JPS6363373A - Granule containing useful microorganism and production thereof - Google Patents
Granule containing useful microorganism and production thereofInfo
- Publication number
- JPS6363373A JPS6363373A JP61205592A JP20559286A JPS6363373A JP S6363373 A JPS6363373 A JP S6363373A JP 61205592 A JP61205592 A JP 61205592A JP 20559286 A JP20559286 A JP 20559286A JP S6363373 A JPS6363373 A JP S6363373A
- Authority
- JP
- Japan
- Prior art keywords
- binder
- granulation
- melting point
- granulated
- mold
- 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
Links
- 239000008187 granular material Substances 0.000 title claims abstract description 30
- 244000005700 microbiome Species 0.000 title claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 239000011230 binding agent Substances 0.000 claims abstract description 28
- 239000000843 powder Substances 0.000 claims abstract description 22
- 238000002844 melting Methods 0.000 claims abstract description 15
- 230000008018 melting Effects 0.000 claims abstract description 15
- 238000010438 heat treatment Methods 0.000 claims abstract description 5
- 238000003756 stirring Methods 0.000 claims abstract description 5
- 238000005469 granulation Methods 0.000 claims description 33
- 230000003179 granulation Effects 0.000 claims description 33
- 230000001580 bacterial effect Effects 0.000 claims description 23
- 239000000126 substance Substances 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 6
- 238000013019 agitation Methods 0.000 claims description 3
- 241000894006 Bacteria Species 0.000 abstract description 21
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 abstract description 18
- 238000000034 method Methods 0.000 abstract description 18
- -1 fatty acid ester Chemical class 0.000 abstract description 15
- 239000004310 lactic acid Substances 0.000 abstract description 9
- 235000014655 lactic acid Nutrition 0.000 abstract description 9
- 235000014113 dietary fatty acids Nutrition 0.000 abstract description 8
- 229930195729 fatty acid Natural products 0.000 abstract description 8
- 239000000194 fatty acid Substances 0.000 abstract description 8
- 229930006000 Sucrose Natural products 0.000 abstract description 5
- 239000000203 mixture Substances 0.000 abstract description 5
- 239000005720 sucrose Substances 0.000 abstract description 5
- 240000004808 Saccharomyces cerevisiae Species 0.000 abstract description 3
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose 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)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 abstract description 3
- 230000006378 damage Effects 0.000 abstract 1
- 239000000155 melt Substances 0.000 abstract 1
- 239000001993 wax Substances 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 230000000813 microbial effect Effects 0.000 description 8
- 238000003860 storage Methods 0.000 description 8
- 229920001577 copolymer Polymers 0.000 description 7
- 241000186000 Bifidobacterium Species 0.000 description 6
- 229920002472 Starch Polymers 0.000 description 6
- 239000002904 solvent Substances 0.000 description 6
- 239000008107 starch Substances 0.000 description 6
- 235000019698 starch Nutrition 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- 241000209094 Oryza Species 0.000 description 4
- 235000007164 Oryza sativa Nutrition 0.000 description 4
- 150000002148 esters Chemical class 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 108090000623 proteins and genes Proteins 0.000 description 4
- 102000004169 proteins and genes Human genes 0.000 description 4
- 235000009566 rice Nutrition 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- 230000004083 survival effect Effects 0.000 description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 3
- GUBGYTABKSRVRQ-QKKXKWKRSA-N Lactose Natural products OC[C@H]1O[C@@H](O[C@H]2[C@H](O)[C@@H](O)C(O)O[C@@H]2CO)[C@H](O)[C@@H](O)[C@H]1O GUBGYTABKSRVRQ-QKKXKWKRSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 239000011162 core material Substances 0.000 description 3
- 230000009849 deactivation Effects 0.000 description 3
- 239000000499 gel Substances 0.000 description 3
- 239000008103 glucose Substances 0.000 description 3
- 239000008101 lactose Substances 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- 229920002554 vinyl polymer Polymers 0.000 description 3
- 241000195649 Chlorella <Chlorellales> Species 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerol Natural products OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000004067 bulking agent Substances 0.000 description 2
