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Production process of glutamic acid and monosodium glutamate

A production process and technology of glutamic acid, applied in the field of production technology of glutamic acid and monosodium glutamate, can solve the problems of increasing waste water, bulky liquid, and poor quality of glutamic acid impurities, saving process water and improving total income. rate, the effect of saving usage

Inactive Publication Date: 2010-06-16
BEIJING PIHUA BIOLOGICAL TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The disadvantages of this process are: the volume of the liquid for ion exchange is huge, which greatly increases the consumption of sulfuric acid and ammonia water, and at the same time inevitably increases a large amount of waste water, the cost of raw materials and environmental protection is high, and the obtained glutamic acid impurities are of poor quality.
[0006] In addition, glutamic acid production adopts a continuous isoelectric process, that is, the glutamic acid fermentation liquid is properly concentrated and controlled at about 40°C, and is continuously added to the isoelectric tank with seed crystals, and sulfuric acid is added at the same time to control the pH value of the isoelectric tank. Around 3.2, the temperature is 40°C for crystallization, the waste water discharge of this process is relatively small, but the extraction rate of glutamic acid and product quality are poor

Method used

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  • Production process of glutamic acid and monosodium glutamate
  • Production process of glutamic acid and monosodium glutamate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] a. Concentration:

[0047] Take the glutamic acid fermentation liquid with a mass percentage concentration of 11% to 12%, enter the four-effect evaporator for concentration, the conditions are: the temperature of the first effect evaporator is 90-95°C, and the glutamic acid concentration after concentration is 17%- 18%, the temperature of the second-effect evaporator is 80-85°C, the concentration of glutamic acid after concentration is 20-22%, the temperature of the third-effect evaporator is 70-75°C, the concentration of glutamic acid after concentration is 25-28% , the temperature of the fourth effect evaporator is 60-65 DEG C, after concentration, a concentrated fermentation broth with a mass percentage concentration of glutamic acid of 30%-32% is obtained, and concentrated condensed water is collected.

[0048] The fermentation broth is first concentrated to reduce the amount of liquid entering the subsequent steps, which can not only reduce the consumption of sulfu...

Embodiment 2

[0073] Steps a~g are the same as embodiment 1.

[0074] h. Crystal transformation, cooling and separation: heating the suspension of glutamic acid crystals containing α-crystal form obtained after the second crystal washing in step d to 80-90° C. to adjust the pH to 4.0-5.0, Cool to 40°C to generate a suspension containing β-crystalline glutamic acid crystals, filter, wash and dehydrate at the same time with a filter separator to obtain β-crystalline glutamic acid crystals, wherein the mother liquor is obtained three times after filtration and returned to step d. In the first crystal washing, add washing water to wash and dehydrate the glutamic acid crystals in the β crystal form, and then return to step d for the second crystal washing.

[0075] i. Neutralization and refining: add soda ash or caustic soda solution to the glutamic acid crystals of β crystal form, neutralize to PH = 7, the obtained crude neutralization solution is refined, and the refined mother liquor and mono...

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Abstract

The invention discloses a production process of glutamic acid and monosodium glutamate, which comprises the following steps: firstly, evaporating and concentrating fermentation liquid; after concentrated sulfuric acid is added for isoelectric operation, cooling to 5-15 DEG C; obtaining an alpha-crystalline glutamic acid crystal suspension after primary separation, primary crystal washing, secondary separation and secondary crystal washing; regulating the pH value to be 4.0-5.0 at 80-90 DEG C, cooling to 35 DEG C, and obtaining a beta-crystalline glutamic acid crystal through filtration and separation, wherein the beta-crystalline glutamic acid crystal can be dried by air flow to obtain glutamic acid products, and the beta-crystalline glutamic acid crystal can be continuously neutralized and refined to obtain monosodium glutamate products; carrying out cyclone precipitation on primary mother liquid after primary separation, removing protein in supernatant liquid by flocculation air flotation process, and drying the protein to obtain bacterial protein powder; and carrying out ion exchange on the deproteinized clear liquid to prepare compound fertilizer. The extraction method of the glutamic acid provided by the invention fundamentally reduces the generation of waste water, improves the extraction yield and the product quality, reduces the amount of water for exchanging ions and washing columns to the minimum, and has higher production efficiency and lower production cost.

Description

technical field [0001] The invention relates to a production process of glutamic acid and monosodium glutamate. Background technique [0002] Monosodium glutamate is a safe seasoning food, which is indispensable in the consumer market. my country is a big producer and consumer of monosodium glutamate, with an annual output of more than 1.7 million tons of monosodium glutamate. The monosodium glutamate industry pays attention to sustainable development, and environmental protection issues have become the key to influence. [0003] Glutamic acid, also known as L-1-aminopropane-1,3-dicarboxylic acid, is divided into α and β crystal forms, and the β form is usually more stable. Glutamic acid is one of the basic amino acids for nitrogen metabolism in living organisms, and it is of great significance in metabolism. Glutamic acid is mainly used to produce umami flavor agents such as monosodium glutamate and chicken essence. [0004] The production process of glutamic acid is mai...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C229/24C07C227/42A23L1/228A23L27/22
Inventor 束松坡凡晓峰黄国营石铁山史光辉杨新尚
Owner BEIJING PIHUA BIOLOGICAL TECH
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