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Catalyst and carrier with function of catalytically synthesizing amine by taking alcohol as raw material as well as preparation method and application of catalyst and carrier

A catalyst and a technology for synthesizing amines, applied in the field of ammoniation reaction, can solve the problems of low catalytic activity, achieve the effects of accelerating the reaction rate, promoting diffusion, and improving the acidity of the carrier

Pending Publication Date: 2022-05-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The purpose of the present invention is to overcome the problem of low catalytic activity in the prior art, and to provide a catalyst and carrier capable of catalytically synthesizing amines with alcohol as a raw material, as well as its preparation method and application

Method used

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  • Catalyst and carrier with function of catalytically synthesizing amine by taking alcohol as raw material as well as preparation method and application of catalyst and carrier
  • Catalyst and carrier with function of catalytically synthesizing amine by taking alcohol as raw material as well as preparation method and application of catalyst and carrier
  • Catalyst and carrier with function of catalytically synthesizing amine by taking alcohol as raw material as well as preparation method and application of catalyst and carrier

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Embodiment approach

[0029] According to the present invention, the carrier can be prepared by an existing method capable of obtaining the ammonia adsorption capacity meeting the above range, and obtaining a carrier with the ammonia adsorption capacity meeting the above range can be implemented by those skilled in the art. However, according to a preferred embodiment of the present invention, the carrier is prepared by a method comprising the following steps: sequentially molding, drying and calcining the mixture containing dopant ions and carrier precursor, wherein the carrier modifier It is at least one of an inorganic acid containing dopant ions and an inorganic salt containing dopant ions (the inorganic acid is not hydrochloric acid), and the temperature of the calcination is above 800°C. The molding method can be kneading, ball rolling or chipping.

[0030] In the preparation method of the above carrier, the carrier precursor can be selected from pseudoboehmite, silicon oxide precursor (such ...

Embodiment 1

[0057] Pseudoboehmite powder (specific surface area 380m 2 / g, pore volume 1.09ml / g) kneaded with dilute acid water containing 5vol% nitric acid and 3.5vol% phosphoric acid, extruded into strips, dried at 120°C for 10h, and then calcined at 850°C for 4h to make the required The carrier, the specific parameters are shown in Table 1.

[0058] 141.56g nickel nitrate hexahydrate (industrial grade, purity 98%) was dissolved into 166mL solution with water, and its pH value was adjusted to 4.3, and the solution was loaded on the obtained 100g alumina carrier by spraying twice, each spraying After immersion, all were dried at 120°C for 8 hours, then calcined at 400°C for 4 hours, then gradually reduced with hydrogen at a rate of 20°C / hour, and finally reduced at 440°C for 3 hours to obtain catalyst C-1 .

Embodiment 2

[0060] Pseudoboehmite powder (specific surface area 400m 2 / g, pore volume 1.15ml / g) kneaded with dilute acid water containing 5vol% nitric acid and 3vol% boric acid, added silica sol (JN-40, Qingdao Ocean) during the kneading process, extruded into strips, dried at 120°C for 12h, Then calcined at 900°C for 4 hours to make the required carrier. The specific parameters are shown in Table 1. The amount of pseudo-boehmite powder and silica sol makes the Al in the carrier 2 o 3 with SiO 2 The weight ratio is 4:1.

[0061] 176.38g of cobalt nitrate hexahydrate (industrial grade, purity 98%) was dissolved into 160mL solution with water, and its pH value was adjusted to 3.9, and the solution was loaded on the obtained 100g carrier by wet immersion twice. All were dried at 120°C for 6 hours, then calcined at 390°C for 4 hours, then gradually reduced with hydrogen at a rate of 20°C / hour, and finally reduced at 460°C for 5 hours to obtain catalyst C-2.

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Abstract

The invention relates to the field of catalysts, and discloses a catalyst with a function of catalytically synthesizing amine by taking alcohol as a raw material, a carrier as well as a preparation method and application of the catalyst. The catalyst contains a carrier, and an active component and an optional auxiliary agent loaded on the carrier, and is characterized in that the carrier has specific characteristic parameters, and the active component is cobalt and / or nickel. The catalyst disclosed by the invention has relatively high catalytic activity and relatively high selectivity when being used for alcohol hydroammonification reaction.

Description

technical field [0001] The invention relates to the field of ammoniation reaction, in particular to a catalyst and carrier capable of catalyzing the synthesis of amines by using alcohol as a raw material, as well as a preparation method and application thereof. Background technique [0002] Amines are very important industrial organic compounds that are widely used in various fields, such as solvents, pharmaceutical intermediates, resin raw materials, textile additives, insecticides, rubber stabilizers, corrosion inhibitors, and also used in cleaning and plastic processing. The three main methods for preparing amines are hydroamination of carbonyl compounds, hydroamination of alcohols, and hydrogenation of nitriles. The hydroamination of carbonyl compounds is, for example, the reaction of acetone, hydrogen and ammonia to generate isopropylamine. The hydrogenation of alcohols is, for example, the hydrogenation of ethanol and ammonia to generate ethylamine, the hydrogenation ...

Claims

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Application Information

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IPC IPC(8): B01J23/75B01J23/755B01J23/889B01J23/89B01J23/80B01J23/843B01J32/00B01J35/10B01J21/04B01J21/12B01J27/043B01J27/138B01J27/185B01J27/187C07C209/16C07C211/10C07C211/12
CPCB01J23/75B01J23/755B01J23/8892B01J23/8896B01J23/892B01J23/80B01J23/8437B01J27/043B01J27/138B01J27/1853B01J27/187B01J21/04B01J21/12C07C209/16C07C211/10C07C211/12B01J35/635B01J35/615
Inventor 田保亮唐国旗向良玉彭晖王国清杨溢宋超
Owner CHINA PETROLEUM & CHEM CORP