JP2009028030A - Production method for siderophore - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for efficiently producing siderophore, using an Aspergillus filamentous fungus. <P>SOLUTION: (1) The production method of the siderophore includes: a cultivation step of cultivating Aspergillus filamentous fungus in a culture solution with the rate of oxygen capacity movement at 8 mmol×l<SP>-1</SP>×h<SP>-1</SP>or higher; and a recovering step of recovering the siderophore from the culture products. (2) Alternatively, the production method of the siderophore includes a cultivation step of cultivating the Aspergillus filamentous fungus, in a culture solution whose inorganic nitrogen source is an ammonium salt and a recovering step of recovering the siderophore from the culture products. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a method for producing a siderophore useful for, for example, pharmaceuticals for iron supplementation and health foods.

  Among the microorganisms, Aspergillus filamentous fungi, which is a type of fungus, have been traditionally used for fermentation of foods and the like. Aspergillus fungi produce a variety of substances that are useful to humans.

Siderophore is one of the useful substances produced by Aspergillus fungi. Siderophores are iron chelators, including ferrichrome. Since ferrichrome chelates iron, it can be used for medicines for supplementing iron, health foods, and the like (see Patent Document 1). However, since siderophore is a secondary metabolite, mass production is extremely difficult, and a method for mass production of siderophore has not been technically established.
JP 2005-225874 A

  An object of the present invention is to provide a method capable of efficiently producing a siderophore using Aspergillus filamentous fungi.

As a result of intensive studies to solve the above-mentioned problems, the present inventors have adjusted the aeration rate to the culture solution and the stirring speed when culturing Aspergillus filamentous fungi, thereby increasing the oxygen capacity transfer rate. It was found that siderophore was efficiently produced in the culture by setting the concentration to 8 mmol·l ⁻¹ · h ⁻¹ or more. Moreover, it discovered that a siderophore was efficiently produced in a culture also by making the inorganic nitrogen source in a culture solution into an ammonium salt.

The present invention has been completed based on the above findings, and provides the following method for producing a siderophore.
Item 1. A method for producing a siderophore comprising a culture step of culturing Aspergillus filamentous fungi in a culture solution having an oxygen capacity transfer rate of 8 mmol·l ⁻¹ · h ⁻¹ or more, and a recovery step of recovering siderophore from the culture.
Item 2. Item 2. The method according to Item 1, wherein the inorganic nitrogen source in the culture solution is an ammonium salt.
Item 3. A method for producing a siderophore, comprising a culture step of culturing Aspergillus fungi in a culture solution whose inorganic nitrogen source is an ammonium salt, and a recovery step of recovering siderophore from the culture.

According to the method for producing a siderophore of the present invention, a siderophore can be efficiently produced using Aspergillus filamentous fungi.
More specifically, in the first method of the present invention, siderophore is efficiently produced in the culture by setting the oxygen capacity transfer rate to 8 mmol·l ⁻¹ · h ⁻¹ or more. The oxygen capacity transfer rate is adjusted by appropriately setting conditions such as the amount of aeration into the culture medium, the stirring speed, the diameter and shape of the stirring blade, the shape of the container, or the oxygen concentration of the gas to be blown, and the pressure in the container. be able to. In the second method of the present invention, siderophore is efficiently produced in the culture by converting the inorganic nitrogen source in the culture solution to an ammonium salt.

  Since the siderophore obtained by the method of the present invention chelates iron, it can be used for pharmaceuticals and health foods for iron supplementation. Since the siderophore obtained by the method of the present invention is produced by Aspergillus filamentous fungi that have been used in the food field for a long time, its safety is high, and there is no concern about side effects caused by taking it continuously for a long time.

Hereinafter, the present invention will be described in detail.
(1) First Method The first method for producing a siderophore according to the present invention comprises culturing an Aspergillus fungus in a culture solution having an oxygen capacity transfer rate of 8 mmol·l ⁻¹ · h ⁻¹ or more. And a recovery step of recovering the siderophore from the culture.

Aspergillus fungi Aspergillus fungi are a type of fungi that have been used for many years in fermented foods such as sake, miso, and soy sauce. The Aspergillus genus fungus used in the method of the present invention is not particularly limited as long as it is a bacterial species that produces siderophore. Examples include Aspergillus glaucus. Among these, Aspergillus oryzae is preferable in terms of producing deferifericlysin (hereinafter referred to as “Dfcy”) useful as an active ingredient of pharmaceuticals and health foods. Aspergillus oryzae Dfcy high-producing mutant 3129-7 (FERM P-20961) is more preferable.

