JPH08332083A - Yeast containing iron at high concentration - Google Patents

Yeast containing iron at high concentration

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Publication number
JPH08332083A
JPH08332083A JP16451195A JP16451195A JPH08332083A JP H08332083 A JPH08332083 A JP H08332083A JP 16451195 A JP16451195 A JP 16451195A JP 16451195 A JP16451195 A JP 16451195A JP H08332083 A JPH08332083 A JP H08332083A
Authority
JP
Japan
Prior art keywords
yeast
iron
magnesium
solution
zinc
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP16451195A
Other languages
Japanese (ja)
Other versions
JP3272571B2 (en
Inventor
Masayasu Ando
正康 安藤
Ryoichi Nakajima
亮一 中島
Setsu Ichigen
摂 一言
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Oriental Yeast Co Ltd
Original Assignee
Oriental Yeast Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Oriental Yeast Co Ltd filed Critical Oriental Yeast Co Ltd
Priority to JP16451195A priority Critical patent/JP3272571B2/en
Publication of JPH08332083A publication Critical patent/JPH08332083A/en
Application granted granted Critical
Publication of JP3272571B2 publication Critical patent/JP3272571B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE: To obtain the subject yeast useful for perorally administrable pharmaceutical preparations, foods and drinks, feeds, baits, etc., containing iron at a high concentration by culturing a yeast in a suspended state under slowly stirring or shaking in a solution containing a specific amount or more of the iron. CONSTITUTION: This yeast contains iron at a high concentration. The yeast is obtained by using ferrous sulfate, preparing a solution containing >=2000ppm ferrous ions in the solution, then suspending a yeast such as a baker's yeast in the solution, slowly stirring and/or shaking the suspension at 30 deg.C for 24hr, collecting the yeast fungal cell in the suspended state by centrifugation and washing the collected yeast fungal cell with ion exchange water. The resultant yeast contains >=15000ppm iron and bivalent iron excellent in absorbability at a high concentration and is useful as a perorally administrable pharmaceutical preparation or various foods such as breads, biscuits or miso. The cell wall of the resultant yeast is destroyed to take out the contents, which are then used to provide foods and drinks such as a juice, an ice cream or a cracker, feeds or baits containing a large amount of iron.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、ミネラル、特に鉄を高
濃度に含有する食用酵母及びその製造方法に関するもの
である。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an edible yeast containing a high concentration of minerals, especially iron, and a method for producing the same.

【0002】[0002]

【従来の技術】鉄分が生体内において重要な微量ミネラ
ルのひとつであることはよく知られている。しかし、近
年、食生活が豊かになり大幅に改善されたとは言え、鉄
が不足気味なのは、発展途上国にとどまらず、先進国に
おいても広く認められているところである。
2. Description of the Related Art It is well known that iron is one of the important trace minerals in the living body. However, although dietary habits have become richer and improved significantly in recent years, iron deficiency is widely recognized not only in developing countries but also in developed countries.

【0003】このような鉄欠乏の改善のため、例えば鉄
欠乏性貧血症状の改善には、従来、硫酸第一鉄等の鉄剤
が使用されてきた。しかし、これらの鉄剤は、貯蔵中あ
るいは消化管中で酸化されて、吸収性にすぐれている二
価の鉄から吸収されづらい三価の鉄化合物になりやすい
という欠点を有している。
In order to improve such iron deficiency, for example, to improve the symptoms of iron deficiency anemia, iron agents such as ferrous sulfate have been conventionally used. However, these iron agents have a drawback in that they are easily oxidized into trivalent iron compounds which are difficult to be absorbed from divalent iron having excellent absorbability during storage or in the digestive tract.

【0004】[0004]

【発明が解決しようとする課題】本発明は、このような
技術の現状に鑑み、鉄、特に吸収性にすぐれた二価の鉄
を高濃度に含有する経口投与可能な製剤ないし飲食品タ
イプの組成物を開発する目的でなされたものである。
SUMMARY OF THE INVENTION In view of the current state of the art, the present invention provides an orally administrable preparation or a food or drink type product containing a high concentration of iron, particularly divalent iron having excellent absorbability. It was made for the purpose of developing a composition.

【0005】[0005]

【課題を解決するための手段】本発明は、上記目的を達
成するためになされたものであって、従来のように鉄化
合物を直接投与するのではなく、食用微生物に鉄分を多
量に摂取蓄積せしめ、この鉄高含有微生物を利用するこ
とにより、いわば間接的に鉄を摂取するシステムに着目
した。
Means for Solving the Problems The present invention has been made in order to achieve the above-mentioned object, and does not directly administer an iron compound as in the prior art, but ingests and accumulates a large amount of iron in edible microorganisms. By using this iron-rich microorganism, we focused on a system that indirectly ingests iron.

【0006】そして各種の食用用途に広く使用されてい
る酵母に着目して鉄塩含有培地で酵母を培養したけれど
も、鉄塩の添加量を高くすると、従来からの技術常識ど
おり、酵母の増殖阻害がひき起こされ、鉄を高濃度に含
有する酵母を得ることはできなかった。
[0006] Then, although yeast was cultivated in an iron salt-containing medium by paying attention to yeasts widely used for various edible uses, if the amount of iron salt added was increased, the growth inhibition of yeast was observed according to the conventional technical common sense. However, it was not possible to obtain yeast containing a high concentration of iron.

【0007】しかしながら本発明者らは、このような技
術常識に敢えて挑戦し、鉄を従来なし得なかった程度の
高濃度に含有する新規酵母を創製するという新規課題を
敢えて設定した。そこで各方面から検討の結果、酵母を
栄養培地で培養するのではなく、鉄高濃度含有液中で非
増殖的に酵母を懸濁状態でゆっくり攪拌したところ、全
く予期せざることに、酵母菌体中に大量に鉄が取り込ま
れるという新知見を得た。しかも、従来の技術常識に反
して、鉄濃度を高めても酵母が死滅することはなく、溶
液中の鉄濃度に応じて酵母菌体中の鉄含量も増加し、乾
燥菌体当たり15,000ppm以上にも達することを
確認した。このように高濃度に鉄を含有した酵母は従来
全く創製し得ないとされていたものである。
[0007] However, the inventors of the present invention dared to challenge such common general knowledge and set a new subject of creating a new yeast containing iron at a high concentration which could not be achieved conventionally. Therefore, as a result of examining from various directions, when the yeast was slowly stirred in a suspension state in a high iron concentration solution in a non-proliferating state, the yeast was not cultivated in a nutrient medium. We obtained a new finding that a large amount of iron is taken into the body. Moreover, contrary to the conventional technical common sense, even if the iron concentration is increased, the yeast is not killed, and the iron content in the yeast cells also increases according to the iron concentration in the solution, and 15,000 ppm per dry cell. I confirmed that it would reach the above. Such yeast containing iron at a high concentration has heretofore been considered to be completely uncreatable.

【0008】本発明は、このような有用新知見を基礎と
し、更に研究の結果、完成されたものであって、その詳
細は以下に述べるとおりである。
The present invention has been completed as a result of further research based on such useful new knowledge, and the details thereof are as described below.

