JP2596418B2 - Useful microorganism-containing granule and method for producing the same - Google Patents
Useful microorganism-containing granule and method for producing the sameInfo
- Publication number
- JP2596418B2 JP2596418B2 JP61205592A JP20559286A JP2596418B2 JP 2596418 B2 JP2596418 B2 JP 2596418B2 JP 61205592 A JP61205592 A JP 61205592A JP 20559286 A JP20559286 A JP 20559286A JP 2596418 B2 JP2596418 B2 JP 2596418B2
- Authority
- JP
- Japan
- Prior art keywords
- granulation
- granules
- cells
- powder
- binder
- 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.)
- Expired - Lifetime
Links
Landscapes
- Dairy Products (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Medicines That Contain Protein Lipid Enzymes And Other Medicines (AREA)
- Agricultural Chemicals And Associated Chemicals (AREA)
Description
【発明の詳細な説明】 [産業上の利用分野] この発明は造粒時の死滅が少なく、かつ保存安定性の
向上した有用微生物含有粒剤およびその製造方法に関す
る。Description: FIELD OF THE INVENTION The present invention relates to a useful microorganism-containing granule which is less killed during granulation and has improved storage stability, and a method for producing the same.
[従来の技術] 酵母、細菌等の有用な微生物は、乳製品、醸造製品等
の食品、乳酸菌製剤、整腸剤等の医薬品あるいは微生物
農薬等に広く利用することができる。[Prior Art] Useful microorganisms such as yeast and bacteria can be widely used in foods such as dairy products and brewed products, lactic acid bacteria preparations, pharmaceuticals such as intestinal medicines, and microbial pesticides.
微生物は、一般に熱に弱く、また水の存在下で失活し
やすいが、乾燥条件下では長期間保存することができる
ので、従来培養液から分離した菌体を、そのままあるい
はこれにでん粉、乳糖、蛋白質、または有機あるいは無
機塩類を加え、低温通気乾燥、真空乾燥あるいは凍結乾
燥して、含水率が10%以下の菌体あるいは菌体含有粉末
として調製されている。Microorganisms are generally vulnerable to heat and are easily deactivated in the presence of water.However, they can be stored for a long time under dry conditions. , Protein, or organic or inorganic salts, and dried at low temperature through aeration, vacuum drying or freeze-drying to prepare cells having a water content of 10% or less or cell-containing powder.
このようにして得られた乾燥菌体は粉末であるため、 (i)表面積が大きく、従って空気との接触面積が大き
くなるため吸湿しやすく、開放系での取扱いに難点があ
ること、 (ii)吸湿姓が大きいため、長期保存する際は、湿気の
遮断によほど注意しないと菌体が死滅してしまうこと、 (iii)粉末状であるため、取扱い時に粉が舞い環境を
汚染し、また工業的に取扱う際にもブリッジングを起こ
しトラブルの原因となること、 (iv)食品等に添加する際に、まま粉になりやすく、取
扱いにくいこと、 (v)医薬等で分包剤の場合に粉末であると全量の取出
しが不便であること、 のような問題点を有する。Since the dry cells obtained in this manner are powder, (i) the surface area is large, and therefore the contact area with air is large, so that it is easy to absorb moisture, and there is a problem in handling in an open system. (Ii) ) Due to its large hygroscopic property, the cells can die if care is taken not to block the moisture during long-term storage. (Iii) Since the powder is in the form of powder, the powder will flutter during handling and contaminate the environment. Causing bridging during industrial handling, causing trouble; (iv) easy to become powder and difficult to handle when added to food, etc .; In the case of powder, it is inconvenient to take out the whole amount, and there are problems such as:
[発明が解決しようとする問題点] そこで、微生物菌体粉末を取扱いやすい顆粒剤に造粒
する方法が種々提案されている。[Problems to be Solved by the Invention] Therefore, various methods for granulating microbial cell powder into granules that are easy to handle have been proposed.
