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A kind of preparation method of propylene glycol

A technology of propylene glycol and co-catalyst, which is applied in the preparation of organic compounds, chemical instruments and methods, preparation of hydroxyl compounds, etc., can solve the problems of difficult suppression of side reactions, low selectivity and yield of propylene glycol, and difficult directional control.

Active Publication Date: 2021-04-06
TONGJI UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, at present, there are many difficulties in realizing the efficient conversion of sugars into propylene glycol by catalytic hydrogenolysis under the same catalyst conditions (taking glucose as an example): one is that the unidirectional isomerization of glucose into fructose is difficult; the other is that C 6 Monosaccharides carry out C 3 -C 3 It is difficult to control bond breaking; the third is difficult to suppress side reactions, and it is difficult to control the four processes of hydrolysis, isomerization, bond breaking and hydrogenation of various initial materials, intermediate products and final products involved in the system.
The above problems together lead to the low selectivity and yield of conversion of sugars to propylene glycol

Method used

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  • A kind of preparation method of propylene glycol
  • A kind of preparation method of propylene glycol
  • A kind of preparation method of propylene glycol

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preparation example Construction

[0038] Such as figure 1 Shown, a kind of preparation method of propylene glycol is provided, and described preparation method comprises the following steps at least,

[0039] S1, forming a mixed system in the reactor with sugars, main catalyst and co-catalyst;

[0040] S2. The mixed system is subjected to a hydrothermal reaction in a reducing gas atmosphere to obtain the propylene glycol, wherein the co-catalyst forms magnesium hydroxide bound to the surface of the main catalyst to form a catalytically active main catalyst- Co-catalyst composite catalyst.

[0041] Below concretely illustrate the present invention from steps S1 and S2,

[0042] Specifically, in step S1, the sugar, the main catalyst and the co-catalyst are mixed in a reactor to form a mixed system, and the reactor includes one of a tank reactor or a fixed-bed reactor. For example, in the tank reactor, the dosage of the sugars includes 10-22.5 mg / ml, and the mass ratio of the main catalyst to the co-catalyst i...

Embodiment 1

[0057] The process of in-situ hydrothermal loading of magnesium hydroxide with a mass fraction of 5%-10% (calculated as MgO) includes adding 200 mg of reduced PtNPs / SiO 2 , 10mg of light magnesium oxide powder, 112.5mg such as glucose and 10ml deionized water are added into a stainless steel reaction kettle with a capacity of 50ml and sealed. Open the intake valve, fill in 1Mpa hydrogen, and then let the gas go, repeat 3 times, so that the air in the reactor is emptied. Finally, fill in 5Mpa hydrogen, close the inlet and outlet valves. The reactor was heated to 180°C for hydrothermal in-situ loading and reaction. The stirring rate is 400 rpm, and the reaction time is 4 hours (time starts when 180° C. is reached). After the reaction was completed and cooled to room temperature, the solid and liquid were centrifuged. The liquid was analyzed by liquid chromatography and gas chromatography; the solid was washed three times with deionized water before reuse or characterization. ...

Embodiment 2

[0059] 200mg reduced PtNPs / Al 2 o 3 , PtNPs / SiO 2 One of , PtNPs / K-10, PtNPs / β-molecular sieve, 10mg-100mg light magnesium oxide powder, 112.5mg such as glucose and 10-20ml deionized water are added into a stainless steel reaction kettle with a volume of 50ml for example and sealed. Open the intake valve, fill in 1Mpa hydrogen, and then let the gas go, repeat 3 times, so that the air in the reactor is emptied. Finally, fill in 5Mpa hydrogen, close the inlet and outlet valves. The reactor was heated to 180°C for hydrothermal in-situ loading and reaction. The stirring rate is 400 rpm, and the reaction time is 4 hours (time starts when 180° C. is reached). After the reaction was completed and cooled to room temperature, the solid and liquid were centrifuged. The liquid was analyzed by gas chromatography to obtain the output of propylene glycol under different conditions, and the influence of different carrier main catalyst-magnesium hydroxide co-catalyst composite materials ...

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Abstract

The invention discloses a preparation method of propylene glycol. The preparation method at least includes the following steps of forming a mixed system in a reactor with sugars, a main catalyst and a cocatalyst. The invention can realize high selectivity and high yield of propylene glycol.

Description

technical field [0001] The invention belongs to the field of environmental chemical industry, and in particular relates to a preparation method of propylene glycol. Background technique [0002] As a high value-added chemical, propylene glycol (1,2-propanediol or 1,3-propanediol) is not only a chemical product that can be used in food, medicine, cosmetics, antifreeze and other industries, but also can be used as an intermediate platform The molecule is used in the production of unsaturated resin polyester. With the increasing demand of various industries, the world's demand for propylene glycol is increasing. At present, the production method of propylene glycol in industry still relies on petrochemical industry. According to the development concept of sustainable development, the green production of propylene glycol can be realized by catalytically converting sugars (such as cellulose, starch, glucose, etc.) into propylene glycol. However, at present, there are many diffic...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C29/00C07C31/20B01J23/42B01J23/58B01J37/18B01J35/00
CPCC07C29/00B01J23/42B01J23/58B01J37/18C07C31/205Y02P20/52C07C29/60B01J21/08B01J37/0201B01J37/0205B01J35/613B01J35/615B01J35/617B01J35/393B01J35/45B01J2235/30B01J23/02B01J23/44B01J23/464B01J35/23B01J35/40B01J35/643B01J35/647B01J35/651
Inventor 沈峥张亚雷顾敏燕
Owner TONGJI UNIV