环氧化蓖麻油的合成与表征

采用酸性氧化铝做催化剂对蓖麻油(CO)进行环氧化,探索环氧化反应时间、反应温度和催化剂等不同条件对蓖麻油环氧化的影响,从而优化出合适的反应条件,采用傅立叶变换红外光谱法(FTIR)、热重分析法(TG)对制备的环氧化蓖麻油(ECO)的结构和性质等进行了研究。利用盐酸-丙酮法对环氧化产物进行环氧值的测定,结果表明,在优化条件下,即采用酸性氧化铝做催化剂,H2O2的滴加温度保持在50～55℃,反应温度65℃,反应时间控制在11.5 h,同时加入尿素做稳定剂,可以提高H2O2的利用率,使环氧化蓖麻油的环氧值达到2.094×10-3mol/g。对ECO的性能表征结果表明,ECO粘度随着环氧值的增大而增大,随着温度的升高而降低。ECO在250℃前能够基本保持稳定,而后开始分解,有3个明显的热分解阶段:250～390℃、390～470℃、470～580℃,ECO的热稳定性较好。     

反应控制相转移催化原位过氧化氢环氧化丙烯反应

 以原位 H₂O₂ 为氧源, 在新型反应控制相转移催化剂 (RCPTC) 作用下丙烯环氧化反应中, 考察了反应温度、反应时间、H₂O₂ 浓度和催化剂浓度对反应性能的影响. 结果表明, 在适宜的反应条件下, RCPTC 催化剂循环使用 5 次后, 环氧丙烷产率仍维持在 85.6% 以上, 且催化剂循环反应 3 次后, 其组成趋于稳定.     

基于 H2/O2 等离子体和钛硅沸石的丙烯气相环氧化方法

 将 H₂/O₂ 非平衡等离子体现场产生的气态 H₂O₂和丙烯与耦合反应器中钛硅沸石 TS-1 直接接触, 实现了丙烯气相环氧化反应. 结果表明, 非平衡等离子体生成气态 H₂O₂ 的速率由介质阻挡放电的输入功率决定, 环氧丙烷的生成速率和选择性取决于钛硅沸石催化剂和反应条件. 在 H₂ 和 O₂ 进料流量分别为 170 和 8 ml/min, 介质阻挡放电输入功率为 3.5 W, 环氧化反应温度为 110 ^oC, 丙烯进料量为 18 ml/min, 催化剂用量为 0.8 g 的条件下, 生成环氧丙烷产率达 246.9 g/(kg•h)、环氧丙烷选择性和 H₂O₂ 有效利用率分别为 95.4% 和 36.1%, 反应 36 h 内未见催化剂失活.     

钙和钒离子对钒-溴过氧化物酶催化 H2O2 氧化环己烯反应的影响

 在溴化钾存在下, 大型海洋藻类珊瑚藻的钒-溴过氧化物酶 (V-BPO) 可在常温下催化 H₂O₂ 环氧化环己烯生成环氧环己烷. 通过用含 1.0 mmol/L 钒离子和 1.0 mmol/L 钙离子的缓冲溶液透析 V-BPO, 用恒流泵向反应体系中连续添加 H₂O₂, 并优化其它反应条件, 可提高该催化反应时空收率. 在优化的反应条件下, 产物环氧环己烷的时空收率为 4.79 g/(h•L), 对 H₂O₂ 的收率为 74%, 均比文献最高值提高了 78%.     

Pt掺杂氧化石墨烯在酸性介质中催化氧还原反应DFT研究

目前Pt基催化剂被公认为是最高效的氧还原催化剂.我们采用了密度泛函理论研究了Pt掺杂5种不同氧化石墨烯和完美石墨烯在酸性环境中的氧还原反应机理,计算了氧还原反应中间体O₂、O、OOH、OH、H₂O和H₂O₂在不同掺杂石墨烯上的吸附性能、反应步骤与反应相对能量变化.结果表明,氧化石墨烯在O₂的活化、中间体吸附、掺杂难度（缺陷形成能）、能带带隙以及在反应中相对能量的降低都优于完美石墨烯,我们的工作将有助于为将来在实验中选择和合成氧还原催化剂提供一定的理论指导意义.     