例えば、含水率4%以下のでん粉およびでん粉加水分
解物または蛋白質の1種または2種以上の打錠用基礎配
合物と凍結乾燥したビフィズス菌を混合し、打錠してビ
フィズス菌含有錠菓を製造する方法(特公昭58−46293
号)、菌体と生でん粉を混合し、凍結乾燥する方法(特
開昭58−14967号)、菌体を海藻ゲルで包括し、菌体含
有粒子ゲルを作る方法(特開昭57−186446号)、乳酸菌
とクロレラ乾燥粉末を濾過層として吸引濾過して得た乳
酸菌を10%ゼラチン溶液中に溶解した後、クロレラ乾燥
粉末中に噴霧した後50〜60#の顆粒状乳酸菌−クロレラ
混合物を製造する方法(特開昭53−99371号)、生菌体
と保護膜形成溶液を混合し、凝固用塩類溶液に注入して
ゲル化包括し、造粒する方法(特開昭60−141281号)が
あるが、これらの方法では、打錠法以外は、いずれも水
系で造粒するものであるため、取扱い時に菌体の死滅率
が大きく効率が悪い。For example, starch and a starch hydrolyzate having a water content of 4% or less, one or two or more basic blends for tableting of protein and a freeze-dried bifidobacterium are mixed, and the mixture is tabletted to give a bifidobacterium-containing tablet confection. Production method (Japanese Patent Publication No. 58-46293)
No.), a method of mixing cells and raw starch and freeze-drying (Japanese Patent Application Laid-Open No. 58-14967), a method of encapsulating the cells in a seaweed gel and producing a cell-containing particle gel (Japanese Patent Application Laid-Open No. 57-186446). No.), lactic acid bacteria obtained by suction filtration of lactic acid bacteria and chlorella dry powder as a filtration layer were dissolved in a 10% gelatin solution, then sprayed into chlorella dry powder, and then a 50-60 # granular lactic acid bacteria-chlorella mixture was obtained. Production method (JP-A-53-99371), a method of mixing viable cells and a protective film-forming solution, injecting into a salt solution for coagulation, gelling and covering, and granulating (JP-A-60-141281) However, in all of these methods, except for the tableting method, granulation is carried out in an aqueous system, so that the mortality of the bacterial cells during handling is large and the efficiency is low.
すなわち、水系で造粒すると、 (1)バインダーは水に可溶な物質を用いるため、親水
性で、造粒後の吸水性、吸湿性が高いこと、 (2)最終的に水を蒸発させるため、水と熱に弱い菌に
適用しにくいこと、 (3)水が蒸発した分だけ粒剤中にポアーが生成し、比
表面積が大きく吸湿しやすいこと、 などの問題点を有している。That is, when granulated in an aqueous system, (1) since the binder uses a water-soluble substance, it is hydrophilic and has high water absorption and hygroscopicity after granulation, and (2) finally evaporates water. Therefore, it is difficult to apply to bacteria that are sensitive to water and heat, and (3) pores are formed in the granules due to the evaporation of water, the specific surface area is large, and moisture is easily absorbed. .
また打錠法においても、本質的に粉体の表面積を改良
できないため保存安定性が悪いことの問題がある。これ
らの問題を解決するためには、非水系で造粒することが
考えられるが、非水系で造粒する方法としては、芯材成
分にバインダーと菌体成分をコーティングする流動造粒
法が提案されているが(特開昭60−221078号)、この方
法では粒剤の中心部に芯材があるため単位重量当り菌数
の少ない粒剤しか得られず、また菌体が粒剤の表面に存
在するため湿度の影響を受けやすく保存安定性が充分で
なく、商品価値は少ない。Also in the tableting method, there is a problem that storage stability is poor because the surface area of the powder cannot be essentially improved. In order to solve these problems, it is conceivable to granulate with a non-aqueous system, but as a method of granulating with a non-aqueous system, a fluid granulation method in which a core component is coated with a binder and a cell component is proposed. However, according to this method, only a granule having a small number of bacteria per unit weight can be obtained due to the presence of a core material in the center of the granule. , It is easily affected by humidity, storage stability is not sufficient, and its commercial value is low.
また、芯材を使うため粒径が大きいものしかできず、
1.0mmφ以下のものを作ることは困難である。In addition, since the core material is used, only those with a large particle size can be made,
It is difficult to make things less than 1.0mmφ.
従って、本発明の目的は、有用微生物含有粒剤におけ
る前記の問題点を解決し、菌体または菌体含有物粉末を
造粒するに際し、失活をできるだけ抑え、適当な強度を
保ち、貯蔵、運搬、使用時に破砕されにくく、かつ吸湿
性が少なく保存時の失活が少ない有用微生物含有粒剤お
よびその製造方法を提供することにある。Accordingly, an object of the present invention is to solve the above-mentioned problems in useful microorganism-containing granules, and to suppress inactivation as much as possible when granulating cells or a cell-containing material powder, maintain appropriate strength, and store, An object of the present invention is to provide a useful microorganism-containing granule which is hardly crushed during transportation and use, has low hygroscopicity, and has little deactivation during storage, and a method for producing the same.