- 229920002301 cellulose acetate Polymers 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 235000013305 food Nutrition 0.000 description 2
- 235000013373 food additive Nutrition 0.000 description 2
- 239000002778 food additive Substances 0.000 description 2
- 238000004108 freeze drying Methods 0.000 description 2
- 235000011187 glycerol Nutrition 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- DNIAPMSPPWPWGF-UHFFFAOYSA-N monopropylene glycol Natural products CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- JNYAEWCLZODPBN-JGWLITMVSA-N (2r,3r,4s)-2-[(1r)-1,2-dihydroxyethyl]oxolane-3,4-diol Chemical compound OC[C@@H](O)[C@H]1OC[C@H](O)[C@H]1O JNYAEWCLZODPBN-JGWLITMVSA-N 0.000 description 1
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 description 1
- 241000589220 Acetobacter Species 0.000 description 1
- GUBGYTABKSRVRQ-XLOQQCSPSA-N Alpha-Lactose Chemical compound O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@H]1O[C@@H]1[C@@H](CO)O[C@H](O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-XLOQQCSPSA-N 0.000 description 1
- 239000004382 Amylase Substances 0.000 description 1
- 108010065511 Amylases Proteins 0.000 description 1
- 102000013142 Amylases Human genes 0.000 description 1
- 241001474374 Blennius Species 0.000 description 1
- 108010059892 Cellulase Proteins 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- 239000004354 Hydroxyethyl cellulose Substances 0.000 description 1
- 229920000663 Hydroxyethyl cellulose Polymers 0.000 description 1
- 239000004166 Lanolin Substances 0.000 description 1
- 239000004367 Lipase Substances 0.000 description 1
- 102000004882 Lipase Human genes 0.000 description 1
- 108090001060 Lipase Proteins 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- 244000294411 Mirabilis expansa Species 0.000 description 1
- 235000015429 Mirabilis expansa Nutrition 0.000 description 1
- 239000007832 Na2SO4 Substances 0.000 description 1
- 108091005804 Peptidases Proteins 0.000 description 1
- 102000035195 Peptidases Human genes 0.000 description 1
- 108010059820 Polygalacturonase Proteins 0.000 description 1
- 239000004365 Protease Substances 0.000 description 1
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 1
- DHKHKXVYLBGOIT-UHFFFAOYSA-N acetaldehyde Diethyl Acetal Natural products CCOC(C)OCC DHKHKXVYLBGOIT-UHFFFAOYSA-N 0.000 description 1
- QJFIVDXVQKTKOO-UHFFFAOYSA-N acetic acid;diethylamino acetate Chemical compound CC(O)=O.CCN(CC)OC(C)=O QJFIVDXVQKTKOO-UHFFFAOYSA-N 0.000 description 1
- 238000005273 aeration Methods 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 235000019418 amylase Nutrition 0.000 description 1
- 239000012164 animal wax Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 235000015278 beef Nutrition 0.000 description 1
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 1
- 239000004204 candelilla wax Substances 0.000 description 1
- 235000013868 candelilla wax Nutrition 0.000 description 1
- 229940073532 candelilla wax Drugs 0.000 description 1
- 239000004203 carnauba wax Substances 0.000 description 1
- 235000013869 carnauba wax Nutrition 0.000 description 1
- 229940082483 carnauba wax Drugs 0.000 description 1
- 229940106157 cellulase Drugs 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 229940088598 enzyme Drugs 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 108010093305 exopolygalacturonase Proteins 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000008273 gelatin Substances 0.000 description 1
- 229920000159 gelatin Polymers 0.000 description 1
- 235000019322 gelatine Nutrition 0.000 description 1
- 235000011852 gelatine desserts Nutrition 0.000 description 1
- 239000001963 growth medium Substances 0.000 description 1
- IUJAMGNYPWYUPM-UHFFFAOYSA-N hentriacontane Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCCCCCCCC IUJAMGNYPWYUPM-UHFFFAOYSA-N 0.000 description 1
- 235000012907 honey Nutrition 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 description 1
- 230000000968 intestinal effect Effects 0.000 description 1
- 235000019388 lanolin Nutrition 0.000 description 1
- 229940039717 lanolin Drugs 0.000 description 1
- 235000019421 lipase Nutrition 0.000 description 1
- 235000013536 miso Nutrition 0.000 description 1
- 235000013557 nattō Nutrition 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000000575 pesticide Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 229940108461 rennet Drugs 0.000 description 1
