杂多酸盐催化合成碳酸丙烯酯

以杂多酸盐为催化剂,尿素(1)和1,2-丙二醇(2)为原料合成了碳酸丙烯酯.考察了不同杂多酸盐的催化活性和影响反应的因素.较适宜的反应条件为: 1 500 mmol, n(1) ∶ n(2)=1 ∶ 2, w(钨硅酸锌)=2.0%,于165 ℃反应6 h,收率97.32%.硅钨酸锌重复使用5次后,收率仍高于90%.     

介孔分子筛MCM-41负载磷钨酸催化合成香兰素1,2-丙二醇缩醛

以香兰素和1,2-丙二醇为原料,以介孔分子筛MCM-41负载磷钨酸为催化剂,环己烷为带水剂,合成了香兰素1,2-丙二醇缩醛.考察了醛醇物质的量比、反应时间、带水剂用量、催化剂用量及负载量对产率的影响.实验表明,介孔分子筛MCM-41负载磷钨酸是合成香兰素1,2-丙二醇缩醛的理想催化剂,较优反应条件为:n(香兰素)∶n(1,2-丙二醇)=1∶2.4,负载量为50%,催化剂用量为反应物总质量的2.0%,带水剂环己烷15mL,回流反应2.0h,香兰素1,2-丙二醇缩醛的收率达92%以上.     

溴化锌-卤化正四丁基铵高效催化合成苯乙烯环状碳酸酯

溴化锌-卤化正四丁基铵二元催化剂高效催化合成苯乙烯环状碳酸酯, 当n-Bu4NI/ZnBr2摩尔比为2时, 在短时间内(30 min)可将苯乙烯环氧化物几乎完全转化为环状碳酸酯, 无其它副产物的生成. 在ZnBr2/n-Bu4NX的催化体系中加入Au/SiO2 氧化催化剂时, 能将苯乙烯直接氧化, 然后碳酰化实现“一锅法”制备环状碳酸酯. 在此合成路线中担载的纳米金催化第一步苯乙烯环氧化反应; ZnBr2/n-Bu4NBr催化第二步CO2环加成反应. 在温和的反应条件下(80 ℃, 1 MPa, 4 h)将环状碳酸酯的产率提高到42%.     

超临界二氧化碳中马来酸锌催化合成环状碳酸酯

在超临界二氧化碳中, 利用马来酸锌催化二氧化碳与环氧化物反应合成环状碳酸酯. 单独使用马来酸锌作为催化剂时, 对二氧化碳与环氧丙烷反应的催化活性较低, 而在DBU、DMAP、三乙胺、吡啶、咪唑或4-氨基吡啶等有机碱的存在下, 反应活性较高, 产物的收率得到明显提高. 有机碱作用的强弱顺序为DBU>Et3N>咪唑>4-氨基吡啶>DMAP>吡啶. 在压力为8 MPa, 温度110 ℃, 反应时间48 h条件下, 马来酸锌与DBU组成的二元催化系统可以催化二氧化碳与环氧丙烷反应, 得到83.4%产率的碳酸丙烯酯. 该二元系统也能催化其它环氧化物高产率地转化为相应的环状碳酸酯.     

酸促进的氨基甲酸酯醇解合成碳酸酯

在较低温度和压力下,以氯化氢为共反应物或沸石分子筛为催化剂,由氨基甲酸酯与醇反应合成多种碳酸酯。氯化铵沉淀的生成或沸石分子筛对氨气的吸附,可推动反应平衡,使碳酸酯的生成达到较高收率。以氯化氢为共反应物时,反应温度为60℃,最高产率达58％;而以沸石分子筛为催化剂,反应温度为140℃时,最高产率是19％。     

磷钨酸铜绿色催化合成缩醛(酮)及其催化活性测定

合成了绿色杂多酸盐催化剂磷钨酸铜;将环己酮、苯甲醛同乙二醇、1,2-丙二醇的缩合反应作为探针反应,测定了催化剂的催化活性,比较系统地考察了催化剂用量、物料配比、反应时间、带水剂用量等因素对反应产率的影响.结果表明:在底物醛(酮)用量0.2 mol、醛(酮)/乙二醇(1,2-丙二醇)摩尔比1.0/1.5、催化剂用量0.5 g、带水剂环己烷用量18 mL、一定温度下回流反应2.0 h,1,4-二氧螺[4,5]癸烷产率为83.3%,3-甲基-1,4-二氧螺[4,5]癸烷产率为89.7%,2-苯基-1,3-二氧环戊烷产率为66.7%,4-甲基-2-苯基-1,3-二氧环戊烷产率为78.5%.     