Pre-culture step In the first production method of the present invention, the pre-culture may or may not be performed before the main culture of Aspergillus filamentous fungi. By performing the pre-culture, the culture time required for the growth of the bacteria can be shortened, and siderophores can be efficiently generated in the main culture process. In addition, it is possible to increase the number of initial bacteria in the main culturing step and prevent contamination due to various bacteria.
As the medium used in the preculture step, a medium usually used for fungal culture can be used without limitation. Examples of such a medium include a zapek dox medium and a malt extract (MA) medium. What is necessary is just to start main culture by diluting a preculture liquid about 5 to 20 times with the culture medium used for main culture. The pre-culture may be performed using a solid medium.

Main culturing step The type of liquid medium used in the main culturing step is not particularly limited, and any known medium used for culturing Aspergillus filamentous fungi can be used without limitation. Carbon sources include high molecular compounds such as starch and dextrin; monosaccharides or oligosaccharides such as glucose, sucrose, fructose, mannitol, sorbitol, galactose, maltose, erythritol, lactose, xylose, inosit, trehalose; A low molecular weight compound can be used. Moreover, as a nitrogen source, in addition to inorganic compounds such as nitrates, nitrites and ammonium salts, organic compounds such as amino acids and protease degradation products of sake lees can be used. In sake lees, sugars in rice are decomposed during fermentation, and most of them are removed, and because they contain protein at a high concentration, the decomposition product of sake lees protease becomes an efficient nitrogen source. The medium may contain minerals such as P, K, S, Mg, Zn, and Cu, and vitamins such as biotin and thiamine. The iron concentration in the medium is preferably about 2 ppm or less. As the liquid medium, typically, a medium such as an iron-restricted zapek dox liquid medium or an iron-restricted malt extract (MA) medium having an iron concentration of about 2 ppm or less can be used. The pH of the culture solution may be about 3-8.

During the main culture are cultured at an oxygen volume moving speed (N _A / V) of the culture solution as a 8mmol · l ^-1 · h ^-1 or more. The oxygen capacity transfer rate is preferably 10 mmol·l ⁻¹ · h ⁻¹ or more, and more preferably 20 mmol·l ⁻¹ · h ⁻¹ or more. This significantly increases the production of siderophore. The upper limit of the oxygen capacity transfer rate is not particularly limited, but is usually about 80 mmol·l ⁻¹ · h ⁻¹ .
Oxygen capacity transfer rate (N _A / V) is the oxygen transfer rate (N _A ) per liquid volume (V) and is expressed as the product of oxygen transfer capacity coefficient (K _L a) and concentration gradient (Δc). It is a value shown by the relationship of the following formula.
Oxygen capacity transfer rate (N _A / V) = (K _L a) × (Δc)
It shows that it has the supply rate which can satisfy | fill the oxygen demand amount of microorganisms continuously, so that an oxygen capacity transfer rate is large.
Oxygen content moving speed (N _A / V), the airflow rate to the culture solution (F), liquid volume (V), the oxygen concentration in the exhaust gas from the culture tank (C _out ^*), the gas in the aerated culture Measure the oxygen concentration (C _in ^* ) and calculate according to the following formula
N _A / V = (F / V) (C _in ^* −C _out ^* )
The oxygen concentration during exhaust and ventilation is a value measured using an exhaust gas analyzer (VA-3000, manufactured by Horiba, Ltd.).
In order to increase the oxygen capacity transfer rate, it is necessary to increase either or both of the oxygen transfer capacity coefficient (K _L a) and the oxygen concentration gradient (Δc). K _L is a liquid film transfer coefficient of oxygen, and a is a gas-liquid contact area per unit volume. Thus, K _L does not change significantly in normal liquid culture, K _L a is changed depending on the magnitude of a. That is, the oxygen transfer capacity coefficient (K _L a) is a value that varies depending on the amount of aeration into the culture solution, the stirring speed, the diameter of the stirring blade, or the shape of the container. The oxygen concentration gradient (Δc) is a value that varies depending on the oxygen concentration in the gas to be vented, the pressure in the container, and the like.
For example, the oxygen capacity moving speed (N _A / V) to 8mmol · l ^-1 · h ^-1 or more in the case of performing culture put broth 3L to aeration-agitation type fermentor 5L, the vent The amount may be about 0.67 to 1 vvm (volume / volume / minute). The diameter of the stirring blade may be about 4 to 7 cm. The stirring speed may be about 300 to 500 rpm. If it is the range of said stirring speed, an oxygen movement capacity | capacitance coefficient can be enlarged and a microbial cell will not be damaged by a shear stress. Also, oxygen may be blown into the culture solution at a higher concentration than air, and pure oxygen is better. What is necessary is just to make the pressure in a container higher pressure than normal pressure, and what is necessary is just to be about normal pressure-about 0.2 MPa. The oxygen concentration gradient can be increased under the above oxygen concentration and pressure conditions.
By appropriately setting the conditions such as the amount of ventilation into the culture medium, the stirring speed, the diameter and shape of the stirring blade, the shape of the container, the oxygen concentration of the gas to be blown, the pressure in the container, etc. within the above ranges, The capacity transfer rate (N _A / V) can be 8 mmol·l ⁻¹ · h ⁻¹ or more. Further, when changing the capacity and culture volume of culture tank, by appropriately setting the conditions of the culture tank according to the above conditions, the oxygen capacity moving speed of the culture solution (N _A / V) to 8 mmol · l ^-1・ It can be h ^-1 or more.
The culture method in the main culturing step may be any of a batch system such as batch culture and fed-batch (half batch) culture, and a continuous culture system such as perfusion culture.
Moreover, although culture | cultivation temperature changes with strains and strains to be used, it may be about 25 to 35 ° C. The culture time may be about 2 to 7 days in batch culture or fed-batch (half batch) culture. In continuous culture, the residence time may be about 2 to 6 days.

