Selective Transformation of Glycerol to Lactic Acid by Porous Multifunctional Mixed Oxide Catalysts Under Alkaline Environment

Abdurahman, Mohamed Hussein; Yaacob, Muhammad Hazim; Basir, Nor Irwin; Abdullah, Ahmad Zuhairi

doi:10.1007/978-3-030-44176-0_9

Cited by 1 publication

(1 citation statement)

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“…This is due to oversaturation of the glycerol market; according to glycerol market analysis, biodiesel industry became the highest contributor to the glycerol market at around 67% in comparison to other contributing industries such as fatty acid (21%), fatty alcohol (8%), soap, and others (4%). The glycerol market is dominated by biodiesel companies, who took over 55% of the market, due to the implementation of anti-dumping duties for biodiesel in the United States and Europe, forcing them to sell the excess glycerol [19,20]. The production of large amounts glycerol and its low price have forced biodiesel enterprises to pay extra for storing and handling the excess glycerol, which consequently can hinder the development of the biodiesel industry [21].…”

Section: Introductionmentioning

confidence: 99%

Production of Propanediols through In Situ Glycerol Hydrogenolysis via Aqueous Phase Reforming: A Review

et al. 2022

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Production of 1,2-propanediol and 1,3-propanediol are identified as methods to reduce glycerol oversupply. Hence, glycerol hydrogenolysis is identified as a thermochemical conversion substitute; however, it requires an expensive, high-pressure pure hydrogen supply. Studies have been performed on other potential thermochemical conversion processes whereby aqueous phase reforming has been identified as an excellent substitute for the conversion process due to its low temperature requirement and high H2 yields, factors which permit the process of in-situ glycerol hydrogenolysis which requires no external H2 supply. Hence, this manuscript emphasizes delving into the possibilities of this concept to produce 1,2-propanediol and 1,3-propanediol without “breaking the bank” with expenses. Various heterogenous catalysts of aqueous phase reforming (APR) and glycerol hydrogenolysis were identified, whereby the combination of a noble metal, support, and dopant with a good amount of Brønsted acid sites are identified as the key factors to ensure a high yield of 1,3-propanediol. However, for 1,2-propanediol, a Cu-based catalyst with decent basic support is observed to be the key for good yield and selectivity of product. The findings have shown that it is possible to produce high yields of both 1,2-propanediol and 1,3-propanediol via aqueous phase reforming, specifically 1,2-propanediol, for which some of the findings achieve better selectivity compared to direct glycerol hydrogenolysis to 1,2-propanediol. This is not the case for 1,3-propanediol, for which further studies need to be conducted to evaluate its feasibility.

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Section: Introductionmentioning

confidence: 99%