离子液体接枝的有机介孔催化剂的制备及催化碳酸丙烯酯水解反应

以甲基咪唑和3-氯-1丙醇为原料合成离子液体（1-羟丙基-3-甲基咪唑四氟硼酸盐,NpmimBF4）,并将其接枝固载到有机介孔材料（FDU-15）上,合成制备了有机介孔催化剂（NpmimBF4- FDU）。采用热重、Ｘ射线衍射、红外光谱及透射电子显微镜等技术手段对催化剂结构进行了表征,并考察了催化剂在碳酸丙烯酯（PC）水解反应中的催化性能,结果表明,该催化体系在常压下能有效催化碳酸丙烯酯水解生成1,2-丙二醇。在催化剂的质量分数为4%、温度80 ℃、反应时间2 h的条件下,1,2-丙二醇的产率大于99%。经简单分离后催化剂可重复使用5次,但活性变化较大。同时对催化碳酸丙烯酯水解生成1,2-丙二醇（PG）的反应机理进行了初步探讨。     

1,7,7-三甲基双环[2.2.1]庚基羟烷基醚的合成

酸催化莰烯与二醇的羟烷氧基化反应是合成标题化合物的可行路线。前人所用酸性催化剂有离子交换树脂及路易斯酸 BF_3·Et_2O。松原义治等报道用离子交换树脂催化茨烯或三环烯分别与乙二醇、1,2-丙二醇反应获得相应的醚,醚化产率分别为42%、33%。Fujioka,Futoshi 等以 BF_3·Et_2O 为催化剂,使莰烯与1,3-丁二醇反应获得产率为34%的醚。迄     

H_4SiW_(12)O_(40)/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(H4S iW12O40/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200 mmol,n(丁酮)∶n(1,2-丙二醇)=1.0∶1.4,w(催化剂)=1.2%(以反应物质量计),反应时间1 h。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%。     

碳酸酯基阳离子Gemini表面活性剂的相转移催化性能研究

采用二月桂酸二丁基锡为催化剂,N,N-二甲基乙醇胺与碳酸二甲酯酯交换反应制得二(N,N-二甲基胺基乙基)碳酸酯(Ⅰ),产率92％(以碳酸二甲酯计);再与1-溴代十六烷反应得到一种含碳酸酯基阳离子Gemini表面活性剂(Ⅱ),产率68.5％[以(Ⅰ)计],用IR、1 HNMR、元素分析表征了其结构.采用(Ⅱ)为固-液相转...     

水合碱金属卤化物催化 CO2 与环氧化物合成环状碳酸酯

 在不添加任何助剂及溶剂的条件下, 考察了水合碱金属卤化物催化 CO2 与环氧丙烷合成碳酸丙烯酯的反应性能. 结果表明, 水合碱金属卤化物表现出远高于无水碱金属卤化物的催化活性, 其中, 以 NaI2H2O 的催化性能最好, 在 120 C, 1 MPa 的条件下反应 1.5 h, 碳酸丙烯酯收率达 97%. 此外, NaI2H2O 在 CO2 与其它环氧化物合成相应环状碳酸酯反应中也表现出较高的催化活性.     

Environmentally benign synthesis of β-hydroxy sulfides using cyclic carbonates catalyzed by large-pore zeolites

Abstract

An efficient one-pot synthesis of β-hydroxy sulfides from thiophenol and cyclic carbonates catalyzed by large-pore zeolites has been reported. Reaction of thiophenol with ethylene carbonate in the presence of the Na-X zeolite catalyst gave the highest yield of 2-(phenylthio)ethanol (100%), while reaction with propylene carbonate a highest yield of regioselective product 1-(phenylthio)propan-2-ol was obtained (97%). Enantiomerically pure 1,2-propylene carbonate gave highly regioselective and stereospecific phenylthiopropanol, demonstrating that original chirality of propylene carbonate is retained. A plausible mechanism has been proposed for zeolite-catalyzed transformation involving a chemoselective nucleophilic attack of thiophenoloxide ion onto the less-substituted carbon of cyclic carbonate. The Na-X zeolite catalyst is recyclable and provides advantages of green chemistry approach to the synthesis of β-hydroxy sulfides without the use of any solvent.     

Synthesis of propylene carbonate from urea and 1,2-propylene glycol over ZnO/NaY catalyst

Propylene carbonate (PC) was produced from 1,2-propylene glycol (1,2-PG) and urea in a continuous-flow fixed bed reactor over heterogeneous ZnO catalyst supported on NaY. Among different ZnO loadings of ZnO/NaY catalysts, 5 wt% ZnO loadings of ZnO/NaY showed the highest activity. Characterization and reaction results indicated that the catalysts with a balanced strength of acid and base sites performed well for the synthesis of propylene carbonate from urea and 1,2-PG.     