[問題点を解決するための手段] 本発明は、有用微生物菌体またはその含有物の粉体
に、融点35〜100℃のバインダー物質を加熱溶融させな
がら粒剤組成物の全重量を基準として10〜50重量%の範
囲で添加し、非水系で攪拌造粒することを特徴とする有
用微生物含有粒剤の製造方法、および前記方法によって
得られる、菌体を粒剤中に実質的に均一に含有すること
を特徴とする有用微生物含有粒剤を提供したものであ
る。[Means for Solving the Problems] The present invention is based on the total weight of the granule composition while heating and melting a binder substance having a melting point of 35 to 100 ° C. to a powder of useful microbial cells or a substance thereof. A method for producing useful microorganism-containing granules, characterized in that the granules are added in the range of 10 to 50% by weight and are stirred and granulated in a non-aqueous system, and the cells obtained by the method are substantially uniform in the granules. The present invention provides a useful microorganism-containing granule characterized in that the granule is contained in a granule.
本発明で造粒の対象となる微生物はいかなる菌体でも
よいが、熱や水分に弱く、保存に難点のある菌体の場合
に特に本発明の特色が生かされる。Microorganisms to be granulated in the present invention may be any cells, but the characteristics of the present invention are particularly useful in the case of cells that are vulnerable to heat and moisture and have difficulty in storage.
例えば、各種プロテアーゼ(低温活性のAPI−21、レ
ンネット等)やリパーゼ、アミラーゼ、セルラーゼ、ペ
クチナーゼ等の有用酵素を生産するBacilles、M.Pusill
us、Asp.niger等の菌体、酒、みそ、しょう油、納豆な
どの醸造分野で使用される各種細菌や酵母類(Sacch.ce
revisiae,Asp.Oryzae,Asp.tamarii,Sacch.rouxii,Bac.n
atto,Bac.Subtillus,Asp.sojae,Acetobacter等)、乳酸
菌やビフィズス菌であるMicococcus属、Streptococcus
属、Pediococcus属、Leuconotoc属、Lactobacillus属、
Bifidobacterium属に属する菌体等が挙げられる。For example, Bacilles, M. Pusill, which produces various proteases (low-temperature active API-21, rennet, etc.) and useful enzymes such as lipase, amylase, cellulase, pectinase, etc.
us, Asp.niger, etc., various bacteria and yeasts (Sacch.ce) used in the brewing field such as sake, miso, soy sauce, natto, etc.
revisiae, Asp.Oryzae, Asp.tamarii, Sacch.rouxii, Bac.n
Atto, Bac. Subtillus, Asp. sojae, Acetobacter, etc.), lactic acid bacteria and bifidobacteria Micococcus genus, Streptococcus
Genus, Pediococcus, Leuconotoc, Lactobacillus,
Bacteria belonging to the genus Bifidobacterium are exemplified.
これらの菌体は、培養液から分離し、そのまま低温通
気乾燥、真空乾燥または凍結乾燥した粉末状態または分
離菌体にでん粉、乳糖、蛋白質あるいは塩類を加えて同
様に乾燥した菌体含有物粉末状態のものが使用される。These cells are separated from the culture solution and dried as they are under low-temperature air-drying, vacuum-dried or freeze-dried, or powdered cells containing starch, lactose, proteins or salts added to the separated cells and dried in the same manner. Is used.
非水系で造粒する方法にも種々考えられ、バインダー
ワックスを有機溶媒に溶解して造粒する方法があるが、
この方法では水系と同様、ポアー率が大で粒剤の物性が
改善されず、又溶媒に対する菌体の影響も大きい。これ
に比較すると溶媒を使わず、バインダーの融点以上に加
熱して造粒する本法は、ポアー率も0.1cc/g以下と小さ
く、溶媒の影響もなく最も良好であることを見いだし
た。There are various methods of granulating in a non-aqueous system, and there is a method of granulating by dissolving a binder wax in an organic solvent,
In this method, as in the case of the aqueous system, the pore rate is large, the physical properties of the granules are not improved, and the influence of the cells on the solvent is large. In comparison with this, it was found that this method of granulating by heating at a temperature higher than the melting point of the binder without using a solvent had a pore rate as small as 0.1 cc / g or less and was the best without the influence of the solvent.
