Method and apparatus for producing biodiesel fuel, and decomposition catalyst for decarboxylation of fat used in the method
    9.
    发明专利
    Method and apparatus for producing biodiesel fuel, and decomposition catalyst for decarboxylation of fat used in the method 有权
    用于生产生物柴油燃料的方法和装置,以及用于在方法中使用的癸烷脱羧的分解催化剂

    公开(公告)号:JP2013241612A

    公开(公告)日:2013-12-05

    申请号:JP2013149190

    申请日:2013-07-18

    发明人: FUJIMOTO KAORU

    摘要: PROBLEM TO BE SOLVED: To provide a method for producing biodiesel fuel, which makes it possible to construct a distributed energy supply system that provides needed energy at a location that require the energy, the system in which the storage stability is excellent, alcohol (auxiliary raw material) is not required, glycerol is not produced as a by-product, impurities such as dienes are unlikely to remain in the product, the amount of coke generated is small, the pour point is low, and blackening and abnormal odors rarely occur by virtue of stability against air or the like, the production efficiency and productivity are excellent to prevent running costs from increasing or productivity from decreasing since being free from ancillary work such as treatment or reactivation of used catalysts, and further capable of contemplating abbreviation of production processes and simplification of reaction apparatuses since a pretreatment for removing free fatty acids from raw material fat or the like is not needed.SOLUTION: A decomposition catalyst for fat decarboxylation and fats are brought into contact at 350°C-475°C to cleave an ester bond portion under the action of the decomposition catalyst for fat decarboxylation, and thus the biodiesel fuel constituting mainly C8-C24 hydrocarbons is obtained by decarboxylation decomposition reaction.

    摘要翻译: 要解决的问题:提供一种生产生物柴油燃料的方法,其可以构建在需要能量的位置提供所需能量的分布式能量供应系统,储存稳定性优异的系统,醇(辅助 原料)不需要副产物,不会产生副产物甘油,二烯等杂质不易残留在产品中,产生的焦炭量少,倾点低,易产生黑化和异味 通过对空气等的稳定性,生产效率和生产率优异,以防止运行成本增加或生产率降低,因为没有诸如使用催化剂的处理或再活化的辅助性工作,并且还能够考虑生产的缩写 处理和简化反应装置,因为用于从原料脂肪或Li除去游离脂肪酸的预处理 ke不需要。溶解:脂肪脱羧和脂肪分解催化剂在350℃-475℃下接触,在分解催化剂的作用下裂解酯键部分进行脂肪脱羧,从而构成生物柴油燃料 主要通过脱羧分解反应获得C8-C24烃。