成对羟基苯甲醛和对羟基苯甲醇. 在反应温度为250 ℃,乙酸/对甲酚比为0.9,催化剂用量为0.35 g和对甲酚流速为1.92 g/h时,生成对羟基苯甲醛的选择性为34.4%,生成对羟基苯甲醇的选择性为65.6%.     

Electrocatalytic Oxidation of Cysteine at a CoSalophen/ n‐(butyl)4SiW12O40 Carbon Paste Electrode

In the present study, a novel mixture consisting of N,N′‐bis(salicylidene)‐1,2‐phenylenediamino cobalt (CoSalophen, CoSal) complex and (n‐butyl)₄SiW₁₂O₄₀ (SiW₁₂), have been used to chemically modify a carbon paste electrode (CPE) for sensitive determination of cysteine (CySH). The electrocatalytic effect of the newly developed modified CPE towards oxidation of CySH was evaluated by comparing cyclic and differential pulse voltammograms in the presence of cysteine at bare, CoSal, SiW₁₂ and CoSal/SiW₁₂ modified CPE. The differential pulse voltammetry method was applied as a sensitive method for quantitative detection of CySH trace amounts, the experimental conditions being optimized in order to evaluate the best analytical parameters of the sensor. Reproducibility and stability studies were also performed and the sensor was applied for the determination of CySH in a pharmaceutical sample and in human blood serum and urine samples.     

H4SiW12O40 as the catalyst for the hydration and alcohol addition to 2-methylpropene

Catalytic hydration of 2-methyl-2-propene to tert-butanol (TBA) and alkylation with methanol to methyl-tert-butyl ether (MTBE) with dodecatungstosilicic acid H₄SiW₁₂O₄₀ as catalyst were investigated in a constant flow reactor at 40–80 °C. The catalyst is active in both reactions and exhibits high selectivities. The mechanisms of both reactions involving protonated intermediates were proposed.     

Direct Synthesis of Acetic Acid from CH4 and CO2 in the Presence of O2 over a V2O5-PdCl2／Al2O3 Catalyst

The possibility of synthesizing acetic acid from CH4 and CO2 in the presence of O2 over a V2O5-PdCl2/Al2O3 catalyst has been explored. The result shows that it is feasible in catalyzing a direct conversion of CH4, CO2 and O2 to acetic acid. It is concluded that both CO2 and O2 are involved in the formation of acetic acid.     

钨硅酸的制备及其在催化合成缩酮(醛)中的应用

本文探讨了钨硅酸的制备方法,以合成环己酮1,2-内二醇缩酮为例验证钨硅酸的催化活性,并探讨了合成其它缩酮（醛）的适宜条件,得到的收率分别为：环己酮1,2-丙二醇缩酮85．5％、环己酮乙二醇缩酮89．6％、丁酮乙二醇缩酮79．5％、丁醛乙二醇缩醛89．1％、丁醛1,2丙二醇缩醛81．5％。     

H4 SiW12 O40 /C催化合成丁酮1,2-丙二醇缩酮

以丁酮和1,2-丙二醇为原料,活性炭负载硅钨酸（H4SiW12O40／C）为催化剂,催化合成了丁酮1,2-丙二醇缩酮。正交试验筛选出最佳反应条件为：丁酮200mmol,n（丁酮）：n（1,2-丙二醇）=1．0：1．4,ω（催化剂）=1．2％（以反应物质量计）,反应时间1h。在此最佳反应条件下,丁酮1,2-丙二醇缩酮的收率可达71．13％。     

载体和担载酸对乙烯直接氧化合成乙酸反应的影响

 在固定床流动反应器上研究了Pd－酸／载体体系催化乙烯直接氧\r\n化合成乙酸的反应，并对载体相同但担载酸强度不同的催化剂的催化活\r\n性进行了比较．结果表明，担载酸的强度明显影响催化剂的活性，酸强\r\n度越大其催化活性越高．用NH3－TPD和异丙醇脱水探针反应表征了二氧\r\n化硅、活性碳和酸性白土三种载体担载的Pd－H4SiW12催化剂的酸性，\r\n并测试了三种催化剂的催化活性．结果表明，载体通过影响担载酸的强\r\n度而影响催化剂的活性，载体上的强酸中心越多，催化剂的活性越高．\r\n测定了二氧化硅、活性碳和酸性白土三种载体担载的Pd－H4SiW12催化\r\n剂上Pd的分散度，并与其催化活性相关联．结果表明，决定乙烯直接氧\r\n化生成乙酸反应活性的主要因素是催化剂的酸强度而不是Pd的分散度．     

Pd/WO3-ZrO2催化剂的结构对乙烯直接氧化制乙酸的影响

利用浸渍法制备了一系列具有不同W/Zr比和不同WO3-ZrO2焙烧温度的1%pd/WO3-ZrO2催化剂.通过X射线衍射、N2吸附、氨程序升温吸附、吡啶吸附红外光谱和程序升温还原方法表征了催化剂的晶体结构、表面状态以及酸性.结果表明,制备条件对W和Pd的表面状态具有很人的影响.随着W/Zr比的增加和焙烧温度的提高,催化剂表而的WOx经历了从聚钨酸物种到聚钨酸/WO3晶体共存再到WO3品体颗粒的转化.W/Zr比为0.2且焙烧湍度为1073K的催化剂具有最多的聚钨酸物种,而该催化剂具有最好的活性.因此,聚钨酸物种的最决定了催化剂的活性.Pd的分散状态只依赖于WO3-ZrO2的焙烧温度.Pd物种分散性好,则乙酸选择性高,而分散性差的人颗粒Pd会导致乙烯的燃烧反应.