造粒時のバインダー物質としては通常下記のようなワ
ックス状の物質が使用される。As the binder substance at the time of granulation, the following wax-like substances are usually used.
(1)動物性または植物性のワックス、例えば牛脂、ラ
イスワックス、木ロウ、密ロウ、キャンデリラワック
ス、カルナウバワックス、ラノリンその他天然系油脂
類、 (2)ショ糖エステル、グリセリン脂肪酸モノ(ジ、ト
リ)エステル、プロピレングリコール脂肪酸(PG)エス
テル、ソルビタン脂肪酸エステル等、 (3)合成高分子で前記(1)、(2)と同様にワック
ス状の性質を有するもの、例えばセルロース誘導体:ベ
ンジルアミノメチルセルロース、ジメチルアミノメチル
セルロース、ピペリジルエチルヒドロキシエチルセルロ
ース、セルロースアセテートジエチルアミノアセテー
ト、セルロースアセテートジブチルアミノヒドロキシプ
ロピルエーテル等;ポリビニル誘導体:ビニルジエチル
アミン−ビニルアセテートコポリマー、ビニルベンジル
アミン−ビニルアセテートコポリマー、ポリビニルジエ
チルアミノアセトアセタール、ビニルピペリジルアセト
アセタール−ビニルアセテートコポリマー、ポリビニル
アセタールジエチルアミノアセテート、ポリジメチルア
ミノエチルメタクリレート、ポリジエチルアミノメチル
スチレン、ポリビニルエチルピリジン、ビニルエチルピ
リジン−スチレンコポリマー、ビニルエチルピリジン−
アクリロニトリルコポリマー、メチルビニルピリジン−
アクリロニトリルコポリマー、メチルビニルピリジン−
スチレンコポリマー等。(1) Animal or vegetable waxes such as beef tallow, rice wax, wood wax, beeswax, candelilla wax, carnauba wax, lanolin and other natural fats and oils, (2) sucrose esters, glycerin fatty acid mono (di (3) synthetic polymers having wax-like properties as in the above (1) and (2), such as cellulose derivatives: benzylamino, etc., tri) esters, propylene glycol fatty acid (PG) esters, sorbitan fatty acid esters, etc. Methylcellulose, dimethylaminomethylcellulose, piperidylethylhydroxyethylcellulose, cellulose acetate diethylaminoacetate, cellulose acetate dibutylaminohydroxypropyl ether, etc .; polyvinyl derivative: vinyl diethylamine-vinyl acetate copolymer , Vinylbenzylamine-vinyl acetate copolymer, polyvinyldiethylaminoacetoacetal, vinylpiperidylacetoacetal-vinylacetate copolymer, polyvinylacetal diethylaminoacetate, polydimethylaminoethyl methacrylate, polydiethylaminomethylstyrene, polyvinylethylpyridine, vinylethylpyridine-styrene copolymer, Vinylethylpyridine-
Acrylonitrile copolymer, methylvinylpyridine-
Acrylonitrile copolymer, methylvinylpyridine-
Styrene copolymer and the like.
本発明で使用するバインダー物質は、融点が100℃以
下、好ましくは40〜60℃のものが適しており、菌体に影
響を与えないものの中から、最終的な使用目的に応じて
最適なものを選択する。The binder material used in the present invention has a melting point of 100 ° C. or less, preferably 40 to 60 ° C., and among those that do not affect the cells, those that are optimal according to the ultimate purpose of use. Select
例えば、乳酸菌やビフィズス菌のように食品添加物と
して使用する場合には、食添用として許可されているも
のの中から選択する必要があり、ショ糖エステル、グリ
セリン脂肪酸エステル、PGエステル、ソルビタン脂肪酸
エステルや天然油脂系のものから選ばれた1種または2
種以上の混合物が使用される。For example, when used as a food additive, such as lactic acid bacteria and bifidobacteria, it is necessary to select from those permitted for food use, such as sucrose esters, glycerin fatty acid esters, PG esters, and sorbitan fatty acid esters. Or one selected from natural oils and fats
Mixtures of more than one species are used.
