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Purification process of methionine

A methionine and process technology, which is applied in the field of methionine purification process, can solve problems affecting product quality and yield, environmental secondary pollution, and accompanying precipitation of salt substances, etc., to simplify the production process, improve product quality, and reduce production. cost effect

Active Publication Date: 2015-09-23
SUNRESIN NEW METERIALS CO LTD XIAN +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the production process of both methods, there will be a process requirement that methionine solution and salt-containing by-products need to be separated. There is no effective desalination method in the existing production methods, resulting in the precipitation of a large amount of salt substances when the product crystallizes, which affects the quality of the product. and yield, increasing the production cost of methionine
[0005] Patent 201310317849.2 "Method and device for removing impurities in secondary methionine mother liquor" discloses a method and device for removing impurities in secondary methionine mother liquor. The method uses diatomite, activated carbon or activated clay. The adsorption efficiency of these adsorbents is It is relatively low, and cannot be recycled through effective means after adsorption, causing secondary pollution to the environment, and is not suitable for industrial applications
Patent 201310194709.5 "A Production Process of Methionine" discloses a method for separating the methionine crystallization mother liquor. The methionine crystallization mother liquor is separated through a continuous chromatographic separation system filled with sodium-type or potassium-type chromatographic resins to obtain a methionine solution and an inorganic salt solution; This method is only suitable for the crystallization mother liquor with low methionine content, but it has not been verified and no effective solution has been proposed for the separation of high-content methionine solution and by-product salts in industrial production

Method used

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  • Purification process of methionine
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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] 1. Resin adsorption: Pass methionine solution (pH: 10.72, methionine content 17.24% (w / w), sodium carbonate content 10.35% (w / w)) through 100ml XDA- 1 Resin bed (produced by Xi'an Lanxiao Technology New Material Co., Ltd.), collect the resin effluent separately, and stop feeding into the resin column when the methionine content in the effluent at the bottom of the resin column is 1.7%.

[0032] 2. Resin desorption: 2BV of 3% sodium hydroxide solution desorbs the resin from top to bottom at a flow rate of 1BV / h, and collects the desorption solution.

[0033] 3. Collect 300 ml of resin effluent, and detect that the content of methionine is 0.02%, and the content of sodium carbonate is 10.35%. 200ml of the desorption solution was collected, the content of methionine was detected to be 24.60%, and the yield of methionine was 95.15%.

Embodiment 2

[0035] 1. Resin adsorption: adjust the pH of the liquid methionine solution to 2.2 with 2% sulfuric acid solution (the content of methionine is 2.8% (w / w), the content of potassium sulfate is 17.4% (w / w)), and the flow rate is 1BV / h from top to bottom Pass through a 100ml XDA-8 resin bed (produced by Xi'an Lanxiao Technology New Materials Co., Ltd.) at a lower uniform speed, collect the resin effluent separately, and stop feeding to the resin column when the methionine content in the effluent at the bottom of the resin column is 0.3%.

[0036] 2. Resin desorption: 3BV of 4% methanol solution desorbs the resin from top to bottom at a flow rate of 1BV / h, and collects the desorption solution.

[0037] 3. Collect 700 ml of resin effluent, and detect that the content of methionine is 0.01%, and the content of potassium sulfate is 17.38%. 302ml of the desorption solution was collected, the content of methionine was detected to be 6.45%, and the yield of methionine was 98.76%.

Embodiment 3- Embodiment 9

[0039] The specific embodiment is the same as that in Example 1, mainly investigating the influence of methionine solutions with different pH on the adsorption capacity of the resin. (Not stated in the experiment are all mass percentage concentrations)

[0040] Methionine content: 2.80%, ammonium sulfate content 43.5%, potassium carbonate content 2.1%. Feed volume 7BV, feed flow rate 1BV / h, prepare 5 parts of XDA-1 resin, each 100ml resin. The methionine solution was adjusted to pH 1.0, 3.0, 7.0, 9.0, 10.0 with 4% sodium hydroxide or 4% sulfuric acid solution respectively, and the adsorption control test was carried out.

[0041] Resin adsorption capacity = (feed methionine content * feed volume - effluent methionine content * effluent volume) / resin volume

[0042] Example

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PUM

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Abstract

The invention provides a purification process of methionine. By separating methionine and by-product salts with macroporous resin, and by absorption and desorption, a methionine product not less than 99% in purity is obtained; the methionine content of the by-products is not greater than 0.03%. The yield of the methionine by the resin is not less than 98%. The purification process has the advantages that the existing production process can be simplified, the methionine quality can be improved, and the methionine production cost can be reduced.

Description

Technical field: [0001] The invention belongs to the field of chemical industry, and in particular relates to a process for purifying methionine. Background technique: [0002] Methionine, also known as methionine or methionine, is closely related to the metabolism of various sulfur-containing compounds in organisms. When methionine is lacking, it will cause loss of appetite, slow growth or no weight gain, kidney enlargement and iron accumulation in the liver, and finally lead to liver necrosis or fibrosis. Another kind of methionine, called methionine hydroxyl derivatives (ie liquid methionine), is widely used as a feed additive and can be used as a methionine nutritional supplement to promote animal growth and development. [0003] Both methionine and liquid methionine are a kind of amino acid, the only difference is that at the α position, the methionine is connected to -NH2, while the liquid methionine is connected to -OH. When the solution pH<pI (isoelectric point)...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C323/58C07C319/28
CPCC07C323/58B01D15/265C07C319/28B01J20/285B01D15/12B01D15/426
Inventor 寇晓康王日升王刚刘琼任婉萍
Owner SUNRESIN NEW METERIALS CO LTD XIAN
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