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JP4005677B2 - Production method of iron-containing yeast - Google Patents
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JP4005677B2 - Production method of iron-containing yeast - Google Patents

Production method of iron-containing yeast Download PDF

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JP4005677B2
JP4005677B2 JP27936297A JP27936297A JP4005677B2 JP 4005677 B2 JP4005677 B2 JP 4005677B2 JP 27936297 A JP27936297 A JP 27936297A JP 27936297 A JP27936297 A JP 27936297A JP 4005677 B2 JP4005677 B2 JP 4005677B2
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Prior art keywords
iron
yeast
cells
added
medium
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JPH11103853A (en
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和弘 濱澤
順一 伊東
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Kohjin Holdings Co Ltd
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Kohjin Holdings Co Ltd
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Description

【0001】
【産業上の利用分野】
本発明は、鉄化合物存在下で特にCandida属の食用酵母を培養することにより、鉄由来の沈澱物を抑え、かつ、酵母の菌体内に鉄含量として2%以上を含有する、健康食品用途向けの酵母の製法に関する。
【0002】
【従来の技術】
近年の健康ブームの中で、栄養素としてのビタミンと共にミネラル、微量元素への関心が高まりつつある。このような中で鉄分は、日本人の場合カルシウムと並び不足していると言われているミネラルの1つである。特に成長期の子供や妊婦は要求量が増大するため、鉄欠乏性貧血症にかかりやすいと言われている。そこで飲み易く吸収され易い形の鉄分が要求されている。
【0003】
鉄分はすでに加工食品等への添加が積極的に行われ、通常、硫酸第一鉄、フマル酸第一鉄、コハク酸第一鉄等が使用されている。しかしながらこれらの化合物は、元々鉄臭さを有する物であり、その為添加量を制限せざるを得ないし、体内への吸収の点でも問題があった。そこで、最近注目されているのが酵母に鉄分を吸収させて、有機鉄の形にして鉄臭さを低減させたり、人間の体内への吸収性を高めた形で供給する試みである。
【0004】
鉄含有酵母の製造方法としては、鉄化合物を含む培地で食用微生物を培養し、鉄を多量に含有する微生物菌体の製造法(特公昭61−9835号公報)、鉄化合物の存在下に、糖類含有栄養培地中で酵母を培養する有機第一鉄含有補血剤組成物の製造法(特開昭58−101686号公報)、炭素源及び窒素源を含有する培地に鉄化合物を添加して微生物を培養することにより、おおむね1%弱の鉄を含有していること、及び培地中のマグネシウムの濃度が10mg/l以下であることが必要な微生物菌体の製造方法(特開昭62−134083号公報)が知られている。さらに、酵母を培養して得た菌体を有機化合物及び二価の水溶性鉄化合物を含有する水溶液に分散し、鉄分を蓄積せしめる二価鉄含有酵母菌体の製造法(特開平5−176758号公報)が知られている。
【0005】
【発明が解決しようとする課題】
上述したように従来の鉄含有菌体を得る方法は、予め鉄化合物を培地中へ添加した培地で微生物を培養、増殖せしめることにより鉄含有菌体を得るか、または予め鉄化合物を添加しない培地で微生物を培養、増殖させ、その後菌体を集菌し鉄化合物を添加して、菌体中に取り込ませて鉄含有菌体を得るものである。前者の方法は一般に鉄による増殖阻害があるため高濃度の鉄の添加ができない。さらに、添加した鉄化合物は培養中に、通気撹拌により比較的短時間の内に酸化が起こり、特に通常の必須の培地成分として添加される燐酸イオンとの間で、燐酸鉄等の不溶性の化合物となり、微生物の鉄分の取り込みを阻害するだけでなく、培養終了後の遠心分離等による菌体分離において、不溶物と菌体との沈降速度に大きな差がないため、菌体との分離が困難である。この不溶物の存在は鉄臭さや色さらに吸収性の面での障害になる。