最終製品の粒剤を長期保存し、安定に保つためには、
吸湿性が小さいほど安定であるので、疎水性部分の割合
が大きいワックス物質を選択すべきであるが、この点か
らは例えば高脂肪酸ショ糖エステル,ソルビタン高脂肪
酸エステル,ライスワックス等が好ましい。To keep the granules of the final product stable for a long time,
Since the smaller the hygroscopicity, the more stable the wax material should be selected because the ratio of the hydrophobic portion is large. From this viewpoint, for example, high fatty acid sucrose ester, sorbitan high fatty acid ester, rice wax and the like are preferable.
本発明では、所望より粒剤中の生菌数を一定に保つた
めの増量剤等の添加剤を造粒時に使用することができ
る。このような添加剤としては、菌体に影響を与えず、
かつ最終目的に合ったもの、例えばでん粉、蛋白質、グ
ルコース、乳糖、無機塩類(Na2SO4等)、有機塩類など
が適宜使用される。In the present invention, an additive such as a bulking agent for keeping the number of viable bacteria in the granules constant can be used at the time of granulation, if desired. Such additives do not affect the cells,
What is suitable for the final purpose, for example, starch, protein, glucose, lactose, inorganic salts (such as Na 2 SO 4 ), and organic salts are appropriately used.
バインダー物質(ワックス)の添加量は造粒しようと
する菌体の物性によって著しく異なるので、最適添加量
はそれぞれの場合について決める必要があるが、通常全
造粒物に対して10〜50重量%の範囲が適当であり、好ま
しくは15〜30重量%が良好である。10重量%以下では造
粒が殆ど不可能であり、一方50重量%以上では造粒時の
大粒化が早く、造粒効率が悪く、また粒剤の物性も好ま
しくない。Since the amount of the binder substance (wax) to be added greatly depends on the physical properties of the cells to be granulated, the optimum amount of addition must be determined for each case. Is appropriate, and preferably 15 to 30% by weight. If it is less than 10% by weight, granulation is almost impossible, while if it is more than 50% by weight, granulation at the time of granulation is quick, the granulation efficiency is poor, and the physical properties of the granules are also unfavorable.
本発明では、前記の乾燥菌体あるいは菌体含有物粉
末、バインダー物質および所望の場合には他の添加剤を
非水系で造粒する。In the present invention, the above-mentioned dried cells or the cell-containing powder, the binder substance and, if desired, other additives are granulated in a non-aqueous system.
造粒法としては転動造粒、流動造粒、押し出し造粒、
スプレー造粒、撹拌造粒などが考えられるが、 (1)転動造粒では前記のように芯材を使うため菌濃
度、粒径、保存安定性に問題があること、 (2)流動造粒では、ポアー率が大きい、強度が弱い、
その他(1)と同様の問題があり、 (3)押し出し造粒では、多量のワックスが必要であ
り、ポアー率が大きく、形状として小さいものはできな
いこと、 (4)スプレー造粒では、溶解したワックスに均一に分
散させることが困難であり、分散に時間がかかり、また
装置が大きいこと、 など欠点を有している。Rolling granulation, fluidized granulation, extrusion granulation,
Spray granulation, stirring granulation, etc. are conceivable. (1) In rolling granulation, the core material is used as described above, so there are problems with the bacterial concentration, particle size, storage stability, and (2) fluidized granulation. In the grains, the pore rate is large, the strength is weak,
Others have the same problems as (1). (3) Extrusion granulation requires a large amount of wax, large pore ratio and small shape cannot be used. (4) Spray granulation dissolves. It is difficult to uniformly disperse the wax in the wax, it takes a long time to disperse the wax, and the apparatus is large.
これらに比較し、溶剤を使わない撹拌造粒法のみがこ
れらの欠点を克服できることを見いだした。In comparison, it has been found that only the stirring granulation method without using a solvent can overcome these disadvantages.
造粒機としては通常撹拌型で、使用するワックスの融
点以上の温度に保持できるように、温水、スチーム、電
熱等によって加熱できる構造のものを使用する。As the granulator, a granulator having a structure which can be heated by hot water, steam, electric heat or the like so as to be maintained at a temperature not lower than the melting point of the wax to be used is used.