【0009】本発明を実施するには、鉄の水溶性塩を多
量に含有する高濃度鉄含有液中で酵母を懸濁せしめ、非
増殖的にゆっくりと酵母が沈降しない程度に攪拌及び/
又は振とうすることが必要である。本発明においては、
酵母を培養するための培地を使用するものではなく、非
増殖的に処理するものである。つまり、菌体の増殖に必
要な物質が実質的に存在しない条件下で、酵母を処理す
るのである。
To carry out the present invention, yeast is suspended in a high-concentration iron-containing solution containing a large amount of a water-soluble salt of iron, and agitated and / or stirred so that the yeast does not settle slowly in a non-proliferative manner.
Or it is necessary to shake. In the present invention,
It does not use a medium for culturing yeast, but treats it non-proliferatively. In other words, yeast is treated under conditions in which substances necessary for the growth of bacterial cells are substantially absent.

【0010】本発明において使用する鉄塩としては、適
度な水溶性を有し、且つ酵母を死滅させるものではな
く、酵母菌体内に効率的に取り込まれるものであれば、
有機、無機を問わずすべての鉄化合物が1種又はそれ以
上使用可能である。その非限定例としては次のものが挙
げられる:硫酸第一鉄、塩化第一鉄、クエン酸第一鉄、
フマル酸第一鉄、グルコン酸第一鉄、酪酸第一鉄、酒石
酸第一鉄、乳酸第一鉄。
As the iron salt used in the present invention, as long as it has appropriate water solubility and does not kill yeast, it can be efficiently taken up in yeast cells.
One or more of all iron compounds, organic or inorganic, can be used. Non-limiting examples of which include: ferrous sulfate, ferrous chloride, ferrous citrate,
Ferrous fumarate, ferrous gluconate, ferrous butyrate, ferrous tartrate, ferrous lactate.

【0011】鉄塩の添加量は、1,500ppmよりも
高濃度とし、2,000ppm以上とするのが好適であ
る。2,000ppmもの高濃度の鉄で酵母を処理すれ
ば、酵母は死滅したり、あるいは死滅しないまでも重大
な悪影響が充分に懸念されるところではあるが、このよ
うな技術常識を本発明は大幅に超越したものであり、全
く予期せざることに、このような高濃度の鉄によっても
酵母が死滅しないどころか、それを大量に菌体内に取り
込ませるのにはじめて成功したものである。しかも更に
10,000ppmもの高濃度の鉄での処理も可能であ
ることも確認している。
The addition amount of the iron salt is higher than 1,500 ppm, preferably 2,000 ppm or more. If yeast is treated with iron at a concentration as high as 2,000 ppm, the yeast may be killed, or even if it is not killed, serious adverse effects may be suspected. Not surprisingly, it was the first time that yeast was not killed by such a high concentration of iron, but it was the first time that it could be taken up into the cells. Moreover, it has been confirmed that treatment with iron having a high concentration of 10,000 ppm is possible.

【0012】その結果、乾燥菌体当たり15,000p
pm以上の鉄を酵母菌体内に取り込ませることに遂に成
功したのである。10,000ppm以上もの鉄を含有
する酵母は、従来存在せず、また、既述したように創製
しようとしても創製できなかった新規有用酵母である。
更に驚異的なことに、本発明によれば、10,000p
pmの鉄溶液を使用することにより、30,000pp
m以上ものきわめて大量の鉄を酵母菌体内に取り込ませ
ることすら可能である。
As a result, 15,000 p per dry cell
Finally, we succeeded in incorporating yeast of pm or more into yeast cells. Yeast containing 10,000 ppm or more of iron has not existed in the past, and is a novel useful yeast that could not be created even if it was attempted to be created as described above.
Even more surprisingly, according to the present invention, 10,000 p
30,000 pp by using pm iron solution
It is even possible to incorporate an extremely large amount of iron of m or more into yeast cells.

【0013】鉄を酵母菌体内に取り込ませるための処理
条件としては、鉄溶液中に酵母を懸濁して、4〜40
℃、好ましくは20〜35℃の温度、0.5〜72時
間、好ましくは1〜36時間、pH4〜7、好ましくは
pH4.5〜6.5とするが、使用する酵母、鉄塩の種
類や濃度に応じて適宜定め、場合によっては上記範囲外
であってもよい。
The treatment conditions for incorporating iron into the yeast cells are as follows.
C., preferably 20 to 35.degree. C., 0.5 to 72 hours, preferably 1 to 36 hours, pH 4 to 7, preferably pH 4.5 to 6.5, but the type of yeast and iron salt used. It may be appropriately determined depending on the concentration, and may be out of the above range in some cases.

【0014】攪拌及び/又は振とうは、酵母と鉄イオン
が接触するだけのゆっくりした速度で行う必要があり、
鉄溶液の粘度や酵母の含有量にもよるが、500rpm
以下、好ましくは200rpm以下のゆるやかな攪拌、
ないしは、振幅12cmの場合、200rpm以下、好
ましくは150rpm以下程度の振とうとするのが良
い。
The stirring and / or shaking must be carried out at a slow speed so that the yeast and iron ions come into contact with each other,
500 rpm, depending on the viscosity of the iron solution and the yeast content
Below, preferably a gentle agitation of 200 rpm or less,
Or, when the amplitude is 12 cm, it is preferable to shake at 200 rpm or less, preferably about 150 rpm or less.

【0015】本発明においては、酵母であれば食用酵母
を含めいかなる酵母も使用することができる。その非限
定例としては、次の各属に属する酵母が挙げられる:サ
ッカロミセス(Saccharomyces)属、トルロプシス(Tor
ulopsis)属、ミコトルラ(Mycotorula)属、トルラス
ポラ(Torulaspora)属、キャンディダ(Candida)属、
ロードトルラ(Rhodotorula)属、ピキア(Pichia)属
その他。
In the present invention, any yeast can be used as long as it is a yeast, including edible yeast. Non-limiting examples include yeasts belonging to each of the following genera: Saccharomyces, Torrlopsis (Tor).
ulopsis genus, Mycotorula genus, Torulaspora genus, Candida genus,
Rhodotorula genus, Pichia genus and others.

【0016】具体的には、Saccharomyces cerevisiae、
同uvarum、同rouxii IFO 0439; Torulopsis utilis、同
candida IFO 0856; Mycotorula japonica、同lipolytic
a; Torulaspora delbrueckii、同fermentati; Candida
sake、同tropicalis、同utilis ATCC 16321; Hansenula
anomala IFO 0140、同suaveolens; Saccharomycopsis
fibligera IFO 1665、同lipolytica ATCC 20182; Rhodo
torula rubra IFO 0870; Pichia farinosa IFO 0607、
その他の酵母が例示される。
Specifically, Saccharomyces cerevisiae,
Uvarum, rouxii IFO 0439; Torulopsis utilis, same
candida IFO 0856; Mycotorula japonica, same lipolytic
a; Torulaspora delbrueckii, fermentati; Candida
sake, tropicalis, utilis ATCC 16321; Hansenula
anomala IFO 0140, suaveolens; Saccharomycopsis
fibligera IFO 1665, same lipolytica ATCC 20182; Rhodo
torula rubra IFO 0870; Pichia farinosa IFO 0607,
Other yeasts are exemplified.