- 108010058314 rennet Proteins 0.000 description 1
- 235000019992 sake Nutrition 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
- 235000013555 soy sauce Nutrition 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000013112 stability test Methods 0.000 description 1
- 150000003445 sucroses Chemical class 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 229920001059 synthetic polymer Polymers 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
- 239000002562 thickening agent Substances 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 239000012178 vegetable wax Substances 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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)
Abstract
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
。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to granules containing useful microorganisms that are less likely to die during granulation and have 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 regulators, 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 sensitive to heat and easily deactivated in the presence of water, but they can be stored for long periods under dry conditions. , protein, or organic or inorganic salts are added thereto and subjected to low-temperature air drying, vacuum drying, or lyophilization to prepare microbial cells or microbial cell-containing powders with a moisture content of 10% or less.
このようにして得られた乾燥菌体は粉末で必るため、
(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)吸湿性が大きいため、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 dried bacterial cells obtained in this way are necessarily in the form of a powder, (i) they have a large surface area and therefore have a large contact area with the air, so they easily absorb moisture and are difficult to handle in an open system; ii) Because it has high hygroscopicity, when storing it for a long period of time, the bacteria will die if you are not careful to block out moisture; (iii) Since it is in powder form, the powder may fly around when handled and contaminate the environment. (iv) When added to foods, etc., they tend to form powder and are difficult to handle; (V) When used in pharmaceuticals, etc. In some cases, if it is in powder form, it is inconvenient to take out the entire amount.
[発明が解決しようとする問題点コ
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 have been proposed for granulating microbial cell powder into easy-to-handle granules.
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58−462
93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57−186
446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, a tablet confectionery containing one or more starch, starch hydrolyzate, or protein with a moisture content of 4% or less is mixed with freeze-dried Bifidobacterium and compressed into tablets. Manufacturing method (Special Publication No. 58-462
No. 93), a method of mixing bacterial cells and raw starch and freeze-drying (Japanese Patent Application Laid-open No. 14967-1982), a method of enclosing bacterial cells in seaweed gel to produce a particle gel containing bacterial cells (Japanese Patent Application Laid-open No. 57-1988) 186
No. 446), the lactic acid bacteria obtained by suction filtration using lactic acid bacteria and chlorella dry powder as a filtration layer were dissolved in a 10% gelatin solution, and then sprayed on the chlorella dry powder.
A method for producing a granular lactic acid bacteria-chlorella mixture (Japanese Unexamined Patent Publication No. 53-99371), a method of mixing viable bacterial cells and a protective film-forming solution, injecting the mixture into a coagulating salt solution to gel and encapsulate it, and granulating it. (Japanese Unexamined Patent Publication No. 60-141281), but these methods, except for the tableting method, are all granulated in an aqueous system, so the killing rate of bacterial cells during handling is high 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。In other words, when granulating in an aqueous system, (1) the binder uses a water-soluble substance, so it is hydrophilic and has high water absorption and hygroscopicity after granulation, and (2) it ultimately evaporates water. Therefore, it is difficult to apply to bacteria that are sensitive to water and heat, and (3) pores are generated in the granules due to the evaporation of water, resulting in a large specific surface area and easy moisture absorption. .
