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A kind of solid acid catalyst tip/atp and its preparation method and application

A solid acid catalyst, catalyst technology, applied in catalyst activation/preparation, catalyst carrier, chemical instruments and methods, etc., can solve the problems of not too high catalytic efficiency, low yield of target product, low catalytic efficiency, etc. Moderate, good market application prospects, stable structure

Active Publication Date: 2018-11-16
RUNTAI CHEM TAIXING CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the disadvantage of heterogeneous catalysts is that the catalytic efficiency is not too high
[0006] At present, the biggest disadvantage of solid acid catalysts is that the catalytic efficiency is not high, and the yield of the target product is low. Therefore, how to improve the catalytic efficiency of the catalyst and the yield of the product is the focus of future research.
What the present invention researches is a kind of novel catalyst, also has not reported about application in cellulose hydrolysis

Method used

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  • A kind of solid acid catalyst tip/atp and its preparation method and application

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] The process flow diagram of the present invention is as figure 1 shown. Specifically, the original attapulgite is first sieved with a 100-mesh sieve to obtain relatively fine attapulgite particles. Weigh 20 g of crude ATP with a solid-to-liquid ratio of 1:10 (g / ml), add it to 5 mol / L hydrochloric acid, condense and reflux for 12 h under magnetic stirring at 80 ° C, and then let stand for 2 h. Then filter and wash until neutral (use silver nitrate solution to detect the presence of no chloride ions). Finally, the pretreated attapulgite was obtained by drying at 105°C for 12 hours.

[0031] 200mL concentration of 1mol / L precipitant (NH 4 ) 2 HPO 4 Added to 100mL concentration is 1mol / LTiCl 4 solution to form a mixed solution. Then, according to the ratio of TiP to ATP of 1:2, ATP after the above-mentioned pretreatment was added to the solution formed above, and then the solution was allowed to stir at room temperature for 24 h. Then the solution was filtered, wash...

Embodiment 2

[0033] Sieve the original attapulgite with a 100-mesh sieve to obtain finer attapulgite particles. Weigh 20 g of ATP crude product at a solid-to-liquid ratio of 1:10 (g / ml), add it to 5 mol / L nitric acid, condense and reflux for 12 h under magnetic stirring at 80 ° C, and then let stand for 2 h. Then filter and wash until neutral. Finally, the pretreated attapulgite was obtained by drying at 105°C for 12 hours.

[0034] 200mL concentration of 1mol / L precipitant (NH 4 ) 2 HPO 4 Added to 100mL concentration is 1mol / LTiCl 4 solution to form a mixed solution. Then, according to the ratio of TiP to ATP of 1:2, ATP after the above-mentioned pretreatment was added to the solution formed above, and then the solution was stirred at room temperature for 24 h. Then the solution was filtered, washed until the pH was around 5, and finally dried at 100°C for 12 hours. The catalyst obtained above was calcined at 500° C. for 3 h, and finally ground to form a solid acid catalyst TiP / ATP...

Embodiment 3

[0036] Sieve the original attapulgite with a 100-mesh sieve to obtain finer attapulgite particles. Weigh 20g of ATP crude product at a solid-to-liquid ratio of 1:10 (g / ml), add it to 5mol / L hydrochloric acid, condense and reflux for 12h under magnetic stirring at 80°C, and then let stand for 2h. Then filter and wash until neutral (use silver nitrate solution to detect the presence of no chloride ions). Finally, the pretreated attapulgite was obtained by drying at 105°C for 12 hours.

[0037] 200mL concentration of 1mol / L precipitant (NH 4 ) 2 HPO 4Added to 100mL concentration is 1mol / LTiCl 4 solution to form a mixed solution. Then, according to the ratio of TiP to ATP of 1:1, ATP after the above-mentioned pretreatment was added to the solution formed above, and then the solution was stirred at room temperature for 24 h. Then the solution was filtered, washed until the pH was around 5, and finally dried at 100°C for 12 hours. The catalyst obtained above was calcined at 5...

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Abstract

The invention discloses a solid acid catalyst TiP / ATP. The solid acid catalyst adopts attapulgite as carrier, and TiP is carried by the carrier. Specifically, TiP / ATP is prepared from TiCl4, ATP and precipitator (NH4)2HPO4 by precipitation and impregnation, TiP / ATP is then activated by calcination, and thereby the solid acid catalyst TiP / ATP is obtained. The solid acid catalyst prepared by the invention can be applied in cellulose hydrolyzation. The yield of HMF obtained by the hydrolyzation of cellulose by the solid acid catalyst prepared by the invention is moderate, the solid acid catalyst is easy to separate and recycle, production cost is reduced, and the solid acid catalyst has a good market application prospect.

Description

technical field [0001] The invention belongs to the field of catalysts, and in particular relates to a solid acid catalyst TiP / ATP and a preparation method and application thereof. Background technique [0002] With the rapid development of economy and society, fossil energy is becoming increasingly exhausted, and the existing fossil energy cannot meet people's needs. At the same time, the use of fossil energy has caused serious environmental pollution. In view of the serious problems of energy crisis and environmental pollution, a new renewable green energy is imminent. [0003] The earth is rich in biomass energy, and the content of biomass energy in my country is also very rich. Through biorefining, biomass is primarily carbohydrates formed through photosynthesis of carbon dioxide and water. Therefore, the carbon dioxide emitted by biomass energy is almost equal to the carbon dioxide absorbed, so biomass energy is a renewable green energy. Biomass can be converted into...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J37/02B01J37/03B01J32/00B01J27/182C07D307/46
Inventor 许琦周吉祥唐喆蔡照胜丁成
Owner RUNTAI CHEM TAIXING CO LTD