JP2020202813A - Culture medium for yeast culture - Google Patents
Culture medium for yeast culture Download PDFInfo
- Publication number
- JP2020202813A JP2020202813A JP2019113658A JP2019113658A JP2020202813A JP 2020202813 A JP2020202813 A JP 2020202813A JP 2019113658 A JP2019113658 A JP 2019113658A JP 2019113658 A JP2019113658 A JP 2019113658A JP 2020202813 A JP2020202813 A JP 2020202813A
- Authority
- JP
- Japan
- Prior art keywords
- yeast
- culture medium
- mass
- magnesium
- yeast culture
- 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.)
- Pending
Links
- 240000004808 Saccharomyces cerevisiae Species 0.000 title claims abstract description 159
- 239000001963 growth medium Substances 0.000 title claims abstract description 52
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- 239000011777 magnesium Substances 0.000 claims abstract description 29
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 29
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 27
- 239000004471 Glycine Substances 0.000 claims abstract description 26
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims abstract description 26
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- 239000004220 glutamic acid Substances 0.000 claims abstract description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 24
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 claims abstract description 22
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 19
- 239000002609 medium Substances 0.000 claims description 41
- 238000000034 method Methods 0.000 claims description 25
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- JRKICGRDRMAZLK-UHFFFAOYSA-L persulfate group Chemical group S(=O)(=O)([O-])OOS(=O)(=O)[O-] JRKICGRDRMAZLK-UHFFFAOYSA-L 0.000 description 1
- RAFRTSDUWORDLA-UHFFFAOYSA-N phenyl 3-chloropropanoate Chemical compound ClCCC(=O)OC1=CC=CC=C1 RAFRTSDUWORDLA-UHFFFAOYSA-N 0.000 description 1
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- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
- 239000003531 protein hydrolysate Substances 0.000 description 1
- 239000008262 pumice Substances 0.000 description 1
- MUPFEKGTMRGPLJ-ZQSKZDJDSA-N raffinose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO[C@@H]2[C@@H]([C@@H](O)[C@@H](O)[C@@H](CO)O2)O)O1 MUPFEKGTMRGPLJ-ZQSKZDJDSA-N 0.000 description 1
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- NGFMICBWJRZIBI-UJPOAAIJSA-N salicin Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1OC1=CC=CC=C1CO NGFMICBWJRZIBI-UJPOAAIJSA-N 0.000 description 1
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- HFHDHCJBZVLPGP-UHFFFAOYSA-N schardinger α-dextrin Chemical compound O1C(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(O)C2O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC2C(O)C(O)C1OC2CO HFHDHCJBZVLPGP-UHFFFAOYSA-N 0.000 description 1
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- 235000019345 sodium thiosulphate Nutrition 0.000 description 1
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- QUEDXNHFTDJVIY-UHFFFAOYSA-N γ-tocopherol Chemical class OC1=C(C)C(C)=C2OC(CCCC(C)CCCC(C)CCCC(C)C)(C)CCC2=C1 QUEDXNHFTDJVIY-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Abstract
Description
本発明は、酵母培養用培地に関する。 The present invention relates to a medium for yeast culture.
酵母は、発酵食品、アルコール、有機酸などの製造に利用されている。さらに、油脂分解能を有する酵母は、グリーストラップなどにおいて、排水中の油脂を分解するために利用されている。 Yeast is used in the production of fermented foods, alcohols, organic acids and the like. Further, yeast having a fat and oil resolution is used for decomposing fats and oils in wastewater in a grease trap or the like.
食品工場の排水には多量の油脂が含まれており、これらの油脂を処理するために除害施設が設けられている。除害施設から排出される処理水には、下水道法または水質汚濁防止法により排水基準が設定されている。 Wastewater from food factories contains a large amount of fats and oils, and abatement facilities are set up to treat these fats and oils. Wastewater standards are set for treated water discharged from abatement facilities by the Sewerage Law or the Water Pollution Control Law.
排水中の油脂濃度が高い場合、処理水が排水基準に適合しないこと、加圧浮上などの処理に使用する薬剤、発生するオイルボール、スカムなどの廃棄にコストがかかること、油脂の付着による配管の閉塞、悪臭の発生といった様々な問題が発生する。 If the concentration of oil and fat in the wastewater is high, the treated water does not meet the wastewater standards, the chemicals used for treatment such as pressure flotation, the cost of disposing of the generated oil balls and scum, etc. Various problems such as blockage of water and generation of foul odor occur.
そこで、除害施設において、効率よく油脂を低減するため、高い油脂分解能を有する微生物を利用する方法が検討されている。例えば、特許文献1には、グリーストラップ内における油脂の低減効果に優れた酵母が開示されている。 Therefore, in order to efficiently reduce fats and oils in abatement facilities, a method of utilizing microorganisms having high fats and oils resolution is being studied. For example, Patent Document 1 discloses yeast having an excellent effect of reducing fats and oils in a grease trap.
酵母の培養では、栄養が豊富な培地であるYM培地やLB培地などが通常使用されている。本発明者の検討によれば、酵母をYM培地やLB培地などで培養すると、培地の単位容量当たりの集菌量が十分ではないという問題があることが判明した。そのため、より培養効率を向上させる、すなわち培地の単位容量当たりの生菌数を増加させる技術が望まれている。 In yeast culture, a nutrient-rich medium such as YM medium or LB medium is usually used. According to the study of the present inventor, it has been found that when yeast is cultured in YM medium, LB medium or the like, there is a problem that the amount of collected bacteria per unit volume of the medium is not sufficient. Therefore, a technique for further improving the culture efficiency, that is, increasing the number of viable cells per unit volume of the medium is desired.
したがって、本発明は、上記事情を鑑みてなされたものであり、単位容量当たりの生菌数を増加させることが可能な培地を提供することを目的とする。 Therefore, the present invention has been made in view of the above circumstances, and an object of the present invention is to provide a medium capable of increasing the number of viable cells per unit volume.
本発明者は、上記課題を解決すべく、鋭意研究を行った。その結果、炭素源、窒素源およびマグネシウム源を含む酵母培養用培地であって、前記窒素源がグルタミン酸とグリシンとを含む、酵母培養用培地によって上記課題が解決されることを見出し、本発明の完成に至った。 The present inventor has conducted diligent research in order to solve the above problems. As a result, they have found that a yeast culture medium containing a carbon source, a nitrogen source and a magnesium source, wherein the nitrogen source contains glutamic acid and glycine, solves the above-mentioned problems. It was completed.
本発明によれば、単位容量当たりの生菌数を増加させることが可能な培地が提供される。 According to the present invention, there is provided a medium capable of increasing the viable cell count per unit volume.
以下、本発明の一形態に係る実施の形態を説明する。本発明は、以下の実施の形態のみには限定されない。 Hereinafter, embodiments according to one embodiment of the present invention will be described. The present invention is not limited to the following embodiments.
本明細書において、範囲を示す「X〜Y」は「X以上Y以下」を意味する。また、特記しない限り、操作および物性等の測定は室温(20〜25℃)/相対湿度40〜50%RHの条件で測定する。 In the present specification, "X to Y" indicating a range means "X or more and Y or less". Unless otherwise specified, the operation and physical properties are measured under the conditions of room temperature (20 to 25 ° C.) / relative humidity of 40 to 50% RH.
<酵母培養用培地>
本発明の一形態によれば、炭素源、窒素源およびマグネシウム源を含む酵母培養用培地であって、前記窒素源がグルタミン酸とグリシンとを含む、酵母培養用培地が提供される。かかる構成により、酵母の培養効率を向上させて、培地の単位容量当たりの生菌数を増加させる(すなわち、培地の単位容量当たりの最大生菌数を増加させる)ことができる。
<Medium for yeast culture>
According to one embodiment of the present invention, there is provided a yeast culture medium containing a carbon source, a nitrogen source and a magnesium source, wherein the nitrogen source contains glutamic acid and glycine. With such a configuration, the yeast culture efficiency can be improved and the viable cell count per unit volume of the medium can be increased (that is, the maximum viable cell count per unit volume of the medium can be increased).
(炭素源)
本発明に係る酵母培養用培地は、炭素源を含む。
(Carbon source)
The yeast culture medium according to the present invention contains a carbon source.