一方、後者の方法は、鉄自体の微生物に対する増殖阻害効果を回避するための手段と考えられるが、燐酸と鉄の化合物は、両者の濃度及び接触時間に依存して増大するため、予め鉄を添加していない培地で培養した微生物菌体を集菌して、後から鉄化合物と接触させて鉄を取り込ませる方法においても、鉄の取り込みを容易にするためには、高濃度の燐酸及び鉄化合物を使用するため燐酸鉄等の生成とその除去が問題になった。
【0006】
本発明者らは、これら欠点を解消した鉄含有酵母の製造方法を先に提案(特願平8−82998号)したが、鉄の含量を例えば2ないし3%以上と更に増加するために、培地中に多量の鉄を添加した場合、鉄含量の高い酵母が取得されるものの、鉄が十分に菌体内に取り込まれず、鉄由来の化合物が沈澱として発酵槽の管壁、特に気液界面の管壁にこびりつくという問題点があった。
【0007】
【課題を解決するための手段】
本発明者等は、かかる課題を解決するため鋭意研究の結果、キャンディダ・ウチリス( Candida utilis )CS−7529(FERM BP−1656)である酵母を、鉄を徐々に添加して培養すると、鉄の取り込み度合いが高くなり、鉄含量の高い菌体が得られると共に、鉄由来の沈澱物も極めて少なくなること、沈澱物が析出しても発酵槽に付着しにくいことを見いだし、本発明を完成するにいたった。
すなわち本発明は、鉄由来の沈澱物を抑えた、鉄を高含有、2%以上含有した酵母の製法を提供するものである。
【0008】
以下に本発明を詳細に説明する。
本発明に使用する酵母は、キャンディダ・ウチリス( Candida utilis )CS−7529(FERM BP−1656)である高RNA含有酵母とする。高RNA含有酵母とは、例えば特公昭56−46824号公報等に開示されているごとく、RNAを菌体重量当たり12重量%以上生成蓄積させる能力をもつ酵母をいう。
【0009】
本発明は、培地中にマグネシウムを20ppm(マグネシウムとして)以上、また、鉄を全鉄量として700〜2000ppmを培養液中に添加することにより実施される。
本発明に用いられるマグネシウムとしては、硫酸マグネスイウム、塩化マグネシウム等を例示することができる。マグネシウムの濃度は20ppm以上必要で、それ以下であると、対糖菌体収率の低下、さらには鉄の蓄積にも悪影響を及ぼす。
本発明に使用する鉄化合物については、適当な水溶性があれば、有機、無機いずれの物質であっても良い。この様な給源の具体例としてクエン酸第一鉄、フマル酸第一鉄、乳酸第一鉄等をあげることができる。この他通常の微生物培養において培地成分として使用される硫酸第一鉄、塩化第一鉄等も当然使用できる。以上のように種々の鉄化合物が使用可能であるが、工業規模の生産を考えると安価でしかも食添用の規格がある、硫酸第一鉄が最も好ましい。これらの添加量としては全鉄量として、700ppm〜2000ppmである必要がある。700ppmより少ないと鉄の蓄積量が2%未満となり、一方2000ppmを越えると増殖阻害が現れはじめ、添加した鉄の蓄積効率が低下する。
【0010】
本発明においては、鉄は、徐々に添加される。添加方法はいずれの方法でもよいが、作業の容易性から、一定の流速で添加する方法が好ましい。添加速度は、鉄としての添加量が10〜150mg/L/時間、好ましくは20〜100mg/L/時間が望ましい。これより添加量が多いと、無機鉄化合物が発酵槽の内壁に付着し易くなり好ましくない。
【0011】
菌株の培地組成として、炭素源としては通常微生物の培養に利用されるグルコース、蔗糖、酢酸、エタノール、糖蜜、亜硫酸パルプ廃液等が用いられ、窒素源としては、尿素、アンモニア、硫酸アンモニウム、塩化アンモニウム 硝酸塩等が使用される。燐酸、カリウム源も燐酸カリウム、燐酸アンモニウム、塩化カリウム等が用いられる。その他微量金属としては、亜鉛、銅、マンガン、鉄イオン等の無機塩が有効である。さらに必要に応じて、コーンスチープリカー、カゼイン、酵母エキス、ペプトン等の有機物を添加しても良い。
【0012】
本発明に使用される菌体は、培養温度20〜33℃の範囲で生育可能であるが、鉄の蓄積には21℃〜24℃の比較的低温が好ましい。
培養pHは3.5〜7.5、好ましくは4.0〜6.0であり、培養時間は炭素源の濃度により異なるが、通常20〜30時間である。
【0013】
本発明において、キャンディダ・ウチリス( Candida utilis )CS−7529(FERM BP−1656)である高RNA含有酵母を使用すると、燐酸の取り込み能力が高いため、燐酸鉄等の沈澱物を可溶化して鉄分をも吸収するため、高濃度の鉄化合物を添加した培地で培養を行っても、増殖阻害がほとんど見られない。
