首页> 外国专利> BIODIESEL PRODUCTION PROCESS FROM ALCOHOL AND TRIGLYCERIDE TRANSESTERIFICATION REACTION IN A MULTI-ZONE TUBULAR REACTOR AND MULTI-ZONE TUBULAR REACTOR

BIODIESEL PRODUCTION PROCESS FROM ALCOHOL AND TRIGLYCERIDE TRANSESTERIFICATION REACTION IN A MULTI-ZONE TUBULAR REACTOR AND MULTI-ZONE TUBULAR REACTOR

机译:多区管反应器和多区管反应器中的醇和三硬脂酸酯的酯交换反应生物柴油的生产过程

摘要

Embodiments of a process for production of biodiesel from a transesterification reaction of alcohol and triglycerides in a multi-zone tubular reactor is disclosed. Alkyl esters and glycerin are formed from reactants in a reaction mixture as the reaction mixture flows through the zones. The zones include an entrance zone, an exit zone, and an intermediate zone between the entrance and exit zones. The zones are characterized by physical properties such as viscosity, density, composition, and flow regime. The entrance and intermediate zones include static mixers that perform structured mixing that increases the conversion and yield. The degree of mixing provided by the mixers is different in the zones to account for differences in physical properties. Additionally, the product stream from the reactor is passed through a coalescer to increase droplet size of a dispersed glycerin phase, facilitating both rapid separation of the glycerin phase from the biodiesel phase, and increased conversion and yield in a decanter.
机译:公开了在多区管式反应器中由醇和甘油三酸酯的酯交换反应生产生物柴油的方法的实施方案。当反应混合物流过区域时,烷基酯和甘油由反应混合物中的反应物形成。这些区域包括入口区域,出口区域以及入口区域和出口区域之间的中间区域。这些区域的特征是物理特性,例如粘度,密度,组成和流动状态。入口区和中间区包括静态混合器,该混合器执行结构化混合以提高转化率和产量。由混合器提供的混合程度在区域中是不同的,以解决物理性质的差异。另外,使来自反应器的产物流通过聚结器以增加分散的甘油相的液滴尺寸,从而促进甘油相与生物柴油相的快速分离,以及在倾析器中增加的转化率和产率。

著录项

  • 公开/公告号BRPI0915080B1

    专利类型

  • 公开/公告日2018-06-19

    原文格式PDF

  • 申请/专利权人 RENEWABLE ENERGY GROUP INC;

    申请/专利号BR2009PI15080

  • 发明设计人 TOM MICHAEL ASHLEY;

    申请日2009-06-03

  • 分类号C10G3;C10L1/30;

  • 国家 BR

  • 入库时间 2022-08-21 12:53:19

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