WO2007063854A1 - Method of producing bacterial cellulose - Google Patents

Method of producing bacterial cellulose Download PDF

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Publication number
WO2007063854A1
WO2007063854A1 PCT/JP2006/323726 JP2006323726W WO2007063854A1 WO 2007063854 A1 WO2007063854 A1 WO 2007063854A1 JP 2006323726 W JP2006323726 W JP 2006323726W WO 2007063854 A1 WO2007063854 A1 WO 2007063854A1
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Prior art keywords
bacterial cellulose
mushroom
producing
cellulose
medium
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PCT/JP2006/323726
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French (fr)
Japanese (ja)
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Yutaka Tamai
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National University Corporation Hokkaido University
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Priority to JP2007547952A priority Critical patent/JPWO2007063854A1/en
Publication of WO2007063854A1 publication Critical patent/WO2007063854A1/en

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    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N1/00Microorganisms, e.g. protozoa; Compositions thereof; Processes of propagating, maintaining or preserving microorganisms or compositions thereof; Processes of preparing or isolating a composition containing a microorganism; Culture media therefor
    • C12N1/20Bacteria; Culture media therefor
    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12PFERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00Preparation of compounds containing saccharide radicals
    • C12P19/04Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds

Definitions

  • the present invention relates to a method for producing nocteria cellulose.
  • Cellulose is the most abundant natural polymer substance on the earth and has been used in various fields since ancient times. Cellulose is the main component of plant cell walls, and most of the cellulose currently used industrially is derived from higher plants.
  • some bacteria are known to produce cellulose!
  • butterias include the genus Darconoacetobacter, the genus Agrobacterium, the genus Rhizopium, the genus Sartina, the genus Syudomonas, the genus Achromopacter, the genus Alkagenes, the genus Erotactor and the genus Azotopacter.
  • one of the genus Darconoacetopactor is known to produce a large amount of cellulose outside the cells.
  • a kind of the genus Darconoacetopactor produces a gel-like cellulose film on the surface of a medium when cultured.
  • Cellulose produced by such bacteria (hereinafter referred to as “cellulose-producing bacteria”) is called bacterial cellulose.
  • this bacterial cellulose is pure cellulose containing no hemicellulose or lignin.
  • Bacterial cellulose is also known to have a different fiber thickness from plant cellulose. Plant cellulose forms very fine fibers called microfibrils by concentrating many cellulose molecular chains, and these microfibrils are further bundled to form a higher-order structure.
  • microfibrils of cellulose secreted from cellulose-producing bacteria form a fine network structure with the same thickness.
  • the thickness of hardwood pulp fibers is about 30 ⁇ m in diameter, whereas the thickness of bacterial cellulose microfibrils is about 0.1 ⁇ m in diameter.
  • bacterial cellulose has characteristics that are not found in plant cellulose! Therefore, various possibilities as industrial materials are expected.
  • Nocteria cell As a method of using loin, its use in separation membranes and medical pads is being studied by taking advantage of the fine network structure and water retention of bacterial cellulose membranes.
  • by cutting the bacterial cellulose film by mechanical treatment it can be used as a papermaking raw material. It is known that when bacterial cellulose fibers obtained by mechanical treatment are mixed with wood pulp, the strength and elastic modulus of paper are improved.
  • Patent Document 1 animal serum was added to the standard medium, and in the method of Patent Document 2, hydrolyzed collagen was added to the standard medium, thereby successfully increasing the production efficiency of bacterial cellulose.
  • Non-Patent Document 1 describes that mannitol is effective in producing bacterial cellulose.
  • Patent Document 1 Japanese Unexamined Patent Publication No. 2000-4895
  • Patent Document 2 JP-A-2005-80571
  • Non-Patent Document l Yasumitsu Uraki et al, Holzaba, Vol.56 (2002), No.4, 341-347. Disclosure of the Invention
  • the conventional method for producing bacterial cellulose still has the problem that the production cost is still high.
  • HS medium Hestrin-Schramm medium
  • media must be purchased or prepared.
  • the raw materials (carbon source), serum, hydrolyzed collagen, etc. must also be purchased or prepared.
  • Such medium constituents are used in large quantities and are expensive, and this increases the manufacturing cost of pacteria cellulose. Therefore, if one of these medium constituents can be used at a low price, it can greatly contribute to the reduction of manufacturing costs.
  • An object of the present invention is to provide a method for producing bacterial cellulose that can produce bacterial cellulose at low cost and a culture medium for culturing cellulose-producing bacteria used therefor.
  • the first of the present invention relates to the following method for producing bacterial cellulose.
  • a method for producing bacterial cellulose comprising a step of culturing a cellulose-producing bacterium in a medium containing a processed fruit body or mycelium of a mushroom.
  • the method for producing bacterial cellulose according to any one of [1] to [3], wherein the treated product contains mannitol.
  • the second of the present invention relates to the following culture medium for culturing cellulose-producing bacteria.
  • a culture medium for culturing cellulose-producing bacteria comprising a processed product of mushroom fruit bodies or mycelium. The invention's effect
  • bacterial cellulose can be produced at low cost.
  • wastes produced during mushroom production and caking can be used as a raw material of a medium for producing bacterial cellulose. Since these wastes can be procured almost free of charge from the producer or processor, the cost of raw materials can be kept as low as possible.
  • waste produced during the production and processing of mushrooms such as a waste fungus bed can be effectively used for IJ.
  • FIG. 1 Graph showing the results of analysis of water-soluble saccharides in each medium.
  • the present inventors paid attention to water-soluble components remaining in wastes during the production and processing of mushrooms as raw materials for the production of nocteria cellulose. Accordingly, the present inventors have completed the present invention as a result of intensive research that it is impossible to produce bacterial cellulose using a water-soluble component in waste as a raw material.
  • the method for producing bacterial cellulose according to the present invention is characterized by culturing cellulose-producing bacteria in a medium containing a treated product obtained from mushrooms (here, "treated product” means water-soluble). What was obtained as a result of applying the component to the mushroom was obtained.
  • a solution containing a water-soluble component derived from a mushroom for example, a compressed solution or an extract
  • a dried product of a water-soluble component derived from a mushroom for example, a product obtained by drying a compressed solution or an extract
  • the term “mushroom” does not mean “a body of a macroscopic size of ascomycetes or basidiomycetes” or “ascomycetes and basidiomycetes forming a large fruiting body” Used to mean “fungi”. That is, “mushroom” in the present specification includes not only fruit bodies but also mycelia.