【0017】また、これらの酵母の内、特に食用酵母と
して、ヒトの飲食、動物の飼料、魚類の餌料に多用され
る酵母としては、Saccharomyces cerevisiae、同uvaru
m、同rouxii、Saccharomycopsis fibligeraその他に属
する、パン酵母、ビール酵母、ブドウ酒酵母、清酒酵
母、アルコール酵母、甘酒酵母、味噌醤油酵母、飼料酵
母、餌料酵母等が挙げられる。
Among these yeasts, especially as edible yeasts, Saccharomyces cerevisiae and uvaru are commonly used as yeasts for human food and drink, animal feed and fish feed.
Examples include baker's yeast, brewer's yeast, wine yeast, sake yeast, alcohol yeast, amazake yeast, miso soy sauce yeast, feed yeast, and feed yeast, which belong to m, rouxii, Saccharomycopsis fibligera and others.

【0018】酵母を懸濁させる液体としては、水を用い
るのが通常である。水は、蒸留水や脱イオン水でもよい
が、水道水で充分である。酵母菌体濃度は、例えば圧搾
酵母として10〜40%、好ましくは10〜20%であ
るが、効率よく鉄を取り込むよう適宜選択する。そし
て、菌体は、鉄分及び/又は酵母菌体が沈殿しない程度
にゆっくりと攪拌及び/又は振とうする。
Water is usually used as the liquid in which the yeast is suspended. The water may be distilled water or deionized water, but tap water is sufficient. The yeast cell concentration is, for example, 10 to 40%, preferably 10 to 20% as the compressed yeast, but is appropriately selected so as to efficiently take in iron. Then, the cells are slowly stirred and / or shaken to the extent that iron and / or yeast cells do not precipitate.

【0019】このようにして鉄を取り込んだ酵母は、遠
心分離、濾過等によって集菌した後、洗浄して目的の菌
体を得、必要があれば凍結乾燥その他常法にしたがって
乾燥菌体とし、各種の用途に使用する。また、希望する
のであれば、菌体を破砕ないし菌体を溶菌して内容物を
取り出し、これを利用することも可能である。
The yeast thus loaded with iron is collected by centrifugation, filtration, etc., and then washed to obtain the desired bacterial cells, and if necessary, freeze-dried or dried cells according to a conventional method. , Used for various purposes. Further, if desired, it is also possible to crush the cells or lyse the cells to take out the contents and use them.

【0020】また、本発明においては、各種ミネラルを
あらかじめ多量に含有せしめておいた酵母を、上記した
通常の酵母の場合と同様に、鉄を2,000ppm以上
含有する溶液中で通気状態にすることなく懸濁状態でゆ
っくりと攪拌及び/又は振とうすることにより、各種の
ミネラルに更に鉄を高濃度に含有する新規なマルチミネ
ラル高含有酵母を創製することができる。
Further, in the present invention, yeast containing a large amount of various minerals in advance is aerated in a solution containing 2,000 ppm or more of iron, as in the case of the above-mentioned ordinary yeast. By slowly stirring and / or shaking in a suspended state without using any of the above, it is possible to create a novel yeast containing a large amount of multi-minerals that further contains iron in a high concentration in various minerals.

【0021】マルチミネラル高含有酵母としては、亜鉛
・鉄高含有酵母、マグネシウム・鉄高含有酵母、マグネ
シウム・亜鉛・鉄高含有酵母等が例示される。
Examples of yeasts with a high content of multi-minerals include yeasts with a high content of zinc and iron, yeasts with a high content of magnesium and iron, yeasts with a high content of magnesium, zinc and iron, and the like.

【0022】亜鉛・鉄高含有酵母は、あらかじめ製造し
ておいた亜鉛高含有酵母を原料酵母とし、本発明に係る
上記した鉄高含有酵母製造条件で鉄を酵母に取り込ませ
る処理により製造することができる。
The zinc-rich iron-rich yeast is produced by using the previously-produced zinc-rich yeast as a raw material yeast, and incorporating iron into the yeast under the above-mentioned iron-rich yeast production conditions according to the present invention. You can

【0023】亜鉛高含有酵母は、亜鉛高含有酵母製造条
件、つまり、亜鉛を50ppm以上含有する溶液中で、
酵母を懸濁状態で非増殖的に攪拌及び/又は振とうする
ことにより製造することができる。
Yeasts high in zinc are produced under the conditions for producing yeasts high in zinc, that is, in a solution containing 50 ppm or more of zinc.
It can be produced by non-proliferatively stirring and / or shaking yeast in suspension.

【0024】本方法を実施するには、亜鉛の水溶性塩を
多量に含有する高濃度亜鉛含有液中で酵母を懸濁せし
め、非増殖的に攪拌及び/又は振とうすることが必要で
ある。本方法においては、酵母を培養するための培地を
使用するものではなく、非増殖的に処理するものであ
る。つまり、菌体の増殖に必要な物質が実質的に存在し
ない条件下で、酵母を処理するのである。
In order to carry out the present method, it is necessary to suspend the yeast in a high-concentration zinc-containing liquid containing a large amount of a water-soluble salt of zinc, and agitate and / or shake it non-proliferatively. . In this method, a medium for culturing yeast is not used, but a non-proliferative treatment is performed. In other words, yeast is treated under conditions in which substances necessary for the growth of bacterial cells are substantially absent.

【0025】使用する亜鉛塩としては、適度な水溶性を
有し、且つ酵母を死滅させるものではなく、酵母菌体内
に効率的に取り込まれるものであれば、有機、無機を問
わずすべての亜鉛化合物が1種又はそれ以上使用可能で
ある。その非限定例としては次のものが挙げられる;硫
酸亜鉛、塩化亜鉛、クエン酸亜鉛、酢酸亜鉛、酒石酸亜
鉛、乳酸亜鉛。
As the zinc salt to be used, any zinc salt, organic or inorganic, can be used as long as it has appropriate water solubility, does not kill yeast, and can be efficiently taken up in yeast cells. One or more compounds can be used. Non-limiting examples include: zinc sulfate, zinc chloride, zinc citrate, zinc acetate, zinc tartrate, zinc lactate.