Recovery Step In the present invention, the recovery step refers to a step of recovering siderophore from the culture.
Aspergillus fungi usually secrete and produce siderophores outside the cells. Therefore, the whole culture medium may be collected while containing the bacterial cells, or may be purified by a known method from the culture medium after removing the bacterial cells by centrifugation or the like.
A siderophore siderophore is an iron ion chelate substance having a molecular weight of 1500 or less produced by bacteria, actinomycetes or eukaryotic microorganisms. Examples of siderophores produced by Aspergillus filamentous fungi include compounds represented by the following general formula (showing a state in which iron is chelated).

(Wherein R ¹ represents a hydrogen atom or a hydroxymethyl group; R ² represents a hydrogen atom, a methyl group or a hydroxymethyl group; and R ³ , R ⁴ and R ⁵ are the same or different and represent a methyl group, N ⁵ - (trans-5-hydroxy-3-methylpent-2-enoyl) group, N ⁵ - (cis-5-hydroxy-3-methylpent-2-enoyl) group, or an N ⁵ - (trans-4-carboxy -3-methylpent-2-enoyl) group.)
R ^{1 to} R ⁵ which are functional groups in the general formula (1) of these compounds are summarized in Table 1 below.

The type of siderophore produced by the method of the present invention is determined by the bacterial species used. When Aspergillus oryzae is used, Dfcy, which is a deferiated form of ferriclysin, is mainly obtained.

(II) Second Method The second method for producing a siderophore according to the present invention comprises culturing an Aspergillus fungus in a culture solution whose inorganic nitrogen source is an ammonium salt, and recovering the siderophore from the culture. And a recovery step.
In the second method, pre-culture may or may not be performed. The conditions for pre-culture are as described for the first method.
As the ammonium salt of the inorganic nitrogen source in the culture solution, a known ammonium salt used for culturing Aspergillus fungi can be used without limitation. Examples of such ammonium salts include ammonium sulfate, ammonium chloride, ammonium nitrate, ammonium carbonate, diammonium citrate, triammonium citrate, ammonium acetate, diammonium hydrogen phosphate, ammonium dihydrogen phosphate, and ammonium formate. Of these, ammonium sulfate is preferable. Ammonium salts can be used alone or in combination of two or more.
The content of the ammonium salt is usually about 0.1 to 2.5% (w / v), preferably about 0.5 to 1.0% (w / v).
Other inorganic nitrogen compounds are not substantially contained except those mixed from the preculture medium. Examples of such inorganic nitrogen compounds other than ammonium salts include nitrates and nitrites.
Other components in the medium and medium conditions such as medium pH are as described for the first method. The culture method, culture temperature, culture time, and recovery step are also the same as in the first method.