炭素源としては、特に制限されず、例えばグルコース、フルクトース、セロビオース、ラフィノース、キシロース、マルトース、ガラクトース、ソルボース、グルコサミン、リボース、アラビノース、ラムノース、スクロース、トレハロース、α−メチル−D−グルコシド、サリシン、メリビオース、ラクトース、メレジトース、イヌリン、エリスリトール、グルシトール、マンニトール、ガラクチトール、N−アセチル−D−グルコサミン、デンプン、デンプン加水分解物、糖蜜、廃糖蜜等の糖類、麦、米等の天然物、グリセロール、メタノール、エタノール等のアルコール類、ヘキサデカン等の炭化水素などが挙げられる。これらの炭素源は、培養する酵母による資化性を考慮して適宜選択される。また、上記炭素源を1種または2種以上選択して使用することができる。 The carbon source is not particularly limited, and is, for example, glucose, fructose, cellobiose, raffinose, xylose, maltose, galactose, sorbose, glucosamine, ribose, arabinose, ramnorth, sucrose, trehalose, α-methyl-D-glucoside, salicin, melibiose. , Lactose, meregitose, inulin, erythritol, glucitol, mannitol, galactitol, N-acetyl-D-glucosamine, starch, starch hydrolysate, sugar such as sugar, waste sugar, natural products such as wheat and rice, glycerol, methanol , Alcohols such as ethanol, hydrocarbons such as hexadecane and the like. These carbon sources are appropriately selected in consideration of the assimilation property of the yeast to be cultured. Moreover, one kind or two or more kinds of the said carbon sources can be selected and used.
酵母としてアステロトレメラ属を用いる場合、炭素源は、培養効率をより向上できるとの観点から、グルコースを含む。 When the genus Asteltremera is used as the yeast, the carbon source contains glucose from the viewpoint that the culture efficiency can be further improved.
(窒素源)
本発明に係る酵母培養用培地は、窒素源を含む。前記窒素源は、必須の成分として、グルタミン酸とグリシンとを含む。
(Nitrogen source)
The yeast culture medium according to the present invention contains a nitrogen source. The nitrogen source contains glutamic acid and glycine as essential components.
本発明に係る酵母培養用培地は、グルタミン酸とグリシンとを含むことにより、グルタミン酸とグリシンとが優先的に酵母内に取り込まれ、またグルタミン酸およびグリシンは分岐アミノ酸のように窒素源カタボライト抑制を受けないため、酵母の培養効率をより向上できると考えられる。 Since the yeast culture medium according to the present invention contains glutamic acid and glycine, glutamic acid and glycine are preferentially incorporated into yeast, and glutamic acid and glycine are not suppressed by the nitrogen source catabolite unlike branched amino acids. Therefore, it is considered that the yeast culture efficiency can be further improved.
グルタミン酸およびグリシンの配合量の合計は、酵母の培養効率をより向上できるとの観点から、炭素源1質量部に対して、好ましくは0.01〜5.0質量部であり、より好ましくは0.1〜2.5質量部である。 The total amount of glutamic acid and glycine blended is preferably 0.01 to 5.0 parts by mass, and more preferably 0, with respect to 1 part by mass of the carbon source, from the viewpoint that the yeast culture efficiency can be further improved. .1 to 2.5 parts by mass.
また、グルタミン酸の配合量は、酵母の培養効率をより向上できるとの観点から、グリシンの配合量を1質量部としたときに、好ましくは0.01〜5.0質量部であり、より好ましくは0.1〜2.5量部である。 Further, the blending amount of glutamic acid is preferably 0.01 to 5.0 parts by mass, more preferably when the blending amount of glycine is 1 part by mass, from the viewpoint that the culture efficiency of yeast can be further improved. Is 0.1 to 2.5 parts by mass.
本発明に係る酵母培養用培地は、窒素源として、グルタミン酸およびグリシン以外の物質をさらに含むことができる。 The yeast culture medium according to the present invention can further contain substances other than glutamic acid and glycine as a nitrogen source.
グルタミン酸およびグリシン以外の窒素源としては、無機窒素源でもよく、有機窒素源でもよい。 The nitrogen source other than glutamic acid and glycine may be an inorganic nitrogen source or an organic nitrogen source.
無機窒素源としては、硝酸ナトリウム、硝酸カルシウムなどの硝酸塩;硝酸アンモニウム、硫酸アンモニウム、塩化アンモニウムなどのアンモニウム塩;亜硝酸ナトリウムなどの亜硝酸塩;アンモニア;尿素などが例示できる。 Examples of the inorganic nitrogen source include nitrates such as sodium nitrate and calcium nitrate; ammonium salts such as ammonium nitrate, ammonium sulfate and ammonium chloride; nitrites such as sodium nitrite; ammonia; urea and the like.
有機窒素源としては、酵母エキス、麦エキス、肉エキス、魚肉エキス、ペプトン、ポリペプトン、麦芽エキス、大豆加水分解物、大豆粉末、カゼイン、ミルクカゼイン、カザミノ酸、アスパラギン酸等の各種アミノ酸、コーンスティープリカー、その他の動物、植物、微生物の加水分解物などが挙げられる。これらの有機窒素源は、培養する酵母による資化性を考慮して適宜選択される。 Organic nitrogen sources include yeast extract, wheat extract, meat extract, fish meat extract, peptone, polypeptone, malt extract, soybean hydrolyzate, soybean powder, casein, milk casein, casamino acid, aspartic acid and other amino acids, and corn steep. Examples include liquor and other animal, plant and microbial hydrolysates. These organic nitrogen sources are appropriately selected in consideration of the assimilation property of the yeast to be cultured.
上記グルタミン酸およびグリシン以外の窒素源を1種または2種以上選択して使用することができる。 One or more nitrogen sources other than the above-mentioned glutamic acid and glycine can be selected and used.
酵母としてアステロトレメラ属を用いる場合、グルタミン酸およびグリシン以外の窒素源は、培養効率をより向上できるとの観点から、好ましくは有機窒素源であり、より好ましくは酵母エキスおよび麦芽エキスの少なくとも一方を含み、さらに好ましくは酵母エキスおよび麦芽エキスを含む。 When the genus Asterotremera is used as the yeast, nitrogen sources other than glutamic acid and glycine are preferably organic nitrogen sources, and more preferably at least one of yeast extract and malt extract, from the viewpoint of improving culture efficiency. Included, more preferably yeast extract and malt extract.
グルタミン酸およびグリシン以外の窒素源を使用する場合、当該窒素源の配合量(2種以上用いる場合はその合計量)は、炭素源1質量部に対して、例えば0.1〜3.0質量部であり、好ましくは0.3〜1.0質量部である。 When a nitrogen source other than glutamic acid and glycine is used, the blending amount of the nitrogen source (the total amount when two or more kinds are used) is, for example, 0.1 to 3.0 parts by mass with respect to 1 part by mass of the carbon source. It is preferably 0.3 to 1.0 parts by mass.
(マグネシウム源)
本発明に係る酵母培養用培地は、マグネシウム源を含む。
(Magnesium source)
The yeast culture medium according to the present invention contains a magnesium source.
本発明に係る酵母培養用培地は、マグネシウム源を含むことにより、アミノ酸の取り込み、すなわちグルタミン酸およびグリシンの取り込みを促進するため、酵母の培養効率をより向上できると考えられる。また、窒素源として、酵母エキス、麦芽エキスなどを用いる場合、これらの窒素源に含まれるアミノ酸の取り込みを促進することで、酵母の培養効率をより向上できると考えられる。 It is considered that the yeast culture medium according to the present invention can further improve the yeast culture efficiency because it promotes the uptake of amino acids, that is, the uptake of glutamic acid and glycine by containing a magnesium source. Further, when yeast extract, malt extract or the like is used as the nitrogen source, it is considered that the yeast culture efficiency can be further improved by promoting the uptake of amino acids contained in these nitrogen sources.