ワックスの添加法としては、造粒する菌体粉末と同時
に粉末状で造粒機に添加する方法、造粒時に予め溶融し
たワックスを添加する方法のいずれでも造粒できるが、
できるだけ短時間で造粒し菌体の死滅を防ぐためには溶
融したワックスをスプレー状態で添加する方法が好まし
い。As a method of adding the wax, any of a method of adding the powder to the granulator in the form of powder at the same time as the cell powder to be granulated, and a method of adding a wax previously melted at the time of granulation can be granulated,
In order to granulate in as short a time as possible and to prevent the death of the cells, it is preferable to add a molten wax in a spray state.
造粒時の温度はバインダーとして用いるワックス状物
質の融点以上、好ましくは融点+5℃の範囲の温度であ
り、このような温度条件下で通常5〜30分間の短時間で
所望の粒径範囲の粒剤を得ることができる。The temperature at the time of granulation is a temperature higher than the melting point of the wax-like substance used as the binder, preferably in the range of the melting point + 5 ° C. Granules can be obtained.
[発明の効果] 本発明によれば、 (1)非水系で低温で造粒するので、造粒時に水および
熱の作用で失活するこがないこと、 (2)得られた粒剤は有用微生物を実質的に均一にバイ
ンダー中に含む構造のため高菌数の粒剤を作ることが可
能であり、また強度も強いこと、 (3)形状は球形に近く、流動性が著しく良好であるこ
と、 (4)バインダーワックスが表面に層を形成する為、表
面にポアーが少なく、吸湿性が改善され、保存時の失活
が少ないこと、 (5)球形に近い形状のため、造粒の最終工程で造粒に
用いたバインダーまたは他のバインダーを容易にコーテ
ィングすることができ、表面に緻密な表皮を持たせた構
造とすることができ、一層保存安定性を向上できるこ
と、 (6)球形で流動性に優れているため、粒剤を他の製品
に混入させる場合に、まま粉になったり、ブリッジング
を起こす可能性がなく、取扱い性が著しく改善されるこ
と、 (7)溶媒(水又は有機溶媒)を使用しないため、溶媒
除去が不用で、プロセスが簡単であること等の優れた効
果が得られる。[Effects of the Invention] According to the present invention, (1) since granulation is performed at a low temperature in a non-aqueous system, there is no inactivation due to the action of water and heat during granulation. (2) The obtained granules are It has a structure that contains useful microorganisms substantially uniformly in the binder, so that it is possible to produce granules with a high number of bacteria, and that it has high strength. (3) The shape is nearly spherical, and the flowability is remarkably good. (4) Since the binder wax forms a layer on the surface, there are few pores on the surface, the hygroscopicity is improved, and there is little deactivation during storage. (5) Granulation due to its nearly spherical shape. (6) that the binder used for granulation or other binder used in the final step can be easily coated, a structure having a dense skin on the surface can be obtained, and the storage stability can be further improved. Because of its spherical shape and excellent fluidity, granules can be used for other products. When mixed with water, there is no possibility of powdering or bridging, and the handling is significantly improved. (7) Since no solvent (water or organic solvent) is used, solvent removal is unnecessary. Excellent effects such as simple process can be obtained.
[実施例] 以下、実施例および比較例を挙げて本発明を説明す
る。[Examples] Hereinafter, the present invention will be described with reference to Examples and Comparative Examples.
実施例1〜5 Lactobacillus属に属する乳酸菌を、でん粉、乳酸等
で希釈し、菌体量を3×1010個/gに調製した乳酸菌含有
物に、表1に示す割合のバインダー(ショ糖エステル−
モノグリセリド及びライスワックス)および増量剤(Na
2SO4)を添加して50〜70℃の温度(実施例1〜5)で造
粒し、生菌残存率を常法により測定して表1に示す結果
を得た。また実施例1、2、4、5で得られた造粒品を
室温および35℃で保存し生菌残存率を測定したところ、
表2に示すように長期間安定保存できることが明らかに
なった。Examples 1 to 5 A lactic acid bacterium belonging to the genus Lactobacillus was diluted with starch, lactic acid, or the like, and a lactic acid bacterium-containing material prepared at a cell amount of 3 × 10 10 cells / g was mixed with a binder (sucrose ester) having a ratio shown in Table 1. −
Monoglycerides and rice waxes) and bulking agents (Na
2 SO 4 ) was added and granulated at a temperature of 50 to 70 ° C. (Examples 1 to 5), and the viable cell remaining ratio was measured by a conventional method to obtain the results shown in Table 1. When the granules obtained in Examples 1, 2, 4, and 5 were stored at room temperature and 35 ° C., and the viable cell survival rate was measured,
As shown in Table 2, it was clarified that long-term stable storage was possible.
