酸化油固定床酶法合成生物柴油研究

酸化油是油脂工业中以皂脚、油脚经酸化处理得到的产品。它的主要成分是游离脂肪酸及中性油，是生产脂肪酸的重要原料，但生产过程中有水解废水的产生，若将其直接排放，既污染了环境又浪费了资源。生物柴油的主要成分是脂肪酸甲酯（fatty acid methyl ester，FAME）。它具有原料丰富而且可再生、可生物降解、无毒、不含芳香烃、二氧化硫等污染物、燃烧排放低、闪点高、运输储存安全等特点。作为石化柴油的潜在替代能源，生物柴油因其独特的优越性和现实的需求越来越受到关注。利用酸化油生产生物柴油不仅可以缓解生物柴油原料不足问题，还可解决酸化油所带来的环境问题。

The convertion of acid oil to biodiesel by use of immobilized Candida lipase absorbed on textile cloth was studied in a fixed bed reactor, which can not only reduce the environmental pollution of acid oil, but also produce a substitute for petroleum diesel. The acid oil mixed with methanol was pumped into three fixed bed reactors in series, and the methanol was added with the molar flow rate same as the acid oil in each reactor. The effects of enzyme content, solvent content, water content, flow rate of reactant and temperature on the enzymatic reaction were analyzed. The result of orthogonal experiments indicates that the optimal transesterification can be performed under the following conditions： immobilized lipase content in acid oil, 20% ; hexane content in acid oil, 10% ; water content in acid oil, 10%, reaction temperature, 50 ℃ ; and flow rate of reactant, 0.08 g/rain. Under these conditions, the FAME content of 90.18% in the product is obtained. The immobilized lipase can be reused with relatively stable activity after glycerol being removed from the surface. By refining, most of the chemical and physical properties of biodiesel will meet the American and Germany biodiesel standards and exceed the Chinese standard of 0^# petroleum diesel except for carbon residue, density and kinematic viscosity.

酸化油固定床酶法合成生物柴油研究

以固定化的假丝酵母酶为催化剂，在三段式固定床反应器内，醇油摩尔比为1：1，采用分级流加甲醇的方式，将高酸值的酸化油转化为生物柴油，探讨了酶量、溶剂量、水量、温度、反应液流速等与产物中甲酯含量的关系。正交实验结果表明，反应的最适条件为酶用量、溶剂量、水量分别为油重的15％、10％、10％，反应液流速为0.8g·min^-1，温度为45℃，在此条件下，产物中甲酯含量达到了90．18％。

生物柴油原料资源利用与开发

发展生物柴油产业是解决我国石化能源短缺与环境污染问题的一个重要措施。在生物柴油产业发展过程中,原料不足成为规模化的瓶颈。我国现阶段油脂资源短缺,耕地资源匮乏,野生油料植物资源丰富,秸秆类农林废弃物资源量巨大。在结合我国国情基础上,分析现今我国生物柴油原料的来源,探讨建立生物柴油原料等级标准应重点考虑的指标,提出解决原料资源的四个措施。

生物柴油转化效果测定方法的研究

生物柴油的生产原料、催化剂、工艺流程等存在多样化特点，为比较各种方法的优劣，需要建立一种适宜、通用的测定方法。通过分析国内外相关测定方法，提出以气相色谱测定反应产物，十七碳脂肪酸甲酯为标准物，内标法计算反应转化率和产率的方法。

Effect of carbon source on growth and lipid accumulation in Chlorella sorokiniana GXNN01

Heterotrophic culture of microalgae to develop methods of increasing biomass productivity and storage lipids has brought new insight to commercial biodiesel production. To understand the relationship between heterotrophy and lipid production, the effects of carbon sources on the growth and lipid accumulation of Chlorella sorokiniana GXNN01 was studied. The alga exhibited an increased growth rate in response to the addition of carbon sources, which reached the stationary phase after 48 h at 30A degrees C. In addition, glucose and NaAc had a significant effect on the lipid accumulation during the early-stationary phase. Specifically, the lipid content was 0.237 +/- 0.026 g g(-1) cell dry weight and 0.272 +/- 0.041 g L-1 when glucose was used as the carbon source, whereas the lipid content reached 0.287 +/- 0.018 g g(-1) cell dry weight and 0.288 +/- 0.008 g L-1 when NaAc was used as the carbon source. The neutral lipid content was found to first decrease and then increase over time during the growth phase. A glucose concentration of 20 mmol L-1 gave the maximal lipid yield and the optimum harvest time was the early-stationary phase.

