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综述了生物柴油的特性及生产方法,介绍了酯交换法制备生物柴油的反应机理及生产工艺,对各种工艺的优缺点进行了剖析,指出了生物柴油技术发展现在面临的问题及研究方向。 相似文献
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植物油脂肪酸甲酯-生物柴油作替代燃料的意义 总被引:7,自引:3,他引:7
植物油脂肪酸甲酯-生物柴油以其优越理化性能迅速成为清洁代用燃料之一。对国内外生物柴油的生产方法、酯交换工艺、酯交换反应催化剂及生产应用状况作了论述。发展生物柴油产业对解决我国柴汽油供需平衡及其依赖进口、农业和生态等等问题有重要的影响意义,提出了该产业的发展对策以及对该产业的展望。 相似文献
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酯交换反应制备生物柴油催化剂的研究进展 总被引:1,自引:0,他引:1
生物柴油是一种环境友好型的可再生资源,本文介绍了生物柴油的制备技术,并综述了采用酯交换反应制备生物柴油所使用的催化剂的研究进展,简述了各种催化剂的优缺点。 相似文献
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超临界酯交换法制备生物柴油工艺基础及其过程强化技术研究 总被引:3,自引:0,他引:3
生物柴油以其优良的环境友好性和可再生性成为近年来的研究热点.简述了生物柴油的特性,比较了生物柴油制备工艺的优缺点,重点介绍了超临界甲醇法制备生物柴油的研究现状,指出以共溶剂和催化剂强化超临界过程可以有效地改善反应条件;同时对超临界甲醇法制备生物柴油的热力学和动力学进行了探讨,包括状态方程、混合体系临界参数、反应速率常数和反应活化能的估算方法;最后对超临界甲醇法制备生物柴油的经济性进行了分析.结果表明,超临界酯交换法具有与传统酸碱催化过程相当的竞争性,尤其是对以餐饮废油等低成本油为原料的生产过程. 相似文献
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用棉籽油制备生物柴油 总被引:16,自引:0,他引:16
采用棉籽油为原料连续化生产生物柴油,研究了工艺及设备的设计。由棉籽油与甲醇在催化剂NaOH存在下由酯交换反应制得生物柴油。在优化条件下反应50 min,转化率达到99%。生产的生物柴油,各项指标与天然柴油相似。其各项燃烧指标优于或与普通柴油相仿,满足欧洲Ⅱ排放标准。 相似文献
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The potential of using dairy waste scum as a feed stock for bio-diesel production was investigated. Present study optimized the parameters involved in transesterification process of Dairy Waste Scum Oil. Gas chromatography was used to determine the fatty acid composition of Dairy Waste Scum Oil. Results revealed that the low free fatty acid content was a notorious parameter to determine the viability of alkaline transesterification. The yield of bio-diesel reached 96.7% when 1.2 wt.% of Potassium Hydroxide, reaction temperature of 75 °C, 30 min of time and 6:1 Methanol oil ratio at 350 rpm. Thermo gravimetric analysis followed the evaluation of transesterification process. The present analysis confirms that bio-diesel from dairy waste scum is quit suitable as an alternative to petroleum diesel with recommended fuel properties as per ASTM standards. This new way for using dairy waste scum reduces the cost of production of bio-diesel and the problem related to the disposal of Dairy scum. 相似文献
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Analysis and comparison of performance and emissions of an internal combustion engine fuelled with petroleum diesel and different bio-diesels 总被引:2,自引:0,他引:2
The performance and emissions of an internal combustion engine (ICE) engine fuelled with two bio-diesels are experimentally measured and analysed according to ISO 8178 standard and compared with that of the petroleum diesel. Two types of bio-diesel, type A and type B (defined in Section 1) with their blends of B5, B10, B20, B50 and B100 are tested and analysed. This study found that the performance of both bio-diesel fuels reduces with increasing blend ratio, with a torque decrease of 5% for both bio-diesels, and a fuel consumption increase of 7-10%. This can be attributed to the lower energy content of bio-diesel when compared with petroleum diesel. For both the bio-diesels, some emissions were found to be higher than petroleum diesel, while some were lower. Nitrogen Oxide (NOx) emissions decreased by 14% for bio-diesel A, but increased by 17% for bio-diesel B. Carbon monoxides (CO) emissions were significantly reduced for both bio-diesel A and B, with reductions of 58% and 27% respectively. Hydrocarbon (HC) emissions were found to increase with increasing blend ratio for both bio-diesels, with an increase of 10% for bio-diesel A and 80% for bio-diesel B. Lastly, Carbon dioxides (CO2) emissions were found to increase, with an increase of 6% for bio-diesel A and 18% for bio-diesel B. The study clearly found that each of the bio-diesels has different scale of effect on ICE performance and emissions and hence, it is essential to test bio-diesels before it can be recommended for mass scale production and for commercial use in ICE. However, the study indicates that the two major pollutant gas emissions are generally reduced when using bio-diesel, therefore bio-diesel can be considered to be a more environmentally friendly, secure and renewable approach of obtaining energy in the long run. 相似文献
