HAIMCM-41介孔分子筛催化1，3-苯并二嗯茂烷合成的研究

研究了HAlMCM-41分子筛催化邻苯二酚与环己酮、丁酮、丙酮、丙醛、丁醛、异丁醛、戊醛、正己醛、正辛醛、苯甲醛、二苯甲酮等十余种醛(酮)的缩合反应.考察了反应时间、酚与醛(酮)的配比、HA1MCM-41分子筛用量、硅铝比、催化剂重用次数等因素对邻苯二酚与醛(酮)反应的影响.结果表明,当邻苯二酚与醛(酮)物质的量比为1:1.4,催化剂用量为3.5g/mol邻苯二酚,反应4h,分子筛n(SiO_2)/n(Al_2O_3)为15时,选择性一般在99.4%以上,转化率也一般在85.6%以上,因此,HAlMCM-41分子筛对邻苯二酚与醛(酮)的反应有较好的催化性能.     

HY分子筛催化1,3-苯并二噁茂烷类化合物合成的研究

研究了HY分子筛催化邻苯二酚与环己酮、丁酮、丙酮、丙醛、丁醛、异丁醛、戊醛、异戊醛、正己醛、正辛醛、苯甲醛、二苯甲酮等十余种醛(酮)的缩合反应。考察了反应时间、酚与醛(酮)的配比、HY分子筛用量等因素对酚与醛(酮)反应的影响。实验发现,当邻苯二酚与醛(酮)摩尔比为1∶1.0、催化剂用量为每mol邻苯二酚2.5g、反应4h,选择性一般在97%以上,醛(酮)的转化率一般在57%以上,表明HY分子筛对邻苯二酚与醛(酮)的反应有较好的催化性能。     

HMCM-22分子筛催化1,3-苯并二噁茂烷类化合物合成的研究

研究了HMCM-22分子筛催化邻苯二酚与环己酮、丁酮、丙酮、丙醛、丁醛、异丁醛、戊醛、异戊醛、正己醛、正辛醛、苯甲醛、二苯甲酮等十余种醛(酮)的缩合反应.考察了反应时间、酚与醛(酮)的配比、HMCM-22分子筛用量等因素对酚与醛(酮)反应的影响.结果表明,当酚与醛(酮)摩尔比为1∶1.4,催化剂用量为3.5 g/1mol醛(酮),反应5 h,选择性一般在97%以上,转化率也一般在70%以上,表明HMCM-22分子筛对邻苯二酚与醛(酮)的反应有较好的催化性能.     

HY分子筛催化1,3-苯并二(噁)茂烷类化合物合成的研究

研究了HY分子筛催化邻苯二酚与环己酮、丁酮、丙酮、丙醛、丁醛、异丁醛、戊醛、异戊醛、正己醛、正辛醛、苯甲醛、二苯甲酮等十余种醛（酮）的缩合反应.考察了反应时间、酚与醛（酮）的配比、HY分子筛用量等因素对酚与醛（酮）反应的影响.实验发现,当邻苯二酚与醛（酮）摩尔比为1：1.0、催化剂用量为每mol邻苯二酚2.5g、反应4h,选择性一般在97%以上,醛（酮）的转化率一般在57%以上,表明HY分子筛对邻苯二酚与醛（酮）的反应有较好的催化性能.     

HMAS-5分子筛催化合成缩醛(酮)

研究了HMAS_5分子筛催化乙二醇与环己酮、丁酮、丙酮、丙醛、丁醛、异丁醛、戊醛、异戊醛、正己醛、正辛醛、苯甲醛等醛(酮)的缩合反应。考察了反应时间、醛(酮)与醇的配比、HMAS_5分子筛用量等因素对醛(酮)与醇缩合反应的影响。结果表明,HMAS_5分子筛对醛(酮)与醇的缩合反应有较好的催化性能,选择性一般在98%以上,转化率也一般在90%以上。     

Ag/ZrO2催化剂上的1,2-丙二醇选择性气相氧化反应

采用浸渍法制备了一系列Ag/ZrO₂催化剂, 考察了Ag/ZrO₂催化剂对1,2-丙二醇选择性氧化合成丙酮醛反应的催化性能. 实验结果表明: 在原料气配比为V(N₂)∶V(O₂)＝300∶19, n(O₂)/n(alcohol)＝1.2, 反应物液时空速为3.2 g/(g•h), 反应温度为673 K时, 1,2-丙二醇选择性氧化合成丙酮醛反应的转化率为95.7%, 选择性为55.3%, 高于传统电解银催化剂. UV-Vis DRS和XPS的研究结果表明: 在Ag/ZrO₂催化剂上存在大量的Ag^＋和Ag_n^δ＋有利于促进催化活性的提高.     

