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A kind of preparation method of catalyst for caprolactam amination

A technology of caprolactam and catalyst, applied in the direction of catalyst activation/preparation, preparation of organic compounds, physical/chemical process catalysts, etc., can solve the problems of low conversion rate, low reaction temperature, low selectivity, etc., and achieve low cost and simple preparation , Preparation and easy-to-obtain effect

Active Publication Date: 2022-04-15
CHINA CATALYST HLDG CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the preparation of 6-aminocapronitrile is mainly obtained by partial hydrogenation of 1,6-adiponitrile. The preparation of 6-aminocapronitrile by caprolactam has a gas phase method and a liquid phase method. The liquid phase method mainly uses phosphate as a catalyst, and the reaction temperature Low, but the conversion rate is relatively low
The gas-phase method uses one or more of alkaline earth metal oxides, transition metal oxides, silicon oxide or alumina as a catalyst. Compared with the liquid-phase method, the conversion rate is higher, but the selectivity is low, and the catalyst is not used for a long time.

Method used

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  • A kind of preparation method of catalyst for caprolactam amination
  • A kind of preparation method of catalyst for caprolactam amination
  • A kind of preparation method of catalyst for caprolactam amination

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0024] Weigh 5g of magnesium nitrate, 5g of aluminum nitrate, 1g of nickel nitrate and 150g of water to prepare a mixed solution, weigh 100g of phospho-aluminum molecular sieve, and add the aqueous solution of the active component to the phospho-aluminum molecular sieve; the rotary evaporator is heated to 60° C. After 4 hours, the water was drained under reduced pressure; the filter cake was dried at 120 °C, formed, and calcined at 550 °C for 6 hours to obtain the catalyst (see the morphology and specific surface area). Figure 1-3 ). 4 g of the calcined catalyst was loaded into a fixed bed, and the temperature was raised to 420° C. The caprolactam was dissolved in acetonitrile and then fed at a space velocity of 0.5h-1. The reaction solution was cooled and collected, and the sampling was controlled. The conversion rate of the raw material caprolactam was 81%, and the product The selectivity of 6-aminocapronitrile is greater than 99.0%.

Embodiment 2

[0026] Weigh 7g of magnesium nitrate, 7g of aluminum nitrate, 1g of nickel nitrate and 170g of water to prepare a mixed solution, weigh 100g of phospho-aluminum molecular sieve, and add the aqueous solution of the active component to the phospho-aluminum molecular sieve; the rotary evaporator is heated to 65 ° C, rotate After 4 hours, the water was drained under reduced pressure; the filter cake was dried at 120 °C, formed, and calcined at 550 °C for 5 hours to obtain the catalyst. 4 g of the calcined catalyst was loaded into a fixed bed, heated to 450 °C, and the caprolactam was dissolved in acetonitrile and fed at a space velocity of 0.5 h-1. The reaction liquid was cooled and collected, and the sampling was controlled. The conversion rate of the raw materials was 82.2%, and the selectivity greater than 99.0%.

Embodiment 3

[0028] Weigh 9g of magnesium nitrate, 9g of aluminum nitrate, 2g of nickel nitrate and 200g of water to prepare a mixed solution, weigh 100g of phospho-aluminum molecular sieve, and add the aqueous solution of the active component into the phospho-aluminum molecular sieve; the rotary evaporator is heated to 65° C. After 4 hours, the water was drained under reduced pressure; the filter cake was dried at 120°C, formed, and calcined at 550°C for 6 hours to obtain the catalyst. 4 g of the calcined catalyst was loaded into a fixed bed, heated to 420°C, and the caprolactam was dissolved in acetonitrile and fed at a space velocity of 0.5h-1. The reaction solution was cooled and collected, and the sampling was controlled. The conversion rate of the raw materials was 82.2%, and the selectivity greater than 99.0%.

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Abstract

The invention discloses a method for preparing a catalyst for ammonification of caprolactam. Aluminophosphorus molecular sieve is used as a carrier, and a certain amount of active components of magnesium nitrate, aluminum nitrate and nickel nitrate are carried by an impregnation method at a certain temperature. After drying, molding and roasting, the ammoniated dehydration catalyst is obtained, and the catalyst is packed in a fixed bed, and caprolactam and ammonia are reacted at 420-500°C and 0-1mpa; the preparation method of the catalyst obtained by this method is simple, and the caprolactam The conversion rate is greater than 80%, and the selectivity of 6-aminocapronitrile is greater than 99%.

Description

technical field [0001] The invention belongs to a method for synthesizing organic compounds, and relates to a method for preparing a catalyst for caprolactam amination. Background technique [0002] 6-Aminocapronitrile is an important chemical intermediate and an important raw material for the preparation of hexamethylenediamine, which can produce the polymer nylon 66. At present, the preparation of 6-aminocapronitrile is mainly obtained by partial hydrogenation of 1 and 6-adiponitrile. The preparation of 6-aminocapronitrile from caprolactam has a gas phase method and a liquid phase method. The liquid phase method mainly uses phosphate as a catalyst. low, but the conversion rate is relatively low. The gas phase method uses one or more of alkaline earth metal oxides, transition metal oxides, silica or alumina as the catalyst. Compared with the liquid phase method, the conversion rate is higher, but the selectivity is low, and the catalyst is not used for a long time. SUMMA...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/83B01J37/02C07C253/00C07C255/24
CPCB01J29/83B01J37/0201C07C253/00C07C255/24
Inventor 王庆吉王蕊李小龙王炳春王贤彬李进
Owner CHINA CATALYST HLDG CO LTD
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