钛基固体超强酸对环己酮乙二醇缩酮催化反应的特性

合成S042-/TiO2、SO42-/TiO2-Ce(Ⅳ)、SO42-/TiO2-ZrO2三种不同的固体超强酸,以环己酮乙二醇缩酮为探针反应,发现550℃下焙烧的SO4 2-/TiO2-Ce(Ⅳ)催化活性最好.并以SO42-/TiO2-Ce(Ⅳ)为催化剂,考察反应温度、催化剂用量、反应时间、反应物配比和带水剂对缩酮化反应转化率和选择性的影响.结果表明,反应温度为110～125℃、催化剂用量占反应物料总质量的0.5%、环己酮和乙二醇物质的量比为1:1.5、反应时间为1 h、环己烷为带水剂时,环己酮的转化率达95.2%,环己酮乙二醇缩酮的选择性98.7%,催化剂的重复使用效果好.     

分子筛超强酸SO_4~(2-)/TiO_2/USY催化合成胡萝卜酸乙酯的研究

以USY分子筛为载体,采用共沉淀-浸渍法制备分子筛超强酸SO42-/Ti O2/USY,用其催化丙二酸、无水乙醇合成胡萝卜酸乙酯。考察了不同反应时间、带水剂种类、带水剂用量、醇酸比、催化剂用量、催化剂重复使用性等因素对反应酯化率的影响。结果表明:在丙二酸用量为0.1mol,醇酸摩尔比为3.1:1,催化剂用量为1.0g,反应时间为3h,带水剂环已烷用量为5m L时,酯化率达到92.13%,催化剂重复使用5次以后仍然有很高的活性。说明SO42-/Ti O2/USY对该反应具有很强且极稳定的催化活性。     

稀土固体超强酸SO4^2-／TiO2／La^3＋催化合成丙酸苄酯

采用浸渍法制备了稀土固体超强酸SO2-4/TiO2/La3+,并运用IR、XRD和Hammett指示剂法对其进行了表征.以制备的固体超强酸SO2-4/TiO23+为催化剂、丙酸和苯甲醇为原料合成了丙酸苄酯.考察了催化剂的制备条件及合成条件对酯化率的影响,结果显示催化剂最佳制备条件钛前体氧化物的浸渍液为含0.07 mol·L-1 La3+的硫酸溶液,焙烧时间3 h,焙烧温度500℃.最佳反应条件醇酸摩尔比为12、催化剂用量为苯甲醇用量的9.3%、反应时间3 h、反应温度120℃,酯化率达84.0%以上.用IR、1H-NMR等手段对产品进行了表征.     

硫酸高铈催化合成丙酸苄酯

以结晶硫酸高铈为催化剂对丙酸苄酯的合成进行了研究，考察了反应时间、催化剂用量、醇酸摩尔比和带水剂等因素对反应的影响，结果表明，在最佳反应条件下，酯化率在85％以上。     

固体酸催化合成邻苯二甲酸二戊酯的研究

以苯酐和正戊醇为原料,采用自制的固体酸SO4^2-／SiO2、SO4^2-／Fe2O3、SO4^2-／SnO2及SO4^2-／TiO2作为催化剂合成邻苯二甲酸二戊酯（DAP）,分别考察固体酸催化剂的种类、固体酸催化剂的用量、醇酐比、反应时间等因素对合成DAP产率的影响。实验结果表明,其优化的工艺操作条件为：苯酐0．1mol,固体酸催化剂SO4^2-／SiO2 1．7g,醇酐比2．4：1,带水剂二甲苯20mL,反应时间3．5h,其产品收率达91．3％以上。SO4^2-／SnO2作为该反应的催化剂具有催化活性高、寿命长、可多次重复使用、产物易纯化分离且产品色泽浅等优点,可望代替传统的浓硫酸作催化剂应用于DAP的合成。     