また、例えば特開昭62−134083号公報に記載されているように、鉄高含有微生物を取得するためには培地中のマグネシウム濃度を低くする必要があることが公知であるが、本発明によると、マグネシウム濃度を公知例より高くすることにより、2%以上の鉄を含有した酵母が容易に製造できる。
【0014】
本発明の特徴は、鉄を徐々に、特に一定の流速で添加し、鉄由来の沈澱物を抑える点にある。これは、培地中の燐酸と鉄が混ざり合って沈澱を生じる度合いを鉄の濃度をコントロールすることによって回避できたものと、本発明者らは推察している。
更に、鉄を徐々に添加することにより、添加した鉄の菌体への取り込み効率も改善されるという予期できない効果が奏され、菌体中にもほとんど低分子の鉄化合物を含まず、極めて良好な鉄高含有酵母が製造できる。
【0015】
【実施例】
以下、本発明を実施例を挙げて説明する。
尚、菌体濃度の測定は、培養液の一定量を取り、遠心分離機で菌体を2回水洗後、その一部を取って105℃、一夜乾燥させた後の重量から求めた。この菌体に取り込まれた鉄含量の測定は、菌体を湿式分解法で灰化した後、原子吸光法で行った。以下の実施例及び参考例における菌体濃度及び菌体内に取り込まれた鉄の濃度の測定はすべて同様の方法で行った。
【0016】
実施例1 酵母の培養と鉄の蓄積
YPD培地(グルコース2%、ポリペプトン2%、イーストエキス1%)100mlを500ml容の三角フラスコに分注し121℃で15分間殺菌した後、キャンディダ・ウチリスCS7529を1白金耳植菌し、30℃で24時間振とう培養し種菌とした。これを30l容発酵槽に全量植菌した。培地としてはグルコース6.5%、燐酸一アンモニウム0.26%、硫酸アンモニウム0.15%、硫酸マグネシウム0.09%、塩化カリウム0.2%、硫酸マンガン2ppm、硫酸亜鉛2ppm、硫酸銅0.4ppmを用い、バッチ培養を行った。培養条件は、槽内液量15L、培養温度30℃、通気量15L/分、撹拌400rpm、pH4.0(アンモニア添加による自動コントロール)にて行った。鉄は、硫酸第一鉄を合計の濃度として5000ppm(鉄として1000ppm)分を別の三角フラスコに入れて溶解し(硫酸第一鉄濃度で7.5%)、121℃、15分間殺菌後、ペリスタリックポンプ(アトー製、SJ1211)で20〜60mg/L/時間の速度で添加した。対照として、硫酸第一鉄5000ppm(鉄として1000ppm)を培地中に最初に添加したものを作成し、以下同様に培養した。
培養の終了は、グルコースが完全に消費された時点とした。
結果を表1に示す。
表1から明かな通り、徐々に添加する方法の方が菌体内の鉄含量が高く、しかも管壁に付着する無機鉄化合物の量も大幅に低下していることが分かる。
【0017】
【表1】

Figure 0004005677
【0018】
実施例2 菌体内に含まれる鉄含量
実施例1で得られた各々の培養液50mlを遠心分離(5000rpm、10分間、日立工機製、SCR18B)し、沈澱物を蒸留水で1回洗浄した(これを初発菌体という。)。ついでこれを1%塩酸溶液40mlに懸濁してよく攪拌後5分間放置した。これを50mlにメスアップし、その中の25mlを取り、遠心分離し、沈澱物を1%塩酸溶液25ml、蒸留水25mlでそれぞれ菌体を洗浄し、沈澱物を50mlにメスアップした(これを塩酸処理菌体という。)。各洗液を集めて100mlにメスアップした。
初発菌体、塩酸処理菌体、洗液は常法に従って湿式分解して鉄濃度を測定した。
測定結果を表2に示す。
表2から明かなように、鉄を徐々に添加することにより菌体内含量が向上するが、これら菌体内の鉄は塩酸抽出液でも菌体外に流出しない、良質のものが多いことが分かる。
【0019】
【表2】
Figure 0004005677
【0020】
【発明の効果】
以上説明してきた通り、本発明によると、鉄を徐々に、特に一定の流速で添加することにより、鉄由来の沈澱物を抑えるとともに、添加した鉄の菌体への取り込み効率も改善され、菌体中の鉄も極めて良好な状態である、鉄を2%以上含有した酵母が製造できる。[0001]
[Industrial application fields]
The present invention suppresses iron-derived precipitates by culturing edible yeast belonging to the genus Candida, particularly in the presence of an iron compound, and contains 2% or more of iron content in the yeast cells for health food applications It is related with the manufacturing method of yeast.
