Preparation technology of propionic acid

A preparation process, propionic acid technology, applied in the field of propionic acid preparation process, can solve the problems of harsh operating conditions, low production efficiency, high cost, etc., achieve the effect of reducing production cost, improving production efficiency and purity, and facilitating industrial promotion and application

Inactive Publication Date: 2018-08-07
SHANDONG PROVINCE & TAI WEI RUN FOOD TECH CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Microorganisms can use a variety of fermentable sugars to produce propionic acid. In industry, various biomass can be hydrolyzed into simple sugars such as glucose or xylose with acid or enzyme, and then introduced into the reactor for fermentation. After the fermentation is completed, milk of lime is added. Precipitate, filter and add sodium sulfate for metathesis reaction, then filter and concentrate, add sulfuric acid for conversion and then carry out fractional distillation. The fermentation reactor can use immobilized protoplast tower reactor, and the cells are fixed in the following form: by immersion method Cover the surface of the pre-sterilized filling ring with a layer of sterilized solution containing 20% ​​gelatin and 1.5% shellac, and spray it with 2.5% glutaraldehyde aqueous solution after drying to cross-link the polymer on the surface of the filling ring , to increase the strength, rinse with sterile water, then sterilize with ethylene glycol, blow out ethylene glycol with sterilized nitrogen, and then add propionic acid bacteria culture solution to the reactor filled with this filled ring, so that It forms a layer of fixed cell membrane on the surface of the filling ring, and then can be continuously fed for fermentation, but the chemical synthesis method has heavy pollution, high cost, and harsh operating conditions. Therefore, the biological fermentation method has become an important way to prepare propionic acid. Among them, biological fermentation The selection of nitrogen source, pH value, and selection of raw materials in the method all have a greater impact on the production of propionic acid. With the improvement of human living standards, the importance of health is getting higher and higher, and the requirements for products are also increasing. More and more strict, the existing biological fermentation of propionic acid has problems such as low production efficiency, low purity and high cost. Therefore, it is very promising to design a production process for propionic acid with high production efficiency and low cost.

Method used

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  • Preparation technology of propionic acid

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Embodiment 1

[0017] Propionic acid preparation process described in the present embodiment, it specifically comprises the following steps:

[0018] (1) Sterilization treatment: steam the fermenter with 0.6Mpa steam for 30 minutes, blow it with sterile air, and dry it;

[0019] (2) Inoculation and saccharification: add 30m 3 deionized water, and then add the screened starch and maltose at a uniform speed, the weight-to-component ratio of starch and maltose is 3:1, add 30 tons of starch and maltose, stir while adding, stir and mix evenly, add steam to cook For 6 hours, the cooking temperature is 120°C, and the steam pressure is 0.2MPa; then after cooling down to 85-90°C, add amylase, glucoamylase and Bacillus, stir evenly, and then put it into a fermenter for closed fermentation;

[0020] (3) Fermentation: After inoculation and saccharification, the starch and maltose are kept at 50°C in the fermentation tank, and sterile air is added, and the air flow rate is controlled at 5m 3 / h, reple...

Embodiment 2

[0026] Propionic acid preparation process described in the present embodiment, it specifically comprises the following steps:

[0027] (1) Sterilization treatment: steam the fermenter with 0.6Mpa steam for 35 minutes, blow it with sterile air, and dry it;

[0028] (2) Inoculation and saccharification: add 40m 3 Then add the screened starch and maltose at a uniform speed, the weight ratio of starch and maltose is 3:1, add 40 tons of starch and maltose, stir while adding, stir and mix evenly, add steam to cook for 7 hours , the cooking temperature is 130°C, the steam pressure is 0.2MPa; then the temperature is lowered to 90°C, amylase, glucoamylase and bacillus are added, after stirring evenly, it is sent into a fermenter for closed fermentation;

[0029] (3) Fermentation: After inoculation and saccharification, the starch and maltose are kept at 60°C in the fermentation tank, and sterile air is added, and the air flow rate is controlled at 5m 3 / h, replenish liquid ammonia, ...

Embodiment 3

[0035] Propionic acid preparation process described in the present embodiment, it specifically comprises the following steps:

[0036] (1) Sterilization treatment: steam the fermenter with 0.6Mpa steam for 40 minutes, blow it with sterile air, and dry it;

[0037] (2) Inoculation and saccharification: add 50m 3 deionized water, and then add the screened starch and maltose at a uniform speed, the weight-to-component ratio of starch and maltose is 3:1, add 50 tons of starch and maltose, stir while adding, stir and mix evenly, add steam to cook For 8 hours, the cooking temperature is 145°C, and the steam pressure is 0.2MPa; then after cooling down to 90°C, add amylase, glucoamylase and Bacillus, stir evenly, and then put it into a fermenter for closed fermentation;

[0038] (3) Fermentation: After inoculation and saccharification, the starch and maltose are kept at 70°C in the fermentation tank, and sterile air is added, and the air flow rate is controlled at 5m 3 / h, replenis...

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Abstract

The invention belongs to the technical field of food additives, and relates to a preparation technology of propionic acid. The preparation technology specifically comprises the following steps of sterilizing, inoculating, saccharifying, fermenting, filtering, discoloring and rectifying in a rectification tank. The preparation technology is characterized in that starch and malt are used as raw materials, and are treated by the steps of high-temperature steam sterilizing, inoculating, saccharifying and fermenting, so as to produce a fermenting solution; the foreign odor gas produced in the fermenting process enters a foreign odor gas treatment system, the sterile air and an inorganic nitrogen source are supplemented in the fermenting process, and the fermenting solution is crystallized, filtered and rectified to extract 99% fermented propionic acid; the steam produced by rectifying is condensed for preparing a culture medium, and the rectified propionic acid is used for producing fermented calcium propionate by a calcium propionate production process. The preparation technology has the advantages that by setting the whole technology steps, the production efficiency and purity of propionic acid are improved, the production cost is reduced, and the preparation technology is suitable for being industrially popularized and applied.

Description

technical field [0001] The invention belongs to the technical field of food additives and relates to a preparation process of propionic acid. Background technique [0002] Propionic acid is an important chemical raw material. Propionic acid and its salts have important uses in food, medicine, cosmetics and other industries. The production methods of propionic acid include chemical synthesis and biological fermentation. Microorganisms can use a variety of fermentable sugars to produce propionic acid. In industry, various biomass can be hydrolyzed into simple sugars such as glucose or xylose with acid or enzyme, and then introduced into the reactor for fermentation. After the fermentation is completed, milk of lime is added. Precipitate, filter and add sodium sulfate for metathesis reaction, then filter and concentrate, add sulfuric acid for conversion and then carry out fractional distillation. The fermentation reactor can use immobilized protoplast tower reactor, and the ce...

Claims

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Application Information

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IPC IPC(8): C12P7/52
CPCC12P7/52
Inventor 周小峰宋成普秦元伦
Owner SHANDONG PROVINCE & TAI WEI RUN FOOD TECH CO LTD
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