Kongprawes Grittima, Wongsawaeng Doonyapong, Hosemann Peter, Ngaosuwan Kanokwan, Kiatkittipong Worapon, Assabumrungrat Suttichai
Research Unit on Plasma Technology for High-Performance Materials Development, Department of Nuclear Engineering, Faculty of Engineering, Chulalongkorn University, Bangkok, 10330, Thailand.
Department of Nuclear Engineering, Faculty of Engineering, Chulalongkorn University, 254 Phayathai Road, Pathumwan, Bangkok, 10330, Thailand.
Sci Rep. 2024 Dec 28;14(1):31295. doi: 10.1038/s41598-024-82691-2.
Glycerol, a by-product of biodiesel production, could be converted into various value-added products. This work focuses on its dehydrogenation to dihydroxyacetone (DHA), which is mainly used in the cosmetics industry. While several methods have been employed for DHA production, some necessitate catalysts and involve harsh reaction conditions as well as long reaction times. A needle-in-tube type dielectric barrier discharge (DBD) plasma technique for catalyst-free and environmentally-friendly glycerol conversion into DHA via dehydrogenation process was investigated using 0.1 M glycerol dissolved in deionized (DI) water at ambient temperature and pressure. The optimal condition was 60 W input power, 5 mm gap distance between the end of the needle and the liquid surface, and 0.5 L/min He flow rate. The highest DHA yield of 29.3% was obtained at 3 h with a DHA selectivity of 51.6% and glycerol conversion of 56.9%. Although the system allowed over 80% of glycerol to transform after 5 h, the DHA yield decreased after 3 h because the DHA product could further react with the reactive species in the plasma. The catalyst-free DBD plasma technique offers a simple and environmentally conscious method for DHA production via the dehydrogenation of glycerol.
甘油是生物柴油生产的副产品,可转化为各种高附加值产品。这项工作聚焦于将其脱氢转化为二羟基丙酮(DHA),DHA主要用于化妆品行业。虽然已有多种方法用于生产DHA,但有些方法需要催化剂,且反应条件苛刻、反应时间长。本文研究了一种针管式介质阻挡放电(DBD)等离子体技术,该技术可在常温常压下,将溶解于去离子(DI)水中的0.1 M甘油通过脱氢过程无催化剂且环保地转化为DHA。最佳条件为输入功率60 W、针端与液面之间的间隙距离5 mm、氦气流速0.5 L/min。在3 h时获得了最高DHA产率29.3%,DHA选择性为51.6%,甘油转化率为56.9%。虽然该系统在5 h后可使80%以上的甘油发生转化,但3 h后DHA产率下降,因为DHA产物会与等离子体中的活性物种进一步反应。无催化剂的DBD等离子体技术为通过甘油脱氢生产DHA提供了一种简单且环保的方法。