Ni/Fe物质的量的比对Ni-Fe催化剂表面性质和二硝基甲苯加氢活性的影响

采用Fe粉置换氯化镍溶液中的Ni²⁺制备了Ni-Fe催化剂, 并应用于催化二硝基甲苯加氢合成甲苯二胺的反应中。运用XRD、低温氮吸附-脱附、H₂-TPD、XPS和TEM等技术手段对不同Ni/Fe物质的量的比(n_Ni/n_Fe)下催化剂进行了表征。结果表明, n_Ni/n_Fe对Ni-Fe催化剂表面性质影响显著。当n_Ni/n_Fe为1:4时, Fe抑制Ni氧化的作用达到最大, Ni-Fe催化剂化学氢吸附量和活性物种Ni的分散度分别达到了0.16 mmol·g^-1和23%, 催化剂性能得到较大的提升。在优化的催化剂制备条件下, DNT(二硝基甲苯)的转化率和TDA(甲苯二胺)的选择性分别达到了~100%和99%。另外, 对Ni-Zn漆原镍(Urushibara Ni)催化剂和Ni-Fe催化剂催化DNT加氢反应进程进行了研究, 发现它们有相同的加氢中间产物, 但反应不同阶段的催化速率存在差异。     

Ni/Fe物质的量的比对Ni-Fe催化剂表面性质和二硝基甲苯加氢活性的影响

采用Fe粉置换氯化镍溶液中的Ni²⁺制备了Ni-Fe催化剂,并应用于催化二硝基甲苯加氢合成甲苯二胺的反应中。运用XRD、低温氮吸附-脱附、H₂-TPD、XPS和TEM等技术手段对不同Ni/Fe物质的量的比(n_Ni/n_Fe)下催化剂进行了表征。结果表明,n_Ni/n_Fe对Ni-Fe催化剂表面性质影响显著。当n_Ni/n_Fe为1:4时,Fe抑制Ni氧化的作用达到最大,Ni-Fe催化剂化学氢吸附量和活性物种Ni的分散度分别达到了0.16 mmol·g^-1和23%,催化剂性能得到较大的提升。在优化的催化剂制备条件下,DNT(二硝基甲苯)的转化率和TDA(甲苯二胺)的选择性分别达到了~100%和99%。另外,对Ni-Zn漆原镍(Urushibara Ni)催化剂和Ni-Fe催化剂催化DNT加氢反应进程进行了研究,发现它们有相同的加氢中间产物,但反应不同阶段的催化速率存在差异。     

P123软模板对CuO-CeO2结构及其CO催化氧化性能的影响

采用软模板水热法制备了不同Cu/Ce物质的量之比的CuO-CeO₂(n_Cu ∶ n_Ce=1∶9、2∶8、3∶7、4∶6、5∶5、6∶4、7∶3)催化剂。考察了n_Cu:n_Ce和制备方法(软模板水热法和无模板共沉淀法)对CuO-CeO₂催化剂低温催化氧化CO性能的影响, 并采用XRD、N₂-吸附脱附、TEM、H₂-TPR和XPS等表征手段对催化剂的结构、氧化还原特性和表面化学状态等进行了分析。结果表明, 随着n_Cu ∶ n_Ce的增加, CuO-CeO₂催化剂的CO催化氧化活性先升高后降低。当n_Cu ∶ n_Ce=5∶5时, 催化剂在100 ℃时CO转化率即达到90%以上。采用软模板水热法制备的CuO-CeO₂催化剂大的比表面积、狭窄的孔道分布结构、活性CuO物种高的分散状态和CuO与CeO₂之间存在强相互作用是其具有优异的CO催化氧化活性的主要原因。     

含硅路易斯酸的发展及其在有机合成中的应用

综述了含硅路易斯酸R₃SiX [X＝I, OTf, NTf₂, C(C₆F₅)Tf₂等]和(R₃SiX＋ML_n)的发展、合成以及它们在有机合成中的应用. 它们主要被用来催化Aldol, 烯丙基化, Diels-Alder, Ene和Friedel-Crafts等反应. 催化剂的用量一般为0.5～20 mol%, 并随着催化剂的活性不同, 反应产率从一般到良好不等. 催化剂活性顺序为R₃SiNTf₂＞R₃SiOTf, (R₃SiX＋ML_n)＞R₃SiX. 也对近年出现的手性含硅路易斯酸的发展和应用进行了概述, 当手性双-(多氟甲磺酰)-亚胺基硅烷用于催化环戊二烯和丙烯酸甲酯的Diels-Alder反应时, ee值高达54%.     