実施例6〜8 Bifidobacterium属に属するビフィズス菌を1×109個
/g含有するよう調製された原末を用いて、表1に示す割
合のバインダー(ショ糖エステル−ソルビタンエステル
−グリセリンエステル、ライスワックス)および増量剤
(Na2SO4、グルコース)を添加して55〜70℃の温度で造
粒し、生菌残存率を測定して表1に示す結果を得た。ま
たこれら3種類の造粒品について前記実施例1〜5と同
様に保存安定性テストを行ったところ良好な結果が得ら
れた。Examples 6 to 8 1 × 10 9 Bifidobacterium belonging to the genus Bifidobacterium
/ g of the bulk powder prepared so as to contain the binder (sucrose ester-sorbitan ester-glycerin ester, rice wax) and a bulking agent (Na 2 SO 4 , glucose) in the proportions shown in Table 1. Granulation was performed at a temperature of 55 to 70 ° C., and the viable cell remaining ratio was measured to obtain the results shown in Table 1. When a storage stability test was performed on these three types of granulated products in the same manner as in Examples 1 to 5, good results were obtained.
比較例1〜2 実施例1〜5と同じ菌体含有物に20%グルコース水溶
液および増量剤(Na2SO4)を表1に示す割合で加えて、
室温で撹拌造粒し、生菌残存率を測定したところ、表1
に示すように極めて低い値しか得られなかった。Comparative Examples 1-2 Examples 1-5 and in the same cell-containing material 20% aqueous solution of glucose and bulking agent (Na 2 SO 4) and added in the proportions shown in Table 1,
The mixture was stirred and granulated at room temperature, and the viable cell remaining ratio was measured.
As shown in the figure, only extremely low values were obtained.
フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C12R 1:225) (C12N 1/20 C12R 1:01) Continued on the front page (51) Int.Cl. 6 Identification number Agency reference number FI Technical indication C12R 1: 225) (C12N 1/20 C12R 1:01)
Claims (5)
に、融点35〜100℃のバインダー物質を加熱溶融させな
がら粒剤組成物の全重量を基準として10〜50重量%の範
囲で添加し、非水系で攪拌造粒することを特徴とする有
用微生物含有粒剤の製造方法。1. A method for adding a binder material having a melting point of 35 to 100 ° C. to a powder of useful microbial cells or a substance containing the same in an amount of 10 to 50% by weight based on the total weight of the granule composition. And a method for producing useful microorganism-containing granules, wherein the granules are stirred and granulated in a non-aqueous system.
量が粒剤組成物の全重量を基準として30重量%以上であ
る特許請求の範囲第1項に記載の製造方法。2. The method according to claim 1, wherein the amount of the powder of the useful microorganism cells or the content thereof is 30% by weight or more based on the total weight of the granule composition.
造粒温度がワックス状物質の融点以上の温度である特許
請求の範囲第1項に記載の製造方法。3. The binder material is a waxy material,
2. The method according to claim 1, wherein the granulation temperature is equal to or higher than the melting point of the wax-like substance.
または異なるバインダーを粒剤表面にコーティングする
特許請求の範囲第1項に記載の製造方法。4. The method according to claim 1, wherein the surface of the granule is coated with a binder used for granulation in the final step of granulation or a different binder.