  • the method for obtaining a processed product of mushroom is not particularly limited as long as water-soluble components such as mannitol and glucose can be obtained from mushrooms.
  • the treated product may be a dry product or an aqueous solution, but an aqueous solution is preferable from the viewpoint of work efficiency.
  • the pressing liquid obtained by the pressing method, the extracting liquid obtained by the water extraction method, or the like can be used as a processed product.
  • human costs can be suppressed.
  • the processed product is obtained as a dry product, it can be treated in the same manner as the above-mentioned pressing solution or extract by making it into an aqueous solution.
  • a specific method for obtaining such a treated product for example, a method for obtaining a compressed liquid by pressing a waste fungus bed after harvesting mushrooms, extraction from the waste fungus bed with water (cold water or hot water). And a method of obtaining an extract, a method of obtaining a squeezed solution by squeezing a stone tip remaining on a fungus bed after harvesting mushrooms, and a method of obtaining a simmered juice (boiled residue) by boiling a mushroom fruit body.
  • the pressed solution, the extract solution, and the boiled residue solution correspond to the processed product.
  • the waste fungus bed contains not only mushroom mycelia but also oga powder and bran, etc., but it may be a processed product of the entire waste fungus bed. Of course, it does not matter if it is a bed after inoculation with the inoculum and before harvesting the mushrooms.
  • the treated product obtained by the above method has different power depending on the type of mushroom to be used and the method of obtaining the treated product.
  • Water-soluble components such as mannitol, glycerol, glucose, fructose, trehalose, arabitol and inositol (Such as sugar and sugar alcohol). These water-soluble components are contained in many mushrooms, although their amounts and proportions vary depending on the species (Journal of Japanese Food Industry Association, Vol.31, No.12, 765-771). Among them, it is preferable that the ratio of mannitol, glycerol and glucose is large, and particularly the ratio of mannitol is large.
  • Non-Patent Document 1 a medium containing mantol is considered suitable for production of bacterial cellulose.
  • the method for producing bacterial cellulose according to the present invention is generally used, and it has been shown that the yield of bacterial cellulose is increased as compared with the method using HS medium (see Examples).
  • the treated product obtained by the above method can be used as a medium as it is simply by adjusting the concentration or sterilizing.
  • the concentration of the medium is the conditions under which the cultivating cellulose-producing bacteria can grow May be selected as appropriate.
  • the Brix concentration should be 3.4%, which is equal to HS medium.
  • the Brix concentration of the medium is not particularly limited.
  • the medium according to the present invention includes a mushroom processed product, or a concentration-adjusted or sterilized product thereof, but may further include an optional component.
  • optional components include a carbon source (eg, glucose), a nitrogen source (eg, amino acid), a metal ion source (eg, calcium salt hydrate), vitamins (eg, riboflavin, etc.) ) And the like, which may be added to the culture medium for microbial culture.
  • the medium according to the present invention may be mixed with a medium such as an HS medium.
  • the type of mushrooms to be treated is not particularly limited as long as the processed product can be obtained, but it is an edible mushroom because a boiled mushroom residue can be used. It is preferable. Moreover, since a waste mushroom bed and a stone thrust can also obtain a processed material, it is more preferable that it is a cultivation mushroom.
  • edible mushrooms include Tamogitake (Pleurot us cornucopiae: uolden Oyster), Enokitake (Flammulina velutipes: Velvet Foot), Gifutake (Pleurotus ostreatus: Oyster Mushroom), and Shirotamogitake (Hypsizygus Elumyus). .
  • the type of cellulose-producing bacterium used in the present invention is not particularly limited as long as it can produce cellulose in the medium.
  • examples include bacteria belonging to the genera Darconoacetobacter, Agrobacterium, Rhizopium, Sartina, Syudomonas, Achromopacter, Alkaligenes, Elopacter, Azotopacter, and the like.
  • Gluconacetobacter xylinus (former name: AcetoDacter xyiinum).
  • a normal culture method for bacteria can be applied.
  • static culture shaking culture or aeration and agitation culture can be mentioned.
  • the culture operation method for example, a batch culture method, a fed-batch culture method, a repeated batch culture method or a continuous culture method can be used.
  • the stirring means for example, an impeller (stirring blade), an air lift type culture device, a pump-driven circulation of culture broth, etc. may be used alone or in combination. Can do.
  • a culture apparatus for normal bacteria can be applied.
  • a jar armor with a stirrer that can keep the inside of the tank at a constant temperature can be used.
  • the culture conditions may be appropriately selected so that the cultivating cellulose-producing bacteria can grow.
  • the culture temperature may be room temperature, for example, 10 to 40 ° C., preferably 25 to 35 ° C.
  • the pH of the medium should be in the range of 3-7, preferably 4-6.
  • the processed product derived from mushrooms in the aqueous solution is weakly acidic (pH 5.0-5.5), so it remains in the dull state as it is. It is suitable for culturing Conoacetobacter-1 'xylinus. Of course, adjust the pH with any alkali and acid.
  • the culture period may be a normal culture period.
  • a bacterial cellulose film on a gel can be obtained in about 7 days.
  • the bacterial cell mouth produced by the method for producing bacterial cellulose according to the present invention may be recovered as it is, or may be subjected to a treatment for removing impurities contained in the recovered material.
  • a treatment for removing impurities include washing with water, pressure dehydration, dilute acid washing, alkali washing, treatment with a bleaching agent such as sodium hypochlorite or hydrogen peroxide, and a lytic enzyme such as lysozyme.
  • Treatment with a surfactant, treatment with a surfactant such as sodium lauryl sulfate or deoxycholate, or heat washing may be performed alone or in combination.
  • the method for producing bacterial cellulose according to the present invention can use mushroom production and waste from the cultivation as a raw material of the medium. Since these wastes can be procured almost free of charge from the producer or processor, the raw material costs can be kept as low as possible. In addition, mushrooms are cultivated all year round, so each waste can be procured stably. Furthermore, since medium preparation from waste can be performed by simple operations such as pressing and water extraction, human costs can be kept low. The residue after the medium is prepared can be used as it is for reuse of conventional waste such as compost, fuel, livestock feed and livestock bedding.
  • the method for producing bacterial cellulose according to the present invention includes the reduction of the waste transportation cost when the mushroom production and the waste at the time of Karoe are used for the above-mentioned conventional waste reuse, In addition, it is possible to improve the storage stability of the waste.
  • the water content of the waste fungus bed is about 70%, and the water content of stone heads and fruit bodies is about 90%.
