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在 1,3,5-三恶烷的添加下,同时将 C 和 C 糖转化为甲基戊二酸二甲酯。

Simultaneous Conversion of C and C Sugars into Methyl Levulinate with the Addition of 1,3,5-Trioxane.

机构信息

Key Laboratory of Biomass Chemical Engineering of Ministry of Education, College of Chemical and Biological Engineering, Zhejiang University, Hangzhou, 310027, China.

School for Engineering of Matter, Transport and Energy, Arizona State University, 551 E. Tyler Mall, Tempe, AZ, 85287, USA.

出版信息

ChemSusChem. 2019 Oct 8;12(19):4400-4404. doi: 10.1002/cssc.201902096. Epub 2019 Sep 4.

Abstract

The simultaneous conversion of C and C mixed sugars into methyl levulinate (MLE) has emerged as a versatile strategy to eliminate costly separation steps. However, the traditional upgrading of C sugars into MLE is very complex as it requires both acid-catalyzed and hydrogenation processes. This study concerns the development of a one-pot, hydrogenation-free conversion of C sugars into MLE over different acid catalysts at near-critical methanol conditions with the help of 1,3,5-trioxane. For the conversion of C sugars over zeolites without the addition of 1,3,5-trioxane, the MLE yield is quite low, owing to low hydrogenation activity. The addition of 1,3,5-trioxane significantly boosts the MLE yield by providing an alternative conversion pathway that does not include the hydrogenation step. A direct comparison of the catalytic performance of five different zeolites reveals that Hβ zeolite, which has high densities of both Lewis and Brønsted acid sites, affords the highest MLE yield. With the addition of 1,3,5-trioxane, the hydroxymethylation of furfural derivative and formaldehyde is a key step. Notably, the simultaneous conversion of C and C sugars catalyzed by Hβ zeolite can attain an MLE yield as high as 50.4 % when the reaction conditions are fully optimized. Moreover, the Hβ zeolite catalyst can be reused at least five times without significant change in performance.

摘要

C 和 C 混合糖同时转化为甲基戊二酸甲酯(MLE)已成为消除昂贵分离步骤的通用策略。然而,C 糖传统上升级为 MLE 非常复杂,因为它既需要酸催化又需要氢化过程。本研究涉及在近临界甲醇条件下,在 1,3,5-三恶烷的帮助下,使用不同的酸催化剂,开发一种一锅法、无氢转化 C 糖为 MLE 的方法。对于没有添加 1,3,5-三恶烷的沸石上 C 糖的转化,由于氢化活性低,MLE 的产率相当低。添加 1,3,5-三恶烷通过提供不包括氢化步骤的替代转化途径,显著提高了 MLE 的产率。五种不同沸石的催化性能的直接比较表明,具有高Lewis 和 Brønsted 酸位密度的 Hβ 沸石提供了最高的 MLE 产率。添加 1,3,5-三恶烷后,糠醛衍生物和甲醛的羟甲基化是关键步骤。值得注意的是,当反应条件完全优化时,Hβ 沸石催化的 C 和 C 糖的同时转化可以达到高达 50.4%的 MLE 产率。此外,Hβ 沸石催化剂至少可以重复使用五次,而性能没有明显变化。

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