Method for preparing N,N-dimethyl cyclohexylamine

A technology of dimethylcyclohexylamine and cyclohexylamine, which can be used in the preparation of reductive alkylation, chemical instruments and methods, purification/separation of amino compounds, etc. The problems of low amine yield and complex dimethylamine recovery and utilization can achieve the effects of reasonable acidity distribution, less side reactions, and high product yield.

Active Publication Date: 2020-06-26
WANHUA CHEM GRP
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The disadvantage of this patent is that the raw material uses an aqueous solution of dimethylamine with a foul smell. Dimethylamine not only causes harm to the environment, but also increases the difficulty and cost of post-processing. In addition, the yield is low, only 98%.
[0008] (1) The use of dimethylamine is easy to cause environmental pollution, the recycling of excess dimethylamine is more complicated, and the unit consumption of dimethylamine is higher
[0009] (2) The yield of N,N-dimethylcyclohe

Method used

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  • Method for preparing N,N-dimethyl cyclohexylamine

Examples

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Example Embodiment

[0045] Example 1

[0046] 1# Modified carrier preparation:

[0047] Weigh 95g of hydrogen type ZSM-5 (with a silicon-to-aluminum ratio of 100), mix magnesium nitrate hexahydrate with 100ml of deionized water to prepare an impregnation solution containing 5g of magnesium oxide (that is, magnesium nitrate can eventually be oxidized to 5g of magnesium oxide), and then heat To form a uniform solution at 80℃, add the weighed hydrogen type ZSM-5 to the dipping solution, immerse it at 80℃ for 12h, and bake it in an oven at 110℃ for 12h; finally move to the muffle furnace, in an air atmosphere It is heated at 3°C / min to 400°C for 8h and calcined to obtain a modified carrier containing 5% MgO+95% hydrogen type ZSM-5.

[0048] 1# Preparation of supported palladium-based catalyst precursor:

[0049] Prepare a nitrate impregnation solution containing 6g palladium, 0.5g cobalt, and 0.2g zinc with 100ml deionized water, heat it to 80℃ to form a homogeneous solution, add 93.3g 1# modified carrier, ...

Example Embodiment

[0050] Example 2

[0051] 2# Modified carrier preparation:

[0052] Weigh 90g of hydrogen type ZSM-5 (with a silicon-to-aluminum ratio of 400), mix barium nitrate hexahydrate with 150ml of deionized water to prepare an immersion solution containing 10g of barium oxide, and then heat to 75°C to form a uniform solution. Hydrogen type ZSM-5 was added to the impregnation solution, immersed at 75°C for 12h, and baked in an oven at 120°C for 12h; finally moved to a muffle furnace, heated at 3°C / min to 450°C for 8h in an air atmosphere, A modified carrier containing 10% BaO+90% hydrogen type ZSM-5 is prepared.

[0053] 2# Preparation of supported palladium-based catalyst precursor:

[0054] Prepare a nitrate impregnation solution containing 4g palladium, 0.5g ruthenium, and 0.05g iron with 100ml deionized water, heat it to 80℃ to form a homogeneous solution, then add 95.45g 2# modified carrier, immerse it at 80℃ for 12h, and then Bake in an oven at 120°C for 12h; finally move to a muffle f...

Example Embodiment

[0055] Example 3

[0056] 3# Modified carrier preparation:

[0057] Weigh 95g of hydrogen type ZSM-5 (with a silicon-to-aluminum ratio of 200), mix magnesium nitrate hexahydrate and barium nitrate hexahydrate with 100ml deionized water to prepare an impregnation solution containing 3g magnesium oxide and 2g barium oxide, and then heat to 90°C to form To homogenize the solution, add the weighed hydrogen type ZSM-5 to the dipping solution, immerse it at 90℃ for 24h, and bake it in an oven at 110℃ for 12h; finally move it to the muffle furnace and place it at 3℃ in an air atmosphere. The temperature is increased to 500°C per minute and calcined for 8 hours to prepare a modified carrier containing 3% MgO + 2% BaO + 95% hydrogen type ZSM-5.

[0058] 3# Preparation of supported palladium-based catalyst precursor:

[0059] Use 200ml of deionized water to prepare a nitrate impregnation solution containing 15g of palladium, 0.1g of ruthenium, 0.1g of cobalt, and 0.4g of cerium, and heat to 80...

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Abstract

The invention discloses a method for preparing N,N-dimethyl cyclohexylamine. The method comprises the following steps: (1) adding cyclohexylamine, a solvent and a supported palladium-based catalyst into a reaction kettle, slowly adding a formaldehyde aqueous solution into the reaction kettle, and carrying out a reaction at a certain reaction temperature under a certain hydrogen pressure; (2) afterthe formaldehyde is dropwise added, raising the reaction temperature to continue the reaction to obtain a N,N-dimethyl cyclohexylamine reaction liquid; and (3) carrying out high-temperature phase splitting on the reaction liquid to obtain an oil-phase crude product, and dehydrating and rectifying the oil-phase crude product to obtain the N,N-dimethylcyclohexylamine product. The method has the advantages of cheap and easily available raw materials, high product yield, high product purity, simple process and low production cost, and is suitable for industrial mass production.

Description

technical field [0001] The invention relates to a preparation method of N,N-dimethylcyclohexylamine. Background technique [0002] N,N-Dimethylcyclohexylamine, the English abbreviation name is DMCHA, which is mainly used in the polyurethane foaming industry. Relatively balanced catalytic performance, mainly used as a gel catalyst, widely used in refrigerator materials and board materials. [0003] There are many preparation routes for N,N-dimethylcyclohexylamine, mainly including: catalytic hydrogenation of N,N-dimethylaniline, hydrogenation of phenol and dimethylamine, hydrogenation of cyclohexylamine and dimethylamine , cyclohexanone (alcohol) and dimethylamine hydrogenation method, etc., of which N,N-dimethylaniline catalytic hydrogenation method, phenol and dimethylamine hydrogenation method, cyclohexylamine and dimethylamine hydrogenation method are only It is limited to laboratory research and has no industrialization. At present, mainstream suppliers at home and ab...

Claims

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Application Information

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IPC IPC(8): C07C211/35C07C209/26C07C209/86B01J29/46
CPCC07C209/26C07C209/86B01J29/46C07C2601/14B01J2229/186B01J2229/40C07C2529/46C07C211/35
Inventor 刘振国张聪颖杨在刚姜瑞航王洪刚张兵周亚文魏运恒
Owner WANHUA CHEM GRP
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