  • the transportation cost and the preservability are also important. Considering that it is desirable to remove moisture from these wastes.
  • the method for producing bacterial cellulose according to the present invention by obtaining a treated product by a pressing method, it is possible to remove moisture from the waste without hindering reuse of the waste.
  • the raw material used for the treatment was waste bed after harvest of Tamogitake (Kalamatsuga powder + bran), Tamogitake crest and fruit body of Tamogitake.
  • the treated product was obtained as an aqueous solution from the waste microbial bed by pressing, cold water extraction and hot water extraction, pressing from the stone tip, and boiling from the fruit body.
  • the resulting treated product was adjusted to a Brix concentration of 3.4% so that the Brix concentration was equal to the HS medium used as a control.
  • a medium obtained by further sterilizing the processed product obtained by the above method was used.
  • the culture medium is prepared by squeezing the waste bacteria bed.
  • the waste microbial bed after harvesting Tamogitake was squeezed at about 500 kN to obtain a squeezed solution.
  • the obtained compressed solution was filtered, the brick concentration was adjusted to 3.4%, and sterilized with an autoclave to obtain a medium.
  • the culture medium is prepared by extracting the waste fungus bed with cold water. Tamogitake Deionized water was added to the harvested fungus bed and stirred for 1 hour at room temperature. The obtained extract was filtered, the Brix concentration was adjusted to 3.4%, and sterilized by autoclave to obtain a medium.
  • the culture medium is prepared by hot water extraction of the waste fungus bed.
  • Tamogitake Deionized water was added to the harvested fungus bed and boiled for 1 hour.
  • the resulting extract is filtered and filtered.
  • the medium was obtained by adjusting the Lix concentration to 3.4% and sterilizing with autoclave.
  • a culture medium is prepared by squeezing a stone tip. After harvesting the bamboo shoots, the stone bumps remaining on the fungus bed were crushed with a mixer. The crushed stone bump was squeezed to obtain a squeezed liquid. The obtained compressed solution was filtered, the Brix concentration was adjusted to 3.4%, and sterilized with an autoclave to obtain a medium.
  • FIG. 1 is a graph showing the results of sugar analysis for each medium.
  • HPLC high performance liquid chromatography
  • FIG. 1 is a graph showing the results.
  • the yield of bacterial cellulose in petri dishes cultured in the above media was 1.2 times (bacterial bed press), 1.2 times (cold water extraction), 1.1 times (hot water extraction) of the HS medium petri dishes in the control experiments. ), 2.8 times (stone squeezed) and 1.7 times (boiled residue). From these data, it was estimated that bacterial cellulose having a residue 1 ton force of 0.2 to 2.0 kg could be produced.
  • the production cost of bacterial cellulose can be reduced, so that it can be used in various applications such as separation membranes, medical's cosmetic pads, speaker cones, cellulose film-forming paints, thickeners, paper, and composite materials. Therefore, bacterial cellulose can be provided at a low cost.

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Abstract

A method of producing a bacterial cellulose whereby the bacterial cellulose can be produced by using a less expensive medium component. According to this method, an aqueous solution of a water-soluble component originating in a mushroom is obtained by pressing or water-extracting a waste mushroom bed remaining after harvesting mushrooms together with mushroom hard tip, or cooking mushroom fruit body in water and collecting the residue. By diluting and sterilizing the above-described aqueous solution, a medium for culturing a cellulose-producing bacterium is prepared. Subsequently, the cellulose-producing bacterium is cultured in this medium to thereby produce the bacterial cellulose.

Description

明 細 書  Specification
ノ クテリアセルロースの製造方法  Nocteria cellulose production method
技術分野  Technical field
[0001] 本発明は、ノ クテリアセルロースの製造方法に関する。  [0001] The present invention relates to a method for producing nocteria cellulose.
背景技術  Background art
[0002] セルロースは地球上で最も豊富な天然高分子物質であり、古くから様々な分野で 利用されている。セルロースは植物細胞壁の主成分であり、現在工業的に使用され ているセルロースの大部分は高等植物由来のものである。  [0002] Cellulose is the most abundant natural polymer substance on the earth and has been used in various fields since ancient times. Cellulose is the main component of plant cell walls, and most of the cellulose currently used industrially is derived from higher plants.
[0003] 一方、バクテリアの中にもセルロースを生産するものが知られて!/、る。そのようなバタ テリアとしては、ダルコノアセトバクター属、ァグロバクテリウム属、リゾピウム属、サル チナ属、シユードモナス属、ァクロモパクター属、アルカリゲネス属、エロパクター属、 ァゾトパクター属などがある。この中でも、ダルコノアセトパクター属の一種はセルロー スを菌体外に大量に生産することが知られて 、る。  [0003] On the other hand, some bacteria are known to produce cellulose! Examples of such butterias include the genus Darconoacetobacter, the genus Agrobacterium, the genus Rhizopium, the genus Sartina, the genus Syudomonas, the genus Achromopacter, the genus Alkagenes, the genus Erotactor and the genus Azotopacter. Among these, one of the genus Darconoacetopactor is known to produce a large amount of cellulose outside the cells.
[0004] ダルコノアセトパクター属の一種は、培養すると培地表面にゲル状のセルロース膜 を生産する。このようなバクテリア(以後、「セルロース生産菌」という)が生産するセル ロースは、バクテリアセルロースと呼ばれている。  [0004] A kind of the genus Darconoacetopactor produces a gel-like cellulose film on the surface of a medium when cultured. Cellulose produced by such bacteria (hereinafter referred to as “cellulose-producing bacteria”) is called bacterial cellulose.
[0005] このバクテリアセルロースは植物セルロースとは異なり、へミセルロースやリグニンを 全く含まない純粋なセルロースである。また、バクテリアセルロースは形成する繊維の 太さが植物セルロースと異なることも知られて 、る。植物セルロースはセルロース分子 鎖が多数集束することでミクロフイブリルと呼ばれる非常に細い繊維を形成し、このミ クロフイブリルがさらに束になって高次構造を形成する。一方、ノ クテリアセルロース は、セルロース生産菌から分泌されたセルロースのミクロフイブリルが、そのままの太 さで微細な網目構造を形成して ヽる。広葉樹パルプの繊維の太さは直径 30 μ m程 度であるのに対し、バクテリアセルロースのミクロフイブリルの太さは直径 0.1 μ m程度 である。  [0005] Unlike bacterial cellulose, this bacterial cellulose is pure cellulose containing no hemicellulose or lignin. Bacterial cellulose is also known to have a different fiber thickness from plant cellulose. Plant cellulose forms very fine fibers called microfibrils by concentrating many cellulose molecular chains, and these microfibrils are further bundled to form a higher-order structure. On the other hand, for noceria cellulose, the microfibrils of cellulose secreted from cellulose-producing bacteria form a fine network structure with the same thickness. The thickness of hardwood pulp fibers is about 30 μm in diameter, whereas the thickness of bacterial cellulose microfibrils is about 0.1 μm in diameter.
