在闭环微型工厂中利用甲醇甲醛溶液生产聚氧化亚甲基二甲醚的实验演示

IF 3.7 3区 工程技术 Q2 ENGINEERING, CHEMICAL
Alvaro Ferre , Johannes Voggenreiter , Christian F. Breitkreuz , Denis Worch , Udo Lubenau , Hans Hasse , Jakob Burger
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引用次数: 0

摘要

链长为 3-5( )的聚氧亚甲基二甲醚被讨论用作合成柴油燃料,因为它们具有显著减少烟尘排放的潜力,同时具有与传统柴油燃料相似的物理化学特性。最近开发的一种直接从甲醇和甲醛水溶液中生产合成柴油的工艺,是一种避免使用昂贵的中间体(如三氧六环、甲缩醛或二甲醚)的可行方法。该工艺由一个反应器、一个蒸馏序列和一个膜装置组成。第一个蒸馏塔特别具有挑战性,因为分离过程具有反应性,存在大量成分,而且甲醛的溶解度有限。迄今为止,这种分离方法的可行性仍有待论证。这项研究介绍了在慕尼黑工业大学施特劳宾校区建立的示范工厂中进行的闭环实验。在蒸馏步骤中,得到的甲醛杂质非常少,约为 800 ppm。实验结果与基于反应平衡阶段模型的模拟结果进行了比较。大多数成分的温度和成分曲线的模拟结果与实验结果一致。虽然膜分离对水的选择性比以前的试验要弱,但足以克服蒸馏界限。此外,本研究还评估了固体沉淀的可能性,探讨了产品质量的权衡,并讨论了工艺的总体质量平衡,证明了工艺的整体可行性。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

Experimental demonstration of the production of poly(oxymethylene) dimethyl ethers from methanolic formaldehyde solutions in a closed-loop mini-plant

Experimental demonstration of the production of poly(oxymethylene) dimethyl ethers from methanolic formaldehyde solutions in a closed-loop mini-plant
Poly(oxymethylene) dimethyl ethers of chain length 3–5 (
) are discussed as synthetic diesel fuels due to their potential to significantly reduce soot emissions while presenting physicochemical properties similar to conventional diesel fuels. A recently developed process to produce
directly from methanol and aqueous formaldehyde is a promising way to avoid expensive intermediates such as trioxane, methylal, or dimethyl ether. The process consists of a reactor, a distillation sequence, and a membrane unit. The first distillation column is particularly challenging due to the reactive character of the separation, the high number of components present, and the limited solubility of formaldehyde. Up to now, the feasibility of this separation has yet to be demonstrated. This work presents closed-loop experiments in a demonstration plant erected at the Campus Straubing of the Technical University of Munich with closing recycle. In the distillation step,
with very small impurities of around 800 ppm of formaldehyde was obtained. The experimental results were compared with simulations based on a reactive equilibrium stage model. The simulations of the temperature and composition profiles for the majority of the components are in line with the experiments. Although the membrane separation exhibited weaker water selectivity than in previous tests, it was sufficient to overcome distillation boundaries. Additionally, this study assesses the potential for solid precipitation, explores trade-offs in product quality, and discusses overall mass balances of the process, demonstrating the overall feasibility of the process.
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来源期刊
Chemical Engineering Research & Design
Chemical Engineering Research & Design 工程技术-工程:化工
CiteScore
6.10
自引率
7.70%
发文量
623
审稿时长
42 days
期刊介绍: ChERD aims to be the principal international journal for publication of high quality, original papers in chemical engineering. Papers showing how research results can be used in chemical engineering design, and accounts of experimental or theoretical research work bringing new perspectives to established principles, highlighting unsolved problems or indicating directions for future research, are particularly welcome. Contributions that deal with new developments in plant or processes and that can be given quantitative expression are encouraged. The journal is especially interested in papers that extend the boundaries of traditional chemical engineering.
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