【0026】亜鉛塩の添加量は、50ppmでも良い結
果が得られるがそれよりも高濃度、2,000ppm以
上、特に好ましくは3,000〜6,000ppmとす
るのが好適である。従来の技術常識からすれば、高濃度
の亜鉛で酵母を処理すれば、酵母は死滅したり、あるい
は死滅しないまでも重大な悪影響が充分に懸念されると
ころではあるが、このような技術常識を本発明は大幅に
超越したものであって、全く予期せざることに、このよ
うな高濃度の亜鉛によっても酵母が死滅しないどころ
か、それを大量に菌体内に取り込ませるのにはじめて成
功したものである。しかも更に10,000ppm以上
の高濃度の亜鉛での処理も可能であることも確認してい
る。
A good result can be obtained even when the amount of the zinc salt added is 50 ppm, but a higher concentration than that, 2,000 ppm or more, particularly preferably 3,000 to 6,000 ppm is suitable. According to the conventional technical common sense, if yeast is treated with a high concentration of zinc, the yeast may be killed, or even if it is not killed, there is a serious fear of serious adverse effects. The present invention is significantly transcendental, and, unexpectedly, it was the first time that yeast was not killed by such a high concentration of zinc, but rather it was first succeeded in incorporating it into the cells. is there. Furthermore, it has been confirmed that treatment with zinc having a high concentration of 10,000 ppm or more is possible.

【0027】その結果、乾燥菌体当たり600〜10,
000ppm以上の亜鉛を酵母菌体内に取り込ませるこ
とがはじめて可能となった。更に驚異的なことに、本発
明によれば、10,000ppmの亜鉛溶液を使用する
ことにより、乾燥菌体当たり30,000ppm以上も
のきわめて大量の亜鉛を酵母菌体内に取り込ませること
すら可能である。
As a result, 600 to 10 per dry cell,
It was possible for the first time to incorporate zinc of 000 ppm or more into yeast cells. Even more surprisingly, according to the present invention, by using a 10,000 ppm zinc solution, it is even possible to incorporate a very large amount of zinc of 30,000 ppm or more per dry cell into yeast cells. .

【0028】亜鉛を酵母菌体内に取り込ませるための処
理条件としては、亜鉛溶液中に酵母を懸濁して、4〜4
0℃、好ましくは20〜35℃の温度、1〜120時
間、好ましくは40〜100時間、pH4〜7、好まし
くはpH4.5〜6.5とするが、使用する酵母、亜鉛
塩の種類や濃度に応じて適宜定め、場合によっては上記
範囲外であってもよい。
The treatment conditions for incorporating zinc into the yeast cells are as follows.
The temperature is 0 ° C., preferably 20 to 35 ° C., 1 to 120 hours, preferably 40 to 100 hours, pH 4 to 7, preferably pH 4.5 to 6.5. It may be appropriately determined depending on the concentration, and may be out of the above range in some cases.

【0029】攪拌及び/又は振とうは、亜鉛液の粘度や
酵母の含有量等にもよるが、500〜1,000rpm
程度の攪拌、ないしは、振幅12cmの場合、100〜
200rpmの振とうとするのがよい。そして更に通気
を行う等、好気的な条件にて行うと良好な結果が得られ
る。通気は0.5〜5vvm程度で行うが、必要ある場
合にはこの範囲を逸脱しても差し支えない。
The stirring and / or shaking depends on the viscosity of the zinc solution, the yeast content, etc., but is 500 to 1,000 rpm.
If the stirring is moderate, or the amplitude is 12 cm, 100-
It is recommended to shake at 200 rpm. Good results can be obtained by performing aeration under aerobic conditions. Aeration is performed at about 0.5 to 5 vvm, but if necessary, the range may be deviated.

【0030】上記のようにして、亜鉛・鉄高含有酵母を
創製することができる。その結果、乾燥菌体当たり亜鉛
を10,000ppm、鉄を15,000ppmあるい
はそれ以上含有する新規マルチミネラル食用酵母を得る
ことができる。
As described above, a zinc-iron-rich yeast can be created. As a result, a novel multi-mineral edible yeast containing 10,000 ppm of zinc and 15,000 ppm or more of iron per dry cell can be obtained.

【0031】マグネシウム・鉄高含有酵母は、あらかじ
め製造しておいたマグネシウム高含有酵母を原料酵母と
し、本発明に係る上記した鉄高含有酵母製造条件で鉄を
酵母に取り込ませる処理により製造することができる。
The magnesium-rich iron-rich yeast is produced by using the previously-produced magnesium-rich yeast as a raw material yeast and treating iron with yeast under the above-mentioned iron-rich yeast production conditions according to the present invention. You can

【0032】マグネシウム高含有酵母は、マグネシウム
高含有酵母製造条件、つまり、マグネシウムを高濃度に
含有する溶液中で、酵母を懸濁状態で非増殖的に攪拌及
び/又は振とうすることにより製造することができる。
The high magnesium content yeast is produced by non-proliferative stirring and / or shaking of the yeast in suspension in a high magnesium content production condition, that is, in a solution containing a high concentration of magnesium. be able to.

【0033】本方法を実施するには、マグネシウムの水
溶性塩を多量に含有する高濃度マグネシウム含有溶液中
で酵母を懸濁せしめ、好気的に攪拌及び/又は振とうす
ることが必要である。本方法においては、最終的に創製
される酵母菌体内のマグネシウム濃度は、酵母を培養す
るための培地組成の如何にかかわらず、酵母を懸濁せし
めた溶液中のマグネシウム濃度に依存している。つま
り、菌体の増殖に必要な物質が存在する条件下であって
も、また実質的に存在しない条件下であっても酵母にマ
グネシウムを取り込ませることは可能である。
In order to carry out the present method, it is necessary to suspend the yeast in a high concentration magnesium-containing solution containing a large amount of a water-soluble salt of magnesium, and aerobically agitate and / or shake it. . In this method, the magnesium concentration in the finally created yeast cells depends on the magnesium concentration in the solution in which the yeast is suspended, regardless of the composition of the medium for culturing the yeast. In other words, it is possible to allow magnesium to be incorporated into yeast even under the condition that a substance necessary for the growth of bacterial cells exists or under the condition that it does not substantially exist.

【0034】本方法において使用するマグネシウム塩と
しては、適度な水溶性を有し、且つ酵母を死滅させるも
のではなく、酵母菌体内に効率的に取り込まれるもので
あれば、有機、無機を問わずすべてのマグネシウム化合
物が1種又はそれ以上使用可能である。その非限定例と
しては次のものが挙げられる:硫酸マグネシウム、塩化
マグネシウム、クエン酸マグネシウム、酢酸マグネシウ
ム、酒石酸第一マグネシウム、乳酸第一マグネシウム。
The magnesium salt used in the present method may be organic or inorganic, as long as it has appropriate water solubility, does not kill yeast, and is efficiently taken up by yeast cells. All magnesium compounds can be used alone or in combination. Non-limiting examples of which include: magnesium sulfate, magnesium chloride, magnesium citrate, magnesium acetate, primary magnesium tartrate, primary magnesium lactate.