[0006] このように、バクテリアセルロースは、植物セルロースでは見られな!/、特徴を有する ことから、工業材料としての様々な可能性が期待されている。例えば、ノ クテリアセル ロースの利用法として、バクテリアセルロース膜の微細な網目構造や保水性の良さを 生かして、分離膜や医療用パッドなどへの利用が検討されている。また、バクテリアセ ルロース膜を機械的処理により裁断することで、製紙原料として利用することも可能と なる。機械的処理によって得られたバクテリアセルロース繊維を木材パルプに混ぜる と、紙の強度や弾性率が向上することが知られている。 [0006] As described above, bacterial cellulose has characteristics that are not found in plant cellulose! Therefore, various possibilities as industrial materials are expected. For example, Nocteria cell As a method of using loin, its use in separation membranes and medical pads is being studied by taking advantage of the fine network structure and water retention of bacterial cellulose membranes. In addition, by cutting the bacterial cellulose film by mechanical treatment, it can be used as a papermaking raw material. It is known that when bacterial cellulose fibers obtained by mechanical treatment are mixed with wood pulp, the strength and elastic modulus of paper are improved.
[0007] 従来、バクテリアセルロースの製造方法としては、果汁、廃糖蜜、古紙、パルプ廃液 などを原料とする方法が試みられている。これらの方法では、前記原料を培地として セルロース生産菌を培養する。し力しながら、これらの方法では、培養前に前記原料 に含まれる多糖を加水分解し、分解生成した単糖を糖アルコールへ変換することな どの前処理を必要とするため、製造コストが高くなるという問題がある。  [0007] Conventionally, as a method for producing bacterial cellulose, a method using fruit juice, molasses, waste paper, pulp waste liquid or the like as a raw material has been attempted. In these methods, cellulose-producing bacteria are cultured using the raw material as a medium. However, these methods require a pretreatment such as hydrolysis of the polysaccharides contained in the raw material and conversion of the decomposed monosaccharides into sugar alcohols before culturing, resulting in high production costs. There is a problem of becoming.
[0008] そこで、製造効率を向上させるため、多くの研究者によってセルロース生産菌培養 用培地の成分検討が進められてきた。例えば、特許文献 1および特許文献 2の方法 が報告されている。特許文献 1の方法では標準培地に動物の血清を添加することで 、また、特許文献 2の方法では標準培地に加水分解コラーゲンを添加することで、バ クテリアセルロースの生産効率を高めることに成功して 、る。  [0008] Therefore, in order to improve the production efficiency, many researchers have been studying the components of the culture medium for cellulose-producing bacteria. For example, the methods of Patent Document 1 and Patent Document 2 have been reported. In the method of Patent Document 1, animal serum was added to the standard medium, and in the method of Patent Document 2, hydrolyzed collagen was added to the standard medium, thereby successfully increasing the production efficiency of bacterial cellulose. And
[0009] また、非特許文献 1では、マン-トールがバクテリアセルロース生産に有効であるこ とが記載されている。  [0009] In addition, Non-Patent Document 1 describes that mannitol is effective in producing bacterial cellulose.
[0010] ところで、今日、キノコの生産および加工において、キノコ収穫後の廃菌床、石突お よびキノコ子実体の水煮残渣液などの廃棄物が大量に生じて 、る。これらの廃棄物 は、堆肥、燃料、家畜飼料または家畜敷料などとして再利用されている。しかしながら 、これらの廃棄物にはキノコの菌糸由来の水溶性成分 (特に、糖および糖アルコール )が豊富に残存していると考えられるが、これらの水溶性成分を有効的に利用してい る例はほとんどなぐ未利用資源となっている。  [0010] By the way, in the production and processing of mushrooms, a large amount of wastes such as a waste fungus bed after harvesting mushrooms, stone bumps and boiled residue of mushroom fruit bodies are generated in large quantities. These wastes are reused as compost, fuel, livestock feed or livestock bedding. However, these wastes are thought to contain abundant water-soluble components (especially sugars and sugar alcohols) derived from the fungi of mushrooms. Examples of effective use of these water-soluble components Is almost always an unused resource.
特許文献 1:特開 2000— 4895号公報  Patent Document 1: Japanese Unexamined Patent Publication No. 2000-4895
特許文献 2 :特開 2005— 80571号公報  Patent Document 2: JP-A-2005-80571
非特許文献 l :Yasumitsu Uraki et al, Holzforschung, Vol.56(2002), No.4, 341-347. 発明の開示  Non-Patent Document l: Yasumitsu Uraki et al, Holzforschung, Vol.56 (2002), No.4, 341-347. Disclosure of the Invention
発明が解決しょうとする課題 [0011] 従来のバクテリアセルロースの製造方法にぉ 、ては、依然として製造コストが高!、と いう問題がある。 Problems to be solved by the invention [0011] The conventional method for producing bacterial cellulose still has the problem that the production cost is still high.
[0012] 前記従来の製造方法および特許文献に記載された製造方法では、ヘストリンーシ ュラム(Hestrin-Schramm)培地(以下、「HS培地」と略記する)のような標準培地が必 要なため、これらの培地を購入または調製しなければならない。また、前記原料 (炭 素源)、血清および加水分解コラーゲンなども購入または調製しなければならない。 このような培地構成成分は、それぞれ大量に使われる上、高価であるため、パクテリ ァセルロースの製造コストを押し上げる要因になっている。したがって、これらの培地 構成成分として、一成分でも低価格のものを用いることができれば製造コスト低減に 大きく貢献できる。  [0012] The conventional manufacturing method and the manufacturing method described in the patent literature require a standard medium such as a Hestrin-Schramm medium (hereinafter abbreviated as "HS medium"). Media must be purchased or prepared. The raw materials (carbon source), serum, hydrolyzed collagen, etc. must also be purchased or prepared. Such medium constituents are used in large quantities and are expensive, and this increases the manufacturing cost of pacteria cellulose. Therefore, if one of these medium constituents can be used at a low price, it can greatly contribute to the reduction of manufacturing costs.