稀土固体超强酸SO2-4/TiO2/La3 +催化合成丙酸苄酯

采用浸渍法制备了稀土固体超强酸SO2-4/TiO2/La3+,并运用IR、XRD和Hammett指示剂法对其进行了表征.以制备的固体超强酸SO2-4/TiO23+为催化剂、丙酸和苯甲醇为原料合成了丙酸苄酯.考察了催化剂的制备条件及合成条件对酯化率的影响,结果显示催化剂最佳制备条件:钛前体氧化物的浸渍液为含0.07 mol·L-1 La3+的硫酸溶液,焙烧时间3 h,焙烧温度500℃.最佳反应条件:醇酸摩尔比为1:2、催化剂用量为苯甲醇用量的9.3%、反应时间3 h、反应温度120℃,酯化率达84.0%以上.用IR、1H-NMR等手段对产品进行了表征.     

TiSiW12O40/TiO2催化合成苹果酯

以固载杂多酸盐TiSiW12O40/TiO2为多相催化剂，通过乙酰乙酸乙酯和乙二醇反应合成了苹果酯，探讨TiSiW12O40/TiO2对缩酮反应的催化活性，较系统地研究了原料量比，催化剂肜量，反应时间诸因素对产品收率的影响，实验表明：TiSiW12O40/TiO2是合成苹果酯的良好催化剂，在n(乙酰乙酸乙酯）：n(乙二醇）＝1：1．5，催化剂用量为反应物料总质量的1．0％，环己烷为带水剂，反应时间50min的优化条件下，苹果酯的收率可达84．1％。     

稀土固体超强酸SO24-/TiO2/La3+催化合成水杨酸异丁酯

研究了以稀土固体超强酸SO24-/TiO2/La3+为催化剂,水杨酸和异丁醇为原料合成水杨酸异丁酯,并考察了影响反应的因素.结果表明,醇酸比为3:1,催化剂用量为1.0 g(水杨酸为0.1 mol的情况下),带水剂苯为15 mL,反应时间为3.0 h是最适宜的反应条件,酯化率达96.2%.     

TiSiW12O40/TiO2催化合成己酸异戊酯

报道了以固载杂多酸盐TiSiW12O40/TiO4为多相催化剂，通过己酸和异戊醇反应合成了己酸异戊酯，探讨了TiSiW12O40/TiO4对酯化反应的催化活性，较系统地研究了醇酸摩尔比，催化剂用量，反应时间诸因素对收率的影响，实验表明：TiSiW12O40/TiO4是合成己酸异戊酯的良好催化剂，在n(醇）：n(酸）＝1．6：1，催化剂用量为反应物总质量的1．5％，反应时间45min，使用环己烷为带水剂的适宜条件下，己酸异戊酯的收率可达91．9％。     

碘催化合成环己酮1,2-丙二醇缩醛

研究了单质碘催化环已酮与1，2-丙二醇的缩醛化反应，考察了反应时间、醇酮摩尔比、催化剂用量、带水剂用量等因素对环已酮乙二醇缩醛收率的影响。结果表明，在回流条件下，醇酮摩尔比为1．3，催化剂用量为52mg(约占反应体系总摩尔数的0．007％)，带水剂环己烷用量为8mL，反应40min后缩醛收率可达79．2％。     

纳米固体酸催化合成无毒增塑剂柠檬酸三辛酯的研究

以柠檬酸和正辛醇为原料,采用自制的纳米固体酸S04^2-／SnO2、SO4^2-／ZrO2、SO4^2-／TiO2及SO4^2-／Fe2O3催化剂合成无毒增塑剂柠檬酸三辛酯（trioctylcitrate,TOC）。分别考察了纳米催化剂种类、催化剂用量、醇／酸物质的量比、反应时间、反应温度等因素对合成TOC反应酯化率的影响,对合成的产品进行红外光谱分析。实验结果表明,自制的固体酸SO4^2-／SnO2催化合成无毒增塑剂柠檬酸三辛酯的最佳反应条件：催化剂用量为1．0g,酸醇比为1：6.3,反应时间1．0h,反应温度190℃。在最佳反应条件下,柠檬酸三辛酯的酯化率可达到98．5％。     

