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无溶剂条件下泛醇单酰基酯生物催化生产及放大的可持续装置

Sustainable Setups for the Biocatalytic Production and Scale-Up of Panthenyl Monoacyl Esters under Solvent-Free Conditions.

作者信息

Nieto Susana, Bernal Juana M, Villa Rocio, Garcia-Verdugo Eduardo, Donaire Antonio, Lozano Pedro

机构信息

Departamento de Bioquimica y Biologia Molecular B e Inmunologia. Facultad de Quimica, Campus de Espinardo, Universidad de Murcia, E-30100 Murcia, Spain.

Department of Biotechnology, Delft University of Technology, Building 58 Van der Maasweg 9, 2629 HZ Delft, The Netherlands.

出版信息

ACS Sustain Chem Eng. 2023 Mar 22;11(14):5737-5747. doi: 10.1021/acssuschemeng.3c00266. eCollection 2023 Apr 10.

Abstract

A sustainable scaling-up process for the biocatalytic production of new bioactive provitamin-B monoacyl esters has been demonstrated. A solvent-free reaction protocol, based on the formation of eutectic mixtures between neat substrates, renders highly efficient direct esterification of free fatty acids (., from C to C alkyl-chain length) with panthenol catalyzed by lipase. The scale-up from 0.5 to 500 g was evaluated by means of using several reaction systems (, ultrasound assistance, orbital shaking, rotary evaporator, and mechanical stirring coupled to vacuum). For all reactor systems, the yield in panthenyl monoacyl esters was improved by increasing the length of the alkyl chain of the fatty acid (, from 63% yield for panthenyl butyrate to 83% yield for panthenyl myristate). The best results (87-95% product yield, for all cases) were obtained upon a scale-up (50-500 g size) and when a vacuum system was coupled to the biocatalytic reaction unit. Under the optimized conditions, a 5-fold reduction of the amount of biocatalysts with respect to reactors without vacuum was achieved. The recovery and reuse of the immobilized enzyme for five operation cycles were also demonstrated. Finally, different metrics have been applied to assess the greenness of the solvent-free biocatalytic synthesis of panthenyl monoesters here reported.

摘要

已证明了一种用于生物催化生产新型生物活性维生素原B单酰酯的可持续扩大规模的过程。基于纯底物之间形成低共熔混合物的无溶剂反应方案,可实现脂肪酶催化的泛醇与游离脂肪酸(即碳链长度为C至C的脂肪酸)的高效直接酯化反应。通过使用多种反应系统(如超声辅助、轨道振荡、旋转蒸发仪以及与真空耦合的机械搅拌)对0.5克至500克的规模扩大进行了评估。对于所有反应器系统,通过增加脂肪酸烷基链的长度(例如,从丁酸泛醇酯的63%产率提高到肉豆蔻酸泛醇酯的83%产率),泛醇单酰酯的产率得到了提高。在规模扩大(50 - 500克规模)且生物催化反应单元与真空系统耦合时,获得了最佳结果(所有情况下产品产率为87 - 95%)。在优化条件下,与无真空的反应器相比,生物催化剂的用量减少了5倍。还证明了固定化酶可回收并重复使用五个操作循环。最后,已应用不同指标来评估本文报道的无溶剂生物催化合成泛醇单酯的绿色程度。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/ab64/10091472/098ef9c4f296/sc3c00266_0002.jpg

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