[0013] 本発明の目的は、安価にバクテリアセルロースを製造することができるバクテリアセ ルロースの製造方法およびそれに用いるセルロース生産菌培養用培地を提供するこ とである。  [0013] An object of the present invention is to provide a method for producing bacterial cellulose that can produce bacterial cellulose at low cost and a culture medium for culturing cellulose-producing bacteria used therefor.
課題を解決するための手段  Means for solving the problem
[0014] 本発明の第一は、以下に示すバクテリアセルロースの製造方法に関する。 The first of the present invention relates to the following method for producing bacterial cellulose.
[1]キノコの子実体または菌糸体の処理物を含む培地中でセルロース生産菌を培 養するステップを有するバクテリアセルロースの製造方法。  [1] A method for producing bacterial cellulose, comprising a step of culturing a cellulose-producing bacterium in a medium containing a processed fruit body or mycelium of a mushroom.
[2]前記処理物は、キノコの子実体または菌糸体の、圧搾液または抽出液である、 [1]記載のバクテリアセルロースの製造方法。  [2] The method for producing bacterial cellulose according to [1], wherein the treated product is a pressed or extracted liquid of a fruit body or mycelium of a mushroom.
[3]前記処理物は、キノコ廃菌床圧搾液、キノコ廃菌床抽出液、キノコ石突圧搾液 、または、キノコ水煮残渣液、のいずれかである、 [1]記載のバクテリアセルロースの 製造方法。  [3] The production of bacterial cellulose according to [1], wherein the treated product is any one of a mushroom waste fungus bed compressed solution, a mushroom waste fungus bed extract, a mushroom stone squeeze solution, or a mushroom boiled residue solution. Method.
[4]前記キノコはタモギタケ(Pleurotus cornucopiae)である、 [1]〜[3]のいずれか に記載のバクテリアセルロースの製造方法。  [4] The method for producing bacterial cellulose according to any one of [1] to [3], wherein the mushroom is Pleurotus cornucopiae.
[5]前記セルロース生産菌はダルコノアセトバクタ^ ~·キシリヌス(Gluconacetobacter xylinus)である、 [1]〜 [3]の!、ずれかに記載のバクテリアセルロースの製造方法。  [5] The method for producing bacterial cellulose according to any one of [1] to [3], wherein the cellulose-producing bacterium is Gluconacetobacter xylinus.
[6]前記処理物はマン-トールを含む、 [1]〜 [3]の 、ずれかに記載のバクテリア セルロースの製造方法。 [0015] 本発明の第二は、以下に示すセルロース生産菌培養用培地に関する。 [6] The method for producing bacterial cellulose according to any one of [1] to [3], wherein the treated product contains mannitol. [0015] The second of the present invention relates to the following culture medium for culturing cellulose-producing bacteria.
[7]キノコの子実体または菌糸体の処理物を含むセルロース生産菌培養用培地。 発明の効果  [7] A culture medium for culturing cellulose-producing bacteria, comprising a processed product of mushroom fruit bodies or mycelium. The invention's effect
[0016] 本発明によれば、安価にバクテリアセルロースを製造することができる。  [0016] According to the present invention, bacterial cellulose can be produced at low cost.
[0017] 本発明では、バクテリアセルロース製造における培地の原料は、キノコの生産およ びカ卩ェ時の廃棄物を用いることができる。これらの廃棄物は、生産元または加工元か らほぼ無償で調達できるので、原料コストを限りなく低く抑えることができる。 [0017] In the present invention, as a raw material of a medium for producing bacterial cellulose, wastes produced during mushroom production and caking can be used. Since these wastes can be procured almost free of charge from the producer or processor, the cost of raw materials can be kept as low as possible.
[0018] また、本発明では、廃菌床などのキノコの生産および加工時の廃棄物を有効的に 禾 IJ用することがでさる。 [0018] Further, according to the present invention, waste produced during the production and processing of mushrooms such as a waste fungus bed can be effectively used for IJ.
図面の簡単な説明  Brief Description of Drawings
[0019] [図 1]各培地中の水溶性糖類の分析結果を示すグラフ  [0019] [Fig. 1] Graph showing the results of analysis of water-soluble saccharides in each medium.
[図 2]各培地におけるバクテリアセルロースの収量を示すグラフ  [Figure 2] Graph showing the yield of bacterial cellulose in each medium
発明を実施するための最良の形態  BEST MODE FOR CARRYING OUT THE INVENTION
[0020] 以下、本発明の実施の形態について詳細に説明する。 Hereinafter, embodiments of the present invention will be described in detail.
[0021] 本発明者らは、ノ クテリアセルロース製造の原料として、キノコの生産時および加工 時の廃棄物中に残存する水溶性成分に着目した。そこで、本発明者らは、廃棄物中 の水溶性成分を原料としてバクテリアセルロースを製造することができな 、か、と鋭意 研究を重ねた結果、本発明を完成するに至ったのである。  [0021] The present inventors paid attention to water-soluble components remaining in wastes during the production and processing of mushrooms as raw materials for the production of nocteria cellulose. Accordingly, the present inventors have completed the present invention as a result of intensive research that it is impossible to produce bacterial cellulose using a water-soluble component in waste as a raw material.
[0022] 本発明に係るバクテリアセルロースの製造方法は、キノコから得られた処理物を含 む培地中でセルロース生産菌を培養することを特徴とする(ここで「処理物」とは、水 溶性成分を得る処理をキノコに対して行った結果得られたものを 、う)。具体的には、 キノコ由来の水溶性成分を含む溶液 (例えば、圧搾液や抽出液など)ゃキノコ由来の 水溶性成分の乾燥物(例えば、圧搾液や抽出液を乾燥させたもの)などが例として挙 げられる。 [0022] The method for producing bacterial cellulose according to the present invention is characterized by culturing cellulose-producing bacteria in a medium containing a treated product obtained from mushrooms (here, "treated product" means water-soluble). What was obtained as a result of applying the component to the mushroom was obtained. Specifically, a solution containing a water-soluble component derived from a mushroom (for example, a compressed solution or an extract) or a dried product of a water-soluble component derived from a mushroom (for example, a product obtained by drying a compressed solution or an extract) Take as an example.