二苯并呫吨类化合物的环氧化反应研究

研究了二苯并呫吨类化合物的环氧化反应条件, 在室温、碱性条件下, 用廉价的H₂O₂作为环氧化剂对二苯并呫吨类化合物进行环氧化, 产率高达91%～98%, 是一种简便合成环氧二苯并呫吨类化合物的方法.     

环境友好催化氧化研究进展

综述了近来使用H₂O₂或O₂作为清洁的氧化剂催化氧化反应的研究进展,重点介绍了杂多酸盐催化剂、金属配合物催化剂及NHPI等催化剂的组成和催化效率,并探讨了各种催化剂的优缺点.     

酸性金属氧化物对锰铈氧化物催化剂脱硝温度窗口的调控作用

利用溶胶-凝胶法,采用三种酸性金属氧化物（氧化铌、氧化钨和氧化钼）对锰铈复合氧化物催化剂进行了改性. 测试了催化剂的氮氧化物选择性催化还原（SCR）活性,以筛选对应不同温度窗口的合适酸性氧化物改性剂. 同时评价了催化剂的NO氧化和NH₃氧化活性. 利用X射线衍射、BET比表面积测试、H₂程序升温还原、NH₃/NO_x程序升温脱附和NH₃/NO_x吸附红外光谱等手段对催化剂进行了表征. MnO_x-CeO₂催化剂表现出良好的低温（100-150 ℃）活性. 酸性金属氧化物的添加削弱了催化剂的氧化还原特性,从而抑制了NH₃的活化和NO₂辅助的快速SCR反应. 与此同时,相对高温（250-350 ℃）区NH₃的氧化也受到了抑制,B酸和L酸上的NH₃吸附得以增强. 因此,催化剂的SCR脱硝温度窗口向高温移动,改性效果Nb₂O₅ < WO₃ < MoO₃.     

Pt/TiO2催化剂上CO氧化反应动力学研究

利用沉积沉淀法制备了Pt/TiO₂催化剂, 将其在不同温度下焙烧, 以得到不同颗粒尺寸的Pt. 并将这些样品用于CO催化氧化反应以及反应动力学研究. 结果表明: 焙烧温度对催化剂有明显影响, Pt 颗粒尺寸随着焙烧温度的升高而增加; 与此同时, CO催化活性随焙烧温度的升高呈先增加后降低的趋势, 其中, 400℃焙烧的样品表现出最高的催化活性. 反应动力学结果表明, 催化剂上CO氧化反应表观速率方程为r=5.4×10^-7p_CO^0.17p_O2^0.36,说明在该催化剂上CO氧化遵循Langmuir-Hinshelwood机理. 同时, 对催化剂进行了CO化学吸附红外光谱和O₂化学吸附表征. 结果表明, 随着焙烧温度的升高, 催化剂上CO和O₂吸附量均呈现先升高后降低的趋势, 这与反应结果和反应动力学方程一致, 说明反应受到催化剂表面上CO和O₂吸附浓度的影响. 而在400℃焙烧的催化剂上, CO和O₂吸附量均最高, 因此其反应活性也最好. 这可能是焙烧过程影响了Pt 和TiO₂之间的相互作用引起的.     

焙烧温度对Mn/Al2O3-TiO2催化剂结构及氧化NO性能的影响

采用溶胶凝胶法和浸渍法制备10% Mn/Al₂O₃-TiO₂催化剂,借助TPO、XRD、O₂-TPD、Raman、XPS等手段,考察焙烧温度(450~650 ℃)对催化剂结构以及氧化NO性能的影响。TPO结果表明催化剂活性随焙烧温度的升高先增后减,其中焙烧温度为550 ℃时催化剂活性最好。XPS结果显示随着焙烧温度的升高(450~550 ℃),催化剂表面Mn³⁺的含量逐渐升高,与催化剂活性的强弱成对应关系,并且催化剂晶格氧含量下降,而表面化学吸附氧从40.9%增加到64.8%。Raman分析显示550 ℃焙烧时,催化剂表面存在丰富的Mn₂O₃活性物种,并且O₂-TPD分析也表明随着焙烧温度的升高,晶格氧向表面化学吸附氧流动,提高了化学吸附态氧物种的含量。这些结果表明Mn₂O₃可能是NO氧化起主要作用的活性Mn物种,释放更多的表面化学吸附氧物种,将有助于促进NO的催化氧化。     