[0002]
[Prior art]
In recent health booms, interest in minerals and trace elements is increasing along with vitamins as nutrients. Under such circumstances, iron is one of the minerals that are said to be deficient alongside calcium in the case of Japanese. In particular, growing children and pregnant women are said to be more susceptible to iron deficiency anemia due to increased demand. Therefore, iron in a form that is easy to drink and absorb is required.
[0003]
Iron has already been actively added to processed foods, and ferrous sulfate, ferrous fumarate, ferrous succinate, etc. are usually used. However, these compounds originally have an iron odor, so the addition amount must be limited, and there is a problem in absorption into the body. Therefore, attention is recently focused on attempts to supply yeast in a form that absorbs iron to reduce the odor of iron in the form of organic iron, or to increase the absorbability into the human body.
[0004]
As a method for producing iron-containing yeast, edible microorganisms are cultured in a medium containing an iron compound, and a method for producing a microbial cell containing a large amount of iron (Japanese Patent Publication No. 61-9835), in the presence of an iron compound, A method for producing an organic ferrous iron-containing hematopoietic composition for culturing yeast in a saccharide-containing nutrient medium (Japanese Patent Laid-Open No. 58-101686), a microorganism containing an iron compound added to a medium containing a carbon source and a nitrogen source In general, a method for producing a microbial cell that needs to contain approximately 1% iron and that the concentration of magnesium in the medium is 10 mg / l or less (JP-A-62-134083). No.) is known. Furthermore, a method for producing a bivalent iron-containing yeast cell in which cells obtained by culturing yeast are dispersed in an aqueous solution containing an organic compound and a divalent water-soluble iron compound to accumulate iron (JP-A-5-176758). No.) is known.
[0005]
[Problems to be solved by the invention]
As described above, the conventional method for obtaining iron-containing cells is to obtain an iron-containing cell by culturing and growing a microorganism in a medium in which an iron compound is previously added to the medium, or a medium in which no iron compound is added in advance. Then, the microorganism is cultured and propagated, and then the cells are collected, an iron compound is added, and the cells are incorporated into the cells to obtain iron-containing cells. The former method is generally unable to add high concentration of iron because of the growth inhibition by iron. Furthermore, the added iron compound is oxidized within a relatively short time by aeration stirring during the culture, and insoluble compounds such as iron phosphate, especially with phosphate ions added as a normal essential medium component. In addition to inhibiting the iron uptake of microorganisms, there is no significant difference in the sedimentation rate between the insoluble matter and the cells in the separation of the cells by centrifugation after completion of the culture, making it difficult to separate them from the cells. It is. The presence of this insoluble matter becomes an obstacle in terms of iron odor, color and absorbency.
On the other hand, the latter method is considered to be a means for avoiding the growth inhibitory effect of iron itself on microorganisms. However, since the compound of phosphoric acid and iron increases depending on the concentration and contact time of both, iron is added in advance. In the method of collecting microbial cells cultured in a medium not added and then bringing it into contact with an iron compound to take up iron, in order to facilitate iron uptake, high concentrations of phosphoric acid and iron Since the compound is used, the production and removal of iron phosphate and the like became a problem.
[0006]
The present inventors previously proposed a method for producing an iron-containing yeast in which these drawbacks have been eliminated (Japanese Patent Application No. 8-82998). In order to further increase the iron content to, for example, 2 to 3% or more, When a large amount of iron is added to the medium, yeast with a high iron content is obtained, but iron is not sufficiently taken into the cells, and iron-derived compounds precipitate as fermenter tube walls, especially at the gas-liquid interface. There was a problem of sticking to the pipe wall.
[0007]
[Means for Solving the Problems]
The present inventors, as a result of intensive studies for solving the above problems, Candida-Uchirisu (Candida utilis ) CS-7529 (FERM BP-1656) yeast, when iron is gradually added and cultured, the degree of iron uptake increases and cells with a high iron content are obtained, and iron-derived precipitates It has been found that the amount of the precipitate is extremely small, and even if the precipitate is deposited, it is difficult to adhere to the fermenter, and the present invention has been completed.
That is, this invention provides the manufacturing method of the yeast which contained iron more highly 2% containing the precipitate derived from iron.
