4.4 Article

Selective Hydrogenolysis of Biodiesel Waste Bioglycerol Over Titanium Phosphate (TiP) Catalysts: The Effect of Pt & WO3 Loadings

Journal

WASTE AND BIOMASS VALORIZATION
Volume 13, Issue 11, Pages 4389-4402

Publisher

SPRINGER
DOI: 10.1007/s12649-022-01909-4

Keywords

Glycerol; 1,3-propanediol; Platinum; WO3; Titanium phosphates

Funding

  1. University of Oulu including Oulu University Hospital
  2. IICT Hyderabad
  3. CSIR, Delhi, India

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The study investigates the production of 1,3-propanediol from glycerol, an important by-product of biodiesel production. By adjusting the composition of the catalyst and reaction conditions, the researchers achieved a sustainable and cleaner process for glycerol conversion with high efficiency.
Glycerol is an important by-product (biowaste) from biodiesel production. Transformation of glycerol into value-added compounds is critical in improving the overall efficiency of the biodiesel production. In this work, a sustainable and cleaner production of 1,3-propanediol (1,3-PDO) by vapor phase hydrogenolysis of glycerol was performed over titanium phosphate (TiP) supported catalysts by varying the Pt and WO3 loadings (5-20 wt.%). The WO3 promoted Pt modified TiP catalysts were prepared by a simple wet impregnation method and characterized by various analytical techniques in determining the key properties. Furthermore, the catalyst activity and stability were studied under different reaction conditions. The synergistic effects of Pt and WO3 loadings on the final performance of the catalyst has been significant in improving the hydrogen transfer rate. Both Pt and WO3 promotional effects is envisaged the enhanced catalytic properties in conjunction with TiP support acidity. WO3 incorporation increased Bronsted acidity and formed strong interactions with Pt over TiP support. Both Lewis and Bronsted acid sites presented but BAS played a key role in enhancing the 1,3-PDO selectivity in a bifunctional dehydration-hydrogenation reaction mechanism of glycerol. The effect of reaction temperature, contact times and the weight hour space velocity were evaluated. Overall, under optimized reaction conditions, 2 wt.% Pt-10 wt.% WO3/TiP catalyst displayed superior activity with a maximum glycerol conversion of similar to 85% and similar to 51% of 1,3-PDO selectivity achieved at time on stream of 4 h. [GRAPHICS] .

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