Stability of intermediates in the glycerol hydrogenolysis on transition metal catalysts from first principles

The hydrogenolysis reaction catalyzed by a transition metal solid catalyst is a potential way to transform glycerol to 1,2-propylene glycol or 1,3-propylene glycol, two important chemicals. We explore the thermodynamic profile of this reaction from first principle simulation, comparing Ni, Rh and Pd catalysts modeled by (111) surfaces. The stability of adsorbed reactants, dehydrated intermediates, and hydrogenated propylene glycol is compared, with a special focus on the factors controlling the selectivity of the reaction. From a global thermodynamic view point, the formation of 1,2-propylene glycol is favored, and in addition the most stable intermediates in the gas phase (acetol and 1,2-aldol) lead to the formation of this product. The metal catalyst has three roles. First it stabilizes the dehydrated intermediates and renders the dehydration more exothermic. Second, the adsorption on the surface modifies the relative stability of the dehydrated intermediates, with implications on the reaction selectivity. Third it catalyses the hydrogenation step, leading to propylene glycol.     

Pd/C: an efficient and heterogeneous protocol for oxidative carbonylation of diols to cyclic carbonate

The present protocol involves highly efficient and practical approach for the synthesis of cyclic carbonate via oxidative carbonylation of diols, glycerol, and its derivatives using Pd/C as a heterogeneous, inexpensive, and recyclable catalyst. The effect of various reaction parameters, such as solvent, base, time, and temperature was investigated and applied for the synthesis of value added cyclic carbonates in a good to excellent yield within shorter reaction time. The developed catalytic system circumvents the use of ligand and dehydrating agent with an additional advantage of palladium catalyst recovery and reuse for up to four consecutive cycles.     

绿色催化二氧化碳、炔丙醇和亲核试剂的三组分反应

近些年来,将CO₂转化为高附加值化学品受到广泛关注。其中,CO₂、炔丙醇和亲核试剂的三组分反应可用于制备用途广泛的羰基化合物,该方法具有步骤经济性、原子经济性等优点。由于CO₂分子具有热力学稳定性和动力学惰性,多数CO₂参与的化学反应在热力学上不支持。然而,CO₂、炔丙醇和双亲核试剂三组分反应是热力学有利的CO₂转化反应,实现了邻二醇或氨基醇和CO₂到环状碳酸酯以及2-噁唑啉酮的高效转化。本综述旨在于总结并讨论近年来CO₂、炔丙醇和亲核试剂三组分反应制备多种羰基化学物的主要进展。     

固体氧化物催化剂酸碱性质对 1,2-丙二醇转化反应的影响

 采用 X 射线衍射、热重、NH3 程序升温脱附、CO2 程序升温脱附等手段研究了 Al2O3, MgO, CaO 和 KNO3 改性 MgO 催化剂的结构和酸碱性质, 并在固定床反应装置上考察了上述催化剂气相催化转化 1,2-丙二醇反应性能. 结果表明, 催化剂表面的酸碱性对 1,2-丙二醇气相转化反应的产物分布有显著影响. Al2O3 催化剂上的产物以丙醛和丙酮为主; MgO 催化剂上的主要产物为丙酮醇; CaO 催化剂上丙酮和丙烯醇选择性相对较高; KNO3 改性 MgO 催化剂上环氧丙烷选择性显著升高. 结合不同催化剂酸碱性质及其反应结果, 提出了 1,2-丙二醇气相转化的 6 个主要反应途径, 明确了各反应途径与催化剂酸碱性质的关系.     

Effect of Solvent Diols and Ligands on the Properties of Sol-Gel Alumina-Silicas

Amorphous alumina-silicas were prepared from a tetra-alkoxysilane and anhydrous aluminum trichloride or an aluminum alkoxide by a sol-gel process using 2-methyl-2,4-pentanediol, pinacol, 1,2-propanediol, 2,3-butanediol or ethylene glycol as the solvent or complexing agent, and the effect of diols and alkoxy groups on the physical and chemical properties of the alumina-silicas was examined. When the diol or the alkoxy group was bulky, the alumina-silicas had relatively larger micropores, a larger pore volume and higher surface areas. In the conversion of methanol catalyzed by the alumina-silicas, the bulkier diols and alkoxides gave catalysts that produced dimethyl ether in higher yield and hydrocarbons in lower yield. Thus, when ethylene glycol was used as the diol, the best catalyst for the production of hydrocarbons, especially the production of olefins such as ethylene, propylene and butene, was obtained. Furthermore, in comparison with alumina-silica prepared by a traditional kneading process, it was found that the sol-gel alumina-silica could efficiently convert methanol to dimethyl ether and hydrocarbons, but the material prepared by kneading had a very low conversion of methanol to other compounds.