【0035】マグネシウム塩の添加量は、液中のマグネ
シウム濃度が50ppm以上となるように設定するのが
好適である。このように高濃度のマグネシウムで酵母を
処理すれば、酵母は死滅したり、あるいは死滅しないま
でも、活性低下等の重大な悪影響が充分に懸念されると
ころではあるが、このような技術常識を本発明は大幅に
超越したものであり、全く予期せざることに、このよう
な高濃度のマグネシウムによっても酵母が死滅しないど
ころか、極めて高濃度のマグネシウムを菌体内に蓄積す
ることができるとともに、酵母の生理活性はほとんど低
下しないという有用な新知見を得た。
The amount of magnesium salt added is preferably set so that the magnesium concentration in the liquid is 50 ppm or more. If yeast is treated with such a high concentration of magnesium, the yeast may be killed, or even if it is not killed, serious adverse effects such as reduced activity may be suspected. The present invention is significantly transcendental and, unexpectedly, not only yeast is not killed by such high concentration of magnesium, but extremely high concentration of magnesium can be accumulated in the bacterial cells, and We obtained a useful new finding that the physiological activity of P.

【0036】その結果、乾燥菌体当たり2,000pp
m以上のマグネシウムを酵母菌体内に取り込ませること
に遂に成功したのである。更に驚異的なことに、本方法
によれば20,000ppmのマグネシウムイオン含有
溶液を使用することにより、乾燥菌体当たり20,00
0ppm以上もの極めて大量のマグネシウムを酵母菌体
内に取り込ませることすら可能である。
As a result, 2,000 pp per dry cell
Finally, we succeeded in incorporating more than m of magnesium into the yeast cells. Even more surprisingly, according to this method, by using a solution containing 20,000 ppm of magnesium ions, it is possible to obtain 20,000 per dry cell.
It is even possible to incorporate a very large amount of magnesium of 0 ppm or more into yeast cells.

【0037】本方法にしたがってマグネシウムを酵母菌
体内に多量に含有せしめるには、マグネシウム溶液中に
湿菌体として5〜30%、好ましくは10〜20%の酵
母を懸濁して、15〜40℃、好ましくは25〜35
℃、更に好ましくは28〜33℃の温度、1〜120時
間、好ましくは36〜96時間の処理時間、pH4〜
7、好ましくはpH4.5〜6.0、通気は0〜5vv
m、好ましくは1〜3vvm、攪拌は使用する設備の規
模によっても異なるが50〜1,000rpm、振とう
する場合は振幅12cmの設備では100〜200rp
m、好ましくは100〜150rpmとするが、使用す
る酵母、マグネシウム塩の種類やその濃度に応じて適宜
選択することができ、必要によっては上記の範囲を逸脱
する場合もある。
In order to make a large amount of magnesium contained in yeast cells according to this method, 5 to 30%, preferably 10 to 20% of yeast as wet cells are suspended in a magnesium solution and the temperature is set to 15 to 40 ° C. , Preferably 25-35
C., more preferably 28 to 33.degree. C., treatment time 1 to 120 hours, preferably 36 to 96 hours, pH 4 to 4.
7, preferably pH 4.5-6.0, aeration 0-5vv
m, preferably 1 to 3 vvm, stirring varies depending on the scale of equipment used, but 50 to 1,000 rpm, and 100 to 200 rp for equipment having an amplitude of 12 cm when shaking.
m, preferably 100 to 150 rpm, but can be appropriately selected depending on the type of yeast and magnesium salt used and the concentration thereof, and may deviate from the above range depending on the necessity.

【0038】上記のようにして、マグネシウム・鉄高含
有酵母を製造することができる。その結果、乾燥菌体当
たりマグネシウムを2,000ppm、鉄を15,00
0ppmあるいはそれ以上含有する新規マルチミネラル
食用酵母を得ることができる。
[0038] As described above, the magnesium-iron-rich yeast can be produced. As a result, magnesium per dry cell was 2,000 ppm and iron was 15,000.
A novel multi-mineral edible yeast containing 0 ppm or more can be obtained.

【0039】マグネシウム・亜鉛・鉄高含有酵母は、あ
らかじめ製造しておいたマグネシウム・亜鉛高含有酵母
を原料酵母とし、本発明に係る上記した鉄高含有酵母製
造条件で鉄を酵母に取り込ませる処理により製造するこ
とができる。
The magnesium / zinc / iron-rich yeast is prepared by using a previously-produced magnesium / zinc-rich yeast as a raw material yeast and incorporating iron into the yeast under the above-described iron-rich yeast production conditions according to the present invention. Can be manufactured by.

【0040】マグネシウム・亜鉛高含有酵母は、マグネ
シウム・亜鉛高含有酵母製造条件、つまり、先に記した
マグネシウム高含有酵母製造条件で得られたマグネシウ
ム高含有酵母を原料酵母として、亜鉛を高濃度に含有す
る溶液中で、酵母を懸濁状態で非増殖的に攪拌及び/又
は振とうすることにより製造することができる。
The magnesium / zinc-rich yeast is produced by using the magnesium / zinc-rich yeast production conditions, that is, the magnesium-rich yeast obtained under the above-described magnesium-rich zinc production conditions as a raw material yeast, in a high zinc concentration. It can be produced by stirring and / or shaking yeast in a suspension containing it in a suspension state non-proliferatively.

【0041】このようにして、マグネシウム・亜鉛・鉄
高含有酵母を創製することができる。その結果、乾燥菌
体当たりマグネシウムを2,000ppm、亜鉛を1
0,000ppm、鉄を15,000ppmあるいはそ
れ以上含有する新規マルチミネラル食用酵母を得ること
ができる。
In this way, a yeast containing a high content of magnesium, zinc and iron can be created. As a result, magnesium per dry cell is 2,000 ppm and zinc is 1
It is possible to obtain a novel multi-mineral edible yeast containing 10,000 ppm and iron of 15,000 ppm or more.

【0042】以下に、本発明の実施例を記述する。Examples of the present invention will be described below.

【0043】[0043]

【実施例1】硫酸第一鉄(FeSO4)を用い、二価の
鉄イオンが溶液中に100〜10,000ppmとなる
ように、溶液を調製し(下記表1)、各濃度の鉄溶液1
00mlにパン酵母(オリエンタル酵母工業(株)製レ
ギュラーイースト)20g(2×109個/ml)を懸
濁し、500ml容坂口フラスコにて、30℃で24時
間振とう(振幅12cm、110rpm)した。
Example 1 Using ferrous sulfate (FeSO 4 ), a solution was prepared so that divalent iron ions would be 100 to 10,000 ppm in the solution (Table 1 below), and an iron solution of each concentration was prepared. 1
20 g (2 × 10 9 cells / ml) of baker's yeast (Regular yeast manufactured by Oriental Yeast Co., Ltd.) was suspended in 00 ml, and shaken in a 500 ml Sakaguchi flask at 30 ° C. for 24 hours (amplitude 12 cm, 110 rpm). .

【0044】振とう後の菌体を遠心分離(3,000×
g、5分)により集菌し、イオン交換水(Milli
Q)で2回洗浄した後、菌体を湿式灰化し、原子吸光分
光光度計により鉄を定量した。また、菌体集菌後の上澄
液及び洗浄液を合わせた液中の残存鉄量は、オルトフェ
ナントリン法により比色定量した。得られた結果を下記
表1に示す。
Centrifugation of the cells after shaking (3,000 x
g, 5 minutes) to collect the bacteria, and deionized water (Milli)
After washing twice with Q), the cells were wet-ashed and iron was quantified by an atomic absorption spectrophotometer. In addition, the amount of residual iron in the combined solution of the supernatant after washing the cells and the washing solution was colorimetrically determined by the orthophenanthrin method. The obtained results are shown in Table 1 below.

