JP2005080625A - Method for producing carotenoid by fermentation method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a carotenoid in a high yield by culturing bacteria capable of producing the carotenoid such as astaxanthin, etc. <P>SOLUTION: This method for producing the carotenoid is provided by culturing a carotenoid-producing bacterium [e.g. Agrobacterium aurantiacus sp. nov N-81106 (FERM P-14023) or its mutants] in a culturing liquid where <0.5 ppm oxygen is present, or the culturing liquid having (-)200 m-(-)70 mV oxidation reduction potential and recovering the carotenoid from microbial cells or the cultured liquid. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

  The present invention relates to a method for producing carotenoids, particularly astaxanthin, which is a fat-soluble pigment. Astaxanthin is a compound useful as a color raising agent for cultured salmon, trout and red sea bream, an egg color tone improving agent, a health supplement, and a pharmaceutical product.

  Astaxanthin is the same carotenoid pigment as β-carotene and lycopene, and is a natural distribution widely distributed in crustaceans such as krill, crabs and shrimp, fish such as red sea bream, salmon and trout, birds such as flamingos, algae and microorganisms. A compound. In recent years, astaxanthin has been increasing in demand as a coloring agent for cultured fish such as salmon, trout, and red sea bream and a color improving agent for chicken eggs, and various physiological effects such as antioxidant activity and anticancer activity have been confirmed. It is also attracting attention as a health supplement.

  Astaxanthin production methods include chemically synthesized products, extracts from natural products, and fermented products by microorganisms. Currently, chemically synthesized products are mainly used due to factors such as price. However, since chemically synthesized products use halogen compounds and heavy metals containing bromine and chlorine as raw materials, there are concerns about safety (see, for example, Patent Document 1), and they are derived from natural products due to the natural and natural orientation of consumers. Astaxanthin has attracted attention.

  Extracts from natural products include extracts from krill and the like, but these are low in content, requiring a great deal of labor for collection, extraction, purification, etc., and have a problem in cost.

  Production methods using microorganisms include Phaffia rhodozyma (for example, see Non-Patent Document 1) for yeast, Hematococcus pluviaris (for example, Non-Patent Document 2) for algae, and Agrobacterium for bacteria. -There is a report of Agrobacterium aurantiacus (see Non-Patent Document 3, for example).

  Phaffia yeast has a slow growth rate and thus has a long culture period, and it is difficult to destroy the cell wall, so that the extraction efficiency is low and the content is low, so that the cost is high. Haematococcus algae has a very slow growth rate, so it has a very long culture period and requires light.Therefore, there are restrictions on location conditions and facilities, and it is necessary to remove contaminants such as chlorophyll. is there. The method using bacteria has a high growth rate and thus a short culture time, and the cell wall is easily destroyed, so that extraction is easy and it is suitable for industrial production of carotenoids.

  A study of carotenoid synthesis using Agrobacterium aurantiacus was reported by Yokoyama et al. And found that the carotenoid components differed by changing the amount of liquid and shaking conditions (see, for example, Non-Patent Document 4). That is, it was shown that the dissolved oxygen concentration in the culture solution affects the carotenoid component, and it was found that oxygen supply conditions lower than those of normal aerobic bacteria are suitable. However, since this report is the result of using a flask, the specific optimum oxygen concentration was not known, and there was a problem when considering industrial production. In addition, there is an example of Paracoccus as another bacterium, which shows that the carotenoid component changes by changing the dissolved oxygen concentration using an oxygen electrode, and a saturated oxygen concentration of 20-30% is suitable for astaxanthin production (For example, refer to Patent Document 2). However, there is no report on the oxygen concentration with a saturated oxygen concentration of 5% or less, and no redox potential is indicated.

