Conversion of phenylacetonitrile in supercritical alcohols within a system containing small volume of water

The reaction of phenylacetonitrile in supercritical methanol and ethanol in a system containing a small volume of water was studied. The effects of various operating conditions, such as reaction temperature, reaction time, the mole ratio of phenylacetonitrile/water/methanol or ethanol on the product yield were systematically investigated. The optimal yield of methyl phenylacetate for phenylacetonitrile in supercritical methanol in a system containing a small volume of water was 70 % at 583 K and 2.5 h. The optimal yield of ethyl phenylacetate for phenylacetonitrile in supercritical ethanol with a small volume of water was 80 % at 583 K and 1.0 h. At the same time, a feasible mechanism was proposed for phenylacetonitrile in supercritical methanol and ethanol in a system containing a small volume of water.     

Novel process for synthesis of 1,1,3,3-tetrabutyl-1-methoxy-3-isocyanatodistannoxane

A new process for synthesis of 1,1,3,3-tetrabutyl-1-methoxy-3-isocyanatodistannoxane (TBMI) from dibutyltin oxide (DSnO), methyl carbamate and methanol was proposed. The structure of the TBMI was confirmed by UV-Vis, elemental analyses, FTIR and HPLC. The effects of various conditions, such as reaction temperature, pressure, reaction time, molar ratio of the reactants and the stirring speed were investigated in the terms of TBMI yield. The experimental results indicated that the optimal reaction conditions were the molar ratio of methyl carbamate:DSnO of 2:1, the reaction time of 3 h, the reaction temperature of 433 K, the methanol:DSnO molar ratio of 2:1, the initial pressure of 0.4 MPa and the stirring speed of 1000 rpm, respectively. TBMI yield of 96.9% was obtained in the optimal reaction conditions. This process shows some advantages like easy to operate, higher yield, shorter reaction time and lower cost.     

Biodiesel fuel production by the transesterification reaction of soybean oil using immobilized lipase

The enzymatic alcoholysis of soybean oil with methanol and ethanol was investigated using a commercial, immobilized lipase (Lipozyme RMIM). The effect of alcohol (methanol or ethanol), enzyme concentration, molar ratio of alcohol to soybean oil, solvent, and temperature on biodiesel production was determined. The best conditions were obtained in a solvent-free system with ethanol/oil molar ratio of 3.0, temperature of 50 degrees C, and enzyme concentration of 7.0% (w/w). Three-step batch ethanolysis was most effective for the production of biodiesel. Ethyl esters yield was about 60% after 4 h of reaction.     

亚/超临界乙醇液化秸秆纤维素解聚反应研究与机理初探

利用间歇式高压反应釜,在反应温度200～330 ℃、乙醇用量0～150 mL条件下,考察了亚/超临界乙醇直接液化秸秆纤维素的解聚行为,并初步探讨了其液化机理。结果表明,反应温度、乙醇用量和反应停留时间对秸秆纤维素的液化均有显著影响,反应温度由200 ℃升高至330 ℃,重油和气体收率分别增加了12.55%、28.83%;乙醇用量增加,反应压力随之升高,乙醇进入超临界状态,残渣和气体收率相比单纯热裂解分别降低11.10%和8.44%。通过GC/MS、FT-IR分析生物油组分和残渣特性,表明秸秆纤维素在亚/超临界乙醇中断键裂解,且酮类和乙酯类化合物是生物油的主要成分。     

Enzymatic Synthesis of Biodiesel via Alcoholysis of Palm Oil

The enzymatic alcoholysis of crude palm oil with methanol and ethanol was investigated using commercial immobilized lipases (Lipozyme RM IM, Lipozyme TL IM). The effect of alcohol (methanol or ethanol), molar ratio of alcohol to crude palm oil, and temperature on biodiesel production was determined. The best ethyl ester yield was about 25 wt.% and was obtained with ethanol/oil molar ratio of 3.0, temperature of 50 °C, enzyme concentration of 3.0 wt.%, and stepwise addition of the alcohol after 4 h of reaction. Experiments with 1 and 3 wt.% of KOH and 3 wt.% of MgO were carried out to compare their catalytic behavior with the enzymatic transesterification results. The commercial immobilized lipase, Lipozyme TL IM, showed the best catalytic performance.     

