共查询到19条相似文献,搜索用时 171 毫秒
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盐地碱蓬油制备生物柴油工艺条件研究 总被引:2,自引:0,他引:2
以盐地碱蓬油为原料制备生物柴油.通过正交实验研究了反应温度、催化剂用量、醇油摩尔比、反应时间、搅拌强度等因素对生物柴油产率的影响.结果表明,在实验范围内各影响因素对生物柴油产率作用的大小依次为:搅拌强度>反应时间>催化剂用量>醇油摩尔比>反应温度.盐地碱蓬油制备生物柴油的最佳工艺参数为:搅拌强度为1 800 r/min,反应时间60min,催化剂KOH用量为盐地碱蓬油质量的1%,醇油摩尔比6/1,反应温度65℃.在该工艺条件下,生物柴油产率达到97.03%. 相似文献
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9-芴酮是重要的精细化工中间体,具有非常高的经济价值,主要由芴催化氧化制得.建立了芴液相氧化反应产物的气相色谱分析方法,解决了反应产物主要组分的定性和定量分析问题.以固体碱为催化剂,考察了催化剂种类、催化剂用量、溶剂种类、氧气流量、温度、反应时间和搅拌速率等因素对反应的影响,并进行了催化剂回收再利用实验.实验结果表明:NaOH是一种高性能、非均相催化剂,在适宜的条件下(催化剂与芴质量比为0.06:1、溶剂用量为30 mL、氧气流量为12 mL/min、反应温度为40 ℃、反应时间为4 h、搅拌速率为300 r/min),芴的转化率在99%以上,9-芴酮收率在95%以上. 相似文献
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以双液相萃取技术处理棉籽,在得到脱毒棉粕的同时得到含有高质量毛油的非极性相。以非极性相作为与甲醇进行酯交换反应的原料,得到脂肪酸甲酯和甘油。考察了非极性相溶剂石油醚与棉籽油的比例对酯交换转化率和洗涤粗产品用水量的影响,确定了石油醚与棉籽油的最佳质量比为3,在此条件下,洗涤用水量可降低一半。考察了醇油比、催化剂用量、反应温度、反应时间等参数对转化率的影响。应用正交实验的方法找出酯交换反应的适宜条件为:醇油比6:1,催化剂用量1.1%,反应温度60℃,反应时间120min。在此反应条件下,产物中脂肪酸甲酯的含量可达97.4%。 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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橄榄油制备生物柴油的工艺研究 总被引:3,自引:0,他引:3
以橄榄油为原料,四氢呋喃作共溶剂,NaOH为催化剂制备生物柴油.用气相色谱分析方法,通过对反应温度、醇油摩尔比、催化剂的量、反应时间的研究,得出在各自的最优化条件下橄榄油的转化率为97.3%. 相似文献
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Heterogeneous catalysis of transesterification using KI/mesoporous silica catalyst was utilized to produce biodiesel from soybean oil and methanol. The effects of reaction temperature, percentage of KI loading, reaction time, and amount of catalyst on the conversion to methyl ester were studied. The results showed that increasing reaction temperature, KI loading and reaction time can enhance the conversion. The optimum condition was the reaction temperature at 70 °C, 15 wt.% of KI, a reaction time of 8 h., and a catalyst amount of 5.0% by weight of the oil which yielded 90.09% of the conversion. The fuel properties of biodiesel from the optimum condition were tested and found that only viscosity showed over standard. However, the high viscosity can be reduced by separation of non-reacting soybean oil. 相似文献
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Lin Liu Ding Ma Huiying Chen Heng Zheng Mojie Cheng Yide Xu Xinhe Bao 《Catalysis Letters》2006,107(1-2):25-30
Zn/I2 was found to be a practical and effective catalyst for the transesterification of soybean oil with methanol. A study for
optimizing the reaction conditions such as the molar ratio of methanol to oil, the reaction time and the catalyst amount,
was performed. The highest conversion of 96% was obtained under the optimum conditions. Further, the effect of free fatty
acids and water in the soybean oil on the catalytic activity of the catalysts was also investigated. 相似文献
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A transesterification reaction of Jatropha curcas oil with methanol in the presence of KOH impregnated CaO catalyst was performed in a simple continuous process. The process variables such as methanol/oil molar ratio (X1), amount of catalyst (X2) and total reaction time (X3) were optimized through response surface methodology, using the Box–Behnken model. Within the range of the selected operating conditions, the optimal ratio of methanol to oil, amount of catalyst and total reaction time were found to be 8.42, 3.17% and 67.9 min, respectively. The results showed that the amount of catalyst and total reaction time have significant effects on the transesterification reaction. For the product to be accepted as a biodiesel fuel, its purity must be above 96.5% of alkyl esters. Based on the optimum condition, the predicted biodiesel conversion was 97.6% while the actual experimental value was 97.1%. The above mentioned results demonstrated that the response surface methodology (RSM) based on Box–Behnken model can well predict the optimum condition for the biodiesel production. 相似文献
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通过利用浓硫酸作催化剂对酸值较高的乌桕油进行预酯化。预酯化后的乌桕油与甲醇在氢氧化钾作为催化剂微波仪中进行酯交换反应得到脂肪酸甲酯,采用单因素实验的方法来研究酯交换反应的最优工艺条件,酯交换反应温度为60℃,反应时间为3min,催化剂KOH的用量为1.0%(油重),酯交换反应的转化率为98.87%。 相似文献