Method for continuously preparing 1,3-propanediol by one-step glycerol conversion
A technology of propylene glycol and glycerin, which is applied in the fields of chemical instruments and methods, elimination of hydroxyl groups, organic chemistry, etc., can solve the problems of limiting the wider application of microbial fermentation methods, low initial concentration of glycerin, complicated separation and purification, etc., to achieve continuous process Low cost of production, separation and purification, simple and easy purification process
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Embodiment 1
[0022] A tubular fixed-bed reactor with a length of 60 cm and an inner diameter of 12 mm was used. The catalyst is zirconia / tungsten oxide composite oxide with platinum attached, the particle size is 20-40 mesh, and the weight ratio of three metal elements is: platinum: tungsten: zirconium = 2: 10: 64.7.
[0023] The above-mentioned catalyst was first passed through hydrogen at 250° C., and then activated for 1 hour. Take 2 ml of the activated catalyst and put it into the reactor.
[0024] The reaction raw materials are glycerol aqueous solution with a weight concentration of 60% and hydrogen, and the hydrogen / glycerol volume ratio is 1200; the glycerin volume space velocity is 0.25h -1 , the reaction temperature is 130°C, and the reaction pressure is 4MPa.
[0025] The raw material glycerol and hydrogen are continuously input from the upper inlet of the reactor. After the reaction, the reaction product is continuously discharged from the lower outlet of the reactor. After ga...
Embodiment 2
[0028] The reaction temperature is 120° C., and other conditions are the same as in Example 1.
[0029] Reaction product obtains through chromatographic analysis, and glycerol transformation rate is 34.8%, contains 7.5% (weight) of 1,3-propanediol, 0.7% (weight) of 1,2-propanediol, 5.9% (weight) of n-propanediol in the reaction mixture alcohol and 1.2% by weight isopropanol. The yield of 1,3-propanediol was 15.3% relative to the charged amount of glycerin (excluding water).
[0030] Compared with Example 1, this example shows that reducing the reaction temperature reduces the conversion rate of glycerol, and the content of 1,3-propanediol and the yield of 1,3-propanediol in the mixture after the reaction are also slightly reduced.
Embodiment 3
[0032] Reaction temperature is 140 ℃, and other conditions are all identical with embodiment 1.
[0033]The reaction product obtains 60.5% of glycerol conversion ratio through chromatographic analysis, contains 10.7% (weight) of 1,3-propanediol, 0.9% (weight) of 1,2-propanediol, 12.4% (weight) of n-propanol and 2.1% by weight isopropanol. The yield of 1,3-propanediol was 21.6% relative to the charged glycerol (water not included).
[0034] Compared with Example 1, this example shows that the temperature of reaction is increased, and the conversion rate of glycerol increases, which improves the weight content of 1,3-propylene glycol and the productive rate of 1,3-propylene glycol in the reaction mixture, but the product 1,3-propylene glycol selectivity is reduced.
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