Effect of iron on growth and lipid accumulation in Chlorella vulgaris

The economic feasibility of algal mass culture for biodiesel production is enhanced by the increase in biomass productivity and storage lipids. Effect of iron on growth and lipid accumulation in marine microalgae Chlorella vulgaris were investigated. In experiment I, supplementing the growth media with chelated FeCl3 in the late growth phase increased the final cell density but did not induce lipid accumulation in cells. In experiment II, cells in the late-exponential growth phase were collected by centrifugation and re-inoculated into new media supplemented with five levels of Fe3+ concentration. Total lipid content in cultures supplemented with 1.2 x 10(-5) mol L-1 FeCl3 was up to 56.6% biomass by dry weight and was 3-7-fold that in other media supplemented with lower iron concentration. Moreover, a simple and rapid method determining the lipid accumulation in C. vulgaris with spectrofluorimetry was developed. (c) 2007 Elsevier Ltd. All rights reserved.

海滨锦葵种子油脂提取及制备生物柴油研究

生物柴油是绿色清洁可再生能源，大力发展生物柴油对解决影响我国经济可持续发展的能源危机和环境危机具有重要意义。 本文就海洋滩涂能源油料植物海滨锦葵油脂的提取和制备生物柴油技术进行了研究。 1、利用超临界CO2流体萃取技术提取海滨锦葵籽油。结果表明超临界CO2流体萃取技术提取海滨锦葵籽油的最佳工艺参数为：萃取压力25MPa，萃取温度45℃，CO2流量18kg.h-1，萃取时间为120min，在该工艺条件下萃取三次，海滨锦葵籽油萃取率达到19.35%。 2、以海滨锦葵籽仁为原料，利用水酶法提取海滨锦葵籽仁油。水酶法提取海滨锦葵籽油的最佳工艺参数为：酶用量0.024ml.g-1，提取温度63℃，固液比1/6，提取时间为230min，在该工艺条件下海滨锦葵籽油提取率达到24.28%。 3、海滨锦葵油制备生物柴油的最佳工艺参数为：搅拌强度为1800r.min-1，催化剂KOH用量为海滨锦葵油质量的1%，醇油摩尔比6/1，反应时间50min，反应温度65℃，在该工艺条件下，酯交换反应三次，酯交换率达到97.8%。 4、利用固定化脂肪酶Novo435催化海滨锦葵油酯交换制备生物柴油。结果表明海滨锦葵油固定化脂肪酶催化法制备制备生物柴油的最优工艺参数为反应温度47℃，反应时间31h，催化剂用量18%，搅拌强度900r.min-1，醇油摩尔比3.2/1。在该工艺条件下酯交换率达到92.68%。 5、利用超临界法制备生物柴油，结果表明海滨锦葵油超临界法制备生物柴油的最佳工艺条件为：反应温度为300℃，反应压力为12MPa，反应时间为9min，搅拌强度为300r.min-1，醇油摩尔比为30/1。在此条件下，酯交换反应三次，酯交换率可达97.62%。 6、利用超声波辅助法制备生物柴油。结果表明海滨锦葵油超声波辅助法制备生物柴油的最佳工艺参数为：超声波功率为180W，催化剂KOH用量为海滨锦葵油质量的0.6%，反应温度65℃，醇油摩尔比7/1，在该工艺条件下酯交换反应三次，酯交换率达到99.85%。