[0023] なお、本明細書で「キノコ」という用語は、「子嚢菌類や担子菌類の肉眼的な大きさ の子実体」の意味ではなぐ「大型の子実体を形成する子嚢菌類および担子菌類」の 意味で用いる。すなわち、本明細書における「キノコ」は、子実体だけでなく菌糸体も 含む。 [0024] キノコ力 処理物を得る方法は、キノコからマン-トールやグルコースなどの水溶性 成分を得られるのであれば、特に限定されない。処理物は乾燥物でも水溶液の状態 でもよいが、水溶液の方が作業効率の点から好ましい。すなわち、圧搾法によって得 られる圧搾液や水抽出法によって得られる抽出液などを、処理物としてそのまま用い ることができる。これらの簡便な方法を用いることにより人的コストを抑えることができる 。なお、処理物を乾燥物として得た場合は、水溶液にすることで前記圧搾液や抽出 液などと同じように扱うことができる。 [0023] In this specification, the term "mushroom" does not mean "a body of a macroscopic size of ascomycetes or basidiomycetes" or "ascomycetes and basidiomycetes forming a large fruiting body" Used to mean “fungi”. That is, “mushroom” in the present specification includes not only fruit bodies but also mycelia. [0024] The method for obtaining a processed product of mushroom is not particularly limited as long as water-soluble components such as mannitol and glucose can be obtained from mushrooms. The treated product may be a dry product or an aqueous solution, but an aqueous solution is preferable from the viewpoint of work efficiency. That is, the pressing liquid obtained by the pressing method, the extracting liquid obtained by the water extraction method, or the like can be used as a processed product. By using these simple methods, human costs can be suppressed. When the processed product is obtained as a dry product, it can be treated in the same manner as the above-mentioned pressing solution or extract by making it into an aqueous solution.
[0025] このような処理物を得る具体的な方法としては、例えば、キノコ収穫後の廃菌床を 圧搾して圧搾液を得る方法、廃菌床から水 (冷水または熱水)で抽出して抽出液を得 る方法、キノコ収穫後に菌床上に残った石突を圧搾して圧搾液を得る方法、キノコ子 実体を水煮して煮汁 (水煮残渣液)を得る方法、などが挙げられる。この場合、圧搾 液、抽出液および水煮残渣液が処理物に相当する。廃菌床にはキノコの菌糸だけで なくォガ粉やフスマなどが含まれるが、廃菌床全体の処理物であっても構わない。ま た、廃菌床ではなぐ種菌接種後かつキノコ収穫前の菌床であっても、もちろん構わ ない。  [0025] As a specific method for obtaining such a treated product, for example, a method for obtaining a compressed liquid by pressing a waste fungus bed after harvesting mushrooms, extraction from the waste fungus bed with water (cold water or hot water). And a method of obtaining an extract, a method of obtaining a squeezed solution by squeezing a stone tip remaining on a fungus bed after harvesting mushrooms, and a method of obtaining a simmered juice (boiled residue) by boiling a mushroom fruit body. . In this case, the pressed solution, the extract solution, and the boiled residue solution correspond to the processed product. The waste fungus bed contains not only mushroom mycelia but also oga powder and bran, etc., but it may be a processed product of the entire waste fungus bed. Of course, it does not matter if it is a bed after inoculation with the inoculum and before harvesting the mushrooms.
[0026] 上記方法によって得られた処理物には、用いるキノコの種類および処理物を得る方 法によって異なる力 マン-トール、グリセロール、グルコース、フルクトース、トレハロ ース、ァラビトールおよびイノシトールなどの水溶性成分 (糖および糖アルコールなど )が含まれている。これらの水溶性成分は、種によりその量および割合が異なるもの の、多くのキノコに含まれている(日本食品工業学会誌, Vol.31, No.12, 765-771) oこ れらの中では、マン-トール、グリセロールおよびグルコースの割合が大きぐ特にマ ン-トールの割合が大きいことが好ましい。非特許文献 1に示されたように、マン-ト ールを含む培地はバクテリアセルロースの生産に好適であると考えられる。実際、本 発明に係るバクテリアセルロースの製造方法は、一般的に用いられて 、る HS培地を 用いた方法に比べてバクテリアセルロースの収量が多くなることが示されて 、る(実施 例参照)。  [0026] The treated product obtained by the above method has different power depending on the type of mushroom to be used and the method of obtaining the treated product. Water-soluble components such as mannitol, glycerol, glucose, fructose, trehalose, arabitol and inositol (Such as sugar and sugar alcohol). These water-soluble components are contained in many mushrooms, although their amounts and proportions vary depending on the species (Journal of Japanese Food Industry Association, Vol.31, No.12, 765-771). Among them, it is preferable that the ratio of mannitol, glycerol and glucose is large, and particularly the ratio of mannitol is large. As shown in Non-Patent Document 1, a medium containing mantol is considered suitable for production of bacterial cellulose. In fact, the method for producing bacterial cellulose according to the present invention is generally used, and it has been shown that the yield of bacterial cellulose is increased as compared with the method using HS medium (see Examples).
[0027] 上記方法によって得られた処理物は、濃度調整または滅菌するだけでそのまま培 地とすることができる。培地の濃度は、培養するセルロース生産菌が生育できる条件 を適宜選択すればよい。例えば、ダルコノアセトパクター 'キシリヌスを培養する場合 は、ブリックス (Brix)濃度を HS培地と等しい 3.4%にすればよい。なお、生育不良が 出な 、限り、培地のブリックス濃度は特に限定されな 、。 [0027] The treated product obtained by the above method can be used as a medium as it is simply by adjusting the concentration or sterilizing. The concentration of the medium is the conditions under which the cultivating cellulose-producing bacteria can grow May be selected as appropriate. For example, when culturing dalconoacetopacter xylinus, the Brix concentration should be 3.4%, which is equal to HS medium. As long as no growth failure occurs, the Brix concentration of the medium is not particularly limited.
[0028] なお、本発明に係る培地は、キノコの処理物、またはそれを濃度調整したものもしく は滅菌したものを含むが、さらに任意成分が含まれていてもよい。任意成分としては 、例えば、炭素源 (例えば、グルコースなど)、窒素源 (例えば、アミノ酸など)、金属ィ オン源 (例えば、塩ィ匕カルシウムの水和塩など)、ビタミン類 (例えば、リボフラビンなど )などの微生物培養用培地に配合されることがある添加物などが挙げられる。また、 本発明に係る培地は、 HS培地などの培地が混合されて 、てもよ 、。  [0028] The medium according to the present invention includes a mushroom processed product, or a concentration-adjusted or sterilized product thereof, but may further include an optional component. Examples of optional components include a carbon source (eg, glucose), a nitrogen source (eg, amino acid), a metal ion source (eg, calcium salt hydrate), vitamins (eg, riboflavin, etc.) ) And the like, which may be added to the culture medium for microbial culture. The medium according to the present invention may be mixed with a medium such as an HS medium.
