共查询到16条相似文献,搜索用时 109 毫秒
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为了考察项目组自行开发的新型催化剂(SXL)的催化效率,以粗菜籽油为原料,SXL为催化剂,酯交换反应为基础,研究产物生物柴油的转化率和产率。结果表明:小试优化反应条件以100 g粗菜籽油为原料油、醇油比(摩尔比)7∶1、催化剂用量(质量分数)为2.5%、反应温度为60℃、反应时间为2 h下,生物柴油转化率和产率均达到98%以上。放大实验结果:在20 L反应釜中,投入6.50 kg粗菜籽油,以小试条件为基础,原料油转化率、生物柴油产率和甘油产率可达95%以上。表明SXL具有良好的发展前景。 相似文献
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采用反相液相色谱分离和紫外检测法定量分析了菜籽油制备生物柴油的主要组分分布及含量。结果表明,各脂肪酸甲酯、甘油单酯、甘油二酯及甘油三酯组分均能达到基线分离,且线性相关性良好,相关系数均在0.999 3以上,加标回收率在99.5%~103.7%之间,RSD在0.45%~2.38%(n)之间,该方法准确可靠。定量分析了菜籽油完全酯交换产品中油酸甲酯、亚油酸甲酯、亚麻酸甲酯组分含量分别为58.45%,20.02%,16.50%,三者之和为94.98%。菜籽油中三油酸甘油酯组分含量为38.76%。 相似文献
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采用等体积浸渍法制备了纳米K2CO3/γ-Al2O3催化剂,并研究了该催化剂的制备条件对酯交换反应的影响。用TEM表征催化剂颗粒的大小,用TG-DSC表征催化剂的热性能。结果显示:催化剂粒径分布在30-50nm之间;催化剂的最佳制备条件是K2CO3负载率(K2CO3占γ-Al2O3质量分数)50%,焙烧温度600℃,焙烧时间4h。利用此催化剂,当醇油物质的量之比为12:1、催化剂用量为油质量的3%、反应时间3h 、反应温度70℃时,生物柴油的得率达到97.90%。生物柴油质量指标符合国家标准。 相似文献
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利用菜籽油脱臭馏出物制备生物柴油新工艺 总被引:1,自引:1,他引:0
以菜籽油脱臭馏出物为原料,首先以D002阳离子交换树脂作催化剂,进行酯化反应,降低原料酸值;然后以氢氧化钾作催化剂进行醇解反应来制备生物柴油的二步法新工艺路线。结果表明:D002阳离子交换树脂具有很强的催化活性,游离脂肪酸最高转化率达97.7%,连续使用4次后,催化活性仍然很高,达96%以上;碱催化过程中甘油酯的最高转化率达97.4%。产品品质大都符合美国ASTMD6751-03生物柴油标准。由此可见,先用树脂催化处理高酸值废油,然后进行碱催化制备生物柴油二步法工艺是一种切实可行的方法。 相似文献
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Karel Komers Frantiek Skopal Radek Stloukal Jaroslav Machek 《European Journal of Lipid Science and Technology》2002,104(11):728-737
The reaction of rapeseed oil with methanol catalyzed by KOH is described by a model consisting of two sequences of consecutive competitive reactions. The first sequence expresses the methanolysis of rapeseed oil to methyl esters (biodiesel) whereas the second sequence describes the always present side reaction‐saponification of glycerides and methyl esters by KOH. The proposed chemical model is described (after rational simplifications) by a system of differential kinetic equations which are solved numerically by two independent computing methods. The thus obtained theoretical kinetic and equilibrium results are compared numerically and/or graphically with the experimental parameters. The latter were obtained by the determination of the relevant components in the actual reaction mixture by analytical methods. According to the experimental results, the proposed reaction scheme is fulfilled with the probability of ca. 78%. The optimal average rate constants and equilibrium constants of individual reaction steps of the discussed scheme are introduced. The limitations of the proposed reaction model are discussed. 相似文献
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用氢氧化钾作催化剂,考察了反应温度、催化剂用量、醇油摩尔比、反应时间对棕榈油和甲醇制备生物柴油产率的影响。结果表明,最佳反应条件为:反应温度40℃,催化剂用量0.6%,醇油摩尔比6∶1,反应时间2.0 h。此时,生物柴油产率可达97.82%。 相似文献
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棕榈油酯交换制备生物柴油的反应动力学 总被引:1,自引:1,他引:0
在甲醇与棕榈油的摩尔比为6∶1和催化剂KOH用量为棕榈油质量1.0%的条件下,研究不同温度下棕榈油制备生物柴油的酯交换反应动力学,采用Origin软件拟合曲线方程,建立棕榈油酯交换反应的宏观动力学模型。研究结果表明:棕榈油制备生物柴油的酯交换反应遵循1.40级动力学方程,反应速率随温度的升高而加快,二者符合Arrhenius方程,该反应的活化能为27.23 kJ/mol,频率因子为1.4×103。文中研究建立的反应动力学模型将对扩大试验研究提供理论依据和基础数据支持。 相似文献
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The kinetics of palm oil and mustard oil transesterification are compared. Transesterification of palm oil and mustard oil using KOH as a catalyst was performed at various reaction temperatures ranging from 40 to 60°C. The reaction steps are reversible and transesterification is favoured at elevated temperatures. The reaction step of triglyceride to diglyceride is the rate determining step (RDS) that controls kinetics of overall transesterification with activation energies of 30.2 and 26.8 kJ/mol for palm oil and mustard oil transesterification, respectively. It is found that percentage of saturated compounds play a vital role on transesterification kinetics. © 2011 Canadian Society for Chemical Engineering 相似文献