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Method for separation and purification of monomethylamine-dimethylamine mixture in methylamine synthesis system

A technology of monomethylamine dimethylamine and dimethylamine, applied in the field of separation, can solve the problems of loss of DMF products, increase of equipment investment, steam consumption, etc., to reduce the loss of dimethylamine, low equipment investment cost, and economic benefits high effect

Active Publication Date: 2017-11-03
TIANJIN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Increase the discharge of the tower kettle, and discharge a large amount of dimethylamine products while draining the water. In the existing process, the discharged heavy components cannot be returned to the previous separation system, otherwise heavy components such as methylethylamine and ethylamine will be released. Accumulated in the system, these components enter the DMF synthesis system with dimethylamine, and other amide by-products will be generated. If they are discharged, more DMF products will be lost, and the problem will become more serious.
The second measure is to further purify by connecting a new tower in series, which not only requires an increase in equipment investment, but more importantly, it consumes steam and increases the energy consumption of the product

Method used

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  • Method for separation and purification of monomethylamine-dimethylamine mixture in methylamine synthesis system
  • Method for separation and purification of monomethylamine-dimethylamine mixture in methylamine synthesis system
  • Method for separation and purification of monomethylamine-dimethylamine mixture in methylamine synthesis system

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Effect test

Embodiment 1

[0023] According to the method of the present invention, the mixed raw materials of monomethylamine and dimethylamine from the dehydration tower are separated, the separation main tower and the side line tower are all packed towers, the feed composition is shown in the data in the table below, and the feed temperature is 50°C. The feed rate is 18 tons / h, the top pressure of the separation main tower is 0.68MPa, the top temperature is 46.3°C, the bottom temperature is 82°C, the reflux ratio is 5.0, the top pressure of the side line tower is 0.66MPa, and the top temperature of the side line column is 62.8 DEG C, reflux ratio is 2.0, separated by rectifying tower, main tower top monomethylamine product and side line tower top dimethylamine product quality are also listed in the table below, the content of water in the side line product dimethylamine is 0.012%.

[0024] Element

Embodiment 2

[0026] According to the method of the present invention, the mixed raw materials of monomethylamine and dimethylamine from the dehydration tower are separated, the separation main tower and the side line tower are all packed towers, the feed composition is shown in the data in the table below, and the feed temperature is 50°C. The feed rate is 18 tons / h, the top pressure of the separation main tower is 0.7MPa, the top temperature is 47.0°C, the bottom temperature is 80°C, the reflux ratio is 7.0, the top pressure of the side line tower is 0.68MPa, and the top temperature is 63.5°C , the reflux ratio is 2.0, separated by the rectifying tower, the main tower top monomethylamine product and the side line tower top dimethylamine product quality are also listed in the table below, and the content of water in the side line product dimethylamine is 0.010%.

[0027] Element

Embodiment 3

[0029]According to the method of the present invention, the mixed raw materials of monomethylamine and dimethylamine from the dehydration tower are separated, the separation main tower and the side line tower are all packed towers, the feed composition is shown in the data in the table below, and the feed temperature is 50°C. The feed rate is 18 tons / h, the top pressure of the separation main tower is 0.60MPa, the top temperature is 41.5°C, the bottom temperature is 75°C, the reflux ratio is 4.0, the top pressure of the side line tower is 0.58MPa, and the top temperature is 58.0°C , the reflux ratio is 0.5, separated by the rectifying tower, the main tower top monomethylamine product and the side line tower top dimethylamine product quality are also listed in the table below, and the content of water in the side line product dimethylamine is 0.008%.

[0030]

[0031]

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PUM

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Abstract

The invention relates to a method for separation and purification of monomethylamine and dimethylamine in a methylamine synthesis system. According to the invention, a mixed raw material of monomethylamine and dimethylamine passing through a dehydration tower is fed from the central part of a main separation tower; light and heavy components are separated in a main separation tower; monomethylamine is distilled off from the top of the main separation tower and flows into a monomethylamine product tank for storage via an output pipeline; the heavy components consisting of water, methanol and a mixture of ethylmethylamine and ethylamine flow into a raffinate tank from the bottom of the main separation tower; dimethylamine gas carrying heavy components flows into a side column only having a rectifying section via a connecting pipeline; in the side column, dimethylamine migrates to the top of the side column, and the carried heavy components return to the main separation tower after mass transfer separation and are then discharged from the bottom of the main separation tower; and a dimethylamine product is obtained from the top of the side column. The method provided by the invention can reduce the content of water in the dimethylamine product and improve the purity of the dimethylamine product without increasing the steam consumption of the product, and has the advantages of low investment cost for equipment, low energy consumption and high economic benefits.

Description

technical field [0001] The invention relates to a separation and purification method for a mixture of monomethylamine and dimethylamine in a methylamine synthesis system, and belongs to the field of separation technology. Background technique [0002] Methylamine products include monomethylamine (MMA), dimethylamine (DMA) and trimethylamine (TMA). Methylamine is produced by the reaction of methanol and ammonia. Among the three methylamines, dimethylamine is used in the largest amount. Dimethylamine is mainly used as a raw material for the production of rubber vulcanization accelerators, leather depilatory agents, medicines, and pesticides. The biggest use of dimethylamine lies in the production of high-quality chemical fiber solvents and polyurethane solvents - N,N-dimethylformamide (DMF) and N,N-dimethylacetamide (DMAC). The purity of the raw material dimethylamine has a great influence on the product quality and cost of the amide. The heavy component moisture and methylet...

Claims

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Application Information

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IPC IPC(8): C07C209/86C07C211/04
CPCC07C209/86C07C211/04
Inventor 杨长生孙斐忠史诺
Owner TIANJIN UNIV
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