[0029] 本発明にお 、て処理されるキノコの種類は、前記処理物を得ることができるもので あれば特に限定されないが、キノコの水煮残渣液を使用できるので、食用キノコであ ることが好ましい。また、廃菌床および石突力も処理物を得ることができるので、栽培 キノコであることがより好ましい。食用栽培キノコとしては、例えば、タモギタケ (Pleurot us cornucopiae: uolden Oyster)、エノキタケ (Flammulina velutipes: Velvet Foot)、ヒ フタケ (Pleurotus ostreatus: Oyster Mushroom)、シロタモギタケ (Hypsizygus ulmarius : Elm Oyster)などが挙げられる。  [0029] In the present invention, the type of mushrooms to be treated is not particularly limited as long as the processed product can be obtained, but it is an edible mushroom because a boiled mushroom residue can be used. It is preferable. Moreover, since a waste mushroom bed and a stone thrust can also obtain a processed material, it is more preferable that it is a cultivation mushroom. Examples of edible mushrooms include Tamogitake (Pleurot us cornucopiae: uolden Oyster), Enokitake (Flammulina velutipes: Velvet Foot), Gifutake (Pleurotus ostreatus: Oyster Mushroom), and Shirotamogitake (Hypsizygus Elumyus). .
[0030] 本発明において使用されるセルロース生産菌の種類は、培地中においてセルロー スを生産できるものであれば特に限定されない。例えば、ダルコノアセトバクター属、 ァグロバクテリウム属、リゾピウム属、サルチナ属、シユードモナス属、ァクロモパクター 属、アルカリゲネス属、エロパクター属、ァゾトパクター属などに属するバクテリアを挙 げることができる。この中でも、ダルコノアセトバクタ一'キシリヌス(Gluconacetobacter xylinus:旧名 AcetoDacter xyiinum)カ奸 し ヽ。  [0030] The type of cellulose-producing bacterium used in the present invention is not particularly limited as long as it can produce cellulose in the medium. Examples include bacteria belonging to the genera Darconoacetobacter, Agrobacterium, Rhizopium, Sartina, Syudomonas, Achromopacter, Alkaligenes, Elopacter, Azotopacter, and the like. Of these, Gluconacetobacter xylinus (former name: AcetoDacter xyiinum).
[0031] 次に、培養方法について説明する。  [0031] Next, the culture method will be described.
[0032] 培養方法は、通常の細菌における培養方法を適用することができる。例えば、静置 培養、振盪培養または通気攪拌培養などが挙げられる。培養操作法としては、例え ば、回分培養法、流加回分培養法、反復回分培養法または連続培養法などを用い ることができる。攪拌手段としては、例えば、インペラ一 (攪拌羽根)、エアーリフト型培 養装置、培養ブロスのポンプ駆動循環などを単独または組み合わせて使用すること ができる。 [0032] As a culture method, a normal culture method for bacteria can be applied. For example, static culture, shaking culture or aeration and agitation culture can be mentioned. As the culture operation method, for example, a batch culture method, a fed-batch culture method, a repeated batch culture method or a continuous culture method can be used. As the stirring means, for example, an impeller (stirring blade), an air lift type culture device, a pump-driven circulation of culture broth, etc. may be used alone or in combination. Can do.
[0033] 培養装置も、通常の細菌における培養装置を適用することができる。例えば、槽内 を一定の温度に保温しうる攪拌機付きジャーフアーメンターなどを用いることができる  [0033] As the culture apparatus, a culture apparatus for normal bacteria can be applied. For example, a jar armor with a stirrer that can keep the inside of the tank at a constant temperature can be used.
[0034] 培養条件は、培養するセルロース生産菌が生育できる条件を適宜選択すればよ!ヽ 。例えば、ダルコノアセトパクター 'キシリヌスを培養する場合は、培養温度は室温、例 えば、 10〜40°C、好ましくは 25〜35°Cの範囲とすればよい。培地の pHは、 3〜7、 好ましくは 4〜6の範囲とすればよいが、水溶液の状態のキノコ由来の処理物は弱酸 性(pH5.0〜5.5)であるため、そのままの状態でダルコノアセトバクタ一'キシリヌスの 培養には好適である。もちろん任意のアルカリおよび酸を用いて pH調整をしてもょ ヽ [0034] The culture conditions may be appropriately selected so that the cultivating cellulose-producing bacteria can grow. For example, when culturing darconoacetopacter xylinus, the culture temperature may be room temperature, for example, 10 to 40 ° C., preferably 25 to 35 ° C. The pH of the medium should be in the range of 3-7, preferably 4-6. However, the processed product derived from mushrooms in the aqueous solution is weakly acidic (pH 5.0-5.5), so it remains in the dull state as it is. It is suitable for culturing Conoacetobacter-1 'xylinus. Of course, adjust the pH with any alkali and acid.
[0035] 培養期間は、通常の培養期間でよい。例えば、ダルコノアセトパクター ·キシリヌスを 用いる場合、約 7日間でゲル上のバクテリアセルロース膜を得ることができる。 [0035] The culture period may be a normal culture period. For example, when using darconoacetopactor xylinus, a bacterial cellulose film on a gel can be obtained in about 7 days.
[0036] 本発明に係るバクテリアセルロースの製造方法によって製造されるバクテリアセル口 ースは、そのまま回収してもよいし、回収物中に含まれる不純物を除去する処理を行 つてもよい。不純物を除去する方法としては、例えば、水洗、加圧脱水、希酸洗浄、 アルカリ洗浄、次亜塩素酸ソーダまたは過酸ィ匕水素などの漂白剤による処理、リゾチ ームなどの菌体溶解酵素による処理、ラウリル硫酸ソーダまたはデォキシコール酸な どの界面活性剤による処理、あるいは加熱洗浄などを単独または組み合わせて行え ばよい。  [0036] The bacterial cell mouth produced by the method for producing bacterial cellulose according to the present invention may be recovered as it is, or may be subjected to a treatment for removing impurities contained in the recovered material. Examples of the method for removing impurities include washing with water, pressure dehydration, dilute acid washing, alkali washing, treatment with a bleaching agent such as sodium hypochlorite or hydrogen peroxide, and a lytic enzyme such as lysozyme. Treatment with a surfactant, treatment with a surfactant such as sodium lauryl sulfate or deoxycholate, or heat washing may be performed alone or in combination.