マグネシウム源としては、特に制限されないが、好ましくはマグネシウム塩である。マグネシウム塩は、例えば硫酸マグネシウム、硝酸マグネシウム、塩化マグネシウム、亜硫酸マグネシウム、チオ硫酸マグネシウム、炭酸マグネシウム、第一リン酸マグネシウム、第二リン酸マグネシウム、第三リン酸マグネシウム、ピロリン酸マグネシウム、亜硝酸マグネシウム、酢酸マグネシウム、クエン酸マグネシウム、シュウ酸マグネシウムおよびこれらの水和物などが挙げられる。マグネシウム塩は、好ましくは硫酸マグネシウムやその水和物(例えば硫酸マグネシウム七水和物)であり、より好ましくは硫酸マグネシウムである。上記マグネシウム源を1種または2種以上選択して使用することができる。 The magnesium source is not particularly limited, but is preferably a magnesium salt. Magnesium salts include, for example, magnesium sulfate, magnesium nitrate, magnesium chloride, magnesium sulfite, magnesium thiosulfate, magnesium carbonate, magnesium primary phosphate, magnesium secondary phosphate, magnesium tertiary phosphate, magnesium pyrophosphate, magnesium nitrite, Examples thereof include magnesium acetate, magnesium citrate, magnesium oxalate and hydrates thereof. The magnesium salt is preferably magnesium sulfate or a hydrate thereof (for example, magnesium sulfate heptahydrate), and more preferably magnesium sulfate. One or two or more of the above magnesium sources can be selected and used.
マグネシウム源の配合量(2種以上用いる場合はその合計量)は、炭素源1質量部に対して、マグネシウム源化合物の質量換算で、例えば0.01〜0.5質量部であり、好ましくは0.1〜0.3質量部である。 The blending amount of the magnesium source (the total amount when two or more kinds are used) is, for example, 0.01 to 0.5 parts by mass, preferably 0.01 to 0.5 parts by mass, in terms of mass of the magnesium source compound with respect to 1 part by mass of the carbon source. 0.1 to 0.3 parts by mass.
(酵母培養用培地の形態)
本発明に係る酵母培養用培地の形態は、特に制限されず、液体状、固体状、固形状のいずれであってもよい。本明細書中、固体状の培地は、液体状の培地を固化させたものを意味する。また、固形状の培地は、本発明に係る酵母培養用培地の成分を含む粒状培地、粉末培地、顆粒状培地、ペレット状培地などを意味する。本発明に係る酵母培養用培地は、好ましくは液体状の培地または固形状の培地である。
(Form of yeast culture medium)
The form of the yeast culture medium according to the present invention is not particularly limited, and may be liquid, solid, or solid. In the present specification, the solid medium means a solidified liquid medium. Further, the solid medium means a granular medium, a powder medium, a granular medium, a pellet medium, or the like containing the components of the yeast culture medium according to the present invention. The yeast culture medium according to the present invention is preferably a liquid medium or a solid medium.
(その他の成分)
本発明に係る酵母培養用培地は、炭素源、窒素源、マグネシウム源および溶媒に加えて、必要に応じて適宜その他の成分を含むことができる。
(Other ingredients)
The yeast culture medium according to the present invention may contain, if necessary, other components in addition to the carbon source, nitrogen source, magnesium source and solvent.
その他の成分としては、例えば溶媒、マグネシウム以外のミネラル、pH調整剤などが挙げられる。 Examples of other components include solvents, minerals other than magnesium, pH adjusters, and the like.
溶媒としては、通常、水が用いられる。水は、純水、蒸留水、脱イオン水、RO水、などが挙げられるが、特に制限はない。 Water is usually used as the solvent. Examples of water include pure water, distilled water, deionized water, RO water, and the like, but there is no particular limitation.
マグネシウム以外のミネラルとしては、例えばリン、硫黄、カリウム、カルシウム、鉄、ナトリウム、コバルト、銅、亜鉛、ニッケル、ホウ素などが挙げられる。これらのミネラルは、培養する酵母による資化性を考慮して適宜選択される。また、上記ミネラルを1種または2種以上選択して使用することができる。 Examples of minerals other than magnesium include phosphorus, sulfur, potassium, calcium, iron, sodium, cobalt, copper, zinc, nickel and boron. These minerals are appropriately selected in consideration of the assimilation property of the yeast to be cultured. In addition, one or more of the above minerals can be selected and used.
pH調整剤としては、例えば硫酸、塩酸、硝酸、酢酸、クエン酸等の酸;水酸化ナトリウム、水酸化カリウム、炭酸ナトリウム、炭酸カリウム等の塩基が挙げられる。 Examples of the pH adjuster include acids such as sulfuric acid, hydrochloric acid, nitric acid, acetic acid and citric acid; and bases such as sodium hydroxide, potassium hydroxide, sodium carbonate and potassium carbonate.
(pH)
本発明に係る酵母培養用培地のpHに特に制限はないが、一般的に酵母の培養は弱酸性条件下において行うことが好ましいことから、好ましくは3.0〜7.0であり、より好ましくは3.5〜6.5である。特に、後述する実施例において用いられている酵母であるアステロトレメラ・ヒュミコラ(Asterotremella humicola)等のアステロトレメラ属の培養に好適である。ここで、酵母培養用培地のpHは、pHメーターを用いて測定することができる。
(PH)
The pH of the yeast culture medium according to the present invention is not particularly limited, but in general, yeast culture is preferably carried out under weakly acidic conditions, and is preferably 3.0 to 7.0, more preferably. Is 3.5 to 6.5. In particular, it is suitable for culturing the genus Asterotremera such as Asterotremella humicola, which is a yeast used in Examples described later. Here, the pH of the yeast culture medium can be measured using a pH meter.
(酵母)
本発明に係る酵母培養用培地で培養される酵母としては、特に制限されないが、アステロトレメラ(Asterotremella)属(現行名:Vanrija属)、クリプトコッカス(Cryptococcus)属、トリコスポロン(Trichosporon)属、ヤロウィア(Yarrowia)属、キャンディダ(Candida)属、ピキア(Pichia)属、ハンセヌラ(Hansenura)属、サッカロマイセス(Saccharomyces)属、クルイベロマイセス(Kluyveromyces)属、リポマイセス(Lipomyces)属、ロードトルラ(Rhodotorula)属、シゾサッカロマイセス(Schizosaccharomyces)属、ラクトバシラス(Lactobacillus)属、エンテロコッカス(Enterococcus)属等の酵母が好ましく用いられる。これらのうち、アステロトレメラ属、クリプトコッカス属、トリコスポロン属、サッカロマイセス属、キャンディダ属、ピキア属、ハンセヌラ属、クルイベロマイセス属、リポマイセス属、ロードトルラ属、シゾサッカロマイセス属、ラクトバシラス属、エンテロコッカス属などの酵母がより好ましく用いられる。
(yeast)
The yeast cultivated in the yeast culture medium according to the present invention is not particularly limited, but is limited to the genus Asterotremella (current name: Vanrija), the genus Cryptococcus, the genus Trichosporon, and the genus Yarrowia (current name: Vanrija). Yeast, Candida, Pichia, Hansenura, Saccharomyces, Kluyveromyces, Lipomyces, Lipomyces, Lipomyces, Lipomyces, Lipomyces Yeasts such as the genus Schizosaccharomyces, the genus Lactobacillus, and the genus Enterococcus are preferably used. Of these, the genus Asterotremera, the genus Cryptococcus, the genus Trichosporon, the genus Saccharomyces, the genus Candida, the genus Pikia, the genus Hansenula, the genus Kruiberomyces, the genus Lipomyces, the genus Rhodtorula, the genus Sizosaccalomyces, the genus Lactobacillus Yeast such as is more preferably used.
本発明に係る酵母培養用培地では、これらの酵母のうち、油分分解活性の高いアステロトレメラ属の培養効率をより向上させることができる。アステロトレメラ属の酵母としては、アステロトレメラ・ヒュミコラ(Asterotremella humicola)、アステロトレメラ・シュードロンガ(Asterotremella pseudolonga)、アステロトレメラ・ロンガ(Asterotremella longa)、アステロトレメラ・アルビダ(Asterotremella albida)、アステロトレメラ・ムッシ(Asterotremella musci)などが挙げられる。アステロトレメラ属の酵母は、好ましくはアステロトレメラ・ヒュミコラであり、より好ましくはアステロトレメラ・ヒュミコラ 2−141−1(受託番号 NITE BP−02641)(以下、単に「2−141−1株」とも称する)である。 In the yeast culture medium according to the present invention, among these yeasts, the culture efficiency of the genus Asterotremera, which has high oil decomposition activity, can be further improved. Yeasts of the genus Asterotremella include Asterotremella humicola, Asterotremella pseudolonga, Asterotremella longa, Asterotremella avitala, Asterotremella, and Asterotremella. Examples include Asterotremella muscii. The yeast of the genus Astero Tremera is preferably Astero Tremera Humicola, more preferably Astero Tremera Humicola 2-141-1 (accession number NITE BP-02641) (hereinafter, simply "2-1141-1 strain". Also called).