【0045】[0045]

【表1】 [Table 1]

【0046】[0046]

【実施例2】硫酸第一鉄(FeSO4)を用い、二価の
鉄イオンが溶液中に5,000ppmとなるように、溶
液を調製し、この鉄溶液1.5Lにパン酵母(オリエン
タル酵母工業(株)製レギュラーイースト)300g
(2×109個/ml)を懸濁し、3L容ジャーファー
メンターにて、30℃で24時間、酵母が沈降しない程
度の200rpmでゆるやかに攪拌した。
Example 2 A solution was prepared using ferrous sulfate (FeSO 4 ) so that the divalent iron ion was 5,000 ppm in the solution, and 1.5 L of this iron solution was added to baker's yeast (Oriental yeast). Industrial Co., Ltd. regular yeast) 300g
(2 × 10 9 cells / ml) was suspended and gently stirred in a 3 L jar fermenter at 30 ° C. for 24 hours at 200 rpm at which yeast did not precipitate.

【0047】所定時間攪拌した後、菌体を遠心分離
(3,000×g、5分)により集菌し、イオン交換水
(MilliQ)で2回洗浄した後、菌体を湿式灰化
し、原子吸光分光光度計により鉄を定量した。また、菌
体集菌後の上澄液及び洗浄液を合わせた液中の残存鉄量
は、オルトフェナントリン法により比色定量した。得ら
れた結果を図1に示す。
After stirring for a predetermined time, the bacterial cells were collected by centrifugation (3,000 xg, 5 minutes), washed twice with ion-exchanged water (MilliQ), wet-ashed and then atomized. Iron was quantified by an absorption spectrophotometer. In addition, the amount of residual iron in the combined solution of the supernatant after washing the cells and the washing solution was colorimetrically determined by the orthophenanthrin method. The obtained results are shown in FIG.

【0048】[0048]

【実施例3】硫酸亜鉛(ZnSO4・7H2O)を用い、
亜鉛イオンが溶液中に5,000ppmとなるように、
溶液を調製し、この亜鉛溶液1.5Lにパン酵母(オリ
エンタル酵母工業(株)製レギュラーイースト)300
g(2×109個/ml)を懸濁し、3L容ジャーファ
ーメンターにて、通気2.0vvm、650rpmで攪
拌し、30℃で72時間、非増殖条件下で処理を行っ
た。
Example 3 Using zinc sulfate (ZnSO 4 .7H 2 O),
So that the zinc ion is 5,000 ppm in the solution,
A solution was prepared, and baker's yeast (Regular yeast manufactured by Oriental Yeast Co., Ltd.) 300
g (2 × 10 9 cells / ml) was suspended, and the mixture was stirred in a 3 L jar fermenter with aeration of 2.0 vvm and 650 rpm, and treated at 30 ° C. for 72 hours under non-growth conditions.

【0049】所定時間通気・攪拌した後、菌体を遠心分
離(3,000×g、5分)により集菌し、イオン交換
水(MilliQ)で2回洗浄した後、菌体を湿式灰化
し、原子吸光分光光度計により、亜鉛を定量した結果、
乾燥菌体当たり14,500ppmの亜鉛が含有されて
いた。
After aeration and stirring for a predetermined time, the cells were collected by centrifugation (3,000 xg, 5 minutes) and washed twice with ion-exchanged water (MilliQ), and then the cells were wet ashed. As a result of quantifying zinc with an atomic absorption spectrophotometer,
It contained 14,500 ppm of zinc per dry cell.

【0050】このようにして得られた亜鉛高含有酵母を
原料酵母として、硫酸第一鉄(FeSO4)を用い、二
価の鉄イオンが溶液中に5,000ppmとなるよう
に、溶液を調製し、この溶液1.5Lにあらかじめ調製
した亜鉛を高濃度に含有した原料酵母300g(2×1
9個/ml)を懸濁し、3L容ジャーファーメンター
にて、30℃で24時間、酵母が沈降しない程度の20
0rpmでゆるやかに攪拌した。
Using the zinc-rich yeast thus obtained as a starting yeast, ferrous sulfate (FeSO 4 ) was used to prepare a solution so that the divalent iron ion would be 5,000 ppm in the solution. 300 L of raw material yeast (2 x 1) containing a high concentration of zinc prepared in advance in 1.5 L of this solution.
( 9 cells / ml) and suspended in a 3 L jar fermenter at 30 ° C. for 24 hours for 20 hours at which yeast does not precipitate.
The mixture was gently stirred at 0 rpm.

【0051】所定時間攪拌した後、菌体を遠心分離
(3,000×g、5分)により集菌し、イオン交換水
(MilliQ)で2回洗浄した後、菌体を湿式灰化
し、原子吸光分光光度計により鉄及び亜鉛を定量した。
得られた結果を表2に示す。
After stirring for a predetermined time, the bacterial cells were collected by centrifugation (3,000 × g, 5 minutes), washed twice with ion-exchanged water (MilliQ), wet-ashed and then atomized. Iron and zinc were quantified by an absorption spectrophotometer.
The obtained results are shown in Table 2.

【0052】[0052]

【表2】 [Table 2]

【0053】[0053]

【実施例4】硫酸マグネシウム(MgSO4・7H2O)
を用い、マグネシウムイオンが溶液中に15,000p
pmとなるように、溶液を調製し、このマグネシウム溶
液1.5Lにパン酵母(オリエンタル酵母工業(株)製
レギュラーイースト)300g(2×109個/ml)
を懸濁し、3L容ジャーファーメンターにて、通気2.
0vvm、650rpmで攪拌し、30℃で72時間の
条件で処理を行った。
Example 4 Magnesium sulfate (MgSO 4 · 7H 2 O)
With magnesium ion in solution at 15,000p
A solution was prepared so as to have pm, and 300 g (2 × 10 9 cells / ml) of baker's yeast (Regular yeast manufactured by Oriental Yeast Co., Ltd.) was added to 1.5 L of this magnesium solution.
And aeration with a 3 L jar fermenter 2.
The mixture was stirred at 0 vvm and 650 rpm and treated at 30 ° C. for 72 hours.

【0054】所定時間通気・攪拌した後、菌体を遠心分
離(3,000×g、5分)により集菌し、イオン交換
水(MilliQ)で2回洗浄した後、菌体を湿式灰化
し、原子吸光分光光度計により、マグネシウムを定量し
た結果、乾燥菌体当たり7,830ppmのマグネシウ
ムが含有されていた。
After aeration and stirring for a predetermined time, the bacterial cells were collected by centrifugation (3,000 xg, 5 minutes), washed twice with ion-exchanged water (MilliQ), and then wet-ashed. As a result of quantifying magnesium with an atomic absorption spectrophotometer, it was found that 7,830 ppm of magnesium was contained per dry cell.