Ultrasound-assisted synthesis of ethyl hexanoate using heterogeneous catalyst: Optimization using Box-Behnken design

Ultrasound-assisted synthesis of ethyl hexanoate was studied in a solvent-free system using Amberlyst-15 as a heterogeneous catalyst. The effect of reaction parameters was evaluated by employing Box Behnken Design. Maximum conversion was obtained as 83.9% experimentally with operating temperature 60 °C, ethanol to hexanoic acid molar ratio as 3, 60% duty cycle, 11% catalyst loading, 10% molecular sieves, and 80 W input power which were optimized through one parameter at a time. The optimal conditions for maximum 86.66% conversion obtained by Box Behnken Design operated in Response Surface Methodology were 62.8 °C temperature, 3.31 ethanol to hexanoic acid molar ratio, and 51.58% duty cycle. The absence of external mass transfer resistances was proved by evaluating Mear's criterion. Thiele modulus and effectiveness factor were determined to study the influence of internal mass transfer resistance qualitatively. The kinetics of the heterogeneous reaction was modeled using Langmuir-Hinshelwood model. The activation energy was calculated as 24.61 kJ/mol.     

微波辅助法合成Hantzsch酯

以芳香醛、乙酰丙酮及碳酸氢铵为原料,固载路易斯酸蒙脱土为催化剂,通过微波辅助法催化合成了5个Hantzsch酯类化合物,其结构经¹H NMR和IR确证。考察了催化剂、溶剂、温度、时间和氮源对产率的影响。结果表明：反应温度60 ℃,微波辐照时间10 min, n(芳香醛) :n(乙酰乙酸乙酯) :n(碳酸氢铵)=2.0:2.0:1.0,氯化镍固载蒙脱土为催化剂（10%）,产率高达97.8%。     

Comparison and optimisation of biodiesel production from <Emphasis Type="Italic">Jatropha curcas</Emphasis> oil using supercritical methyl acetate and methanol

In this study, biodiesel has been successfully produced by transesterification using non-catalytic supercritical methanol and methyl acetate. The variables studied, such as reaction time, reaction temperature and molar ratio of methanol or methyl acetate to oil, were optimised to obtain the optimum yield of fatty acid methyl ester (FAME). Subsequently, the results for both reactions were analysed and compared via Response Surface Methodology (RSM) analysis. The mathematical models for both reactions were found to be adequate to predict the optimum yield of biodiesel. The results from the optimisation studies showed that a yield of 89.4 % was achieved for the reaction with supercritical methanol within the reaction time of 27 min, reaction temperature of 358°C, and methanol-to-oil molar ratio of 44. For the reaction in the presence of supercritical methyl acetate, the optimum conditions were found to be: reaction time of 32 min, reaction temperature of 400°C, and methyl acetate-to-oil molar ratio of 50 to achieve 71.9 % biodiesel yield. The differences in the behaviour of methanol and methyl acetate in the transesterification reaction are largely due to the difference in reactivity and mutual solubility of Jatropha curcas oil and methanol/methyl acetate.     

布洛芬-扑热息痛孪药的合成

以布洛芬（IPF）和扑热息痛（PCM）为原料,无水丙酮和乙酸乙酯为溶剂,二环己基碳二亚胺（DCC）为脱水剂,4-二甲氨基吡啶（DMAP）为催化剂,合成了布洛芬-扑热息痛孪药（PHI）,以重结晶法对目标产物进行纯化,产物结构经IR和1H NMR确定。 探讨了原料比例、脱水剂用量、催化剂用量、反应时间和溶媒用量对目标物产率的影响,并采用正交试验筛选最优合成工艺,最终确定的最优反应条件为:n(PCM)∶n(IPF)=1∶1.5,催化剂的最佳用量为布洛芬质量的10%,反应时间为8 h,溶媒体积为70 mL（V(乙酸乙酯)∶V(丙酮)=1∶1）,在该条件下,目标物PHI的产率为66.53%。     

氧化铅在氨基甲酸乙酯与乙醇合成碳酸二乙酯反应中的催化作用

研究了氧化铅在氨基甲酸乙酯(EC)与乙醇反应合成碳酸二乙酯(DEC)中的催化作用.结果表明,氧化铅具有很好的稳定性,重复使用5次,其催化活性无明显下降.回收的催化剂为立方晶相金属Pb和斜方晶相PbO2的混合物,结合反应结果可认为,该混合物为反应的活性组分.结果还发现,PbO与DEC反应是PbO被还原为Pb的主要原因.     