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型口当
り菌数の少ない粒剤しか(q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。Furthermore, the tableting method also has the problem of poor storage stability because the surface area of the powder cannot essentially be improved. In order to solve these problems, granulation using a non-aqueous system may be considered, but a fluid granulation method in which the core component is coated with a binder and a bacterial component has been proposed as a non-aqueous granulation method. However, (Japanese Patent Application Laid-Open No. 60-221078),
In this method, since the core material is in the center of the granule, only granules with a small number of bacteria per unit type can be used.Also, since the bacteria are present on the surface of the granule, it is susceptible to humidity and has poor storage stability. is not sufficient, and the product 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
.0.φ以下のものを作ることは困難である。In addition, because a core material is used, only particles with a large particle size can be produced;
.. 0. It is difficult to make something smaller than φ.
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。Therefore, an object of the present invention is to solve the above-mentioned problems in granules containing useful microorganisms, suppress deactivation as much as possible when granulating bacterial cells or bacterial cell-containing powders, maintain appropriate strength, and store. It is an object of the present invention to provide a granule containing useful microorganisms that is difficult to crush during transportation and use, has low hygroscopicity, and is less likely to be deactivated 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、非水系で撹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 provides a powder of useful microorganism cells or their contents,
A method for producing useful microorganism-containing granules, characterized by stirring and granulating in a non-aqueous system while heating and melting a binder substance with a melting point of 35 to 100°C, and a method for producing granules containing useful microorganisms, which is obtained by the method, and in which microbial cells are substantially contained in the granules. The present invention provides granules containing useful microorganisms, which are characterized by uniformly containing useful microorganisms.
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、保存に難点のおる菌体の場合に
特に本発明の特色が生かされる。The microorganism to be granulated in the present invention may be any type of microbial cell, but the features of the present invention are particularly useful in the case of microbial cells that are sensitive to heat and moisture and are difficult to preserve.
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Ba−cille
s、 M、 Pu5illus 、 Asp、 nig
er等の菌体、酒、みそ、しよう油、納豆などの醸造分
野で使用される各種細菌や酵母類(Sacch、cer
evisiae、 Asp。For example, various proteases (low temperature active API-21,
rennet, etc.), lipase, amylase, cellulase,
Ba-cille produces useful enzymes such as pectinase
s, M, Pu5illus, Asp, nig
Various bacteria and yeasts used in the field of brewing sake, miso, soy sauce, natto, etc.
evisiae, Asp.
0ryzae、 Asp、tamarii、 5ac
ch、rouxii、 8ac、na−tto、 B
ac、5ubtillus、 Asp、5ojae、
Acetobac−ter等)、乳酸菌やビフィズ
ス菌である旧coco−ccus属、5treptoc
occus属、PediOCOCCIJS ill、し
euconotoc属、LaCtObaCr + +u
s属、Bifidobacte−rium属に属する菌
体等が挙げられる。0ryzae, Asp, tamarii, 5ac
ch, rouxii, 8ac, na-tto, B
ac, 5ubtillus, Asp, 5ojae,
Acetobac-ter, etc.), lactic acid bacteria and bifidobacteria of the former Coco-ccus genus, 5treptoc
occus, PediOCOCCIJS ill, euconotoc, LaCtObaCr + +u
Examples include bacterial cells belonging to the genus S and Bifidobacterium.
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 bacterial cells can be isolated from the culture medium and directly dried through low-temperature aeration, vacuum dried, or freeze-dried to form a powder, or starch, lactose, protein, or salts may be added to the isolated bacterial cells and dried in the same manner to form a bacterial cell-containing powder. are used.