【0055】このようにして得られたマグネシウム高含
有酵母を原料酵母として、硫酸第一鉄(FeSO4)を
用い、二価の鉄イオンが溶液中に5,000ppmとな
るように、溶液を調製し、この鉄溶液1.5Lにあらか
じめ調製したマグネシウムを高濃度に含有した原料酵母
300g(2×109個/ml)を懸濁し、3L容ジャ
ーファーメンターにて、30℃で24時間、酵母が沈降
しない程度の200rpmでゆるやかに攪拌した。
Using the magnesium-rich yeast thus obtained as a raw material yeast, ferrous sulfate (FeSO 4 ) was used to prepare a solution so that divalent iron ions would be 5,000 ppm in the solution. Then, 300 g (2 × 10 9 pieces / ml) of the raw material yeast containing a high concentration of magnesium prepared in advance was suspended in 1.5 L of this iron solution, and the yeast was suspended in a 3 L jar fermenter at 30 ° C. for 24 hours. The mixture was gently stirred at 200 rpm at which it did not settle.

【0056】所定時間攪拌した後、菌体を遠心分離
(3,000×g、5分)により集菌し、イオン交換水
(MilliQ)で2回洗浄した後、菌体を湿式灰化
し、原子吸光分光光度計により鉄及びマグネシウムを定
量した。得られた結果を表3に示す。
After stirring for a predetermined time, the cells were collected by centrifugation (3,000 xg, 5 minutes), washed twice with ion-exchanged water (MilliQ), wet-ashed, and then atomized. Iron and magnesium were quantified by an absorption spectrophotometer. Table 3 shows the obtained results.

【0057】[0057]

【表3】 [Table 3]

【0058】[0058]

【実施例5】硫酸亜鉛(ZnSO4・7H2O)を用い、
亜鉛イオンが溶液中に5,000ppmとなるように、
溶液を調製し、この亜鉛溶液1.5Lに、実施例4に記
載した条件にしたがって製造したマグネシウム高含有酵
母300g(2×109個/ml)を懸濁し、3L容ジ
ャーファーメンターにて、通気2.0vvm、650r
pmで攪拌し、30℃で72時間、非増殖条件下で処理
を行った。
Example 5 Using zinc sulfate (ZnSO 4 .7H 2 O),
So that the zinc ion is 5,000 ppm in the solution,
A solution was prepared, and 300 g (2 × 10 9 cells / ml) of the magnesium-rich yeast produced according to the conditions described in Example 4 was suspended in 1.5 L of this zinc solution, and the suspension was placed in a 3 L jar fermenter. Aeration 2.0 vvm, 650r
The mixture was stirred at pm and treated at 30 ° C. for 72 hours under non-growth conditions.

【0059】所定時間通気・攪拌した後、菌体を遠心分
離(3,000×g、5分)により集菌し、イオン交換
水(MilliQ)で2回洗浄した後、菌体を湿式灰化
し、原子吸光分光光度計によりマグネシウム及び亜鉛を
定量したところ、乾燥菌体当たりマグネシウム6,57
0ppm、亜鉛11,300ppmを同時に含有する酵
母菌体が得られた。
After aeration and stirring for a predetermined time, the cells were collected by centrifugation (3,000 xg, 5 minutes), washed twice with ion-exchanged water (MilliQ), and then wet-ashed. Quantitative analysis of magnesium and zinc with an atomic absorption spectrophotometer showed that magnesium per dry cell was 6,57
Yeast cells simultaneously containing 0 ppm and 11,300 ppm of zinc were obtained.

【0060】このようにして得られたマグネシウム・亜
鉛高含有酵母を原料酵母として、硫酸第一鉄(FeSO
4)を用い、二価の鉄イオンが溶液中に5,000pp
mとなるように、溶液を調製し、この鉄溶液1.5Lに
あらかじめ調製したマグネシウム及び亜鉛を高濃度に含
有した原料酵母300g(2×109個/ml)を懸濁
し、3L容ジャーファーメンターにて、30℃で24時
間、酵母が沈降しない程度の200rpmでゆるやかに
攪拌した。
The magnesium / zinc-rich yeast thus obtained was used as a starting yeast, and ferrous sulfate (FeSO 4
4 ), divalent iron ions in the solution are 5,000pp
A solution was prepared so that the amount of m becomes m, and 300 g (2 × 10 9 pieces / ml) of the raw material yeast containing a high concentration of magnesium and zinc prepared in advance was suspended in 1.5 L of this iron solution, and 3 L jar fur was prepared. With a mentor, the mixture was gently stirred at 30 ° C. for 24 hours at 200 rpm at which yeast did not settle.

【0061】所定時間攪拌した後、菌体を遠心分離
(3,000×g、5分)により集菌し、イオン交換水
(MilliQ)で2回洗浄した後、菌体を湿式灰化
し、原子吸光分光光度計によりマグネシウム、亜鉛及び
鉄を定量した。得られた結果を表4に示す。
After stirring for a predetermined time, the bacterial cells were collected by centrifugation (3,000 × g, 5 minutes), washed twice with ion-exchanged water (MilliQ), wet-ashed and then atomized. Magnesium, zinc and iron were quantified by an absorption spectrophotometer. The results obtained are shown in Table 4.

【0062】[0062]

【表4】 [Table 4]

【0063】[0063]

【実施例6】実施例2に記載した条件と同一の条件で、
24時間処理した酵母を集菌し、洗浄した後、鉄高含有
酵母を得た。この鉄高含有酵母を用いて、下記の表5の
食パン配合にて製パン試験を行った。対照区として、鉄
高含有酵母の原料酵母としたパン酵母(オリエンタル酵
母工業(株)製レギュラーイースト)を用いた。また、
できた食パンを湿式灰化し、原子吸光分光光度計により
鉄を定量した。得られた結果を表6に示す。
Example 6 Under the same conditions as described in Example 2,
After the yeast treated for 24 hours was collected and washed, a high iron content yeast was obtained. Using this iron-rich yeast, a bread-making test was conducted with the bread composition shown in Table 5 below. As a control, baker's yeast (regular yeast manufactured by Oriental Yeast Co., Ltd.), which was used as a raw material yeast for the iron-rich yeast, was used. Also,
The resulting bread was wet ashed and iron was quantified by an atomic absorption spectrophotometer. The obtained results are shown in Table 6.

【0064】[0064]

【表5】 [Table 5]

【0065】[0065]

【表6】 [Table 6]

【0066】[0066]

【発明の効果】本発明によって、乾燥菌体当たり15,
000ppm以上という大量の鉄を酵母に含有せしめる
ことがはじめて可能となった。このように大量の鉄を含
有した酵母は、従来得ることができず、全く新規な酵母
である。
According to the present invention, 15
It became possible for the first time to make yeast contain a large amount of iron of 000 ppm or more. Such a yeast containing a large amount of iron cannot be obtained in the past and is a completely novel yeast.

