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Method for separating and purifying glycine by using N, N-dibutyl ethanolamine

A technology of glycine and ethanolamine, applied in chemical instruments and methods, preparation of organic compounds, preparation of aminohydroxy compounds, etc., can solve problems such as difficulty in product separation, and achieve the effects of green operation process, convenient large-scale operation, and convenient addition.

Pending Publication Date: 2022-05-27
YANGZHOU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In general, the advantage of homogeneous reactions lies in their higher activity and selectivity, but the separation of products is more difficult

Method used

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  • Method for separating and purifying glycine by using N, N-dibutyl ethanolamine
  • Method for separating and purifying glycine by using N, N-dibutyl ethanolamine
  • Method for separating and purifying glycine by using N, N-dibutyl ethanolamine

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0042] Dissolve 4 g of crude glycine in 10 mL of water, stir magnetically at room temperature until completely dissolved, to obtain a solution of crude glycine. Take 20ml of N,N-dibutylethanolamine and add it to the crude glycine solution, pass CO for 12h at 5°C 2 . The solid and liquid were obtained by centrifugation, the solid was washed three times with ethanol, and dried in an oven at 100 °C for 8 h to obtain a fine glycine product.

[0043] The liquid obtained by centrifugation was heated at 60 °C for 6 h, and liquid-liquid separation was performed. The upper layer was recovered as oil phase N,N-dibutylethanolamine, and ammonia water was added to the lower water phase of the mother liquor. The molar ratio of the water phase and the ammonia water was 1:3, and the liquid - Liquid separation, recovery of the upper oil phase N,N-dibutylethanolamine.

[0044] The yield of the above method for separating and purifying glycine is 80%, and the recovery rate of N,N-dibutylethano...

Embodiment 2

[0046] Dissolve 4 g of crude glycine in 10 mL of water, stir magnetically at room temperature until completely dissolved, to obtain a solution of crude glycine. Take 20ml of N,N-dibutylethanolamine and add it to the crude glycine solution, pass CO for 12h at 10°C 2 . The solid and liquid were obtained by centrifugation, the solid was washed three times with ethanol, and dried in an oven at 100 °C for 8 h to obtain a fine glycine product.

[0047] The liquid obtained by centrifugation was heated at 60 °C for 6 h, and liquid-liquid separation was performed. The upper layer was recovered as oil phase N,N-dibutylethanolamine, and ammonia water was added to the lower water phase of the mother liquor. The molar ratio of the water phase and the ammonia water was 1:3, and the liquid - Liquid separation, recovery of the upper oil phase N,N-dibutylethanolamine.

[0048] The yield of separation and purification of glycine by the above method is 76%, and the recovery rate of N,N-dibutyl...

Embodiment 3

[0050] Dissolve 4 g of crude glycine in 10 mL of water, stir magnetically at room temperature until completely dissolved, to obtain a solution of crude glycine. Take 20ml of N,N-dibutylethanolamine and add it to the crude glycine solution, pass CO for 12h at 15°C 2 . The solid and liquid were obtained by centrifugation, the solid was washed three times with ethanol, and dried in an oven at 100 °C for 8 h to obtain a fine glycine product.

[0051] The liquid obtained by centrifugation was heated at 60 °C for 6 h, and liquid-liquid separation was performed. The upper layer was recovered as oil phase N,N-dibutylethanolamine, and ammonia water was added to the lower water phase of the mother liquor. The molar ratio of the water phase and the ammonia water was 1:3, and the liquid - Liquid separation, recovery of the upper oil phase N,N-dibutylethanolamine.

[0052] The yield of the above method for separating and purifying glycine is 69%, and the recovery rate of N,N-dibutylethan...

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Abstract

The invention provides a method for separating and purifying glycine by using N, N-dibutyl ethanolamine, and glycine is separated and purified by using a hydrophilic variable carbon dioxide switch solvent constructed by the N, N-dibutyl ethanolamine. The introduced carbon dioxide is non-toxic, non-corrosive, non-chlorinated, cheap and rich, is convenient to add and convenient for large-scale operation, and can be easily removed through air or heating, and the operation process is green and economical. The mother liquor separated and purified by the method can be heated to recover the N, N-dibutyl ethanolamine on the upper layer of the mother liquor, and ammonia water is added into the lower layer of the mother liquor to recover part of the N, N-dibutyl ethanolamine, so that the consumption of the N, N-dibutyl ethanolamine is fundamentally reduced, and the N, N-dibutyl ethanolamine can be recycled for multiple times. The yield of the purified industrial glycine can reach 83%, and the recovery rate of the N, N-dibutyl ethanolamine is 85%.

Description

technical field [0001] The invention belongs to the technical field of chemical separation, in particular to a method for separating and purifying glycine by utilizing N,N-dibutylethanolamine. Background technique [0002] Glycine is a building block of proteins, and it is often used as a food additive or as a raw material for agrochemicals and synthetic drugs. China is the world's major producer of glycine, but it also consumes a large amount of glycine every year. my country's industrial production of glycine mainly adopts the monochloroacetic acid (MAC) method. This method has low requirements for equipment, simple technological process, easy-to-obtain raw materials, and can produce glycine on a large scale, but the crude glycine produced contains ammonium chloride, etc. Inorganic salts that cannot be separated. In the existing glycine separation and purification process, methanol is generally added in the purification stage, and glycine and ammonium chloride are separat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C229/08C07C227/40C07C213/10C07C215/08
CPCC07C229/08C07C227/40C07C213/10C07C215/08Y02P20/10
Inventor 周莹王剑吴栓王雅琼
Owner YANGZHOU UNIV