...
首页> 外文期刊>Reaction Chemistry & Engineering >Solketal production in a solvent-free continuous flow process: scaling from laboratory to bench size
【24h】

Solketal production in a solvent-free continuous flow process: scaling from laboratory to bench size

机译:索替代生产在无溶剂的连续流程过程中:从实验室扩展到长凳尺寸

获取原文
获取原文并翻译 | 示例
   

获取外文期刊封面封底 >>

       

摘要

The extended use of biodiesel as a fuel from renewable sources involves an increase in glycerol linked to the transesterification process. Therefore, it would be desirable to find new valorization routes for this by- product. One of the most promising pathways to transform glycerol into added-value products is acetalization with carbonyl compounds. The aim of this work is to scale the process of solketal production from the acetalization reaction in a solvent-less continuous process on the bench scale. The thermody- namic and kinetic parameters were obtained in a batch reactor, using ethanol as the solvent and an ion- exchange resin as the catalyst. The experimental work on this scale was carried out under different opera- tion conditions: acetone/glycerol molar ratio (from 2 to 10), temperature (from 298 to 333 K) and amount of catalyst added (% wt related to the initial glycerol weight from 1 to 5). Three typical mechanisms of heterogeneous catalysts were proposed as reaction rate equations (Langmuir-Hinshelwood, Eley-Rideal and low-range adsorption (LRA) mechanisms) in order to obtain an adequate fitting with the experimental data. The equation based on the LRA catalyst mechanism was selected as the most plausible model according to the minimized root mean square deviation calculated. In order to verify these results on a greater scale, an experimental study was carried out to validate this kinetic model in a bench-scale reactor in a solvent-less continuous flow process. This is the first time in which solketal production was tested on the bench or pilot scale in the absence of ethanol and, therefore, the stability of the operation and the cat- alyst were evaluated. From the comparison between the estimated and experimental conversion on the bench-scale, the proposed model was able to adequately predict the performance of the acetalization re- action under fixed conditions (from 313 to 333 K), with an error range of approximately 5% and 10% as the maximum error.
机译:生物柴油作为来自可再生源的燃料的延长使用涉及与酯交换过程相关的甘油的增加。因此,希望找到该副产品的新的算法路线。将甘油转化为添加值产物的最有前景的途径之一是用羰基化合物进行缩醛化。这项工作的目的是将Solkeral生产的过程从缩放在替补秤上的溶剂的连续过程中扩展了甲基化反应。在批量反应器中获得热流和动力学参数,用乙醇作为溶剂和作为催化剂的离子交换树脂。在不同的操作条件下进行该规模的实验工作:丙酮/甘油摩尔比(从2至10),温度(298至333 k)和加入催化剂的量(与初始甘油重量相关的%wt从1到5)。提出了三种异质催化剂的典型机制作为反应速率方程(Langmuir-Hinshelwood,Eley-rideal和低范围吸附(LRA)机制),以获得具有实验数据的充分拟合。根据基于LRA催化剂机理的基于LRA催化剂机理的等式,根据基于最小化的均线平均方偏差计算。为了验证这些结果,进行了更大的规模,进行了实验研究,以在溶剂的连续流程过程中验证在长凳尺度反应器中的该动力学模型。这是第一次在没有乙醇的长凳或试验尺度上测试蜕皮生产,因此,评估操作和猫的稳定性。从估计和实验转化之间的比较,所提出的模型能够充分预测固定条件下的缩醛化再动的性能(从313到333 k),误差范围约为5%和最大误差10%。

著录项

  • 来源
    《Reaction Chemistry & Engineering》 |2019年第10期|共11页
  • 作者单位

    CEPSA Compania Espanola de Petroleo S. A. U. Research Center. Av. Punto Com 1.28805 Alcala de Henares Spain;

    Departamento de Ingenieria Quimica y Ambiental Escuela Tecnica Superior de Ingenieria Universidad de Sevilla Camino de los Descubrimientos s/n. 41092 Sevilla Spain.;

    CEPSA Compania Espanola de Petroleo S. A. U. Research Center. Av. Punto Com 1.28805 Alcala de Henares Spain;

  • 收录信息
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类 物理化学(理论化学)、化学物理学;
  • 关键词

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