上述の酵母は、ATCC、NBRC、DSMZ等のカルチャーコレクションから入手可能である。 The yeasts mentioned above are available from cultural collections such as ATCC, NBRC, DSMZ and the like.
(酵母培養用培地の調製方法)
本発明に係る酵母培養用培地の調製方法は、特に制限されず、従来公知の方法を用いることができる。
(Method of preparing medium for yeast culture)
The method for preparing the yeast culture medium according to the present invention is not particularly limited, and conventionally known methods can be used.
本発明に係る酵母培養用培地が固形状の培地である場合、例えば、炭素源、窒素源(グルタミン酸およびグリシンを必須に含む)およびマグネシウム源、ならびに必要に応じてグルタミン酸およびグリシン以外の窒素源およびマグネシウム以外のミネラルを混合することで調製することができる。混合後は、必要に応じて粉砕、乾燥などを行ってもよい。 When the yeast culture medium according to the present invention is a solid medium, for example, a carbon source, a nitrogen source (essentially containing glutamic acid and glycine) and a magnesium source, and if necessary, a nitrogen source other than glutamic acid and glycine and It can be prepared by mixing minerals other than magnesium. After mixing, it may be crushed, dried or the like, if necessary.
また、本発明に係る酵母培養用培地が液体状の培地である場合、例えば、炭素源、窒素源(グルタミン酸およびグリシンを必須に含む)およびマグネシウム源、ならびに必要に応じてグルタミン酸およびグリシン以外の窒素源およびマグネシウム以外のミネラルを溶媒(例えば、水)に溶解することで調製することができる。また、上記固形状の培地を溶媒に溶解することで調製することもできる。酵母培養用培地のpHを調整する必要がある場合、pH調整剤として、上記酸やアルカリを用いればよい。また、必要に応じて消泡剤を添加してもよい。 When the yeast culture medium according to the present invention is a liquid medium, for example, a carbon source, a nitrogen source (essentially containing glutamic acid and glycine) and a magnesium source, and, if necessary, nitrogen other than glutamic acid and glycine. It can be prepared by dissolving the source and minerals other than magnesium in a solvent (eg, water). It can also be prepared by dissolving the solid medium in a solvent. When it is necessary to adjust the pH of the yeast culture medium, the above acid or alkali may be used as the pH adjusting agent. In addition, an antifoaming agent may be added if necessary.
本発明に係る酵母培養用培地が液体状の培地である場合、各成分の配合量は以下のとおりである。 When the yeast culture medium according to the present invention is a liquid medium, the blending amount of each component is as follows.
炭素源の配合量(2種以上用いる場合はその合計量)は、酵母培養用培地全量に対して、例えば0.01〜20.0w/v%であり、好ましくは0.1〜10.0w/v%であり、より好ましくは0.5〜3.0w/v%である。 The blending amount of the carbon source (the total amount when two or more kinds are used) is, for example, 0.01 to 20.0 w / v%, preferably 0.1 to 10.0 w, based on the total amount of the yeast culture medium. / V%, more preferably 0.5 to 3.0 w / v%.
グルタミン酸およびグリシンの配合量の合計は、酵母培養用培地全量に対して、例えば0.01〜5.0w/v%であり、好ましくは0.1〜2.5w/v%である。 The total amount of glutamic acid and glycine to be blended is, for example, 0.01 to 5.0 w / v%, preferably 0.1 to 2.5 w / v%, based on the total amount of the yeast culture medium.
グルタミン酸およびグリシン以外の窒素源を使用する場合、当該窒素源の配合量(2種以上用いる場合はその合計量)は、酵母培養用培地全量に対して、例えば0.1〜3.0w/v%であり、好ましくは0.3〜1.0w/v%である。 When a nitrogen source other than glutamic acid and glycine is used, the blending amount of the nitrogen source (the total amount when two or more kinds are used) is, for example, 0.1 to 3.0 w / v with respect to the total amount of the yeast culture medium. %, Preferably 0.3 to 1.0 w / v%.
マグネシウム源の配合量(2種以上用いる場合はその合計量)は、酵母培養用培地全量に対して、マグネシウム源化合物の質量換算で、例えば0.01〜0.5w/v%であり、好ましくは0.1〜0.3w/v%である。 The blending amount of the magnesium source (the total amount when two or more kinds are used) is, for example, 0.01 to 0.5 w / v% in terms of mass of the magnesium source compound with respect to the total amount of the yeast culture medium, which is preferable. Is 0.1 to 0.3 w / v%.
<酵母の培養方法および増殖方法>
本発明の一実施形態では、上記酵母培養用培地で酵母を培養することを有する、酵母の培養方法が提供される。本実施形態では、酵母培養用培地は液体状の培地である。
<Yeast culture method and growth method>
In one embodiment of the present invention, there is provided a method for culturing yeast, which comprises culturing yeast in the above-mentioned yeast culture medium. In this embodiment, the yeast culture medium is a liquid medium.
本発明に係る酵母の培養は、通常の方法によって行うことができる。酵母の種類によって、好気的条件下または嫌気的条件下で培養する。前者の場合には、酵母の培養は、振とうあるいは通気撹拌などによって行われる。また、酵母を連続的にまたはバッチで培養してもよい。培養条件は、適宜選択され、本発明に係る酵母が増殖できる条件であれば特に制限されず、培養する酵母の種類に応じて適宜選択されうる。また、酵母培養培地に添加する菌体量についても、特に制限されず、適宜調整することができる。 The yeast according to the present invention can be cultured by a usual method. Depending on the type of yeast, it is cultured under aerobic or anaerobic conditions. In the former case, yeast is cultured by shaking or aeration and stirring. Yeast may also be cultured continuously or in batches. The culturing conditions are appropriately selected, and are not particularly limited as long as the yeast according to the present invention can grow, and can be appropriately selected depending on the type of yeast to be cultivated. Further, the amount of bacterial cells added to the yeast culture medium is not particularly limited and can be appropriately adjusted.
培養温度は、通常15〜50℃であり、好ましくは25〜40℃である。例えば、酵母として2−141−1株を用いる場合、培養温度は、通常15〜35℃であり、好ましくは20〜30℃である。 The culture temperature is usually 15 to 50 ° C, preferably 25 to 40 ° C. For example, when a strain 2-141-1 is used as yeast, the culture temperature is usually 15 to 35 ° C, preferably 20 to 30 ° C.
本発明の酵母培養用培地で酵母を培養する場合、様々な形態の酵母を用いることができる。例えば、酵母は、培養液中に懸濁された状態、培養液から固形分として回収された状態、乾燥された状態、担体に固定化された状態などでありうる。 When culturing yeast in the yeast culture medium of the present invention, various forms of yeast can be used. For example, yeast can be suspended in a culture medium, recovered as solids from the culture medium, dried, or immobilized on a carrier.
培養液から固形分として回収した酵母を使用する場合、回収方法は当業者に公知のいずれの手段をも採用できる。例えば、上述の方法により培養した酵母の培養液を、遠心分離やろ過などにより固液分離し、固形分を回収して得ることができる。この固形分を乾燥(例えば、凍結乾燥)すれば、乾燥された状態の酵母を得ることができる。 When yeast recovered as solid content from the culture solution is used, any means known to those skilled in the art can be adopted as the recovery method. For example, the yeast culture solution cultured by the above method can be obtained by solid-liquid separation by centrifugation, filtration, or the like, and the solid content can be recovered. If this solid content is dried (for example, freeze-dried), yeast in a dried state can be obtained.
担体に固定化された状態の酵母を使用する場合、酵母を固定化する担体としては、酵母を固定化することができるものであれば特に制限されず、一般的に微生物を固定化するのに使用される担体が同様にしてあるいは適宜修飾されて使用される。例えば、アルギン酸、ポリビニルアルコール、ゲランガム、アガロース、セルロース、デキストラン等のゲル状物質に包括固定する方法や、ガラス、活性炭、ポリスチレン、ポリエチレン、ポリプロピレン、木材、シリカゲル等の表面に吸着固定する方法などが使用できる。 When yeast in a state of being immobilized on a carrier is used, the carrier for immobilizing yeast is not particularly limited as long as it can immobilize yeast, and generally for immobilizing microorganisms. The carrier used is used in the same manner or modified as appropriate. For example, a method of comprehensively fixing to a gel-like substance such as alginic acid, polyvinyl alcohol, gellan gum, agarose, cellulose, dextran, or a method of adsorbing and fixing to the surface of glass, activated carbon, polystyrene, polyethylene, polypropylene, wood, silica gel, etc. is used. it can.