聚6-羟基己酸碱性条件下的水解反应研究

探究了碱性条件下聚6-羟基己酸水解反应的机理和最优化工艺条件。实验过程中选用碱度较大的氢氧化钠及碱度较小的碳酸氢钠作为反应试剂。研究表明:碱度不同,其反应机理,反应工艺条件亦不同。碱度越大,OH~-浓度越大,亲核基团[OH~-]直接进攻聚6-羟基己酸的酯基结构,使酯基键发生断裂反应,生成小分子的6-羟基己酸;反应工艺条件缓和,在100℃的集热式恒温加热磁力搅拌器中既可完全解聚。碱度大的氢氧化钠参与反应的最优化工艺条件:氢氧化钠/聚6-羟基己酸摩尔比为4.4,乙二醇/聚6-羟基己酸摩尔比为6.5,水用量100g,催化剂0.1g,反应时间2h,反应温度100℃条件下,6-羟基己酸产率达到84.07%;碱度小的碳酸氢钠钠参与反应的最优化工艺条件:碱度越小,OH~-浓度越小,在反应初期亲核基团[-OCH_2CH_2OH]占主导地位,发生醇解反应的概率大,整个反应体系为醇解反应与水解反应相互促进进行;反应工艺条件苛刻,须在180℃密闭高压釜中完全解聚。碳酸氢钠/聚6-羟基己酸摩尔比为1.1,乙二醇/聚6-羟基己酸摩尔比为3,水用量100g,催化剂0.1g,反应时间1h,反应温度180℃~190℃条件下,6-羟基己酸产率达到90.38%。在整个反应系统中,乙二醇作为溶剂来使用。     

铌酸催化液相合成乙酸乙酯

报道了铌酸催化乙醇与乙酸的液相酯化反应考察了反应温度、催化剂用量、酸醇比、反应时间对产品乙酸乙酯经的影响。在优化条件下,产品收率棕达８８．０％,选择性为１００％,同时我们采用自制间式反应,对催化剂的稳定性进行了考察,发现铌酸在该实验条件下,能保持较高的稳定性和较高的催化活性。     

负载型磷钨酸催化剂的制备及催化合成ＥＴＢＥ的性能研究

采用水热法合成纯硅介孔分子筛Si-MCM-41, 并用浸渍法将磷钨酸(PWA)负载到介孔分子筛Si-MCM-41上, 制得了磷钨酸负载量不同的催化剂x%PWA/MCM-41. 利用XRD, FT-IR, Py-IR, BET, TEM对载体和催化剂进行分析. 结果表明, 负载后的PWA颗粒粒径明显减小, 粒径约为10个纳米, PWA在载体表面实现了均匀分布, 通过叔丁醇和乙醇在高压反应釜内生成乙基叔丁基醚的反应测试催化剂的催化性能. 结果表明, 负载型催化剂和纯PWA相比, 前者使叔丁醇(TBA)的转化率、ETBE的选择性有很大提高, 当磷钨酸负载量为30%时TBA的转化率最大. 最优的催化剂制备及反应条件是: 载体550 ℃煅烧脱模, PWA负载量为30%, 催化剂煅烧温度为300 ℃, 醚化反应温度为120 ℃, 乙醇与叔丁醇的摩尔比为2∶ 1, 催化剂的用量为1.4 g.     

细胞粘附位点RGD前体二肽的化学合成与酯化

摘要利用一种新颖的化学法合成了细胞粘附位点RGD前体二肽GD(Gly-Asp). 并利用ROH-HCl法进一步完成了GD二肽乙酯化和甲酯化. 考察了GD二肽对乙醇/甲醇的摩尔比,  反应温度和反应时间对酯化收率的影响, 使GD二肽酯化的条件得到了优化, GD二肽对乙醇/甲醇的摩尔比为1∶40,  反应温度30℃,  反应时间1~2.5 h,   最大收率为80%~85%. 利用质谱分析法确证了两种GD二肽酯为Gly-Asp-(OEt)2 和Gly-Asp-(OMe)2.     

水/有机溶剂双相体系中色氨酸合成酶酶法合成L-色氨酸

在水/有机溶剂双相体系中,利用重组大肠杆菌DM206 [pET28a-trpBA/BL21 (DE3)]色氨酸合成酶催化L-丝氨酸和吲哚合成了L-色氨酸.考察了有机溶剂、有机相乙酸乙酯体积分数、反应温度、水相pH、底物L-丝氨酸与吲哚摩尔比、底物L-丝氨酸浓度、表面活性剂和酶添加量对色氨酸合成酶酶活的影响.结果表明,酶...     

