Simultaneous Synthesis of Dimethyl Carbonate and Poly（ethylene terephthalate） Using Alkali Metals as Catalysts

Dimethyl carbonate （DMC） and poly（ethylene terephthalate） was simultaneously synthesized by the transesterification of ethylene carbonate （EC） with dimethyl terephthalate （DMT） in this paper. This reaction is an excellent green chemical process without poisonous substance. Various alkali metals were used as the catalysts. The results showed alkali metals had catalytic activity in a certain extent. The effect of reaction condition was also studied. When the reaction was carded out under the following conditions： the reaction temperature 250℃, molar ratio of EC to DMT 3 ： 1, reaction time 3h, and catalyst amount 0.004 （molar ratio to DMT）, the yield of DMC was 68.9%.     

生物转化植物纤维产酒精的研究进展

植物纤维是潜在的可再生资源，利用微生物对其进行降解、转化以实现工业化低成本生产，已成为研究的热点。从生物方法角度对植物纤维为原料产酒精的3个阶段：原料预处理、纤维素酶糖化和发酵进行全面的阐述，包括微生物及其作用机理和处理工艺等方面的内容。     

Ethanolysis of rapeseed oil: Quantitation of ethyl esters,mono-, di-, and triglycerides and glycerol by high-performance size-exclusion chromatography

High-performance size-exclusion chromatography (HPSEC) was used to evaluate the influence of different variables affecting the transesterification of rapeseed oil (RSO) with anhydrous ethanol and sodium ethoxide as catalyst. The effect of temperature, ethanol/RSO molar ratio, catalyst concentration, and time can be interpreted by observing the variations of the reaction medium composition. HPSEC has made the quantitation of ethyl esters, mono-, di-, and triglycerides and glycerol possible. The best results for laboratory-scale reactions were obtained at 80°C with a 6:1 molar ratio of EtOH/RSO and 1% of NaOEt by weight of RSO.     

Lipase PS-catalyzed transesterification of citronellyl butyrate and geranyl caproate: Effect of reaction parameters

Pseudomonas sp. lipase PS was immobilized by adsorption and tested for its ability to catalyze the synthesis of citronellyl butyrate and geranyl caproate by transesterification in n-hexane. The reaction parameters investigated were: enzyme load, effect of substrate concentration, added water, temperature, time course, organic solvent, pH memory, and enzyme reuse. Yields as high as 96 and 99% were obtained for citronellyl butyrate and geranyl caproate, respectively, with 300 units (approx. 15% w/w of reactants) of lipase PS. Increasing amounts of terpene alcohol inhibited lipase activity, while excess acyl donor (triacylglycerol) concentration enhanced ester production. Optimal yields were obtained at temperatures from 30–50°C after 24-h incubation time. Yields of 90 and 99% were obtained for citronellyl and geranyl esters, respectively, with 2% added water. Solvents with log P values ≥ 2.5 showed the highest conversion yields. pH 7 and 6–8 seemed to be ideal for citronellyl butyrate and geraniol caproate, respectively. The lipase remained active after reusing 12 times.     

响应面法优化鸡脂酶解工艺

通过单因素实验考察了脂肪酶、乳化剂、反应温度、pH值、反应时间、酶添加量及摇床转速等影响鸡脂脂肪酶水解的因素.采用响应面分析法对反应温度、酶添加量、pH值和反应时间等工艺参数进行了优化研究.结果表明,二次多项式模型符合实验数据.反应获得较优酸值时反应参数条件为：温度46.6℃,加酶量0.5%,pH值6.4,反应时间4.33 h.     

碱性蛋白酶水解豌豆蛋白的条件优化

采用碱性蛋白酶对豌豆蛋白进行水解,通过单因素试验,分析了温度、pH、酶与底物浓度比、底物浓度、水解时间对水解度影响,并在单因素试验的基础上,利用响应面分析法,优化确定的豌豆蛋白酶水解最佳条件为:温度54.5℃,pH7.9,酶与底物浓度比1.5%,底物浓度2.9%,水解时间3.0 h,最佳酶水解条件下的水解度为13.42%.     

G8r菌产人参皂苷糖苷酶的酶性质及酶水解作用

对由Absidia sp.G8r菌产的人参皂苷糖苷酶(Glc8)进行了分离纯化,并对其酶性质和酶水解作用进行了研究.结果表明,该酶的分子质量约为72 ku,酶反应的最适温度和pH分别为30 ℃和5.0,在20～60 ℃、pH 3.0～7.0条件下稳定性较好.该酶水解人参皂苷Rb1生成人参皂苷C-K,水解过程是分步进行的...     

碱性[Bmim]Im离子液体催化合成DEHC

研究了在1-丁基-3-甲基咪唑阳离子与咪唑阴离子搭配的碱性[Bmim]Im离子液体催化作用下,碳酸二甲酯(DMC)与异辛醇(EHOH)通过两步酯交换法制备碳酸二异辛酯(DEHC)的合成工艺.确定了合成DEHC的最佳反应条件为:催化剂用量为原料总质量的2.0%,醇酯摩尔比为4:1,一步反应温度90℃,反应时间2 h,二步...     

Biodiesel development from high acid value polanga seed oil and performance evaluation in a CI engine

Non-edible filtered high viscous (72 cSt at 40 °C) and high acid value (44 mg KOH/gm) polanga (Calophyllum inophyllum L.) oil based mono esters (biodiesel) produced by triple stage transesterification process and blended with high speed diesel (HSD) were tested for their use as a substitute fuel of diesel in a single cylinder diesel engine. HSD and polanga oil methyl ester (POME) fuel blends (20%, 40%, 60%, 80%, and 100%) were used for conducting the short-term engine performance tests at varying loads (0%, 20%, 40%, 60%, 80%, and 100%). Tests were carried out over entire range of engine operation at varying conditions of speed and load. The brake specific fuel consumption (BSFC) and brake thermal efficiency (BTE) were calculated from the recorded data. The engine performance parameters such as fuel consumption, thermal efficiency, exhaust gas temperature and exhaust emissions (CO, CO₂, HC, NO_x, and O₂) were recorded. The optimum engine operating condition based on lower brake specific fuel consumption and higher brake thermal efficiency was observed at 100% load for neat biodiesel. From emission point of view the neat POME was found to be the best fuel as it showed lesser exhaust emission as compared to HSD.     

MoO3/SO4^2- —TiO2 catalyst for transesterification of dimethyl cabonate with phenol

A new MoO3/SO4^2- -TiO2 catalyst was prepared by a conventional impregnation of SO42-/TiO2 as carrier with an aqueous solution of ammonium molybdate and used for the synthesis of transesterification of dimethyl carbonate （DMC） with phenol.A series of MoO3/SO42--TiO2 catalysts with different MoO3 loadings were investigated and characterized using X-ray diffraction （XRD）,Fourier transform infrared spectrometer （FTIR）,NH3-temperature programmed desorption （NH3-TPD） and X-ray photoelectron spectroscopy （XPS）.The results show that MoO3 loading is related to the activity of transesterification reaction.With the increase of MoO3 loading,the activity of transesterification reaction increases.The sulfur species in the catalyst have an influence on the molybdenum species,and lead to an increase in the electropositive of molybdenum,which promotes the catalytic activity of MoO3/SO42--TiO2.Among the series of catalysts prepared,MoO3/SO42--TiO2 with 10% MoO3 and 823 K calcinated is found to be the most active catalyst for transesterification reaction.Under the reaction conditions of 453 K and 12 h,the conversion of DMC is 30.5 %,and the yields of MPC and DPC reach 21.2 % and 8.7 %,respectively.