EXAMPLES Hereinafter, the present invention will be described in more detail based on examples. However, the present invention is not limited to these examples.

Production Method of Siderophore Examples 1 to 4 described later were basically performed under the following conditions. The conditions changed in each embodiment will be described later.
<Pre-culture process>
Under the conditions shown in Table 2 below, preculture of Dfcy high-producing mutant Aspergillus oryzae 3129-7 strain (FERM P-20961) was performed.

^* Sake lees protease decomposed powder was obtained by degrading sake lees with protease and prepared by the following method. That is, 600 ml of distilled water was added to 300 g of a lyophilized product of sake lees and homogenized, and 0.6 g of a commercially available protease, Sumiteam LP (manufactured by Shin Nippon Chemical Industry Co., Ltd.) was added and reacted at 50 ° C. for 16 hours with stirring. After the reaction is completed, the enzyme is inactivated by heating at 80 ° C. for 10 minutes, and then insoluble residue is removed by centrifugation (11000 rpm, 15 minutes), and the supernatant is dehumidified and dried until it becomes a powder in a freeze dryer. We used what we did.

<Main culture process>
The main culture was performed under the conditions shown in Table 3 below.

^* Sake lees protease protease powder is the same as pre-culture.

Measurement method of oxygen capacity transfer rate It was calculated by substituting each numerical value into the following equation.
Oxygen content moving speed _{(N A / V) = (} F / V) (C in * -C out *)
F: Aeration volume to culture medium
V: Volume of culture solution
C _in ^* : Oxygen concentration in the gas aerated in the culture
C _out ^* : Oxygen concentration in the exhaust from the culture tank
C _in ^* and C _out ^* were measured using an exhaust gas analyzer (VA-3000, manufactured by Horiba, Ltd.).

Method for Measuring Dfcy Production Amount 10 μl of 0.2 M citrate buffer (pH 4.0) and 10 μl of 3000 ppm FeCl ₃ solution were added to 100 μl of the culture supernatant, and iron was chelated to Dfcy to obtain ferriclysin (Fcy).
This Fcy solution was subjected to reverse phase chromatographic analysis using HPLC (manufactured by SHIMADZU; Prominence), and an Fcy peak was identified using a wavelength of 430 nm, which is an absorption wavelength specific for Fcy, as an index. Fcy was quantified from the peak area. The Dfcy amount was calculated by multiplying the quantified Fcy amount by the molecular weight ratio of Dfcy to Fcy of 0.93 (744/800).

Example 1
Examination of the effect of oxygen capacity transfer rate on Dfcy productivity (1) (aeration condition)
The oxygen capacity transfer rate was changed by changing the aeration conditions during culture, and the influence of the oxygen capacity transfer rate on the productivity of Dfcy was verified. That is, the oxygen capacity transfer rate and Dfcy between when air is vented at 0.67 (vvm) and when oxygen (concentration is about 100%, the same applies hereinafter) is vented at 0.33 (vvm). The production amount was compared. The preculture conditions are as shown in Table 2 above. The main culture conditions were as shown in Table 3 above, except that 1.0% (w / v) NaNO ₃ was added as a nitrogen source, and (NH ₄ ) ₂ SO ₄ was not added. No pH control was performed. Moreover, the stirring speed at the time of main culture was 300 rpm, and cultured for 48 hours.
The results are shown in Table 4 below.

  From Table 4, it can be seen that the Dfcy production amount is nearly doubled when oxygen is ventilated compared to when air is aerated.