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Manuel Garcia-Perez Jun Shen Xiao Shan Wang Chun-Zhu Li 《Fuel Processing Technology》2010,91(3):296-27
This paper describes the production and fuel properties of fast pyrolysis oil/bio-diesel blends. The bio-oils used in this study were produced from the fast pyrolysis of woody biomasses, oil mallee and pine. The bio-diesel employed was derived from canola vegetable oil. The conditions used to prepare the bio-oil/bio-diesel blends, as well as some of the fuel properties of the resulting bio-diesel rich phase, are reported. The experimental results show that the solubility of fast pyrolysis oils in bio-diesel is not as high as was previously reported for decanted oils obtained by Auger pyrolysis. The carboxylic acids, mono-phenols, furans and lignin derived oligomers were the compounds most soluble in bio-diesel, while the sugars, on the other hand, showed poor solubility. Although the presence of phenols enhances the oxidation stability of the bio-diesel rich phases, other fuel properties deteriorate. For example, the content of solid residues increased primarily because of the solubilisation of lignin derived oligomers, which were quantified by UV-fluorescence. Concentrations as high as 3.5 mass % of these compounds were observed in the bio-diesel rich phase. The solubility of bio-oil in bio-diesel was enhanced by using ethyl acetate/bio-diesel blends. Some fuel properties of the bio-diesel rich phase, after the removal of ethyl acetate, are reported. 相似文献
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J.A.Z. Pieterse S. van EijkH.A.J. van Dijk R.W. van den Brink 《Fuel Processing Technology》2011,92(3):616-623
Sorption of sulfur components in the liquid phase was used to desulfurize ultra low sulfur diesel (ULSD) to below 1 ppmw S. Several concepts of sorption were considered by using both physisorption and chemisorption materials and conditions. Adsorption assisted by reaction with Ni sorbent was found to be most successful. Using a pre-commercial diesel representing a mature diesel on all aspects except for the absence of fuel stabilizers and bio-diesel, a sulfur breakthrough capacity of 2 mg S/g could be achieved using a Ni-sorbent at an acceptable LHSV of 0.7 h− 1 on average. However, successive experiments indicated that the desulfurization capacity depended strongly on the presence of fuel-additive and bio-diesel in commercial ULSD. The presence of the cetane improver 2-ethylhexylnitrate (2EHN) was shown to decrease the sulfur capacity by roughly 50%. The presence of bio-diesel (fatty acid methyl ester, abbreviated to FAME) was shown to completely disable the desulfurization process. This was confirmed by comparing BP Ultimate diesel with FAME (obtained in 2008) and without FAME (obtained in 2006). From this evaluation it turned out that the targeted breakthrough capacity of 1 mg S/g sorbent was within reach for commercial ULSD until late 2006 when adding bio-diesel to ULSD became common practice in Europe. Several attempts to remove the additives prior to desulfurization by using copper loaded zeolites, active carbon and silica gel proved unsuccessful to bring the sulfur adsorption capacity for current diesel to the level observed for 2EHN and FAME-free diesel. It is concluded that sorption in the liquid phase does not yet represent a viable desulfurization technology for ultra-low sulfur diesel. 相似文献
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本文将根据生物柴油近年来国内外的发展趋势,着重讨论生物柴油的制备工艺,酸碱催化、酶催化和离子催化等不同生物柴油的生产方式和不同的性质,所涉及的相关技术问题,以及用生命周期循环来评价生物柴油工艺和技术的可行性。 相似文献