また、酵母を担体に固定化する方法もまた特に制限されず、一般的な微生物の固定化方法が同様にしてあるいは適宜修飾されて使用される。例えば、酵母の培養液を担体に流し込むことによる固定化法、アスピレーターを用いて担体を減圧下におき、酵母の培養液を担体に流し込むことによる固定化法、および酵母の培養液を滅菌した培地と担体との混合物に流し込み、振とう培養し、上記混合物から取り出した担体を自然乾燥する方法などが挙げられる。 Further, the method for immobilizing yeast on the carrier is also not particularly limited, and a general method for immobilizing microorganisms is used in the same manner or appropriately modified. For example, the immobilization method by pouring the yeast culture solution into the carrier, the immobilization method by placing the carrier under reduced pressure using an aspirator and pouring the yeast culture solution into the carrier, and the medium in which the yeast culture solution is sterilized. Examples thereof include a method of pouring into a mixture of yeast and a carrier, culturing with shaking, and air-drying the carrier taken out from the mixture.
本発明の好ましい形態において、保存中の酵母の生存性の観点から、酵母は、生菌製剤の形態で使用される。酵母としては、上記酵母を用いることができる。上記酵母を用いる場合、生菌製剤は、多孔質担体上に形成された酵母含有層を含み、前記酵母含有層が、乾燥菌体として1質量部の前記酵母に対して、0.8質量部以上1.5質量部未満のトレハロース、0.01〜5質量部の乳タンパク質、0.03〜10質量部のアミノ酸、および0.02〜10質量部の金属塩を含むものである。トレハロースが、酵母含有層中に、乾燥菌体として1質量部の前記酵母に対して、0.8質量部以上含まれることで、製剤化をする際の酵母の生存率を向上させることができ、また、1.5質量部未満含まれることで、生菌製剤の保存期間中の酵母の生存率の低下を防止することができる。酵母の製剤化の際の生存率と保存期間中の生存率とのさらなる好適なバランスの観点から、酵母含有層のトレハロース含有量は、乾燥菌体換算で1質量部の酵母に対して、好ましくは0.9質量部を超えて1.5質量部未満であり、より好ましくは1質量部以上1.4質量部以下である。 In the preferred form of the present invention, the yeast is used in the form of a live bacterial preparation from the viewpoint of the viability of the yeast during storage. As the yeast, the above-mentioned yeast can be used. When the above yeast is used, the viable bacterial preparation contains a yeast-containing layer formed on a porous carrier, and the yeast-containing layer is 0.8 parts by mass with respect to 1 part by mass of the yeast as a dry bacterial cell. It contains less than 1.5 parts by mass of trehalose, 0.01 to 5 parts by mass of milk protein, 0.03 to 10 parts by mass of amino acids, and 0.02 to 10 parts by mass of metal salt. When trehalose is contained in the yeast-containing layer in an amount of 0.8 parts by mass or more with respect to 1 part by mass of the yeast as a dried bacterial cell, the survival rate of the yeast at the time of formulation can be improved. Further, when it is contained in an amount of less than 1.5 parts by mass, it is possible to prevent a decrease in the survival rate of yeast during the storage period of the viable bacterial preparation. From the viewpoint of a more preferable balance between the survival rate during yeast formulation and the survival rate during the storage period, the trehalose content of the yeast-containing layer is preferable with respect to 1 part by mass of yeast in terms of dried cells. Is more than 0.9 parts by mass and less than 1.5 parts by mass, and more preferably 1 part by mass or more and 1.4 parts by mass or less.
なお、トレハロース以外の二糖類、たとえばスクロース、ラクトース、マルトース等のトレハロース以外の二糖類を、1種単独でまたは2種以上を混合して、トレハロースと併用してもよい。この場合、トレハロース以外の二糖類の含有量は、乾燥菌体として1質量部の無芽胞菌に対して、例えば0.01質量部以上0.8質量部未満であり、好ましくは0.1質量部以上0.5質量部以下である。 Disaccharides other than trehalose, for example, disaccharides other than trehalose such as sucrose, lactose, and maltose may be used alone or in combination of two or more in combination with trehalose. In this case, the content of the disaccharide other than trehalose is, for example, 0.01 part by mass or more and less than 0.8 part by mass, preferably 0.1 part by mass, with respect to 1 part by mass of the non-spore-forming bacterium as a dried bacterial cell. Parts or more and 0.5 parts by mass or less.
酵母含有層中の乳タンパク質としては特に制限されず、従来公知の各種の乳タンパク質を含む材料を用いることができる。全脂粉乳のような乳脂肪分の多い原料を用いることもできるが、グリーストラップで使用するような油脂分解用生菌製剤を製造する場合は、製剤中の油分は少ない方が好ましいので、例えば、好ましい具体例としては、カゼイン、カゼインナトリウム、ホエイ、濃縮ホエイ、ホエイタンパク質濃縮物(WPC)、ホエイタンパク質分離物(WPI)、ホエイパウダー、スキムミルク、乳タンパク濃縮物(MPC)、脱脂粉乳、α−ラクトアルブミン、β−ラクトグロブリン等が例示でき、これらを1種単独でまたは2種以上を混合して用いることができる。乳タンパク質が、酵母含有層中に、乾燥菌体として1質量部の前記酵母に対して、0.01〜5質量部、好ましくは0.02〜1質量部、より好ましくは0.05〜0.5質量部含まれることで、製剤化をする際の酵母の生存率を向上させることができる。 The milk protein in the yeast-containing layer is not particularly limited, and conventionally known materials containing various milk proteins can be used. It is possible to use a raw material having a high milk fat content such as skim milk powder, but when producing a viable bacterial preparation for fat decomposition such as used in a grease trap, it is preferable that the oil content in the preparation is low, so for example. , Preferred specific examples include casein, casein sodium, whey, concentrated whey, whey protein concentrate (WPC), whey protein isolate (WPI), whey powder, skim milk, milk protein concentrate (MPC), skim milk powder, α. -Lactalbumin, β-lactoglobulin and the like can be exemplified, and these can be used alone or in combination of two or more. The milk protein is contained in the yeast-containing layer in an amount of 0.01 to 5 parts by mass, preferably 0.02 to 1 part by mass, more preferably 0.05 to 0, based on 1 part by mass of the yeast as dried cells. By containing 5.5 parts by mass, the survival rate of yeast at the time of formulation can be improved.
酵母含有層中のアミノ酸は、例えばグリシン、アラニン、バリン、ロイシン、イソロイシン、フェニルアラニン、グルタミン、グルタミン酸、アスパラギン、アスパラギン酸、システイン、リジン、セリン、スレオニン、メチオニン、トリプトファン、ヒスチジン、アルギン、プロリン、チロシン、およびこれらの誘導体が例示できる。アミノ酸の誘導体としては、アミノ酸の塩(例えば、カリウム塩、ナトリウム塩)、エステル体、水和物、溶媒和物等が例示できる。上記のアミノ酸は、1種を単独で、または2種以上を混合して用いることができる。アミノ酸が、酵母含有層中に、乾燥菌体として1質量部の前記酵母に対して、0.03〜10質量部、好ましくは0.1〜5質量部、より好ましくは0.1〜3質量部含まれることで、製剤化をする際の酵母の生存率を向上させることができる。なお、油分分解層中に2種以上のアミノ酸が含まれる場合、上記数値は、2種以上の合計量を示す。 Amino acids in the yeast-containing layer include, for example, glycine, alanine, valine, leucine, isoleucine, phenylalanine, glutamine, glutamic acid, asparagine, aspartic acid, cysteine, lysine, serine, threonine, methionine, tryptophan, histidine, argin, proline, tyrosine, And these derivatives can be exemplified. Examples of the amino acid derivative include amino acid salts (for example, potassium salt and sodium salt), esters, hydrates, solvates and the like. The above amino acids may be used alone or in admixture of two or more. Amino acids are contained in the yeast-containing layer in an amount of 0.03 to 10 parts by mass, preferably 0.1 to 5 parts by mass, more preferably 0.1 to 3 parts by mass, based on 1 part by mass of the yeast as dried cells. By including the part, the survival rate of yeast at the time of formulation can be improved. When two or more kinds of amino acids are contained in the oil decomposition layer, the above numerical values indicate the total amount of two or more kinds.