用环境友好催化剂俣成丙酸苄酯的研究

应用环境友好催化剂H－β沸石催化苯甲醇与丙酸的酯化反应,合成了丙酯苄酯。研究结果表明,H－β沸石 具有较高的催化活性。考察了苯甲醇／丙酸摩尔比、催化剂用量、反应温度、反应时间和带水剂环己烷用量对酯产率的影响。在典型反应条件（苯甲醇／丙酸摩尔比＝1.15:1、10.5gH－β沸石/摩尔丙酸、反应温度160℃ 、反应时间3.5h和20mL环己烷／摩尔丙酸）下,所得丙酸苄酯的产率为77％,该催化剂易于回收且可重复使用,具有良好的活性稳定性,并研究了用某些金属阳离子改性的β沸石的催化活性。     

Preparation and Catalytic Activity of SO42-/TiO-La2O3 in Synthesis of Butyl Butyrate

Butyl butyrate is a very important compound, which is transparent liquid and has the pear,apple flavor. Natural exist is in the fruit, such as apple, pear, banana, grape and strawberry, etc.Primarily used for to prepare the edible spice and is also widely used in industrial intermediate product, solvent and synthetic perfumery. Until now, there are many methods to synthesize it.Conventionally H2SO4 was reported, but it causes many problems, such as the erosion of equipment,easily causes the vice-reaction, difficulty for after-treatment, environment pollution etc. A new environmentally friendly catalyst, SO42-/TiO2-La2O3 was prepared. And catalytic activity of catalyst in esterification of n-butanoic acid and n-butyl alcohol with SO42-/TiO2-La2O3 as catalyst has been no report up to now. Therefore, studying on the synthetic catalyst has theoretical and practical significances. The catalytic activity of catalyst in esterification of n-butanoic acid and n-butyl alcohol was measured.In this paper, we fast reported the preparation of SO42-/riO2-La2O3 and discussed the factors influencing the synthesis catalyst. The catalyst rare earth solid superacid SO42-/TiO2-La2O3 was The precipitate was filtered and washed thoroughly with distilled water until chloride ions were free.furnace at 480 ℃ for 3 h, and finally stored in a desiccator until use.The factors influencing the synthesis were discussed and the best conditions were found out. The experiment indicated that this catalyst has the following advantage. The amount of catalyst was little and getting high yield, its product has a good quanlity and is favour of reducing erosion of equipment, avoiding environment pollution. The optimum conditions are: molar ratio of n-butanoic acid to n-butyl alcohol was 1:1.5, the quantity of catalyst was equal to 1.5% of feed stocks, the reaction temperature was 93-114 ℃, and the reaction time was 1.0 h. Rare earth solid superacid SO42-/TiO2-La2O3 is an excellent catalyst for synthetizing butyl butyrate and its yield can reach over 90.0%.A good catalyst should be able to be used repeatedly. The reusing of the catalyst was studied. We found that the catalytic activities of our catalyst are almost unchanged after it had been used five times. From the above results and discussion, we can see that the synthesis of n-butyl butyrate by SO42-/TiO2-La2O3 instead of H2SO4 has a great prospect of application. It has a good applied foreground.     

Synthesis of glycerin triacetate over molding zirconia-loaded sulfuric acid catalyst

Zirconia-loaded sulfuric acid (SO24- /ZrO2) catalysts were prepared by impregnation method, molded by punch tablet machine and characterized by X-ray diffraction. SO42- /ZrO2 catalyst was used to obtain glycerol triacetate (GTA) directly from glycerin. The effect of some factors, such as different temperatures of calcination and catalysts molded or not, on the reusable times of catalysts and the yield of GTA were investigated. The optimum reaction conditions were shown as follows: the reaction temperature was 403 K; the reaction time continued for 8 h; the amount of molded catalysts was 5 wt% of glycerin and the molar ratio of glycerin to acetic acid was 1 : 8. The yield of GTA was 97.93% under the optimum condition.     