环氧蓖麻油合成条件优化

在无溶剂条件下制备环氧蓖麻油,对参加环氧化反应的有机酸和催化剂进行选择,研究了反应时间和反应温度对产物环氧值的影响。通过正交实验对环氧化合成条件进行优化,结果表明,蓖麻油／乙酸／双氧水／磷酸（质量比）=1：0．15：0．8：0．01,反应温度50℃,反应时间3h,所得产品环氧值达6．95％,采用FT-IR和1HNMR方法对产品进行了表征。整个过程操作简单,反应时间短,反应条件温和。     

Development of completely bio‐based epoxy networks derived from epoxidized linseed and castor oil cured with citric acid

Bio‐based epoxy resins were synthesized from nonedible resources like linseed oil and castor oil. Both the oils were epoxidized through in situ method and characterized via Fourier transform infrared and ¹H‐NMR. These epoxidized oils were crosslinked with citric acid without using any catalyst and their properties compared with diglycidyl ether of bisphenol A‐epoxy. The tensile strength and modulus of epoxidized linseed oil (ELO) were found to be more than those of epoxidized castor oil (ECO)‐based network. However, elongation at break of ECO was significantly higher than that of both ELO and epoxy, which reveals its improved flexibility and toughened nature. Thermogravimetric analysis revealed that the thermal degradation of ELO‐based network is similar to that of petro‐based epoxy. Dynamic mechanical analysis revealed moderate storage modulus and broader loss tangent curve of bio‐based epoxies confirming superior damping properties. Bioepoxies exhibit nearly similar contact angle as epoxy and display good chemical resistant. The preparation method does not involve the use of any toxic catalyst and more hazardous solvents, thus being eco‐friendly.     

Optimization of Biodiesel Production from Castor Oil Using Response Surface Methodology

The short supply of edible vegetable oils is the limiting factor in the progression of biodiesel technology; thus, in this study, we applied response surface methodology in order to optimize the reaction factors for biodiesel synthesis from inedible castor oil. Specifically, we evaluated the effects of multiple parameters and their reciprocal interactions using a five-level three-factor design. In a total of 20 individual experiments, we optimized the reaction temperature, oil-to-methanol molar ratio, and quantity of catalyst. Our model equation predicted that the following conditions would generate the maximum quantity of castor biodiesel (92 wt.%): a 40-min reaction at 35.5 °C, with an oil-to-methanol molar ratio of 1:8.24, and a catalyst concentration of 1.45% of KOH by weight of castor oil. Subsequent empirical analyses of the biodiesel generated under the predicted conditions showed that the model equation accurately predicted castor biodiesel yields within the tested ranges. The biodiesel produced from castor oil satisfied the relevant quality standards without regard to viscosity and cold filter plugging point.     

Castor oil modified by epoxidation,transesterification, and acrylation processes: Spectroscopic characteristics

In the present study, castor oil (CO) was modified by epoxidation, transesterification, and acrylation processes. In situ epoxidation method was used to prepare epoxidized castor oil (ECO) in acetic acid with hydrogen peroxide in the presence of Seralite SRC-120 catalyst. Transesterified epoxidized castor oil was synthesized from the reaction of methanol in the presence of sodium methoxide catalyst. The acrylated epoxidized castor oil was synthesized from the reaction of ECO with acrylic acid containing hydroquinone. Chemical structures of modified CO were analyzed by Fourier transform infrared spectroscopy and proton nuclear magnetic resonance spectra analysis.     

Kinetics of the Production of Castor Oil Maleate through the Autocatalyzed Thermal Reaction and the Free Radical Reaction

Castor oil maleate is used in drying oils, water‐soluble paints, healthcare products, synthetic lubricants, and as a monomer in several polymers. This maleate can be produced by a direct autocatalyzed reaction between castor oil and maleic anhydride. However, the reaction rate can be increased using a free radical catalyst. In this work, the influence of the concentration of benzoyl peroxide (BPO) and temperature in the kinetics and productivity of castor oil maleate was studied. The optimal operating condition was found at 120°C, 1 mol of maleic anhydride/mol of castor oil, and 0.003 mol of BPO/mol of castor oil, yielding 90.0% of castor oil maleate in 90 min. A kinetic model was developed, and the model parameters were estimated both for the thermal autocatalyzed reaction and the free radical reaction.     

Synthesis, characterization, degradation of biodegradable castor oil based polyesters

A new family of castor oil based biodegradable polyesters was synthesized by catalyst free melt condensation reaction between two different diacids and castor oil with d-mannitol. The polymers synthesized were characterized by NMR spectroscopy, FT-IR and the thermal properties were analysed by DSC. The results of DSC show that the polymer is rubbery in physiological conditions. The contact angle measurement and hydration test results indicate that the surface of the polymer is hydrophilic. The mechanical properties, evaluated in the tensile mode, shows that the polymer has characteristics of a soft material. In vitro degradation of polymer in PBS solution carried out at physiological conditions indicates that the degradation goes to completion within 21 days and it was also found that the rate of degradation can be tuned by varying the curing conditions.     

Synthesis of environmental benign biolubricant from wild castor seed by reactive extraction and optimization

Castor oil alkyl esters are a possible biolubricant since they contain 90% hydroxyl fatty acid, which improves the oil's lubricity. Due to the limitations of the conventional approach, castor oil propyl ester (COPE) from wild castor seed was synthesized by reactive extraction. The factors influencing yield of reaction was optimised by response surface methodology to obtain a high yield. The influence of amount of catalyst, propanol to oil proportion, temperature, and rotating speed on castor oil propyl ester yield was investigated using a central composite design.The optimised reaction condition is propanol to oil molar proportion of 275: 1 with 1.5 wt% of catalyst loading at 90 °C and rotating speed of 450 rpm with COPE yield of 78.6% in 3hrs. Physico-chemical properties of alkyl esters were determined. COPE can be employed as a bioadditive to ultra-low sulphur diesel fuels due to its high lubricity.     

不同异氰酸酯固化的蓖麻油／酚氧树脂聚氨酯的力学性能

以ＢＦ３·ＯＥｔ２为催化剂，４，４－二羟基二苯基丙烷与环氧氯丙烷反应，生成端羟基的酚氧树脂（Ａ），Ａ与蓖麻油（Ｂ）混合，用３种异氰酸酯（ＴＤＩ、ＩＰＤＩ和ＨＤＩ）作为固化剂，制得交联聚氨酯。研究了这３种聚氨酯的力学性能及形态与组成和二异氰酸酯结构的关系；改变ＮＣＯ／ＯＨ摩尔比及Ｂ与Ａ的质量比，可以制得具有较好力学性能的聚氨酯材料。蓖麻油，酚氧树脂，聚氨酯，力学性能     

红花籽油的环氧化工艺

以双氧水为氧化剂,甲酸为氧载体,用强酸性阳离子交换树脂作催化剂,结合正交实验和单因素实验,确定红花籽油环氧化反应的最佳工艺条件为：在少量金属掩蔽剂乙二胺四乙酸二钠（EDTA）存在下,红花籽油、88%甲酸、30%双氧水和阳离子交换树脂的质量比为1∶0.244∶1.665∶0.035,在60 ℃下反应6 h,搅拌速度400 r/min,产品的环氧值可达到7以上。     

Optimization of biodiesel production from castor oil

The transesterification of castor oil with ethanol in the presence of sodium ethoxide as catalyst is an exceptional option for the Brazilian biodiesel production, because the castor nut is quite available in the country. Chemically, its oil contains about 90% of ricinoleic acid that gives to the oil some beneficial characteristics such as its alcohol solubility at 30°C. The transesterification variables studied in this work were reaction temperature, catalyst concentration and alcohol oil molar ratio. Through a star configuration experimental design with central points, this study shows that it is possible to achieve the same conversion of esters carrying out the transesterification reaction with a smaller alcohol quantity, and a new methodology was developed to obtain high purity biodiesel.