In particular, hydrogenolysis of glycerol, a bio-diesel by-product, can produce propylene glycol (PG), 1,3-propanediol, ethylene glycol (EG), as well as propanols for many downstream applications such as anti-freezes, polyesters, pharmaceuticals, and solvents.
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Propylene glycol is also used to create artificial smoke or fog used in fire-fighting training and in theatrical productions. Other names for propylene glycol are 1,2-dihydroxypropane, 1,2-propanediol, methyl glycol, and trimethyl glycol.
Characterization and Experimental Investigation of Glycerol and Propylene glycol in Water Solutions for cool Thermal Energy Storage Abstract: This study aims to develop PCM for low
Owing to its abundant feedstock and unique properties, glycerol is a good candidate in catalysis, high-value-added chemical conversion, and solvents. It can also be used as an energy transportation medium attributed to its high
Factors to Consider When Buying Glycol Storage Tanks. The storage tank type and material among other properties largely depend on the glycol compound to be stored in it, such as ethylene glycol or propylene glycol, among other
The hydrogenolysis of glycerol leads to the production of glycols, 1,2-propylene glycol (1,2-PG) and 1,3-propylene glycol (1,3-PG). In particular, 1,3-PG has the highest added
Main Difference – Propylene Glycol vs Glycerin. Propylene glycol and glycerin often appear the same since they are colourless, odourless, sweet and syrupy. Although they share some physical properties, they have
The energy content of the pure glycerol is 19.0 MJ/kg, however for crude glycerol it is 25.30 MJ/kg, possibly due to presence of methanol and biodiesel [10]. Such high energy content of crude glycerol indicates its
Simple Summary: Propylene glycol (PG) and glycerol are common energy substances used to supplement the feed of transitioning ruminants in order to minimize the development of metabolic
In particular, hydrogenolysis of glycerol, a bio-diesel by-product, can produce propylene glycol (PG), 1,3-propanediol, ethylene glycol (EG), as well as propanols for many downstream applications such as anti-freezes,
Research on the use of biomass resources for the generation of energy and chemical compounds is of great interest worldwide. The development and growth of the biodiesel industry has led to a parallel market for the supply
The result showed that glycerol and propylene glycol in water solutions suitable to be used as PCM for cold thermal energy storage applications. Published in: 2018 International
The present invention describes a process for the production of propylene glycol from glycerol, the transformation of purified glycerol to propylene glycol being carried out by means of a reaction
The synthesized catalysts produced 43.3% glycerol conversion and 76.1% selectivity at 200°C, 5 MPa H 2 for 6 h (Yu et al., 2010). Table 2 summarizes previous studies on the use of metal-based catalyst for hydrogenolysis of glycerol to propylene glycol.
However, majority of the worldwide consumption of propylene glycol is from petroleum-based propylene oxide, a process that is characterized by greenhouse gas emission release. Hydrogenolysis of glycerol is an alternative route for the production of propylene glycol.
Any product that may be evaluated in this article or claim that may be made by its manufacturer is not guaranteed or endorsed by the publisher. Hydrogenolysis of glycerol to propylene glycol represents one of the most promising technologies for biomass conversion to chemicals. However, conventional h...
In the presence of hydrogen, the vapor-phase reaction facilitates the conversion of glycerol to propylene glycol in a single reactor. Although this approach has been demonstrated in a continuous process, challenges of scalability and catalyst recycling still remain.
Moreover, the selected route for the production of acetol and propylene glycol from glycerol includes a vapor-phase reaction over the copper-chromite catalyst in a packed bed reactor. In the presence of hydrogen, the vapor-phase reaction facilitates the conversion of glycerol to propylene glycol in a single reactor.
Studies on the conventional catalytic hydrogenolysis of glycerol to renewable propylene glycol Catalyst: Cu–Cr. Pressure= 4.15 MP, temp=210 ° C, time =10 h, catalyst=5% w/w of glycerol Catalyst: 5 wt.% Ru/Al 2 O 3 and 5 wt.% Pt/Al 2 O 3 mixtures. No external hydrogen, time: 6 h, temp= 220 ° C.
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