非水系で造粒する方法にも種々前えられ、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、ボ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
して造粒する水沫は、ポアー率も0.ICC/ 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 non-aqueous granulation methods, including one in which binder wax is dissolved in an organic solvent for granulation, but like the aqueous method, this method has a large bore ratio and improves the physical properties of the granules. Moreover, the influence of bacterial cells on the solvent is also large. In comparison, water droplet, which does not use a solvent and is granulated by heating above the melting point of the binder, has a pore ratio of 0. It was found that the ICC/g was small, less than ICC/g, and was the most favorable without being affected by 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 a binder substance during 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、ツルご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ービニル
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−7クリロニトリ
ルコボリマー、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, honey wax, candelilla wax, carnauba wax, lanolin and other natural fats and oils, (2) Sucrose esters, glycerin fatty acid mono( (3) Synthetic polymers having wax-like properties similar to (1) and (2) above, such as di-, tri) esters, propylene glycol fatty acid (PG) esters, and Tsurugatan fatty acid esters, such as cellulose derivatives. :benzylaminomethylcellulose, dimethylaminomethylcellulose,
Piperidylethyl hydroxyethyl cellulose, cellulose acetate diethylamino acetate, cellulose acetate dibutylamino hydroxypropyl ether, etc.: Polyvinyl derivatives: vinyl diethylamine-vinyl acetate copolymer, vinylbenzylamine-vinyl acetate copolymer, polyvinyl diethylaminoacetoacetal, vinyl piperidyl acetoacetal-vinyl acetate copolymer , polyvinyl acetal diethylaminoacetate, polydimethylaminoethyl methacrylate, polydiethylaminomethylstyrene, polyvinylethylpyridine, vinylethylpyridine-styrene copolymer, vinylethylpyridine-7crylonitrile copolymer, methylvinylpyridine-acrylonitrile copolymer, methylvinylpyridine-styrene Copolymers etc.
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 substance used in the present invention is suitably one with a melting point of 100°C or less, preferably 40 to 60°C, and is selected from among those that do not affect the bacterial cells, depending on the final 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 using lactic acid bacteria and bifidobacteria as food additives, it is necessary to select from among those permitted as food additives, such as sucrose ester, glycerin fatty acid ester, PG ester, and sorbitan fatty acid ester. 1 or 2 selected from natural fats and oils
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
湿性が小ざ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。In order to keep the final product granules stable for a long period of time, the lower the hygroscopicity, the more stable it is, so a wax material with a large proportion of hydrophobic parts should be selected.From this point of view, for example, Preferred are high fatty acid sucrose ester, sorbitan high fatty acid ester, rice wax, and the like.
本発明では、所望に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(Na2804等)、有機塩類
などが適宜使用される。In the present invention, additives such as fillers may be used during granulation to maintain a constant number of viable bacteria in the granules, if desired. As such additives, those that do not affect the bacterial cells and are suitable for the final purpose, such as starch, protein, glucose, lactose, inorganic salts (such as Na2804), and organic salts, are used as appropriate.
バインダー物質(ワックス)の添加】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15〜30ffl但%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。Addition of binder substance (wax) varies significantly depending on the physical properties of the bacteria to be granulated, so the optimum amount to be added needs to be determined for each case, but it is usually 10 to 50% by weight based on the total granulated material. A suitable range is 15 to 30 ffl (%). If it is less than 10% by weight, granulation is almost impossible, while if it is more than 50% by weight, the granules become large quickly during granulation, 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 dried bacterial cells or bacterial cell-containing powder,
The binder material and other additives if desired are granulated in a non-aqueous system.
造粒法としては転勤造粒、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)転勤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、ボアー率が大きい、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、ボアー率が大きく、形状として小
さいものはてぎないこと、
(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おり、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。Possible granulation methods include transfer granulation, fluidized granulation, extrusion granulation, spray granulation, and agitation granulation. (1) Transfer granulation uses a core material as described above, so the bacterial concentration (2) Fluid granulation has a large bore ratio, low strength, and other problems similar to (1); and (3) Extrusion granulation has problems with large amounts of wax. (4) With spray granulation, it is difficult to uniformly disperse the wax in the melted wax, it takes time to disperse, and the equipment is expensive. It has disadvantages such as being 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 to these, it was found that only the agitation granulation method that does not use a solvent can overcome these drawbacks.