U.S. Pat. No. 4,283,559

Andrews, A.M. G. Phytochemistry, 15, 1003, 1976. Renstrom, B et al., Phytochemistry, 20, 2561, 1981. Yokoyama, A et al., Biochem. Biotech. Biochem. , 58, 1842, 1994 FEMS Microbiol. Letters, 128, 139, 1995 JP 2001-35295 A

  An object of the present invention is to provide a method for producing carotenoids in high yield by culturing bacteria capable of producing carotenoids such as astaxanthin.

  The present inventors have found that carotenoids can be efficiently produced by limiting the oxygen concentration or redox potential in the culture solution, and have completed the present invention.

  That is, the present invention cultivates a carotenoid-producing bacterium in a culture solution containing less than 0.5 ppm of oxygen or a culture solution having a redox potential of −200 mV to −70 mV, and recovers the carotenoid from the microbial cell or the culture solution. This is a method for producing carotenoids. The present invention is described in further detail below.

  The bacterium used in the present invention is not particularly limited as long as it is carotenoid-producing. For example, bacteria belonging to the genus Agrobacterium can be used, and among them, Agrobacterium aurantiacus sp. nov N-81106 (FERM P-14023) and its mutants are preferable. An example of such a mutant strain is TSUG1C11 strain (FERM P-19146).

  As the culture solution used in the present invention, any one can be used as long as carotenoid-producing bacteria can grow and produce carotenoids. For example, as a carbon source, molasses, glucose, fructose, maltose, sucrose, starch , Lactose, glycerol, acetic acid, etc., nitrogen sources include natural ingredients such as corn steep liquor, peptone, yeast extract, meat extract, soybean meal, ammonium salts such as ammonium acetate, ammonium chloride, ammonium sulfate, glutamic acid, aspartic acid Amino acids such as glycine, inorganic salts include monosodium phosphate, disodium phosphate, monopotassium phosphate, dipotassium phosphate and sodium chloride, and metal ions include magnesium chloride and sulfuric acid. Magnesium, ferrous sulfate, ferric sulfate, ferrous chloride, ferric chloride, copper Down iron, ammonium iron sulfate, calcium chloride dihydrate, calcium sulfate, yeast extract and biotin, nicotinic acid, thiamine, riboflavin, inositol, pyridoxine, or the like can be used as vitamins.

  In the present invention, carotenoid-producing bacteria are cultured in a culture solution containing less than 0.5 ppm of oxygen or a culture solution having a redox potential of −200 mV to −70 mV. A culture solution in which oxygen having a minimum detection limit of less than 0.1 ppm of an ordinary oxygen electrode is present or a culture solution having a redox potential of −180 to −100 mV is preferred. The oxygen concentration of the culture solution may be measured directly, but when the measurement is difficult due to the dilution of less than 0.5 ppm, the oxidation-reduction potential can be used as the index, so the oxidation-reduction potential -200 mV to- A culture solution of 70 mV may be used.

  Other culture conditions are not particularly limited as long as carotenoid-producing bacteria can grow and produce carotenoids. For example, the culture temperature is preferably 15 to 35 ° C., and the pH is preferably 6 to 9. The time is preferably 24 to 168 hours. In order to produce carotenoids more efficiently, the number of cells is increased by culturing in a culture solution having a higher oxygen concentration or oxidation-reduction potential than that described above at the initial stage of the culture, and then in the above range. It is preferable to culture using a culture solution having an oxygen concentration or a redox potential.

  The method for recovering carotenoid in the present invention is not particularly limited as long as it is stably and efficiently recovered from the bacterial cells or the culture solution. For example, the extraction solvent is methanol, ethanol, isopropyl alcohol, acetone, methyl ethyl ketone, methyl isobutyl ketone, dichloromethane, Chloroform, dimethylformamide, dimethylsulfoxide and the like are preferable. The quantification of the extracted carotenoid is preferably performed by high performance liquid chromatography in which various carotenoids are separated and excellent in quantification.

  Examples of the carotenoid produced in the present invention include astaxanthin, adonixanthin, phenicoxanthine, canthaxanthin, echinenone, β-carotene and the like. In particular, astaxanthin is preferably produced by this method.