[0008]
The present invention is described in detail below.
Yeast used in the present invention, Candida-Uchirisu (Candida utilis ) CS-7529 (FERM BP-1656) is a high RNA-containing yeast. The high RNA-containing yeast, for example as disclosed in Japanese Patent Publication 56-46824 Patent Publication, it had a yeast having the ability to RNA to be produced and accumulated more than 12 wt% per cell weight.
[0009]
The present invention is carried out by adding 20 ppm (as magnesium) or more of magnesium to the culture medium and adding 700 to 2000 ppm of iron as the total iron amount to the culture solution.
Examples of magnesium used in the present invention include magnesium sulfate and magnesium chloride. The concentration of magnesium is required to be 20 ppm or more, and if it is less than that, it will adversely affect the yield of microbial cells and further the accumulation of iron.
The iron compound used in the present invention may be any organic or inorganic substance as long as it has an appropriate water solubility. Specific examples of such a source include ferrous citrate, ferrous fumarate, ferrous lactate and the like. In addition, ferrous sulfate, ferrous chloride and the like used as medium components in normal microorganism culture can be used as a matter of course. As described above, various iron compounds can be used, but ferrous sulfate, which is inexpensive and has standards for food addition, is most preferable in view of production on an industrial scale. As these addition amounts, the total iron amount needs to be 700 ppm to 2000 ppm. If the amount is less than 700 ppm, the amount of accumulated iron becomes less than 2%. On the other hand, if the amount exceeds 2000 ppm, growth inhibition starts to appear, and the accumulated efficiency of added iron decreases.
[0010]
In the present invention, iron is gradually added. Any addition method may be used, but a method of adding at a constant flow rate is preferable from the viewpoint of easy work. The addition rate as iron is 10 to 150 mg / L / hour, preferably 20 to 100 mg / L / hour as iron. If the added amount is larger than this, the inorganic iron compound tends to adhere to the inner wall of the fermenter, which is not preferable.
[0011]
As the medium composition of the strain, glucose, sucrose, acetic acid, ethanol, molasses, sulfite pulp waste liquid, etc. that are usually used for culturing microorganisms are used as the carbon source, and urea, ammonia, ammonium sulfate, ammonium chloride, nitrate as the nitrogen source Etc. are used. As the phosphoric acid and potassium source, potassium phosphate, ammonium phosphate, potassium chloride and the like are used. As other trace metals, inorganic salts such as zinc, copper, manganese and iron ions are effective. Further, if necessary, organic substances such as corn steep liquor, casein, yeast extract and peptone may be added.
[0012]
The cells used in the present invention can grow at a culture temperature of 20 to 33 ° C, but a relatively low temperature of 21 to 24 ° C is preferable for the accumulation of iron.
The culture pH is 3.5 to 7.5, preferably 4.0 to 6.0, and the culture time is usually 20 to 30 hours, although it varies depending on the concentration of the carbon source.
[0013]
In the present invention, Candida-Uchirisu (Candida utilis ) CS-7529 (FERM BP-1656), a high RNA-containing yeast, has a high phosphate uptake capacity, solubilizes precipitates such as iron phosphate and also absorbs iron, so high concentration Even when culturing in a medium supplemented with an iron compound, growth inhibition is hardly observed.
Further, as described in, for example, JP-A-62-134083, it is known that the magnesium concentration in the medium needs to be lowered in order to obtain a high iron-containing microorganism. And by making magnesium concentration higher than a well-known example, the yeast containing 2% or more of iron can be manufactured easily.
[0014]
A feature of the present invention is that iron is gradually added, particularly at a constant flow rate, to suppress iron-derived precipitates. The present inventors presume that this can be avoided by controlling the concentration of iron to the extent that phosphoric acid and iron in the medium are mixed to cause precipitation.
Furthermore, by gradually adding iron, an unexpected effect of improving the uptake efficiency of the added iron into the microbial cells is achieved, and the microbial cells contain almost no low-molecular iron compounds and are extremely good. A high iron content yeast can be produced.
[0015]
【Example】
Hereinafter, the present invention will be described with reference to examples.
The bacterial cell concentration was determined from the weight after taking a certain amount of the culture solution, washing the bacterial cells twice with a centrifuge, and taking a portion of them and drying them at 105 ° C. overnight. The iron content incorporated into the cells was measured by the atomic absorption method after ashing the cells by a wet decomposition method. In the following Examples and Reference Examples, the bacterial cell concentration and the concentration of iron incorporated into the bacterial cell were all measured by the same method.