造粒機としては通常攪拌型で、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M4造のものを使用する。The granulator used is usually a stirring type M4 type granulator that can be heated with hot water, steam, electric heat, etc. so as to maintain the temperature above the melting point of the wax 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
。Wax can be added to the granulator by adding it in powder form to the granulator at the same time as the bacterial powder to be granulated, or by adding pre-melted wax during granulation, but it is possible to granulate it in the shortest possible time. In order to prevent the killing of granulated microbial cells, it is preferable to add molten wax in the form of a spray.
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 during granulation is higher than the melting point of the wax-like substance used as a binder, preferably in the range of +5°C to the melting point, and under such temperature conditions, the desired particle size range can be formed in a short period of usually 5 to 30 minutes. 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とがないこと、(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
除去か不用で、プロセスが簡単でお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 in a non-aqueous system at a low temperature, there is no deactivation due to the action of water and heat during granulation, and (2) the obtained granules are Because it has a structure that contains useful microorganisms substantially uniformly in the binder, it is possible to make granules with a high number of bacteria, and it is also strong; (3) the shape is close to spherical, and it has extremely good fluidity. (4) Because the binder wax forms a layer on the surface, there are fewer pores on the surface, improving hygroscopicity and reducing deactivation during storage. (5) Because the binder wax forms a layer on the surface, it is less likely to be deactivated during storage. (6) The binder used for granulation or other binders can be easily coated in the final step of granulation, and a structure with a dense skin can be formed on the surface, further improving storage stability. Because it is spherical and has excellent fluidity, when the granules are mixed into other products, there is no possibility of them becoming lumpy or causing bridging, and the handling properties are significantly improved. (7) Solvent Since no water or organic solvent is used, there is no need to remove the solvent, and excellent effects such as a 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。[Example] The present invention will be explained below with reference to Examples and Comparative Examples.
実施例1〜5
tactobac i l Ius属に属する乳酸菌を
、でん粉、乳糖等で希釈し、菌体辺を3×1010個/
cJ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)および増母剤(Na2S04)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(q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
°C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 Lactic acid bacteria belonging to the genus Tactobacillus Ius were diluted with starch, lactose, etc., and the number of bacterial cells was 3 x 1010/
A binder (sucrose ester monoglyceride and rice wax) and a thickener (Na2S04) in the proportions shown in Table 1 were added to the lactic acid bacteria-containing material prepared in cJ.
The pellets were granulated at a temperature of ~70°C (Examples 1 to 5), and the survival rate of viable bacteria was measured by a conventional method, and the results shown in Table 1 were obtained (q). The granulated product was kept at room temperature and at 35°C.
When the sample was stored at °C and the survival rate of viable bacteria was measured, it was found that it could be stored stably for a long period of time, as shown in Table 2.
実施例6〜8
Bifidobacterium Qに属するビフィズ
ス菌を1×109個/9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(ショ糖工ステル
−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19だ。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 Using a bulk powder prepared to contain 1 x 109/9 bifidobacteria belonging to Bifidobacterium Q, a binder (sucrose ester-sorbitan ester-glycerin ester, rice Wax) and bulking agents (Na2so4, glucose) were added and granulated at a temperature of 55 to 70°C, and the survival rate of viable bacteria was measured. The results shown in Table 1 were 19. Furthermore, when a storage stability test was conducted 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(直しか得られなかった
。Comparative Examples 1 to 2 20% glucose aqueous solution and bulking agent (Na2SO4) were added to the same bacterial cell content as in Examples 1 to 5 in the proportions shown in Table 1, granulated with stirring at room temperature, and the survival rate of viable bacteria was measured. As a result, as shown in Table 1, the results were extremely low (only a fixed amount could be obtained).
