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Method of producing 1-aminonaphthalene through fixed bed hydrogenation process

A technology of aminonaphthalene and hydrogenation method, which is applied to the preparation of amino compounds, chemical instruments and methods, and the preparation of organic compounds. High hydrogenation activity and resistance to sulfur toxicity, high reaction conversion rate and yield, simple and convenient recovery method

Inactive Publication Date: 2017-07-14
江苏华达化工集团有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The industrial production of menaphthylamine mainly adopts the nitration of industrial naphthalene to obtain nitronaphthalene and then reduces it to obtain menaphthylamine. The main reduction methods include alkali sulfide or iron powder reduction method and catalytic hydrogenation reduction method. The alkali sulfide reduction method is as described in the patent CN101973894A. The production of carnaphthylamine by sulfur and caustic soda reduction has the following main disadvantages: low product yield, poor appearance, and a large amount of difficult-to-treat waste water and waste residues, which do not meet the requirements of clean production, high energy consumption, and do not meet energy conservation and emission reduction requirements. The requirements have been gradually replaced by the catalytic hydrogenation reduction method
The catalysts that have been industrialized mainly include palladium carbon and Raney nickel. However, due to the small amount of sulfur-containing compound impurities brought by industrial naphthalene, the catalyst is easily poisoned by sulfur-containing compounds in the actual hydrogenation process, and the catalyst cannot be recycled, resulting in high catalyst cost. high
Other catalyst reports include nickel-copper composite catalysts or nitrogen-doped carbon nanotubes, such as Chinese patents CN102304053A and CN105753717A, but they are still in the experimental stage at present, and no industrialization reports have been seen.
In addition, the catalytic hydrogenation synthesis of menaphthylamine in these prior art usually adopts intermittent production mode, which has low efficiency, low catalyst activity, low yield, needs continuous replenishment, less times of mechanical application, short life, and inconvenient operation. Or small test stage, industrial implementation is more difficult

Method used

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Examples

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preparation example Construction

[0021] The preparation process of the supported nickel catalyst is as follows: the preparation process of the supported nickel catalyst is: the soluble nickel salt and the nitrate react under the action of the precipitant to obtain precipitation, filter the distilled water and wash, and then dry to obtain the crude product of the supported catalyst. The solid is calcined at 200-600° C. for 2-5 hours under a nitrogen atmosphere, and at 300-550° C. for 2-4 hours under a hydrogen atmosphere to obtain a supported nickel catalyst.

[0022] Wherein, the nitrate includes one or both of magnesium nitrate and aluminum nitrate; the precipitation agent includes sodium silicate or sodium carbonate.

[0023] The obtained supported nickel catalyst has a clover shape. The main features are as follows: 1. High mechanical strength (>20N / cm); 2. High physical surface area (100-300m 2 / g); 3. The pore size can be adjusted (6~12nm) to adapt to different molecular sizes; 4. The surface area of ​​...

Embodiment 1

[0025] Dissolve 1-nitronaphthalene in ethanol for later use, and the weight ratio of 1-nitronaphthalene to ethanol is 1:2. Fill the Ni / MgAlO catalyst in the reactor, raise the temperature to 170°C under a flowing hydrogen atmosphere, pass through the phosphating solution to start phosphine (the phosphating solution is a triphenylphosphine solution with a mass concentration of 7.5%), and after the phosphination is completed, hydrogen air Speed ​​is 500h -1 , the temperature was raised to 300°C and the aging was started for 4h.

[0026] The fixed-bed feed pump pumps the 1-nitronaphthalene solution into the fixed-bed reactor, and feeds hydrogen to control the fixed-bed temperature at 200°C, hydrogen pressure at 3.0MPa, and space velocity at 0.25h -1 , carry out the hydrogenation reaction, and at the same time use the reflux pump to pump out the reaction solution flowing out from the fixed bed, the flow rate of the feed pump is 40ml / h, collect the reaction solution, and obtain 1-...

Embodiment 2

[0028] This embodiment is basically the same as Embodiment 1, the only difference being that the temperature of the fixed bed is controlled to 130°C. After 4000 hours of continuous production, the product conversion rate is 99.6%, and the yield is 99.2%; after more than 5000 hours, the conversion rate is 98%, and the yield is 97.8%.

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Abstract

The invention discloses a method of producing 1-aminonaphthalene through a fixed bed hydrogenation process. The method includes the following steps: loading a supported nickel catalyst in a fixed bed reactor and activating the catalyst; pumping a 1-nitronaphthalene solution into the fixed bed reactor and feeding hydrogen to perform a hydrogenation reaction; when the reaction is finished, collecting a reaction liquid, and performing distillation to remove the solvent to prepare the 1-aminonaphthalene. The supported nickel catalyst has very high hydrogenation activity and sulfur toxicity resistance, and is more than 5000 h in activity stability, can be recycled and is prolonged in service life, thereby reducing production cost. In addition, the method has simple process and convenient operation, is economical and safe, is high in productivity, reaction conversion rate and yield, and satisfies industrial production demands.

Description

technical field [0001] The invention relates to the technical field of fine chemical preparation, in particular to a method for producing 1-aminonaphthalene by a fixed-bed hydrogenation method. Background technique [0002] Menaphthylamine, also known as 1-aminonaphthalene, α-aminonaphthalene, α-naphthylamine or 1-naphthylamine, is a white needle crystal with an unpleasant smell. Slightly soluble in water, easily soluble in ethanol and ether. The product is an intermediate of various dye products such as direct dyes, acid dyes, ice dyes and disperse dyes. It is the main raw material of various rubber antioxidants and is also used in organic synthesis. The industrial production of menaphthylamine mainly adopts the nitration of industrial naphthalene to obtain nitronaphthalene and then reduces it to obtain menaphthylamine. The main reduction methods include alkali sulfide or iron powder reduction method and catalytic hydrogenation reduction method. The alkali sulfide reductio...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C209/36C07C211/58B01J23/755B01J35/10
CPCC07C209/36B01J23/755B01J23/78B01J35/613B01J35/647B01J35/615C07C211/58
Inventor 徐光辉芮杰周豪
Owner 江苏华达化工集团有限公司
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