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Catalyst for preparing 1,2-propylene glycol by glycerinum hydrogenation and preparation method thereof

A catalyst and hydrogen preparation technology, which is applied in chemical instruments and methods, organic compound/hydride/coordination complex catalysts, physical/chemical process catalysts, etc., can solve the problem of high equipment investment costs, complex catalyst systems, and harsh reaction conditions and other issues, to achieve good industrial application prospects, low production costs, and short production cycles

Active Publication Date: 2014-03-26
CHINA PETROLEUM & CHEM CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Under the condition that the temperature is higher than 200°C and the pressure is higher than 20MPa, this method can obtain 1,2-propanediol in high yield, but the reaction conditions are harsh and the catalyst system is complex
[0007] Chinese patent CN 1061968C describes a method for preparing 1,2-propanediol by catalytic hydrogenolysis of glycerol under high temperature and high pressure. Using a catalyst containing metal cobalt, copper, molybdenum and manganese, the yield of 1,2-propanediol can be as high as 95%, but the reaction pressure is 20~32MPa, higher pressure will lead to higher investment cost of the device and greater difficulty in operation
[0012] 3. Catalysts containing metal cobalt, copper, molybdenum and manganese, the reaction pressure is as high as 20~32MPa, and the higher pressure leads to higher investment cost and more difficult operation of the device
[0013] 4. Using Cu-based catalysts and using gas-phase glycerin feed requires a higher ratio of hydrogen to glycerin, resulting in higher energy consumption and high raw material costs

Method used

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  • Catalyst for preparing 1,2-propylene glycol by glycerinum hydrogenation and preparation method thereof
  • Catalyst for preparing 1,2-propylene glycol by glycerinum hydrogenation and preparation method thereof
  • Catalyst for preparing 1,2-propylene glycol by glycerinum hydrogenation and preparation method thereof

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0049] (1) Catalyst preparation: Weigh 9.44g copper nitrate, 1.91g potassium chloride, and 10g silicotungstic acid, respectively, and dissolve them in distilled water, immerse them in 41.5g aluminum oxide carrier, let stand for 5h, dry at 120℃, 400 After calcination at ℃ for 5 hours, a catalyst containing 5% copper, 2% potassium, 10% silicotungstic acid, and 83% aluminum oxide can be prepared.

[0050] (2) The reaction is carried out in a continuous flow fixed-bed reactor: the catalyst loading is 10ml, the reaction pressure is 6MPa, the reaction temperature is 185℃, and the glycerol volumetric space velocity is 1.0h -1 , The hydrogen / glycerol molar ratio is 3:1, the reaction time is 10h, and the test results are shown in Table 1.

Embodiment 2

[0052] (1) Catalyst preparation: Weigh 17.32g of nickel nitrate, 7.28g of cobalt nitrate, and 7.5g of silicotungstic acid, respectively, and dissolve them in distilled water, immerse them on 37.5g of aluminum oxide carrier, stand for 5h, and dry at 120℃, 450 After calcination at ℃ for 5 hours, a catalyst containing 7% nickel, 3% cobalt, 15% silicotungstic acid, and 75% aluminum oxide can be prepared.

[0053] (2) The reaction is carried out in a continuous flow fixed-bed reactor: the catalyst loading is 10ml, the reaction pressure is 5MPa, the reaction temperature is 190℃, and the glycerol volumetric space velocity is 0.8h -1 , The hydrogen / glycerol molar ratio is 4:1, the reaction time is 15h, and the test results are shown in Table 1.

Embodiment 3

[0055] (1) Catalyst preparation: Weigh 22.88g zinc nitrate, 8.99g manganese chloride, and 7.5g phosphotungstic acid respectively, dissolve them in distilled water, immerse them on 35g silica carrier, let stand for 5h, dry at 120℃, 400℃ After calcination for 5 hours, a catalyst containing 10% zinc, 5% manganese, 15% phosphotungstic acid and 70% silica can be prepared.

[0056] (2) The reaction is carried out in a continuous flow fixed-bed reactor: the catalyst loading is 10ml, the reaction pressure is 5.5MPa, the reaction temperature is 195℃, and the volumetric space velocity of glycerol is 1.2h -1 , The hydrogen / glycerol molar ratio is 5:1, the reaction time is 20h, and the test results are shown in Table 1.

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Abstract

The invention discloses a catalyst for preparing 1,2-propylene glycol by glycerinum hydrogenation and a preparation method of the catalyst, and belongs to a catalyst containing metal or a metallic oxide. The catalyst is characterized by comprising the following raw material components in percentage by weight: 10%-40% of heteropoly acid, 30%-90% of a carrier, 5%-20% of active components, and 0.5%-10% of a modified component. The catalyst and the preparation method thereof provided by the invention have the advantages that the activity is high, the selectivity is good, a reaction condition is mild, the reaction speed is high, the conversion rate of the raw materials is high, and the energy consumption is low. The catalyst provided by the invention has an acid site and a metal hydrogenation site, is a dual-function catalyst, is high in reactivity, selectivity and stability, still keeps the high efficiency at the large air speed, and has good industrial application prospect; the catalyst provided by the invention has the advantages that the operating pressure is low, the equipment investment is saved, the energy consumption is low, and the glycerinum conversion rate can achieve 90.12%.

Description

Technical field [0001] The invention is a catalyst for preparing 1,2-propanediol by hydrogenation of glycerol and a preparation method thereof. Belongs to catalysts containing metals or metal oxides. Background technique [0002] 1,2-Propylene glycol is an important chemical raw material, which is mainly used as raw material for unsaturated polyester resin, epoxy resin and polyurethane resin. Among them, unsaturated polyester is widely used in surface coatings and reinforced plastics. Because of its low toxicity, wettability and excellent solubility, propylene glycol is widely used in food, medicine and cosmetics, and is used to produce tobacco wetting agents, small animal foods, polymer plasticizers and special plasticizers. Recently, it has developed new applications for liquid detergents. [0003] In recent years, with the shortage of energy in the world, the biodiesel industry has developed rapidly. The process of preparing biodiesel produces a large amount of by-product glyc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J31/26B01J31/18B01J31/38C07C31/20C07C29/60
Inventor 贾庆龙菅秀君楚庆岩王申军刘淑芝何宗华马瑞杰潘清
Owner CHINA PETROLEUM & CHEM CORP
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