Claims (1)
5〜100℃のバインダー物質を加熱溶融させながら、
非水系で撹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。 2)バインダー物質がワックス状物質であり、その添加
量が10〜50重量%の範囲である特許請求の範囲第1
項に記載の製造方法。 3)造粒温度がバインダー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。 4)造粒の最終工程で造粒に用いたバインダーまたは異
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。 5)有用微生物菌体またはその含有物の粉体に、融点3
5〜100℃のバインダー物質を加熱溶融させながら、
非水系で撹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
。[Claims] 1) Powder of useful microorganism cells or their contents has a melting point of 3
While heating and melting the binder material at 5 to 100°C,
A method for producing granules containing useful microorganisms, characterized by stirring and granulating them in a non-aqueous system. 2) Claim 1, wherein the binder substance is a waxy substance, and the amount added is in the range of 10 to 50% by weight.
The manufacturing method described in section. 3) The manufacturing method according to claim 1, wherein the granulation temperature is higher than the melting point of the binder material. 4) The manufacturing method according to claim 1, wherein the surface of the granules is coated with the binder used for granulation or a different binder in the final step of granulation. 5) The powder of useful microorganisms or their contents has a melting point of 3.
While heating and melting the binder material at 5 to 100°C,
A granule containing useful microorganisms, which is obtained by agitation granulation in a non-aqueous system, and is characterized in that the granule substantially uniformly contains bacterial cells.
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 true JPS6363373A (en) | 1988-03-19 |
JP2596418B2 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) |
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EP0470287A1 (en) * | 1989-02-10 | 1992-02-12 | Showa Denko Kabushiki Kaisha | Granular material for control of soil-borne diseases and method for control of soil-borne diseases with the granular material |
US5288488A (en) * | 1990-02-23 | 1994-02-22 | Auburn University | Method of controlling foliar microorganism populations |
JP2007515182A (en) * | 2003-12-23 | 2007-06-14 | コンパニー ジェルヴェ ダノン | Foods containing lactic acid bacteria granules |
JP2012518027A (en) * | 2009-02-19 | 2012-08-09 | ユーリア カサーレ ソシエテ アノニム | Granules containing filamentous fungi and method for preparing the same |
WO2019082907A1 (en) * | 2017-10-27 | 2019-05-02 | クミアイ化学工業株式会社 | Microorganism lyophilized composition |
CN114940785A (en) * | 2022-05-20 | 2022-08-26 | 万华化学集团股份有限公司 | High-rigidity scratch-resistant antibacterial polyethylene film and preparation method thereof |
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CN113677212A (en) | 2019-03-28 | 2021-11-19 | 森永乳业株式会社 | Heat-resistant bacterial composition |
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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 |
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1986
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Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
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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 |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0470287A1 (en) * | 1989-02-10 | 1992-02-12 | Showa Denko Kabushiki Kaisha | Granular material for control of soil-borne diseases and method for control of soil-borne diseases with the granular material |
US5288488A (en) * | 1990-02-23 | 1994-02-22 | Auburn University | Method of controlling foliar microorganism populations |
JP2007515182A (en) * | 2003-12-23 | 2007-06-14 | コンパニー ジェルヴェ ダノン | Foods containing lactic acid bacteria granules |
JP2012518027A (en) * | 2009-02-19 | 2012-08-09 | ユーリア カサーレ ソシエテ アノニム | Granules containing filamentous fungi and method for preparing the same |
WO2019082907A1 (en) * | 2017-10-27 | 2019-05-02 | クミアイ化学工業株式会社 | Microorganism lyophilized composition |
EP3702441A4 (en) * | 2017-10-27 | 2020-12-02 | Kumiai Chemical Industry Co., Ltd. | Microorganism lyophilized composition |
JPWO2019082907A1 (en) * | 2017-10-27 | 2021-03-04 | クミアイ化学工業株式会社 | Microbial freeze-dried composition |
US11639491B2 (en) | 2017-10-27 | 2023-05-02 | Kumiai Chemical Industry Co., Ltd. | Microorganism lyophilized composition |
CN114940785A (en) * | 2022-05-20 | 2022-08-26 | 万华化学集团股份有限公司 | High-rigidity scratch-resistant antibacterial polyethylene film and preparation method thereof |
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 |
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