首页> 外文会议>Hydrothermal Reactions and Techniques >THE INDUSTRIAL PRODUCTION PROCESS OF METHYL ESTERS OF FATTY ACIDS BY CATALYST-FREE SUPERCRITICAL METHANOL
【24h】

THE INDUSTRIAL PRODUCTION PROCESS OF METHYL ESTERS OF FATTY ACIDS BY CATALYST-FREE SUPERCRITICAL METHANOL

机译:无催化剂超临界甲醇制脂肪酸甲​​酯的工业生产过程

获取原文
获取原文并翻译 | 示例

摘要

The process for producing methyl esters of fatty acids (bio diesel fuel) from vegetable oil such as soybean oil and rapeseed oil has been promoted commercially. Most of methods for bio diesel fuel production use the alkaline catalyst to promote transesterification of triglycerides. But, this process has a few disadvantages such as removal catalyst and saponified by-products, separation of the crude glycerol after reaction. Furthermore, free-fatty acids contained in oil are not esterified under alkaline-catalysed method. The fundamental studies of catalyst-free method have been curried out using super critical methanol. Generally, the condition of transesterification with supercritical methanol is required high temperature and pressure to obtain high conversion of transesterification from triglycerides. We have developed the industrial process for producing high quality bio diesel fuel by utilization of the transesterification from crude fatty acids. It is known that triglycerids are conversed to crude fatty acids by hydrolysis easily. After that, the crude fatty acids are smoothly esterified by catalyst-free supercritical methanol. The advantage of this method is that the operating condition of transesterification is reasonable (less than 573 K, 20 MPa). This operating condition is available for practical plants sufficiently. In fact, triglycerides as main ingredient of vegetable oil is required higher condition (more than 623 K, 45 MPa) in order to obtain complete transesterification. We have refined methyl esters of fatty acids produced using this method by distillation and mechanical separation methods and established the basic production process of methyl esters of fatty acids by catalyst - free supercritical methanol. As a result, approximately 90 wt% of crude fatty acids is converted and refined to methyl esters, and it was confirmed that the residue after refining were available for fuel of general-boiler. Therefore, the clean and zero-emission process can be realized for the industrial production of bio diesel fuel from vegetable oil.
机译:由植物油例如大豆油和菜籽油生产脂肪酸的甲酯(生物柴油)的方法已经商业推广。用于生产生物柴油燃料的大多数方法都使用碱性催化剂来促进甘油三酸酯的酯交换反应。但是,该方法具有一些缺点,例如除去催化剂和皂化副产物,反应后分离粗制甘油。此外,油中所含的游离脂肪酸在碱催化方法下不会被酯化。已经使用超临界甲醇进行了无催化剂方法的基础研究。通常,需要高温和高压下与超临界甲醇进行酯交换的条件,以从甘油三酸酯获得酯交换的高转化率。我们已经开发了利用粗脂肪酸的酯交换反应生产高质量生物柴油的工业方法。众所周知,甘油三酸酯容易通过水解转化为粗脂肪酸。之后,粗脂肪酸被无催化剂的超临界甲醇平稳地酯化。该方法的优点是酯交换反应的操作条件是合理的(小于573 K,20 MPa)。该操作条件对于实际工厂是足够可用的。实际上,甘油三酸酯作为植物油的主要成分需要更高的条件(大于623 K,45 MPa)才能获得完全的酯交换作用。我们通过蒸馏和机械分离方法精制了使用该方法生产的脂肪酸甲酯,并建立了无催化剂超临界甲醇生产脂肪酸甲酯的基本生产工艺。结果,约90wt%的粗脂肪酸被转化并精制为甲酯,并且证实了精制后的残余物可用于普通锅炉的燃料。因此,可以实现从植物油工业生产生物柴油的清洁和零排放过程。

著录项

相似文献

  • 外文文献
  • 中文文献
  • 专利
获取原文

客服邮箱:kefu@zhangqiaokeyan.com

京公网安备:11010802029741号 ICP备案号:京ICP备15016152号-6 六维联合信息科技 (北京) 有限公司©版权所有
  • 客服微信

  • 服务号