に、融点35〜100℃のバインダー物質を加熱溶融させな
がら粒剤組成物の全重量を基準として10〜50重量%の範
囲で添加し、非水系で攪拌造粒して得られる、菌体を実
質的に粒剤中に均一に含有することを特徴とする有用微
生物含有粒剤。5. A method for adding a binder material having a melting point of 35 to 100 ° C. to a powder of useful microbial cells or a substance containing the same in an amount of 10 to 50% by weight based on the total weight of the granule composition. And useful microorganism-containing granules obtained by stirring and granulating in a non-aqueous system, wherein the granules substantially uniformly contain bacterial cells in the granules.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61205592A JP2596418B2 (en) | 1986-09-01 | 1986-09-01 | Useful microorganism-containing granule and method for producing the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61205592A JP2596418B2 (en) | 1986-09-01 | 1986-09-01 | Useful microorganism-containing granule and method for producing the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6363373A JPS6363373A (en) | 1988-03-19 |
JP2596418B2 true JP2596418B2 (en) | 1997-04-02 |
Family
ID=16509433
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61205592A Expired - Lifetime JP2596418B2 (en) | 1986-09-01 | 1986-09-01 | Useful microorganism-containing granule and method for producing the same |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2596418B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020196844A1 (en) | 2019-03-28 | 2020-10-01 | 森永乳業株式会社 | Heat-resistant bacterium composition |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2714681B2 (en) * | 1989-02-10 | 1998-02-16 | 昭和電工株式会社 | Control agent for soil disease and method for preventing soil disease |
US5288488A (en) * | 1990-02-23 | 1994-02-22 | Auburn University | Method of controlling foliar microorganism populations |
FR2863828B1 (en) * | 2003-12-23 | 2007-02-02 | Gervais Danone Sa | LIQUID FOOD PRODUCT COMPRISING PELLETS OF LACTIC ACID BACTERIA |
EP2223600A1 (en) * | 2009-02-19 | 2010-09-01 | Urea Casale S.A. | Granules containing filamentary fungi and method of preparation thereof |
JP7384347B2 (en) * | 2017-10-27 | 2023-11-21 | クミアイ化学工業株式会社 | Microbial freeze-dried composition |
CN114940785B (en) * | 2022-05-20 | 2023-05-26 | 万华化学集团股份有限公司 | High-rigidity scratch-resistant antibacterial polyethylene film and preparation method thereof |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5732221A (en) * | 1980-08-05 | 1982-02-20 | Morinaga & Co Ltd | Preparation of tablet confection containing lactobacillus bifidus |
JPS5733543A (en) * | 1980-08-06 | 1982-02-23 | Lotte Co Ltd | Oil or fat containing lactobacillus bifidus |
JPS60221078A (en) * | 1984-04-18 | 1985-11-05 | Morinaga Milk Ind Co Ltd | Granular product of useful microorganism powder and its preparation |
-
1986
- 1986-09-01 JP JP61205592A patent/JP2596418B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020196844A1 (en) | 2019-03-28 | 2020-10-01 | 森永乳業株式会社 | Heat-resistant bacterium composition |
Also Published As
Publication number | Publication date |
---|---|
JPS6363373A (en) | 1988-03-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6229188B2 (en) | Stabilized composition for biomaterials | |
US4888171A (en) | Granular product of dried microorganism cells and manufacturing method therefor | |
US6306427B1 (en) | Pellets containing active ingredients protected against degradation in the rumen of ruminants | |
EP1812025B1 (en) | Stabilized bacteriophage formulations | |
CN1036923C (en) | Desiccant, dehydration therewith, and dehydrated product obtainable threby | |
CN102482635B (en) | Coated dehydrated microorganism with enhancing stability and viability | |
BRPI1013809B1 (en) | dry, stable powder composition, comprising biologically active microorganisms and / or bioactive materials and methods of manufacturing the same | |
BRPI0207372B1 (en) | Process for obtaining a dry, low water consuming consumable product comprising fresh probiotics | |
CA2586619A1 (en) | Bacteriophage compositions | |
JPH0710344B2 (en) | Method for dehydrating hydrated substance by anhydrous glycosyl fructose | |
AU2017219895A1 (en) | Stabilizing methods for coating seeds with biological materials | |
JP2596418B2 (en) | Useful microorganism-containing granule and method for producing the same | |
Harel et al. | Protection and delivery of probiotics for use in foods | |
JP2968089B2 (en) | Coating material and enteric-coated granules using the same | |
JPS594976B2 (en) | Method for producing chewing gum containing Bifidobacterium | |
EP2968579B1 (en) | Stable bioactive substances and methods of making | |
WO2019144979A1 (en) | Method for granulating and coating probiotics and granulated core obtained using same | |
EP1213347A1 (en) | A method for preserving cells by processing the same into dry products | |
JP3202053B2 (en) | Enteric granules | |
JPH0761255B2 (en) | Method for producing stabilized spore-forming viable cell preparation | |
JPH06133735A (en) | Enteric-coated lactobacillus granule | |
JP2857885B2 (en) | Manufacturing method of granulated powder | |
JPH0367552A (en) | Stable spore-forming variable cell drug, production thereof and pellet | |
JPH07236430A (en) | Rumen by-pass preparation of for ruminant, capable of being pelletized | |
JP2001501084A (en) | Method for producing solid objects and uses of such objects |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |