共查询到20条相似文献,搜索用时 140 毫秒
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研究了反应温度,反应时间,氧气流量,催化剂用量,底物浓度对氧气液相氧化邻硝基甲苯制邻硝基苯甲醛的影响。发现在反应温度0℃-5℃,反应时间4.5小时,氧气流量30ml/min,催化剂加入2g/l,物料溶剂体积比在6.50时,可获得61.44%的转化率及30.74%的收率。 相似文献
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氧气液相氧化对硝基甲苯制备对硝基苯甲酸反应条件的研究 总被引:1,自引:0,他引:1
研究了反应压力,反应温度和反应时间对氧气液相氧化对硝基甲苯合成对硝基苯甲酸收率的影响。发现以甲醇或苯/甲醇为溶剂,在50℃,2.0mpa氧压下反应48小时可分别获得89.1%和79.3%的对硝基苯甲酸收率,且对硝基苯甲酸粗品纯度达93%以伞? 相似文献
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研究了一种在乙醇水溶液中,以取代铁卟啉为仿生催化剂,催化氧气氧化邻硝基甲苯绿色合成邻硝基苯甲酸的新方法。考察了不同取代铁卟啉催化剂对反应活性和主产物选择性的影响,发现所有铁卟啉均有活性,且卟啉环外取代基从强给电子基(—OH)到吸电子基(—NO2)变化时,其催化活性(原料转化率)变化不大,但对主产物的选择性影响却很明显,其中T(p-Cl)PPFeCl的催化活性和选择性均为最好,含最强给电子基(—OH)或最强吸电子基(—NO2)的金属卟啉对主产物的选择性均最低。考察了溶剂中乙醇的体积分数对反应的影响,发现在乙醇浓度为80 % 时,产物的选择性最高。系统地考察了碱浓度、氧气压力、温度、时间、原料初始浓度等因素对反应的影响,找到了优化的工艺条件。发现以T(p-Cl)PPFeCl为催化剂,当乙醇浓度为80%、碱浓度为3. 75 mol·L-1时,在2. 0 MPa、55℃条件下反应12 h,邻硝基甲苯的转化率达到79. 7%,邻硝基苯甲酸的选择性和收率分别可达95. 8% 和76. 3%。 相似文献
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Zhiyong Tang Lianyuan Wang Jichu Yang 《European Journal of Lipid Science and Technology》2007,109(6):585-590
Transesterification of the crude Jatropha curcas L. oil catalyzed by micro‐NaOH in supercritical/subcritical methanol was studied. The effects of various reaction variables such as the catalyst content, reaction temperature, reaction pressure and the molar ratio of methanol to oil on the conversion of crude Jatropha curcas L. oil to biodiesel were investigated. The results showed that even micro‐NaOH could noticeably improve this reaction. When NaOH was added from 0.2 to 0.5 to 0.8 wt‐‰ of triacylglycerols, the transesterification rate increased sharply; when the catalyst content was further increased, the reaction rate was just poorly improved. It was observed that increasing the reaction temperature had a favorable influence on the methyl ester yield. For the molar ratio ranging from 18 to 36, the higher the molar ratio of methanol to oil was charged, the faster the transesterification rate seemed. At the fixed stirring rate of 400 rpm, when the catalyst content, reaction temperature, reaction pressure and the molar ratio of methanol to oil were developed at 0.8 wt‐‰ NaOH, 523 K, 7.0 MPa and 24 : 1, respectively, the methyl ester yield could reach 90.5% within 28 min. Further, the kinetics of this reaction was involved and the results showed that it was a pseudo‐first‐order reaction whose apparent activation energy was 84.1 kJ/mol, and the pre‐exponential factor was 2.21×105. 相似文献
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A new process, coupling reaction and azeotropic distillation was proposed for the synthesis of glycerol carbonate (GC) from glycerol (G) and dimethyl carbonate (DMC). The bench scale experimental investigation was systematically conducted for this new process. With calcium oxide (CaO) as the solid catalyst, the high yield of glycerol carbonate can be obtained at a low molar ratio of dimethyl carbonate to glycerol with the method of coupling reaction and azetropic distillation. The effect of azeotropic agents on glycerol carbonate yield was explored, and indicated that benzene was the most effective azeotropic agent. The effects of the process parameters, tower height, amount of added benzene, final temperature of tower bottom and reflux ratio were investigated. Glycerol carbonate yield can be as high as 98% under the conditions at molar ratio of dimethyl carbonate to glycerol 1:1, final temperature of tower bottom 85 °C, 1.5 mass ratio of added benzene to that in the azeotrope with methanol theoretically produced and reflux ratio 4. By continuously removing methanol from reaction system with the method of coupling reaction and azeotropic distillation, the yield of glycerol carbonate can be retained at high level using the recycled catalyst. 相似文献
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Transesterification of the crude oil of rapeseed with NaOH in supercritical and subcritical methanol
Transesterification reaction of the crude oil of rapeseed with supercritical/subcritical methanol in the presence of a relatively low amount of NaOH was successfully carried out, where soap formation didn't occur. The main factors affecting the methyl ester yield during the transesterification reaction were the catalyst content, the reaction temperature, the molar ratio of alcohol to oil and the water content. High methyl ester yield and fast reaction rate could be obtained even if the reaction pressure was relatively low. In addition, kinetics of the transesterification reaction was also discussed. 相似文献
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以1,4-二氧六环为溶剂,NaOH为催化剂,对废弃的含4,4'-联苯二酚(BP)单元的芳香族聚酯型液晶高分子(LCP),在常压下通过水解反应回收制备4,4'-联苯二酚进行了研究。在反应混合物的质量比m(LCP)∶m(溶剂)∶m(H2O)∶m(NaOH)=1∶4∶1.5∶0.6的最优条件下,液晶高分子的水解率达97%以上。通过在水解液中加入HCl并控制其pH在8.5,沉淀得到4,4'-联苯二酚。4,4'-联苯二酚经水洗、干燥、甲醇重结晶后,液相色谱检测其纯度可达99.9%,从废弃液晶高分子中制备4,4'-联苯二酚的收率为70%。 相似文献
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以NaOH、正硅酸乙酯和乙醇为原料,经溶胶-凝胶法制备新型固体碱催化剂(Na/SiO2),用于催化大豆油与甲醇的酯交换反应制备生物柴油,研究催化剂焙烧温度、n(NaOH)∶n(SiO2)、n(甲醇)∶n(大豆油)、催化剂用量和反应时间对产率的影响以及催化剂的稳定性。结果表明,固体碱催化剂Na/SiO2在大豆油与甲醇的酯交换反应中具有较高的催化活性,在催化剂焙烧温度600 ℃、n(NaOH)∶n(SiO2)=2∶1、n(甲醇)∶n(大豆油)=15∶1、催化剂用量为大豆油质量的7%和反应时间3 h的条件下,脂肪酸甲酯产率可达97.42%,催化剂在稳定性试验中呈现出优良的稳定性。 相似文献
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