  According to the present invention, it has become possible to efficiently produce carotenoid compounds such as astaxanthin by controlling the oxygen concentration or redox potential of the culture solution.

  EXAMPLES Hereinafter, although an Example demonstrates this invention further in detail, this invention is not limited to these.

Carotenoid Quantification Method Carotenoid quantification was measured by high performance liquid chromatography using a reverse phase column, and the following procedure was used. That is, a part of the culture solution is centrifuged to collect the cells, and an appropriate amount of pure water is added and suspended in a tube mixer for 10 minutes. Next, 9 times the amount of acetone is added to pure water, stirred for 30 minutes with a tube mixer, centrifuged at 14,000 rpm for 5 minutes, and the supernatant is collected. The carotenoid produced | generated in ODS-80TM, a brand name, Tosoh Co., Ltd. use was quantified.

Example 1
300 ml of the medium having the composition shown in Table 1 was placed in a 500 ml Erlenmeyer flask and sterilized at 121 ° C. for 20 minutes, and then Agrobacterium aurantiacus sp. Nov. N-81106 (FERM P-14023) was inoculated and cultured at 25 ° C. for 1 day at a shaking speed of 100 revolutions per minute as a preculture. Among the media shown in Table 1, peptone 30g / L, yeast extract 15g / L, glucose 2.5L medium 2.5L was placed in a 5L fermenter and sterilized at 121 ° C for 20 minutes The obtained preculture liquid was inoculated. The culture conditions were a temperature of 22 ° C., a stirring rate of 350 revolutions per minute, a pH of 7.0 to 7.2, and aeration was controlled at 1 VVM with air and cultured for about 72 hours. Table 2 shows the total carotenoid content in the cells after completion of the culture, the average redox potential and dissolved oxygen concentration after 24 hours of culture, and Table 3 shows the analysis results of carotenoid components. A redox potential electrode and a dissolved oxygen electrode manufactured by METTLER TOLEDO were used.

実施例２
攪拌数を毎分４５０回転としたこと以外は実施例１と同様な手順で培養を行ない、途中グルコースを７０ｇ加えた。この培養で得られた菌体内の総カロテノイド量、培養２４時間以降の平均酸化還元電位および溶存酸素濃度を表２に、カロテノイド成分の分析結果を表３に示した。

Example 2
Cultivation was performed in the same procedure as in Example 1 except that the number of stirring was 450 rpm, and 70 g of glucose was added on the way. Table 2 shows the total carotenoid content in the cells obtained by this culture, the average redox potential and dissolved oxygen concentration after 24 hours of culture, and Table 3 shows the analysis results of the carotenoid components.

Example 3
Cultivation was performed in the same procedure as in Example 1 except that the number of stirring was 500 rpm, and 63 g of glucose was added on the way. Table 2 shows the total carotenoid content in the cells obtained by this culture, the average redox potential and dissolved oxygen concentration after 24 hours of culture, and Table 3 shows the analysis results of the carotenoid components.

Comparative Example 1
The culture was performed in the same manner as in Example 1 except that the number of stirring was 550 rpm. Table 2 shows the total carotenoid content in the cells obtained by this culture, the average redox potential and dissolved oxygen concentration after 24 hours of culture, and Table 3 shows the analysis results of the carotenoid components.

Claims (3)

Carotenoid producing bacteria characterized by culturing a carotenoid producing bacterium in a culture solution containing less than 0.5 ppm oxygen or a culture solution having a redox potential of -200 mV to -70 mV, and recovering the carotenoid from the microbial cell or culture solution Manufacturing method. The method according to claim 1, wherein the carotenoid-producing bacterium is a bacterium belonging to the genus Agrobacterium. 3. The production method according to claim 2, wherein the Agrobacterium is Agrobacterium aurantiacus sp. nov N-81106 (FERM P-14023) or a variant thereof.