固体超强碱催化环戊酮的Self-Aldol Condensation反应研究

2-环亚戊基环戊酮是一种重要的香料中间体,本文以环戊酮为原料,固体超强碱为催化剂,分别选用环己烷、苯、石油醚为带水剂,通过Aldol自缩合反应合成了环戊酮的二聚体2-环亚戊基环戊酮.考察了催化剂用量、带水剂种类、反应时间对环戊酮二聚体2-环亚戊基环戊酮收率的影响,最终确定最佳实验方案:环己烷为带水剂,催化剂用量为环戊酮...     

稀土固体超强酸SO42-/TiO2/La3+催化合成丁酸异戊酯

丁酸异戊酯是无色至淡黄色透明油状液体,有近似生梨和香蕉香甜气。天然品存在于椰子油、可可豆、苹果、香蕉、葡萄、草莓等中,是我国ＧＢ２７６０－８６规定允许使用的食用香料,主要用以配制香蕉、菠萝、杏、樱桃和杂锦水果等型香精;也可用作提取天然香料的溶剂、乙酸纤维素的溶剂及增塑剂。通常它是在硫酸催化下由丁酸和异戊醉酯化反应而得［１,２］,反应时间长,副反应多,对设备腐蚀严重,废水排放量大,后处理工艺复杂。为此,本实验选用稀土固体超强酸ＳＯ４２－／ＴｉＯ２／Ｌａ３＋作为催化剂进行某些酸与异戊醇的酯化反应。 …     

固体超强酸SO4^2—／TiO2 催化合成异戊酸异戊酯

异戊酸异戊酯是ＧＢ2 760 - 86规定为允许使用的食用香料 ,也可微量用于化妆品、皂用香精中[1] 。异戊酸异戊酯传统合成方法为硫酸催化下由异戊酸与异戊醇直接酯化反应制得[2 ] ,由于浓硫酸易使有机物炭化、氧化 ,故副反应多、酯产物色泽深、产率受影响的诸多缺点 ,因此 ,有人开发了由异戊醇一步法合成异戊酸异戊酯的方法[3～ 5] ,但异戊酸异戊酯的收率不高 ,仅为 5 8～70 .6%。本文采用更换酯化反应催化剂的方法 ,以ＳＯ2 -4 ＴｉＯ2 固体超强酸作为催化剂 ,对异戊酸异戊酯的合成进行了研究。1　实验1 1　ＳＯ2 -4 ＴｉＯ2 固体超强酸的制…     

稀土固体超强酸SO_4~(2-)/TiO_2/La~(3 )催化合成水杨酸异丁酯

研究了以稀土固体超强酸SO_4~(2-)/TiO_2/La~(3 )为催化剂,水杨酸和异丁醇为原料合成水杨酸异丁酯,并考察了影响反应的因素。结果表明,醇酸比为3:1,催化剂用量为1.0g(水杨酸为0.1mol的情况下),带水剂苯为15mL,反应时间为3.0h是最适宜的反应条件,酯化率达96.2％。     

Synthesis of butyrate using a heterogeneous catalyst based on polyvinylpolypyrrolidone

A heterogeneous polyvinylpolypyrrolidone supported Brønsted acidic catalyst ([PVPP-BS]HSO₄) was used to synthesize butyrate in this paper. The prepared catalysts were characterized by FT-IR, TG, and FESEM and their catalytic activity in butyric acid esterification with benzyl alcohol was investigated. The influencing factors such as the amount of catalyst, reaction temperature, and reaction time were carefully studied. Under the optimized condition with the butyric acid to benzyl alcohol mole ratio of 1: 1.2 and the reaction temperature of 130°C, the yield of benzyl butyrate reached 96.8 % within 4 h in the presence of 8 mass % of catalyst. Moreover, the catalyst could be reused six times without noticeable drop in activity. This catalyst was also used to synthesize other kinds of butyrates achieving the butyrate yield above 90 %.