Study on catalytic synthesis of 1,3-benzodioxoles by HY zeolite

The acetalization and ketalization of various aldehydes and ketones with catechol by using HY zeolite as catalyst were studied. Effect of the reaction time, mole ratio of reactants, and amount of catalyst on the yield of benzodioxoles were investigated. Results show that HY is an efficient catalyst for the acetalization and ketalization with high conversion and selectivity in mild conditions. The best reaction conditions: molar ratio of catechol to aldehydes or ketones is 1:1.4, catalyst amount is 3.5 g/l mol catechol, reaction time is 5 h. Under these conditions, the conversion and selectivity were over 50% and 97%, respectively. Translated from Huaxue Tongbao 2006, 69(6) (in Chinese)     

Acetalization of carbonyl compounds with 2, 2, 4-trimethyl-1, 3- pentanedio catalyzed by novel carbon based solid acid catalyst

The synthesis of 2, 4-diisopropyl-5,5-dimethy1- 1.3-dioxane through the acetalization of isobutyraldehyde with 2, 2, 4-trimethy1-1,3-pentanediol （TMPD） catalyzed by the novel carbon based acid was first carried out. High conversion （≥98%） and specific selectivity were obtained using the novel carbon based acid, which kept high activity after it was reused 5 times. Moreover. the catalyst could be used to catalyze the acetalization and ketalization of different aldehydes and ketones with superior yield. The yield of several products was over 90%. The novel heterogeneous catalyst has the distinct advantages of high activity, strikingly simple workup procedure, non-pollution, and reusability, which will contribute to the success of the green process greatly.     

Study on ketalization reaction of poly(vinyl alcohol) by ketones. VIII. kinetic study on acetalization and ketalization reactions of poly(vinyl alcohol)

The kninetics of acid-catalyzed acetalization and ketalization of poly(vinyl alcohol) (PVA) were systematically studied in completely homogeneous media with carefully selected solvents. Thus the acetalization reaction was run in water with six aldehydes [R₁CHO (R₁ = H, CH₃, C₂H₅, n-C₃H₇, i-C₃H₇, ClCH₂)], whereas the ketalization in dimethylslfoxide with 11 ketones [R₂CH₃CO (R₂ = CH₃, C₂H₅, n-C₃H₇, i-C₃H₇, n-C₄H₉, i-C₄H₉, tert-C₄H₉, C₆H₅CH₂, C₆H₅CH₂CH₂), cyclopentanone, and cyclohexanone]. The latter was difficult to proceed in aqueous media. Both reactions were reversible and bimolecular and, despite the use of different solvents, gave similar heats of reaction (7.5 kcal/mol) and activation energies (ca. 15 kcal/mol) except for the case of formaldehyde and chloroacetaldehyde; however the equilibrium constants at 25°C showed that the acetalization is thermodynamically much more favored than the ketalization (ca. 5000 vs. 0.01–0.9), probably because of steric hindrance of the ketone substrate. The rate constants of hydrolysis (reverse reactions) for the poly(vinyl acetal) and poly(vinyl ketal) followed the Hammett-Taft equation to give a single p* (=3.60) that is very close to that for the hydrolysis of diethyl acetal and ketal. From these and other data, it was concluded that the polymer hydrolysis, as well as PVA acetalization and ketalization, are all electrophilic reaction where the formation of hemiacetal or hemiketal is the rate-determining step. © 1996 John Wiley & Sons, Inc.     

功能化离子液体在缩醛（酮）反应中催化性能的研究

研究了磺酸功能化离子液体在缩醛(酮)反应中的催化性能.系统考察了离子液体催化剂、反应时间、反应温度、底物用量比和催化剂用量等因素的影响以及底物的适用性.研究结果表明:磺酸功能化离子液体[C4H8SO3Hm im]p-TSA是缩醛(酮)反应有效的催化剂,其催化活性主要由阳离子决定;该催化体系具有很好的重复使用性,经十次循环后催化活性未见明显降低.     

固体超强酸催化下的醛酮自身缩合及其溶剂效应的研究

研究了在三种固体超强酸催化下醛(酮)自身的羟醛缩合反应,系统考察了反应时间,催化剂用量等因素对反应的影响,优化了反应条件.同时,对该反应的溶剂效应进行了研究.结果表明,当催化剂用量为2 g/1 mol醛(酮),反应5 h,转化率可达40%,溶剂对该反应有明显的抑制作用.超强酸对各种醛都具有较好的催化活性,其催化醛类化合物自身缩合的转化率都在48%以上,选择性在95%以上,证明固体超强酸对该缩合反应有较好的催化活性和选择性.     

Highly Active Copper‐Network Catalyst for the Direct Aldol Reaction

The development of a highly active solid‐phase catechol–copper network catalyst for direct aldol reaction is described. The catalyst was prepared from an alkyl‐chain‐linked bis(catechol) and a copper(II) complex. The direct aldol reaction between carbonyl compounds (aldehydes and ketones) and methyl isocyanoacetate was carried out using 0.1–1 mol % [Cu] catalyst to give the corresponding oxazolines at yields of up to 99 % and a trans/cis ratio of >99:1. The catalyst was reused with no loss of catalytic activity. A plausible reaction pathway is also described.     

Synthesis of gem-Dihydroperoxides from Ketones and Aldehydes Using Silica Sulfuric Acid as Heterogeneous Reusable Catalyst

Silica sulfuric acid (SSA) was found to efficiently catalyze the conversion of aldehydes and ketones directly into the corresponding gem-dihydroperoxides (DHPs) on treatment with aqueous 30% H₂O₂ at room temperature. Mild reaction conditions, good to excellent yields, short reaction times, low environmental impact, and recyclability of the catalyst are the main advantages of this synthetic method.