Example 2
Examination of the effect of oxygen capacity transfer speed on Dfcy productivity (2) (stirring blade speed)
The oxygen volume transfer speed was changed by changing the stirring blade speed during the culture, and the influence of the oxygen capacity transfer speed on the productivity of Dfcy was verified. That is, the oxygen capacity transfer speed and the production amount of Dfcy were compared by changing the stirring speed to 100 rpm, 300 rpm, 500 rpm, and 700 rpm. The preculture conditions are as shown in Table 2 above. The main culture conditions were as shown in Table 3 above, except that 1.0% (w / v) NaNO ₃ was added as a nitrogen source, and (NH ₄ ) ₂ SO ₄ was not added. No pH control was performed. For aeration, air was set to 0.67 vvm and cultured for 64 hours.
The results are shown in Table 5 below.
From Table 5, it can be seen that the higher the oxygen capacity transfer rate, the greater the Dfcy production amount. Moreover, the optical microscope photograph of the microbial cell after culture | cultivating for 64 hours when stirring speed is 300 rpm, 500 rpm, and 700 rpm is shown in FIG. The cells are sheared when the stirring speed is 700 rpm. It can also be seen that if the stirring speed is increased too much, the cells are sheared and the Dfcy production amount does not increase to meet the increase in oxygen capacity transfer speed.
From Tables 4 and 5, it was shown that Dfcy can be produced at high yields by setting the oxygen capacity transfer rate to 8 mmol·l ⁻¹ · h ⁻¹ or more. In addition, as a method for increasing the oxygen capacity transfer rate, there are methods such as oxygen aeration and increase in the stirring speed, but it has also been shown that the stirring speed needs to be set in a range where the cells are not sheared.

Example 3
Examination of Influence of Kind of Inorganic Nitrogen Source on Dfcy Production The influence of the kind of nitrogen source in the culture solution on the productivity of Dfcy was verified. That is, the amount of Dfcy produced was compared between when sodium nitrate was used as the nitrogen source and when ammonium sulfate was used. The preculture conditions are as shown in Table 2 above. The main culture conditions were as shown in Table 3 above, and the pH of the medium was controlled by adding 12.5% aqueous ammonia so that it did not become 4.0 or less only when ammonium sulfate was used. The aeration and agitation speeds were 0.67 vvm and 300 rpm for air up to 16 hours after the start of culture, and 0.5 vvm and 450 rpm for oxygen thereafter. Incubated for a total of 64 hours.
The results are shown in Table 6 below.

  As shown in Table 6, it was shown that the productivity of Dfcy was higher when ammonium sulfate was added as the N source than when sodium nitrate was added as the N source.

Example 4
Kind of produced siderophore Aspergillus oryzae strain 1013 (FERM P-16528) is cultured under conditions shown below using an iron-restricted medium and an iron-added medium, and the final concentration (500 ppm) of FeCl ₃ is cultured in the culture supernatant. A siderophore was detected by HPLC analysis with and without addition of the solution.
<Culture conditions>
The preculture conditions are as shown in Table 2 above. The main culture conditions were as shown in Table 3 above, and the pH of the medium was controlled by adding 12.5% aqueous ammonia so that it did not become 4.0 or less only when ammonium sulfate was used. The aeration and stirring speeds were 0.67 vvm and 300 rpm for air up to 16 hours after the start of culture, and oxygen was 0.5 vvm and 450 rpm only when ammonium sulfate was used thereafter. Incubated for a total of 64 hours.
<HPLC analysis conditions>
10 μl of 0.2 M citrate buffer (pH 4.0) and 10 μl of 3000 ppm FeCl ₃ solution were added to 100 μl of culture supernatant to chelate iron to the siderophore.
This was subjected to reverse phase chromatographic analysis using HPLC (manufactured by SHIMADZU; Prominence), and Fcy and other siderophores were identified using a wavelength of 430 nm, which is an absorption wavelength specific for siderophores, as an index. Each siderophore was compared in production by peak area ratio.
The results are shown in Table 7 below.

In addition, when no iron was added to the culture supernatant, none of the peaks of Dfcy and other siderophores A and B were detected.
The results are shown in FIG. Since the peak detected for the first time after adding FeCl ₃ solution to the supernatant of the culture broth obtained by iron-restricted culture is considered to be the siderophore peak, 1013 strain produces two siderophores in addition to Dfcy. You can see that

  The production method of the present invention can be suitably used to efficiently produce a siderophore useful as a pharmaceutical or health food for iron supplementation.

2 is an optical micrograph of the cells cultured in Example 2. 6 is an HPLC chart of Example 4.

Claims (3)

A method for producing a siderophore comprising a culture step of culturing Aspergillus filamentous fungi in a culture solution having an oxygen capacity transfer rate of 8 mmol·l ⁻¹ · h ⁻¹ or more, and a recovery step of recovering siderophore from the culture.   The method according to claim 1, wherein the inorganic nitrogen source in the culture solution is an ammonium salt.   A method for producing a siderophore, comprising a culture step of culturing Aspergillus fungi in a culture solution whose inorganic nitrogen source is an ammonium salt, and a recovery step of recovering siderophore from the culture.