酵母含有層中の金属塩は、例えばナトリウム(Na)、カリウム(K)、マグネシウム(Mg)、カルシウム(Ca)、マンガン(Mn)、鉄(Fe)、ニッケル(Ni)、亜鉛(Zn)、銅(Cu)などの金属元素の、硫酸塩、亜硫酸塩、次亜硫酸塩、過硫酸塩、チオ硫酸塩、炭酸塩、リン酸塩、ピロリン酸、塩酸塩、硝酸塩、亜硝酸塩、酢酸塩、プロピオン酸塩、酪酸塩、クエン酸塩、シュウ酸塩、ハロゲン化物(たとえば、フッ化物、塩化物、臭化物、ヨウ化物)等が例示できるが、これらに限定されない。金属塩は、より具体的には、例えば、硫酸ナトリウム、亜硫酸ナトリウム、次亜硫酸ナトリウム、チオ硫酸ナトリウム、炭酸ナトリウム、過硫酸ナトリウム、リン酸一ナトリウム、リン酸二ナトリウム、リン酸三ナトリウム、酢酸ナトリウム、硝酸ナトリウム、亜硝酸ナトリウム、酢酸ナトリウム、クエン酸ナトリウム、シュウ酸ナトリウム、塩化ナトリウム、硫酸カリウム、亜硫酸カリウム、次亜硫酸カリウム、チオ硫酸カリウム、炭酸カリウム、過硫酸カリウム、リン酸一カリウム、リン酸二カリウム、リン酸三カリウム、酢酸カリウム、硝酸カリウム、亜硝酸カリウム、酢酸カリウム、クエン酸カリウム、シュウ酸カリウム、塩化カリウム、硫酸マグネシウム、亜硫酸マグネシウム、チオ硫酸マグネシウム、炭酸マグネシウム、第一リン酸マグネシウム、第二リン酸マグネシウム、第三リン酸マグネシウム、ピロリン酸マグネシウム、硝酸マグネシウム、亜硝酸マグネシウム、酢酸マグネシウム、クエン酸マグネシウム、シュウ酸マグネシウム、塩化マグネシウム、硫酸カルシウム、亜硫酸カルシウム、チオ硫酸カルシウム、炭酸カルシウム、硝酸カルシウム、亜硝酸カルシウム、酢酸カルシウム、クエン酸カルシウム、シュウ酸カルシウム、塩化カルシウム等が例示できる。上記の金属塩は、1種を単独で、または2種以上を混合して用いることができる。金属塩が、酵母含有層中に、乾燥菌体として1質量部の前記酵母に対して、0.02〜10質量部、好ましくは0.05〜1.5質量部、より好ましくは0.1〜1質量部含まれることで、生菌製剤の保存期間中の酵母の生存率の低下を防止することができる。なお、酵母含有層が2種以上の金属塩を含む場合、上記数値は、2種以上の合計量を示す。 The metal salts in the yeast-containing layer include, for example, sodium (Na), potassium (K), magnesium (Mg), calcium (Ca), manganese (Mn), iron (Fe), nickel (Ni), zinc (Zn), Sulfates, sulfites, hyposulfates, persulfates, thiosulfates, carbonates, phosphates, pyrophosphates, hydrochlorides, nitrates, nitrites, acetates, propions of metal elements such as copper (Cu) Examples include, but are not limited to, acid salts, butyrates, citrates, oxalates, halides (eg, fluorides, chlorides, bromides, iodides). More specifically, the metal salt is, for example, sodium sulfate, sodium sulfite, sodium hyposulfate, sodium thiosulfate, sodium carbonate, sodium persulfate, monosodium phosphate, disodium phosphate, trisodium phosphate, sodium acetate. , Sodium nitrate, sodium nitrite, sodium acetate, sodium citrate, sodium oxalate, sodium chloride, potassium sulfate, potassium sulfite, potassium hyposulfate, potassium thiosulfate, potassium carbonate, potassium persulfate, monopotassium phosphate, phosphoric acid Dipotassium, tripotassium phosphate, potassium acetate, potassium nitrate, potassium nitrite, potassium acetate, potassium citrate, potassium oxalate, potassium chloride, magnesium sulfate, magnesium sulfite, magnesium thiosulfate, magnesium carbonate, primary magnesium phosphate, first Magnesium diphosphate, magnesium tertiary phosphate, magnesium pyrophosphate, magnesium nitrate, magnesium nitrite, magnesium acetate, magnesium citrate, magnesium oxalate, magnesium chloride, calcium sulfate, calcium sulfite, calcium thiosulfate, calcium carbonate, nitrate Examples thereof include calcium, calcium nitrite, potassium acetate, calcium citrate, calcium oxalate, and calcium chloride. The above metal salts may be used alone or in admixture of two or more. The metal salt is 0.02 to 10 parts by mass, preferably 0.05 to 1.5 parts by mass, more preferably 0.1 parts by mass, relative to 1 part by mass of the yeast as dried cells in the yeast-containing layer. By containing ~ 1 part by mass, it is possible to prevent a decrease in the survival rate of yeast during the storage period of the viable bacterial preparation. When the yeast-containing layer contains two or more kinds of metal salts, the above numerical values indicate the total amount of two or more kinds.
保存期間中における酵母の生存率が特に優れるという観点から、金属塩が、Na、K、MgおよびCaからなる群から選択される元素の、硫酸塩、炭酸塩、リン酸塩、またはそれらの組み合わせであることが好ましく、Mgおよび/またはCaの硫酸塩であることがより好ましい。なお、上記の「金属塩」には、金属塩の水和物や溶媒和物も含まれる。 Sulfates, carbonates, phosphates, or combinations thereof, in which the metal salt is an element selected from the group consisting of Na, K, Mg and Ca, from the viewpoint of particularly excellent yeast viability during the storage period. Is preferable, and it is more preferable that it is a sulfate of Mg and / or Ca. The above-mentioned "metal salt" also includes hydrates and solvates of metal salts.
酵母含有層には、上記の各成分のほか、任意に、例えばグルコース、フルクトース等の単糖類;スクロース、ラクトース、マルトース等のトレハロース以外の二糖類;シクロデキストリン、ヒドロキシプロピルセルロース、ヒドロキシプロピルメチルセルロース、カルボキシメチルセルロース、結晶セルロース、コーンスターチ等の多糖類;大豆タンパク等のタンパク質;大豆ペプチド、ゼラチン、ペプトン、トリプトン等のタンパク加水分解物やペプチド;大豆油、菜種油、パーム油、ゴマ油、オリーブ油等の油脂;アスコルビン酸やその塩、トコフェロール等のビタミン類;ポリグリセリン脂肪酸エステル、ショ糖脂肪酸エステル、ソルビタン脂肪酸エステル等の界面活性剤;ポリエチエレングリコール、グリセリンなどが含まれてもよい。 In addition to the above components, the yeast-containing layer may optionally contain monosaccharides such as glucose and fructose; disaccharides other than trehalose such as sucrose, lactose and maltose; cyclodextrin, hydroxypropyl cellulose, hydroxypropyl methyl cellulose and carboxy. Polysaccharides such as methyl cellulose, crystalline cellulose and corn starch; proteins such as soy protein; protein hydrolysates and peptides such as soy peptide, gelatin, peptone and tripton; fats and oils such as soybean oil, rapeseed oil, palm oil, sesame oil and olive oil; ascorbin Vitamins such as acids, salts thereof and tocopherols; surfactants such as polyglycerin fatty acid ester, sucrose fatty acid ester and sorbitan fatty acid ester; polyethylene glycol, glycerin and the like may be contained.
生菌製剤に用いられうる多孔質担体の材料としては、特に制限されるものではないが、例えば、珪藻土、パーライト、バーミキュライト、タルク、クレー、ゼオライト、ベントナイト、カオリン、炭酸カルシウム、活性白土、二酸化チタン、珪砂、軽石、活性炭、カーボンブラック、グラファイト、ポリ乳酸、ポリスチレン、ポリ塩化ビニル等が例示できるが、これらに限定されない。多孔質担体の材料は、製剤化をする際の酵母の生存率の観点から、好ましくは珪藻土である。 The material of the porous carrier that can be used in the viable bacterial preparation is not particularly limited, but is, for example, diatomaceous earth, pearlite, vermiculite, talc, clay, zeolite, bentonite, kaolin, calcium carbonate, activated clay, titanium dioxide. , Diatomaceous earth, pumice stone, activated carbon, carbon black, graphite, polylactic acid, polystyrene, polyvinyl chloride and the like, but are not limited thereto. The material of the porous carrier is preferably diatomaceous earth from the viewpoint of yeast survival rate at the time of formulation.