苯胺与氨基甲酸甲酯合成苯氨基甲酸甲酯反应研究

以无水氯化锌为催化剂,考察了温度、时间、催化剂含量及原料配比等条件对合成反应的影响,确定了最优化反应条件,并初步探讨了反应机理.最佳反应条件下MPC收率可达89.90%,选择性为99.76%.     

Improved Enzyme Stability in Lipase-Catalyzed Synthesis of Fatty Acid Ethyl Ester from Soybean Oil

In this work, we describe the optimization of the ethanolysis of soybean oil by the enzyme Lipozyme™ TL-IM in the lipase-catalyzed biodiesel synthesis and the improvement of the enzyme stability over repeated batches. The studied process variables were: reaction temperature, substrate molar ratio, enzyme content, and volume of added water. Fractional factorial design was used to analyze the variables so as to select those with higher influence on the reaction and then perform a central composite design to find the optimal reaction conditions. The optimal conditions found were: temperature, 26 °C; substrate molar ratio, 7.5:1 (ethanol/oil); enzyme content, 25% in relation to oil weight; and added water, 4% in relation to oil weight. Under these conditions, the yield conversion obtained was 69% in 12 h. The enzyme stability assessment in repeated batches was carried out by washing the immobilized enzyme with different solvents (n-hexane, water, ethanol, and propanol) after each batch. In the treatment with n-hexane, around 80% of the enzyme activity still remains after seven cycles of synthesis, suggesting its economical application on biodiesel production.     

超临界CO2+EtOH+CO+H2四元体系压力和温度变化规律及超临界性质的研究

在5～11MPa的范围内,利用恒容静态平衡法详细考察了CO2密度在0.542～0.590g/cm3范围的不同组成的超临界CO2+EtOH+CO+H2四元体系的压力和温度的变化规律,并测定了相应的临界温度和临界压力.模拟了超临界丙烯氢甲酰反应体系的相行为.结果发现,CO+H2加入量的增多可明显改变超临界CO2+EtOH+CO+H2四元体系的超临界性质,主要表现为该体系的临界温度随着CO和H2摩尔分数的增加而线性降低,临界压力随着CO和H2摩尔分数的增加而线性增加.在相同的CO和H2组成下,超临界四元体系的压力随着体系温度的增加而线性增加,并且p-T线的斜率基本相同.在相同温度下超临界四元体系的压力随着体系中CO和H2摩尔分数的增加线性增加,并且不同温度时的变化率基本相同.     

Optimization of supercritical fluid extraction of geniposidic acid from plantain seeds using response surface methodology

The process parameters of supercritical CO₂ (SCCO₂) plus modifer for the extraction of geniposidic acid from plantain seeds were studied using a Box–Behnken design. The effects of independent variables, that is, ethanol concentration (0–70%, ethanol:water, v/v), extraction pressure (10–30 MPa), and temperature (50–80°C) on the yield of geniposidic acid were evaluated. Results indicated that the data could be well fitted to a second-order polynomial model. The effects of ethanol concentration and temperature, as well as the interaction between ethanol concentration and temperature were significant (p < 0.05). The yield (8.9 mg/g) of modified SCCO₂ extraction at optimal conditions was compared with that obtained by Soxhlet extraction or ultrasound assisted extraction.     

疏水双功能介孔固体酸的合成及其在乙酸乙酯酯化反应中的应用

通过水热合成法一步合成了具有不同疏水基团－CH₃ 、－(CH₃)₂ 和－(CH₃)₃的双功能介孔固体酸SBA-15-SO₃H－(CH₃)_x催化剂。通过X射线粉末衍射(XRD)、N₂吸脱附、元素分析等方法对催化剂进行了表征,并在乙酸乙酯酯化反应中进行催化性能评价。结果表明,随着疏水前驱体中甲基数的增加,样品的疏水性增强。SBA-15-SO₃H-(CH₃)_x催化剂的催化活性随着疏水性的增强而提高,而具有较强疏水性的材料SBA-15-SO₃H-(CH₃)₃在反应中具有较高的催化性能。以SBA-15-SO₃H-(CH₃)₃为催化剂,酯化反应的最优条件为：温度为120℃,乙酸与乙醇摩尔比为4∶1,催化剂质量分数为1 %,反应时间为1h。在此条件下,乙醇的转化率和乙酸乙酯的选择性分别为93%和100%。