[0016]
Example 1 Yeast Culture and Iron Accumulation YPD medium (glucose 2%, polypeptone 2%, yeast extract 1%) 100ml was dispensed into a 500ml Erlenmeyer flask and sterilized at 121 ° C for 15 minutes, and then Candida utilis. One platinum ear of CS7529 was inoculated and cultured at 30 ° C. with shaking for 24 hours to form an inoculum. All of this was inoculated into a 30 liter fermenter. The culture medium is glucose 6.5%, monoammonium phosphate 0.26%, ammonium sulfate 0.15%, magnesium sulfate 0.09%, potassium chloride 0.2%, manganese sulfate 2ppm, zinc sulfate 2ppm, copper sulfate 0.4ppm Was used for batch culture. The culture conditions were as follows: the amount of liquid in the tank was 15 L, the culture temperature was 30 ° C., the aeration rate was 15 L / min, the stirring was 400 rpm, and the pH was 4.0 (automatic control by adding ammonia). Iron was dissolved in 5000 ppm (1000 ppm as iron) content of ferrous sulfate as a total concentration in another Erlenmeyer flask (7.5% ferrous sulfate concentration), sterilized at 121 ° C. for 15 minutes, The mixture was added at a rate of 20 to 60 mg / L / hour with a peristaltic pump (manufactured by Ato, SJ1211). As a control, ferrous sulfate 5000 ppm (1000 ppm as iron) was first added to the medium, and the same culture was performed.
The culture was terminated when glucose was completely consumed.
The results are shown in Table 1.
As is clear from Table 1, it can be seen that the method of gradually adding has a higher iron content in the cells and the amount of the inorganic iron compound adhering to the tube wall is greatly reduced.
[0017]
[Table 1]
Figure 0004005677
[0018]
Example 2 Iron content contained in bacterial cells 50 ml of each culture solution obtained in Example 1 was centrifuged (5000 rpm, 10 minutes, manufactured by Hitachi Koki, SCR18B), and the precipitate was washed once with distilled water ( This is called the first cell.) This was then suspended in 40 ml of 1% hydrochloric acid solution and allowed to stand for 5 minutes after stirring. This was made up to 50 ml, 25 ml of it was taken and centrifuged, the precipitate was washed with 25 ml of 1% hydrochloric acid solution and 25 ml of distilled water, respectively, and the precipitate was made up to 50 ml. This is called hydrochloric acid-treated cells.) Each wash was collected and made up to 100 ml.
The initial cells, hydrochloric acid-treated cells, and the washing solution were subjected to wet decomposition according to a conventional method, and the iron concentration was measured.
The measurement results are shown in Table 2.
As is apparent from Table 2, the content of the bacterial cells is improved by gradually adding iron, but it can be seen that there are many good quality irons that do not flow out of the bacterial cells even with a hydrochloric acid extract.
[0019]
[Table 2]
Figure 0004005677
[0020]
【The invention's effect】
As described above, according to the present invention, by gradually adding iron, particularly at a constant flow rate, the iron-derived precipitate is suppressed, and the efficiency of incorporating the added iron into the cells is improved. Yeast containing 2% or more of iron, in which the iron in the body is also in a very good state, can be produced.

Claims (2)

培地中にマグネシウムを20ppm(マグネシウムとして)以上添加して酵母を培養し鉄含有酵母を製造する方法において、該酵母がキャンディダ・ウチリス( Candida utilis )CS−7529(FERM BP−1656)である高RNA含有酵母であり、鉄を培養液中に徐々に添加し、全鉄量として700〜2000ppm添加することを特徴とする、鉄由来の沈殿物を抑えた、菌体内に鉄含量として2%以上を含有する酵母菌体の製法。In a method for culturing yeast by adding 20 ppm (as magnesium) or more of magnesium to a medium to produce an iron-containing yeast, the yeast is produced by Candida utilis ( Candida utilis ) CS-7529 (FERM BP-1656), a high RNA-containing yeast, wherein iron is gradually added to the culture medium, and 700-2000 ppm is added as the total iron content, and this is an iron-derived precipitate. A method for producing yeast cells that contain 2% or more of iron as the iron content in which the substances are suppressed. 鉄としての添加量が10〜150mg/L/時間である請求項1記載の製法。The process according to claim 1, wherein the amount of iron added is 10 to 150 mg / L / hour.
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