Preparation method of solid acid esterification catalyst

A technology of esterification and catalyst, applied in physical/chemical process catalysts, chemical instruments and methods, chemical/physical processes, etc., can solve the problems of low catalytic activity of solid acid, inability to catalyze esterification reaction, affecting catalyst activity, etc. To achieve the effect of strong acidity, low production cost and preventing agglomeration

Inactive Publication Date: 2011-05-25
XIAMEN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

If the pH value is too low, it will affect the activity of the catalyst, or even basically no acidity, and it will not be able to catalyze the esterification reaction
The classic precipitation and impregnation method to prepare SO 4 2- / ZrO 2 In the case of solid acid, the method of adding concentrated ammonia water to the zirconium salt solution is generally adopted. During the precipitation process, a gradient change in pH value will occur, making the resulting precipitation uneven, and ultimately resulting in low catalytic activity of the solid acid.

Method used

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  • Preparation method of solid acid esterification catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] 0.1mol / L of ZrO(NO 3 ) 2 Solution 200ml and mass fraction are 25%~28% concentrated ammonia water 26ml, add dropwise and stir simultaneously, ZrO(NO 3 ) 2 The ratio of the rate of addition of the solution to the concentrated ammonia water is 8: 1, and the pH value of the control is 9 to produce Zr(OH) 4 Precipitation, aging for 1 h, filtration, and vacuum drying to obtain a zirconium hydroxide precursor. Then impregnate 0.5mol / gH according to 15ml / g zirconium hydroxide precursor 2 SO 4 The ratio of the solution, the zirconium hydroxide precursor is impregnated, dried and calcined in a muffle furnace at 550°C for 3h to obtain SO 4 2- / ZrO 2 solid acid catalyst.

[0026] will get SO 4 2- / ZrO 2 Solid acid catalyst is used for the esterification reaction of higher fatty acid oleic acid and glycerin, in reactor, add 26.7g oleic acid, 90ml soybean oil, 45ml n-butanol, 45ml glycerol, at normal pressure, under 140 ℃, add 1wt% solid Acid Catalyst SO 4 2- / ZrO 2 , ...

Embodiment 2

[0028] Under stirring at room temperature, 0.5mol / L of ZrO(NO 3 ) 2 200ml of the solution and 130ml of concentrated ammonia water with a mass fraction of 25% to 28%, were added dropwise and stirred simultaneously, ZrO(NO 3 ) 2 The ratio of the rate of addition of the solution to the concentrated ammonia water is 1.5: 1, and the pH value of the control is 8 to produce Zr(OH) 4 Precipitation, aging for 8 hours, filtration, and vacuum drying to obtain a zirconium hydroxide precursor. Then impregnate 1mol / g H with 10ml / g zirconium hydroxide precursor 2 SO 4 The ratio of the solution, the zirconium hydroxide precursor is impregnated, dried and calcined in a muffle furnace at 650°C for 3h to obtain SO 4 2- / ZrO 2 solid acid catalyst.

[0029] will get SO 4 2- / ZrO 2 The solid acid catalyst was used for the esterification reaction of higher fatty acid oleic acid and glycerin, carried out according to the method described in Example 1, and the esterification rate was 78% af...

Embodiment 3

[0031] Under stirring at room temperature, 1mol / L of ZrO(NO 3 ) 2 Solution 200ml and mass fraction are 25%~28% concentrated ammonia water 260ml, add dropwise and stir simultaneously, ZrO(NO 3 ) 2 The ratio of the rate of addition of the solution to the concentrated ammonia water is 1: 1.3, and the pH value of the control is 10 to produce Zr(OH) 4 Precipitation, aging for 24 hours, filtration, and vacuum drying to obtain a zirconium hydroxide precursor. Then impregnate 1mol / g H with 15ml / g zirconium hydroxide precursor 2 SO 4 The ratio of the solution, the zirconium hydroxide precursor is impregnated, dried and calcined in a muffle furnace at 800°C for 3h to obtain SO 4 2- / ZrO 2 solid acid catalyst.

[0032] will get SO 4 2- / ZrO 2The solid acid catalyst was used for the esterification reaction of higher fatty acid oleic acid and glycerin, carried out according to the method described in Example 1, and the esterification rate was 69% after 4 hours of reaction.

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Abstract

The invention provides a preparation method of a solid acid esterification catalyst, relating to a catalyst. The preparation method has the following beneficial effects: the activity of a solid acid catalyst can be remarkably improved, and especially, the catalytic activity of the catalyst reaches or approaches liquid acid level when the catalyst is used for catalyzing esterification reaction of higher fatty acid. The preparation method comprises the following steps: simultaneously dropwise adding zirconium salt solution used as a raw material and ammonia water serving as a precipitator and stirring the two substances to ensure the pH value to be 8-10 to generate zirconium hydroxide precipitate; aging and then drying the zirconium hydroxide precipitate; soaking the dried zirconium hydroxide in sulfuric acid solution to obtain a solid acid esterification catalyst precursor; and drying and then calcining the solid acid esterification catalyst precursor to obtain the SO4<2-> / ZrO2 solid acid esterification catalyst. By using the preparation method, the following defects are overcome: the esterification reaction catalysts in the prior art pollute environment, have high cost and low catalyst activity and can not participate in the esterification reaction of the higher fatty acid.

Description

technical field [0001] The invention relates to a catalyst, in particular to a preparation method of a solid esterification catalyst. Background technique [0002] Organic esters are widely used in organic synthesis industries such as solvents, plasticizers, resins, coatings, flavors and fragrances, cosmetics, medicines, and surfactants. Esterification is an important part of chemical production, an important way to synthesize raw materials and intermediates, and the main source of many daily and production supplies. The esterification reaction generally uses an acid catalyst. With the development of society, human beings have higher and higher requirements for the environment. Traditional liquid acid catalysts are easy to corrode equipment, produce a large amount of industrial wastewater, and easily cause damage to the environment. Therefore, they are gradually being replaced by environmentally friendly solid acid catalysts. replaced. [0003] In 1979, Makoto Hino and Ka...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J21/06B01J35/02
Inventor 张国玉杨乐夫蔡钒方维平蔡俊修
Owner XIAMEN UNIV
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