Reusability studies with Lewis and Brønsted acid catalysts for dehydration of the primary alcohol 1-hexanol under energy-saving conditions†

Adil Allahverdiyev and Harald Gröger
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Abstract

In general, currently there is an urgent need to switch from fossil-based materials to renewable resources and this is also the case for production of alkenes with a chain length of up to C6 due to their broad application range as bulk chemicals. For instance, such C6 alkenes (hexenes) are accessible from 1-hexanol, for which recently a sustainable technical approach based on CO2 and water as renewable raw materials was reported by Siemens and Evonik Industries, making use of artificial photosynthesis in combination with microbial syngas fermentation. In continuation of our very recent comprehensive study on dehydration of 1-hexanol and other alcohols with a focus on Lewis acids and initial reusability studies over a few reaction cycles, the current study presents a simplified strategy for the reuse of the Lewis acid catalysts Cu(OTf)2 and Hf(OTf)4 and the Brønsted acid TfOH as well as a proof-of-concept for efficient recycling over 20 cycles. Over the course of the study, the catalysts demonstrated an average alkene yield of 71–77%, with no loss of activity. The production costs were calculated on the basis of industry-appropriate prices, with the lowest being 0.34 $ per kg. A successful initial lab scale-up with a 100-fold increase in reaction volume indicates a TRL4 for the developed process and enabled a product formation of 1.3 kg. Thus, these studies underline the technical feasibility of the developed dehydration process using 1-hexanol, for which catalyst recycling represents a key criterion.

Abstract Image

Lewis和Brønsted酸催化剂在节能条件下脱水伯醇1-己醇的可重复使用性研究
总的来说,目前迫切需要从化石基材料转向可再生资源,对于链长高达C6的烯烃的生产也是如此,因为它们作为散装化学品的应用范围很广。例如,从1-己醇中可以获得C6烯烃(己烯),西门子和赢创工业最近报道了一种基于二氧化碳和水作为可再生原料的可持续技术方法,利用人工光合作用与微生物合成气发酵相结合。我们最近对1-己醇和其他醇的脱水进行了全面的研究,重点是刘易斯酸和几个反应周期的初步可重用性研究,目前的研究提出了一个简化的刘易斯酸催化剂Cu(OTf)2和Hf(OTf)4以及Brønsted酸TfOH的重复使用策略,并对20个循环的有效回收进行了概念验证。在整个研究过程中,催化剂的平均烯烃产率为71-77%,且没有活性损失。生产成本按行业合理价格计算,最低为每公斤0.34美元。最初的实验室放大实验成功,反应体积增加了100倍,表明该工艺的TRL4达到了1.3 kg的产量。因此,这些研究强调了利用1-己醇开发脱水工艺的技术可行性,其中催化剂回收是一个关键标准。
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