なお、上記生菌製剤に用いられうる多孔質担体における「多孔質」とは、担体の表面に多数の小さな気泡状の空隙を有する状態をいう。好ましくは、多孔質担体の嵩密度(タッピング嵩密度)が0.01〜2g/mlである。上記のような嵩密度の多孔質担体を用いることにより、製剤化工程後の酵母の生存率をより一層向上できる。多孔質担体の嵩密度は、より好ましくは0.05〜1.5g/mlであり、更に好ましくは0.2〜1g/mlである。なお、上記の嵩密度は、タッピング嵩密度測定法により測定した値である。 The term "porous" in the porous carrier that can be used in the viable bacterial preparation means a state in which a large number of small bubble-like voids are present on the surface of the carrier. Preferably, the bulk density (tapping bulk density) of the porous carrier is 0.01 to 2 g / ml. By using the bulky porous carrier as described above, the survival rate of yeast after the formulation step can be further improved. The bulk density of the porous carrier is more preferably 0.05 to 1.5 g / ml, still more preferably 0.2 to 1 g / ml. The above bulk density is a value measured by the tapping bulk density measuring method.
製剤化をする際の酵母の生存率の観点から、担体は、平均粒径(直径、体積基準)が1〜300μmの粒子状であることが好ましく、平均粒径(直径、体積基準)が10〜200μmの粒子状であることがより好ましく、30〜150μmであることが更に好ましい。なお、担体の粒径は、レーザー回折法にて測定した値である。 From the viewpoint of the viability of yeast during formulation, the carrier is preferably in the form of particles having an average particle size (diameter, volume standard) of 1 to 300 μm, and an average particle size (diameter, volume standard) of 10. It is more preferably in the form of particles of about 200 μm, and even more preferably 30 to 150 μm. The particle size of the carrier is a value measured by a laser diffraction method.
生菌製剤は、上記生菌製剤に用いられうる多孔質担体に対して、噴霧液を噴霧して製剤化することができる。前記噴霧液は、上述した酵母とトレハロース、乳タンパク質、アミノ酸、金属塩および必要に応じてその他の成分とを、水に添加し、必要に応じて撹拌して調製することができる。噴霧液の調製に用いる水としては、例えば水道水、蒸留水、イオン交換水、純水、超純水など、いずれを使用してもよいが、不純物の少ない蒸留水、イオン交換水、純水、または超純水を用いることが好ましい。メタノール、エタノール、プロパノール等の低級アルコールや、アセトンなどの極性溶媒を、適宜水に添加した混合液を用いてもよい。 The viable bacterial preparation can be formulated by spraying a spray solution onto the porous carrier that can be used for the viable bacterial preparation. The spray solution can be prepared by adding the above-mentioned yeast and trehalose, milk protein, amino acids, metal salts and, if necessary, other components to water, and stirring as necessary. As the water used for preparing the spray liquid, for example, tap water, distilled water, ion-exchanged water, pure water, ultrapure water, etc. may be used, but distilled water with less impurities, ion-exchanged water, pure water, etc. may be used. , Or ultrapure water is preferably used. A mixed solution in which a lower alcohol such as methanol, ethanol or propanol or a polar solvent such as acetone is appropriately added to water may be used.
上記生菌製剤に用いられうる多孔質担体への噴霧液の噴霧は、例えば流動層造粒機を用いて行うことができる。流動層造粒法により製剤化することにより、酵母含有層を比較的低温で多孔質担体上に形成することができる。このため、製剤化をする際の生存率の向上の観点から有利である。また、流動層造粒法により製剤化することにより、上記の酵母含有層を均一に多孔質担体上に形成することができる、という点においても有利である。 The spray solution can be sprayed onto the porous carrier that can be used in the viable cell preparation, for example, by using a fluidized bed granulator. By formulating by the fluidized bed granulation method, the yeast-containing layer can be formed on the porous carrier at a relatively low temperature. Therefore, it is advantageous from the viewpoint of improving the survival rate at the time of formulation. It is also advantageous in that the yeast-containing layer can be uniformly formed on the porous carrier by formulating by the fluidized bed granulation method.
多孔質担体に対する噴霧液の噴霧量は任意に設定でき、特に制限されるものではないが、1質量部の多孔質担体に対して、噴霧液の固形分として、例えば、0.1〜10質量部となる割合であり、好ましくは0.5〜2質量部となる割合である。 The amount of the spray liquid sprayed on the porous carrier can be arbitrarily set and is not particularly limited, but the solid content of the spray liquid is, for example, 0.1 to 10 mass with respect to 1 part by mass of the porous carrier. It is a ratio of parts, preferably 0.5 to 2 parts by mass.
噴霧液は、通常は50〜300g/分程度の速度で多孔質担体へ噴霧される。 The spray liquid is usually sprayed onto the porous carrier at a rate of about 50 to 300 g / min.
流動層造粒法により製剤化する場合は、温風の温度は酵母の耐熱性等を考慮して適宜設定すればよいが、例えば、入口温度30〜60℃であり、好ましくは35〜50℃である。流動層の温度も酵母の耐熱性等を考慮して適宜設定すればよいが、例えば、温度30〜60℃であり、好ましくは35〜50℃である。噴霧後、噴霧液を噴霧した多孔質担体を流動層造粒機内でそのまま乾燥してもよいし、別途乾燥機で乾燥してもよい。 When formulating by the fluidized bed granulation method, the temperature of the warm air may be appropriately set in consideration of the heat resistance of yeast and the like. For example, the inlet temperature is 30 to 60 ° C, preferably 35 to 50 ° C. Is. The temperature of the fluidized bed may be appropriately set in consideration of the heat resistance of yeast and the like. For example, the temperature is 30 to 60 ° C, preferably 35 to 50 ° C. After spraying, the porous carrier sprayed with the spray liquid may be dried as it is in the fluidized bed granulator, or may be dried separately in the dryer.
粉末化した生菌製剤は、用途に応じて、公知のコーティング剤で表面の一部または全部を被覆してもよい。また、滑沢剤(例えば、タルク、マイカ、シリカ、ステアリン酸マグネシウム)、乾燥剤(酸化カルシウム、シリカゲル)、フィラーなどの粉末を、任意の割合で生菌製剤と混合し、混合製剤としてもよい。また、所望の粒度となるように製剤を粉砕したり、分級をしたりしてもよい。 The powdered viable bacterial preparation may be partially or wholly coated with a known coating agent, depending on the intended use. Further, powders such as a lubricant (for example, talc, mica, silica, magnesium stearate), a desiccant (calcium oxide, silica gel), and a filler may be mixed with a viable bacterial preparation in an arbitrary ratio to prepare a mixed preparation. .. Further, the preparation may be pulverized or classified so as to have a desired particle size.
保存期間中の酵母の生存率の観点から、製剤化後の生菌製剤の水分含量は、3〜8質量%であることが好ましく、4.5〜7.5質量%であることがより好ましい。 From the viewpoint of the survival rate of yeast during the storage period, the water content of the viable bacterial preparation after formulation is preferably 3 to 8% by mass, more preferably 4.5 to 7.5% by mass. ..
本発明の酵母培養用培地を用いることにより、酵母の培養効率を向上させて、培地の単位容量当たりの生菌数を増加させる(すなわち、培地の単位容量当たりの最大生菌数を増加させる)ことができる。例えば、後述する実施例に記載の方法で培養した場合、従来使用されているYM培地では、アステロトレメラ・ヒュミコラ(Asterotremella humicola)を24〜72時間培養しても、その生菌数は、4.3×108〜4.8×108CFU/mLである。一方、本発明の酵母培養用培地を用いることで、24時間程度培養すれば、アステロトレメラ・ヒュミコラ(Asterotremella humicola)を1.1×109CFU/mLまで増殖させることができる。 By using the yeast culture medium of the present invention, the yeast culture efficiency is improved and the viable cell count per unit volume of the medium is increased (that is, the maximum viable cell count per unit volume of the medium is increased). be able to. For example, when culturing by the method described in Examples described later, in the conventionally used YM medium, even if Asterotremella humicola is cultured for 24 to 72 hours, the viable cell count is 4. .3 × 10 8 to 4.8 × 10 8 CFU / mL. On the other hand, by using a medium for yeast cultures of the present invention, when cultured for about 24 hours, it can be grown Asuterotoremera & Humicola the (Asterotremella humicola) to 1.1 × 10 9 CFU / mL.