【0067】本発明によって創製された鉄高含有酵母
は、各種の用途に広く利用することができ、鉄分を大量
に含有したパン、ビスケット、味噌等各種の食品を得る
ことができる。また、酵母の細胞壁を破壊し、内容物を
取り出し、これを用いてジュース、アイスクリーム、ク
ラッカー等各種の飲食品の製造にも利用することができ
るし、鉄分を多量に含む飼料や餌料も製造することがで
きる。
The iron-rich yeast created by the present invention can be widely used for various purposes, and various foods such as bread, biscuits, and miso containing a large amount of iron can be obtained. In addition, the cell wall of yeast can be destroyed, the contents can be taken out, and it can be used for the production of various foods and drinks such as juice, ice cream, crackers, and also for the production of feed and feed containing a large amount of iron. can do.

【0068】また本発明においては、酵母を培養すると
いう従来のシステムを採用せず、鉄塩の高濃度水溶液中
で酵母を攪拌するという全く新しいシステムを採用して
いる。そのため、培地を必要としないことにより、コス
トの低減化が図られるのみでなく、単に鉄塩の水溶液で
あるために酵母菌体の集菌後の洗浄も極めて簡単です
み、菌体の分離、精製も極めて容易に実施することがで
きる。
Further, in the present invention, the conventional system of culturing yeast is not adopted, but a completely new system of stirring yeast in a high concentration aqueous solution of iron salt is adopted. Therefore, not only does the need for a medium not only reduce costs, but because it is an aqueous solution of iron salts, washing the yeast cells after harvesting is extremely easy, and separation of the cells can be achieved. Purification can also be carried out very easily.

【0069】また更に本発明によれば、鉄のほかに各種
のミネラルも大量に酵母に含有せしめることが可能とな
ったので、鉄分のほかに更に例えば亜鉛及び/又はマグ
ネシウムといったミネラルを高濃度に含有した新規酵母
(マルチミネラル高含有酵母)も創製可能となり、各種
の用途に使用することができる。
Furthermore, according to the present invention, various minerals in addition to iron can be contained in yeast in a large amount. Therefore, in addition to iron, minerals such as zinc and / or magnesium can be highly concentrated. It is also possible to create new yeast containing yeast (yeast with high content of multi-minerals), which can be used for various purposes.

【図面の簡単な説明】[Brief description of drawings]

【図1】乾燥酵母菌体内鉄濃度と処理時間との関係を示
す。
FIG. 1 shows the relationship between iron concentration in dried yeast cells and treatment time.

─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───

【手続補正書】[Procedure amendment]

【提出日】平成7年11月1日[Submission date] November 1, 1995

【手続補正1】[Procedure Amendment 1]

【補正対象書類名】明細書[Document name to be amended] Statement

【補正対象項目名】図面の簡単な説明[Name of item to be corrected] Brief description of the drawing

【補正方法】変更[Correction method] Change

【補正内容】[Correction content]

【図面の簡単な説明】[Brief description of drawings]

【図1】乾燥酵母菌体内鉄濃度と処理時間との関係を示
す。
FIG. 1 shows the relationship between iron concentration in dried yeast cells and treatment time.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 鉄を高濃度に含有してなる食用酵母。1. An edible yeast containing a high concentration of iron. 【請求項2】 鉄を乾燥菌体当たり15,000ppm
以上含有してなる食用酵母。
2. Iron is 15,000 ppm per dry cell.
An edible yeast containing the above.
【請求項3】 鉄を2,000ppm以上含有する溶液
中で、酵母を懸濁状態でゆっくりと攪拌及び/又は振と
うすること、を特徴とする鉄を乾燥菌体当たり15,0
00ppm以上含有する食用酵母の製造法。
3. Iron in a solution containing 2,000 ppm or more of iron, wherein the yeast is slowly stirred and / or shaken in a suspended state, and the amount of iron per dry cell is 15.0.
A method for producing edible yeast containing at least 00 ppm.
【請求項4】 酵母としてミネラルを高濃度に含有して
なる酵母を使用すること、を特徴とする請求項3に記載
の方法。
4. The method according to claim 3, wherein yeast containing a high concentration of minerals is used as yeast.
【請求項5】 ミネラルが、亜鉛及び/又はマグネシウ
ムであること、を特徴とする請求項4に記載の方法。
5. The method according to claim 4, characterized in that the mineral is zinc and / or magnesium.
JP16451195A 1995-06-08 1995-06-08 Iron-rich yeast Expired - Lifetime JP3272571B2 (en)

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Application Number Priority Date Filing Date Title
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Publication Number Publication Date
JPH08332083A true JPH08332083A (en) 1996-12-17
JP3272571B2 JP3272571B2 (en) 2002-04-08

Family

ID=15794557

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Application Number Title Priority Date Filing Date
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Country Link
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* Cited by examiner, † Cited by third party
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JP2006238878A (en) * 2005-02-07 2006-09-14 Japan Tobacco Inc Production method of iron yeast
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JP2014200183A (en) * 2013-04-03 2014-10-27 オリエンタル酵母工業株式会社 Red rice additive and production method thereof, red rice and production method thereof, and kit for production of red rice additive
KR20150056593A (en) 2012-09-13 2015-05-26 오리엔탈 이스트 컴파니 리미티드 High-Iron-Content Yeast Extract, Method for Producing Same, And Food Product
CN105010761A (en) * 2015-08-21 2015-11-04 河南艾格多科技有限公司 Method for producing yeast fermented zinc-selenium compound feed additive
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Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006238878A (en) * 2005-02-07 2006-09-14 Japan Tobacco Inc Production method of iron yeast
WO2009084122A1 (en) * 2007-12-28 2009-07-09 Japan Tobacco Inc. Iron-enriched composition
JPWO2009084122A1 (en) * 2007-12-28 2011-05-12 日本たばこ産業株式会社 Iron-reinforced composition
KR20150056593A (en) 2012-09-13 2015-05-26 오리엔탈 이스트 컴파니 리미티드 High-Iron-Content Yeast Extract, Method for Producing Same, And Food Product
JPWO2014042046A1 (en) * 2012-09-13 2016-08-18 オリエンタル酵母工業株式会社 High iron content yeast extract, method for producing the same, and food
TWI629939B (en) * 2012-09-13 2018-07-21 東方酵母工業股份有限公司 High-iron-content yeast extract, method for producing the same, and foods
JP2014200183A (en) * 2013-04-03 2014-10-27 オリエンタル酵母工業株式会社 Red rice additive and production method thereof, red rice and production method thereof, and kit for production of red rice additive
CN105010761A (en) * 2015-08-21 2015-11-04 河南艾格多科技有限公司 Method for producing yeast fermented zinc-selenium compound feed additive
CN105010735A (en) * 2015-08-21 2015-11-04 河南艾格多科技有限公司 Method for producing yeast fermentation state manganese feed additive by using beer waste liquids
CN105053567A (en) * 2015-08-21 2015-11-18 河南艾格多科技有限公司 Method for producing yeast-fermented copper feed additive by beer wastewater

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