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Preparation method of catalyst for preparing arylamine from nitro compound through hydrogenation

A technology of nitro compounds and hydrogenation catalysts, which is applied in the preparation of amino compounds, organic compounds, catalyst activation/preparation, etc. It can solve the problems of difficult wastewater treatment, waste of resources, long process flow, etc., to ensure filtration performance, Improve activity and eliminate the effect of internal diffusion

Pending Publication Date: 2022-05-27
WANHUA CHEM GRP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

TDI tar residues are dense solids. At present, after being broken, they are treated by incineration, which causes waste of resources and produces a large amount of nitrogen oxides; patent CN201520845024.7 provides a method for resource utilization of TDI tar residues and recovery of TDA, using high temperature The method of high-pressure hydrolysis converts urea and CDI in the tar residue to TDA, thereby recovering TDA, but this method produces a large amount of difficult-to-treat wastewater in the production process
Patent CN201910304883.8 provides a method of using TDI tar residue to prepare liquid fuel, but the preparation process is relatively complicated, and a large amount of N in tar will also produce a large amount of NOx when incinerated as liquid fuel
Patent CN201910304878.7 provides a recovery method for the precious metal Pt element in TDI tar residue, the process flow is long and the recovery economy is not high

Method used

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  • Preparation method of catalyst for preparing arylamine from nitro compound through hydrogenation
  • Preparation method of catalyst for preparing arylamine from nitro compound through hydrogenation

Examples

Experimental program
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Effect test

Embodiment 1

[0046] Weigh 300g of TDI tar residue A, grind it, the average particle size of the tar residue after grinding is 11 μm, and roast the tar residue after grinding at 380°C for 2h in a nitrogen atmosphere for pyrolysis treatment (NH4 is generated during the roasting process. 3 and CO 2 ), cooling to obtain a porous carbon carrier, the carrier content of N element is 0.3%, and the content of Ni element is 0.3%.

[0047] Weigh 0.80g La (NO 3 ) 3 ·6H 2 O, 1.43g Fe(NO 3 ) 3 ·9H 2 O, 19.82g Ni (NO 3 ) 2 ·6H 2 O, 19.91g EDTA in 300ml deionized water, 30wt% ammonia water was slowly added dropwise to the above solution under vigorous stirring, the pH value was adjusted to 8, 5.5g carrier powder was added, and 28KHz was ultrasonically treated at 25°C for 12h, then Dry at 120°C for 12h. A solid powder was obtained, which was refluxed and reduced in a 50 wt% hydrazine hydrate aqueous solution for 2 hours. The reduced catalyst was filtered, washed with deionized water until neutral...

Embodiment 2

[0049] Weigh 300g of TDI tar residue B, and roast the tar residue after grinding at 450°C for pyrolysis treatment for 4h in a nitrogen atmosphere (NH is generated during the roasting process. 3 and CO 2 ), cooling to obtain a porous carbon carrier, the carrier content of N element is 0.1%, and the content of Ni element is 0.1%.

[0050] Weigh 0.21g LaCl 3 ·6H 2 O, 0.29g FeCl 3 , 2.21g NiCl 2 , 4.98g of EDTA in 200ml of deionized water, 50wt% ammonia water was slowly added dropwise to the above solution under vigorous stirring, the pH value was adjusted to 8.5, 8.8g of carrier powder was added, and 35°C was ultrasonically treated at 40KHz for 10h, at 150 Dry at ℃ for 24h. The solid powder was obtained, which was refluxed and reduced in a 60 wt% hydrazine hydrate aqueous solution for 3 hours. The reduced catalyst was filtered, washed with deionized water until neutral, and calcined at 300°C for 4 hours in a nitrogen environment to obtain catalyst B. The Ni content of catal...

Embodiment 3

[0052] Weigh 300g of TDI tar residue C, grind it, the average particle size of the tar residue after grinding is 15 μm, and roast the tar residue after grinding at 600°C for 0.5h in a nitrogen atmosphere for pyrolysis treatment (NH4 is generated during the roasting process. 3 and CO 2 ), cooling to obtain a porous carbon support, the content of N element in the support is 1%, and the content of Pt element is 0.05%.

[0053] Weigh 0.133g La (NO 3 ) 3 ·6H 2 O, 3.61g Fe(NO 3 ) 3 ·9H 2 O, 0.33g PdCl 2 , 0.80gH 2 PtCl 6 ·6H 2 O, 1.55g CrDTA in 300ml deionized water, 30wt% ammonia water was slowly added dropwise to the above solution under vigorous stirring, the pH value was adjusted to 8, 8.9g carrier powder was added, and 30°C was ultrasonically treated at 34KHz for 12h. Dry at 120°C for 12h. The solid powder was obtained, which was refluxed and reduced in a 55 wt% hydrazine hydrate aqueous solution for 2 hours. The reduced catalyst was filtered, washed with deionized w...

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Abstract

The invention provides a preparation method of a catalyst for preparing arylamine through liquid phase hydrogenation of a nitro compound. The catalyst is prepared by adopting an impregnation method and comprises the steps of carrier preparation, loading, reduction and roasting activation. According to the method, the catalyst carrier is prepared from the TDI tar residues, resource utilization of the TDI tar is achieved, hydrogenation activity of the catalyst is enhanced through the synergistic effect of the N element in the TDI tar residues and the hydrogenation activity metal while the hydrogenation activity metal in the TDI tar residues is recycled, and the activity of the hydrogenation catalyst is improved. The invention also provides application of the catalyst in preparation of aniline through hydrogenation, and the catalyst is excellent in reaction performance and good in stability.

Description

technical field [0001] The invention belongs to the field of catalysts, and in particular relates to a preparation method of a catalyst for preparing aromatic amines by hydrogenation of nitro compounds. Background technique [0002] Aromatic amines are important intermediates for the synthesis of many fine chemicals and are widely used, mainly for the manufacture of dyes, drugs, resins, etc., such as aniline (AN), toluenediamine (TDA), etc. With the rapid development of (MDI), methyl diisocyanate, etc., the demand for aromatic amines is increasing day by day. [0003] Catalytic hydrogenation of nitro compounds is the main method for industrial production of aromatic amines, mainly including gas-phase hydrogenation technology and liquid-phase hydrogenation technology. The gas-phase hydrogenation technology requires a large amount of circulating hydrogen, which requires a high capacity of the circulating hydrogen compressor, the reaction temperature is not easy to control, th...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/83B01J23/89B01J35/10B01J37/08B01J37/03B01J37/34B01J37/16C07C209/36C07C211/51C07C211/46
CPCB01J23/83B01J23/894B01J37/084B01J37/035B01J37/343B01J37/16B01J37/082C07C209/36B01J35/393B01J35/23B01J35/615C07C211/51C07C211/46Y02P20/584
Inventor 胡淼邓如雷魏立彬黄舜尧吴雪峰
Owner WANHUA CHEM GRP CO LTD