上述のとおり、本発明の酵母培養用培地は、従来の培地に比べて、酵母の培養効率を向上させて、培地の単位容量当たりの生菌数を増加させる(すなわち、培地の単位容量当たりの最大生菌数を増加させる)ことができる。そのため、本発明の一実施形態では、上記酵母培養用培地で酵母を培養することを有する、酵母の増殖を促進する方法が提供される。 As described above, the yeast culture medium of the present invention improves the yeast culture efficiency and increases the number of viable cells per unit volume of the medium (that is, per unit volume of the medium) as compared with the conventional medium. (Maximum viable cell count can be increased). Therefore, in one embodiment of the present invention, there is provided a method for promoting the growth of yeast, which comprises culturing yeast in the above-mentioned yeast culture medium.
本発明の効果を、以下の実施例および比較例を用いて説明する。ただし、本発明の技術的範囲が以下の実施例のみに制限されるわけではない。 The effects of the present invention will be described with reference to the following examples and comparative examples. However, the technical scope of the present invention is not limited to the following examples.
(酵母培養用培地の調製)
下記表1の組成となるように、各成分を蒸留水に溶解し、実施例の酵母培養用培地を調製した。なお、実施例の酵母培養用培地のpHは、調整していない。
(Preparation of yeast culture medium)
Each component was dissolved in distilled water so as to have the composition shown in Table 1 below, and the yeast culture medium of the example was prepared. The pH of the yeast culture medium of the examples was not adjusted.
下記表2の組成となるように、各成分を蒸留水に溶解し、YM培地(比較例)を調製した。YM培地のpHは、調整していない。 Each component was dissolved in distilled water to prepare a YM medium (comparative example) so as to have the composition shown in Table 2 below. The pH of the YM medium has not been adjusted.
(生菌製剤の調製)
アステロトレメラ・ヒュミコラ(Asterotremella humicola)2−141−1株(2018年2月21日付で、独立行政法人製品評価技術基盤機構 特許微生物寄託センター(千葉県木更津市かずさ鎌足2−5−8)に寄託されており、その受領番号は、NITE BP−02641である)を下記の液体培地に接種して、ジャーファーメンターにて30℃で48時間(撹拌速度:300rpm)培養し、培養液を得た。
(Preparation of live bacterial preparation)
Asterotremella humicola 2-141-1 strain (February 21, 2018, National Institute of Technology and Evaluation Patent Microorganisms Depositary Center (2-5-8 Kazusakamatari, Kisarazu City, Chiba Prefecture) (The receipt number is NITE BP-02641) is inoculated into the following liquid medium and cultured in a jar fermenter at 30 ° C. for 48 hours (stirring rate: 300 rpm) to prepare the culture solution. Obtained.
液体培地の作製方法:終濃度が0.18%(w/v)ポリペプトン、0.12%(w/v)肉エキス、0.07%(w/v)NaHCO3、0.005%(w/v)NaCl、0.002%(w/v)KCl、0.002%(w/v)CaCl2・2H2O、0.003%(w/v))MgSO4・7H2Oとなるように純水に溶解した。塩酸にてpH5に調整後、オートクレーブ滅菌したものを液体培地とした。 Method for preparing liquid medium: final concentration 0.18% (w / v) polypeptone, 0.12% (w / v) meat extract, 0.07% (w / v) NaCl 3 , 0.005% (w) /v)NaCl,0.002%(w/v)KCl,0.002%(w/v)CaCl 2 · 2H 2 O, a 0.003% (w / v)) MgSO 4 · 7H 2 O Soaked in pure water. After adjusting to pH 5 with hydrochloric acid, autoclave sterilized medium was used as a liquid medium.
得られた培養液を10分間遠心分離(×10,000g)し、菌体を回収した。得られた菌体に対して酵母を11重量%、トレハロースを14重量%、スキムミルクを3重量%(乳タンパク質としては1重量%)、グリシンを3重量%、MgSO4・7H2Oを1重量%、CaSO4・2H2Oを1質量%となるように蒸留水に添加し、混合して噴霧液を調製した。なお、乳タンパク質としては、固形分中にタンパク質を35重量%、乳糖を52重量%の割合で含むスキムミルクを用いた。 The obtained culture solution was centrifuged (× 10,000 g) for 10 minutes, and the cells were collected. The resulting 11 wt% of yeast with respect to cells, trehalose 14 weight%, the skim milk 3% (1% by weight as a milk protein), glycine 3 wt%, 1 weight MgSO 4 · 7H 2 O %, was added to distilled water to 1 mass% of CaSO 4 · 2H 2 O, was prepared by mixing the spray solution. As the milk protein, skim milk containing 35% by weight of protein and 52% by weight of lactose in the solid content was used.
流動層造粒機(FA−LAB−1、株式会社パウレック社)に300gの珪藻土(平均粒径75μm、嵩密度0.32g/ml、ラヂオライト(登録商標)♯3000、昭和化学工業株式会社)をセットした。珪藻土に対して、1077gの上記噴霧液を143g/分の速度で噴霧するとともに、40℃の温風を送風して内容物を流動させた状態で乾燥させた。噴霧後、引き続いて流動層造粒機内で40℃の温風を40分間送風して、造粒物を乾燥させた。これにより、生菌製剤を得た。生菌製剤の水分含量は5.5重量%であった。 300 g of diatomaceous earth (average particle size 75 μm, bulk density 0.32 g / ml, radiolite (registered trademark) # 3000, Showa Chemical Industry Co., Ltd.) in a fluidized bed granulator (FA-LAB-1, Paulec Co., Ltd.) Was set. 1077 g of the above spray liquid was sprayed on the diatomaceous earth at a rate of 143 g / min, and warm air at 40 ° C. was blown to dry the contents in a flowing state. After spraying, warm air at 40 ° C. was subsequently blown in the fluidized bed granulator for 40 minutes to dry the granulated product. As a result, a viable bacterial preparation was obtained. The water content of the viable bacterial preparation was 5.5% by weight.
(酵母の培養)
以下の方法により、酵母を培養した。
(1)500mLのトールビーカーに上記の酵母培養用培地またはYM培地を200mL分注した。
(2)(1)のトールビーカーに上記調製した生菌製剤を6mg(酵母:5.1×107CFU/L)添加した。
(3)生菌製剤を添加した後、(2)のトールビーカーを30℃、24時間で好気培養して、培養液を得た。
(Yeast culture)
Yeast was cultivated by the following method.
(1) 200 mL of the above yeast culture medium or YM medium was dispensed into a 500 mL tall beaker.
(2) the viable cell preparations prepared above tall beaker (1) 6 mg (Yeast: 5.1 × 10 7 CFU / L ) was added.
(3) After adding the viable cell preparation, the tall beaker of (2) was aerobically cultured at 30 ° C. for 24 hours to obtain a culture solution.
(酵母の生菌数の算出)
実施例および比較例において、培養開始から24時間ごとに培養液をサンプリングし、5% Tween80溶液で段階希釈し、寒天で固化させたNB培地の表面に塗布した。塗布後30℃で48時間培養して培地上に形成された2−141−1株のコロニーを測定した。結果を表3に示す。
(Calculation of viable yeast count)
In Examples and Comparative Examples, the culture broth was sampled every 24 hours from the start of the culture, serially diluted with a 5% Tween 80 solution, and applied to the surface of the NB medium solidified with agar. After application, the colonies of the 2-141-1 strain formed on the medium were measured by culturing at 30 ° C. for 48 hours. The results are shown in Table 3.
表3に示すように、実施例では、比較例と比べて、2−141−1株の培養効率を大幅に向上できることが分かる。 As shown in Table 3, it can be seen that in the examples, the culture efficiency of the 2-141-1 strain can be significantly improved as compared with the comparative examples.
Claims (10)
前記窒素源がグルタミン酸とグリシンとを含む、酵母培養用培地。 A yeast culture medium containing a carbon source, a nitrogen source and a magnesium source.
A medium for yeast culture in which the nitrogen source contains glutamic acid and glycine.
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