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Long chain normal dibasic acid production method

A long-chain dibasic acid and production method technology, applied in the direction of microorganism-based methods, biochemical equipment and methods, separation/purification of carboxylic acid compounds, etc., can solve the problem of increasing production costs, high prices, and downstream product applications Field limitations and other issues to achieve the effect of expanding applications

Active Publication Date: 2006-12-27
CATHAY R&D CENT CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, DuPont produces dodecanedibasic acid by chemical synthesis method, which uses n-butene as raw material. This chemical synthesis process needs to go through seven steps of high temperature and high pressure chemical reactions. This method has obvious disadvantages: organic monoacid as impurity Exists because it terminates polymerization, removing monoacids would increase production costs, which is a thorny issue; dibasic acids with longer carbon chains cannot be produced
Dodecane dibasic acid is a product produced by chemical method. A small number of manufacturers occupy a monopoly position in the world, and the price has remained high for a long time, which seriously affects the cost of downstream products. other long-chain dibasic acids, which limits the application of downstream products
[0006] At present, the patented technology for the production of long-chain dibasic acids at home and abroad is to use alkanes as substrates to produce dibasic acids by biological fermentation or to use fatty acids as substrates to synthesize dibasic acids by chemical methods. Domestic fermentation methods produce long-chain dibasic acids based on alkanes. substances, but the concept of substrate conversion rate is not proposed in the patent, and the conversion rate of substrate alkanes is crucial to the production cost of dibasic acids
Abroad, there are reports on the fermentation of dibasic acids with fatty acids as substrates, but they all stay at the scale of shake flasks, and the level is relatively low. 8 -C 14 Fatty acids as substrates, fermented to produce C 8 -C 10 dibasic acid, the acid production level is only 10g / L, and cannot produce C 11 -C 18 dibasic acid
Although there are many patents on the extraction and refining of dibasic acids at home and abroad, none of them can solve the problem of product quality, and the products obtained by the proposed process are difficult to apply to the fields of nylon and polyester.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Embodiment 1: the preparation of seed solution

[0023] 1) Take the glycerol tube strain of Candida tropicalis (CCTCC NO: M203052) and inoculate it into 500 mL seeds filled with 200 mL liquid medium (10 g / kg peptone, 5 g / kg yeast extract, 10 g / kg glucose, natural pH) Cultivate in the bottle at 35°C, 300rpm shaker for 10-15 hours;

[0024] 2) Take the above-mentioned shaking flask seeds, insert them into a 10L fermenter equipped with 5L seed medium (10g / kg peptone, 10g / kg yeast extract, 10g / kg glucose, natural pH), and cultivate them at 35°C for 24 hours to produce Get the primary seed solution for later use.

[0025] 3) With 16M 3 Medium 20M 3 In the fermenter, the above-mentioned first-level seed liquid is inserted, and the second-level seed tank cultivation is started. The fermentation medium formula is the same level as the seed tank. Cultivate at 29°C for 16 hours to prepare secondary seed solution for future use.

Embodiment 2

[0026] Example 2 Oleic acid fermentation

[0027] In a 30L fermenter equipped with 15L medium, respectively insert 1.5L of the primary seed solution of Example 1 to start fermentation. The fermentation medium of the fermenter is: potassium dihydrogen phosphate 10g / kg, magnesium sulfate 0.5g / kg, urea 5.0g / kg, corn steep liquor 10g / kg, glucose 40g / kg, pH 5.8, sterilized at 121°C for 20 minutes . Dissolution of oleic acid, feed sugar and alkali. Cultivate at 35°C, rotation speed 500rpm, ventilation rate 7.5vvm, and tank pressure 0.05Mpa. After 3 hours of fermentation, start adding glucose at a rate of 100g / hr. After 48 hours, reduce the speed of sugar flow to 70g / hr. After 96 hours Reduce the sugar flow rate to 40g / hr, and stop adding sugar 5 hours before the end of fermentation; 3 hours after adding glucose, start to flow oleic acid at a rate of 30g / hr, and stop oleic acid flow about 20 hours before the end of fermentation. From inoculation to the end of fermentation, the tot...

Embodiment 3

[0028] Embodiment 3 Undecyl n-alkanes (DC 11 ) fermentation

[0029] installed in 100M 3 200M of medium 3 In the fermenter, the primary seed liquid is inserted to start fermentation. The composition of the fermentation medium is: glucose 10g / L, KH 2 PO 4 15g / L, yeast extract 10g / L, corn steep liquor 5g / L, urea 4.5g / L, NaCl 1g / L, KNO3 7g / L, natural pH, sterilized at 121℃. Dissociation of alkanes and feed sugars. Cultivate at 29°C under the conditions of ventilation rate 0.5vvm and tank pressure 1.0Mpa. 20 hours before fermentation, the pH was natural, and the growth of bacteria was the main factor. When the growth optical density (OD 600 ) greater than 0.6, start to add C 11 Alkanes, to control the C in the fermentation broth 11 The alkane concentration is maintained at about 5% (V:V), and the pH is adjusted to 7.0 at the same time. Within 48 hours, the pH is adjusted to 7.0 with NaOH solution every 4 hours. For 48-72 hours, the pH is adjusted to 7.5 with NaOH soluti...

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PUM

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Abstract

The invention discloses a method for preparing a normal long chain binary acid. The method comprises the following steps: C9-C18 alkane or fatty acid is served as substrate and converted to relative long chain binary acid by fermentation method or enzyme method; the reaction liquid is pretreated for removing the thallus and residual alkane or fatty acid, a binary acid clear liquid is obtained, acidification crystallization is carried out, the acidification crystallization liquid is filtered by pressing, and the binary acid crude product is obtained; the binary acid crude product is refined by using knifing vaporization and short path distillation device under the vacuum condition or by using organic solvent. The normal long chain binary acid prepared by the method has high thermal stability and can be used for preparing nylon, thermosol, and polyester materials.

Description

technical field [0001] The invention relates to a production method of a normal long-chain dibasic acid, in particular, the invention relates to a method for producing a high thermal stability normal long-chain dibasic acid by a biological method. Background technique [0002] Long-chain dibasic acid (DCA) is the basic monomer raw material for a series of special synthetic materials. Long-chain dibasic acid and its derived monomers can be used to produce special nylon, polycarbonate, powder coatings, spices, hot melt adhesives, special lubricants It is an important raw material for synthetic spices, engineering plastics, cold-resistant plasticizers, high-grade lubricants, polyamide hot-melt adhesives, and powder coatings. [0003] At present, DuPont produces dodecanedibasic acid by chemical synthesis method, which uses n-butene as raw material. This chemical synthesis process needs to go through seven steps of high temperature and high pressure chemical reactions. This metho...

Claims

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Application Information

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IPC IPC(8): C12P7/44C12R1/74C07C55/02C07C51/43
Inventor 邱勇隽李乃强胡兵衷金生
Owner CATHAY R&D CENT CO LTD
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