[0037] 本発明に係るバクテリアセルロースの製造方法は、培地の原料としてキノコの生産 およびカ卩ェ時の廃棄物を用いることができる。これらの廃棄物は、生産元または加工 元からほぼ無償で調達できるので、原料コストを限りなく低く抑えることができる。また 、キノコの菌床栽培は通年行われているため、各廃棄物を安定して調達することがで きる。さらに、廃棄物からの培地調製は、圧搾、水抽出などの簡便な操作で可能であ るため、人的コストも低く抑えることができる。なお、培地を調製した後の残渣は、堆肥 、燃料、家畜飼料、家畜敷料などの従来の廃棄物の再利用用途にそのまま用いるこ とが可能である。 [0038] また、本発明に係るバクテリアセルロースの製造方法は、キノコの生産およびカロェ 時の廃棄物を上記従来の廃棄物の再利用用途に用いる際に、前記廃棄物の輸送コ ストの抑制、および前記廃棄物の保存性の向上を実現することができる。廃菌床の含 水率は約 70%、石突および子実体の含水率は約 90%であるが、これらの廃棄物を 上記再利用用途に用いるためには、輸送コストおよび保存性の点力も考慮すると、こ れらの廃棄物から水分を除去することが望まし 、。本発明に係るバクテリアセルロー スの製造方法では、圧搾法によって処理物を得ることによって、廃棄物の再利用を妨 げることなく廃棄物の水分を除去することができる。 [0037] The method for producing bacterial cellulose according to the present invention can use mushroom production and waste from the cultivation as a raw material of the medium. Since these wastes can be procured almost free of charge from the producer or processor, the raw material costs can be kept as low as possible. In addition, mushrooms are cultivated all year round, so each waste can be procured stably. Furthermore, since medium preparation from waste can be performed by simple operations such as pressing and water extraction, human costs can be kept low. The residue after the medium is prepared can be used as it is for reuse of conventional waste such as compost, fuel, livestock feed and livestock bedding. [0038] In addition, the method for producing bacterial cellulose according to the present invention includes the reduction of the waste transportation cost when the mushroom production and the waste at the time of Karoe are used for the above-mentioned conventional waste reuse, In addition, it is possible to improve the storage stability of the waste. The water content of the waste fungus bed is about 70%, and the water content of stone heads and fruit bodies is about 90%. However, in order to use these wastes for the above-mentioned reuse applications, the transportation cost and the preservability are also important. Considering that it is desirable to remove moisture from these wastes. In the method for producing bacterial cellulose according to the present invention, by obtaining a treated product by a pressing method, it is possible to remove moisture from the waste without hindering reuse of the waste.
[0039] 以下、実施例を参照しながら本発明を詳細に説明するが、本発明はこの実施例に より限定されるものではない。 Hereinafter, the present invention will be described in detail with reference to examples, but the present invention is not limited to these examples.
実施例  Example
[0040] (培地調製) [0040] (Preparation of medium)
処理物の原料は、タモギタケ収穫後の廃菌床 (カラマツォガ粉 +フスマ)、タモギタ ケ石突およびタモギタケの子実体を用いた。処理物は、廃菌床からは圧搾、冷水抽 出および熱水抽出によって、石突からは圧搾によって、子実体からは水煮によって、 水溶液として得た。得られた処理物は、対照として用いた HS培地とブリックス濃度が 等しくなるように、それぞれのブリックス濃度を 3.4%に調整した。以上の方法で得ら れた処理物をさらに滅菌したものを培地とした。  The raw material used for the treatment was waste bed after harvest of Tamogitake (Kalamatsuga powder + bran), Tamogitake crest and fruit body of Tamogitake. The treated product was obtained as an aqueous solution from the waste microbial bed by pressing, cold water extraction and hot water extraction, pressing from the stone tip, and boiling from the fruit body. The resulting treated product was adjusted to a Brix concentration of 3.4% so that the Brix concentration was equal to the HS medium used as a control. A medium obtained by further sterilizing the processed product obtained by the above method was used.
[0041] 以下、各原料力もの培地の調製方法についてより具体的に説明する。 [0041] Hereinafter, a method for preparing a medium having each raw material strength will be described more specifically.
[0042] まず、廃菌床を圧搾することによって培地を調製した場合である。タモギタケ収穫後 の廃菌床を約 500kNにて圧搾し、圧搾液を得た。得られた圧搾液をろ過し、ブリック ス濃度を 3.4%に調整し、オートクレープで滅菌することで、培地を得た。 [0042] First, the culture medium is prepared by squeezing the waste bacteria bed. The waste microbial bed after harvesting Tamogitake was squeezed at about 500 kN to obtain a squeezed solution. The obtained compressed solution was filtered, the brick concentration was adjusted to 3.4%, and sterilized with an autoclave to obtain a medium.
[0043] 次に、廃菌床カも冷水抽出することによって培地を調製した場合である。タモギタケ 収穫後の廃菌床に脱イオン水を加え、室温で 1時間攪拌した。得られた抽出液をろ 過し、ブリックス濃度を 3.4%に調整し、オートクレープで滅菌することで、培地を得た [0043] Next, it is a case where the culture medium is prepared by extracting the waste fungus bed with cold water. Tamogitake Deionized water was added to the harvested fungus bed and stirred for 1 hour at room temperature. The obtained extract was filtered, the Brix concentration was adjusted to 3.4%, and sterilized by autoclave to obtain a medium.
[0044] 次に、廃菌床カも熱水抽出することによって培地を調製した場合である。タモギタケ 収穫後の廃菌床に脱イオン水を加え、 1時間煮沸した。得られた抽出液をろ過し、ブ リックス濃度を 3.4%に調整し、オートクレープで滅菌することで、培地を得た。 [0044] Next, it is a case where the culture medium is prepared by hot water extraction of the waste fungus bed. Tamogitake Deionized water was added to the harvested fungus bed and boiled for 1 hour. The resulting extract is filtered and filtered. The medium was obtained by adjusting the Lix concentration to 3.4% and sterilizing with autoclave.
[0045] 次に、石突を圧搾することによって培地を調製した場合である。タモギタケ収穫後に 菌床上に残った石突をミキサーで粉砕した。粉砕された石突を圧搾し、圧搾液を得 た。得られた圧搾液をろ過し、ブリックス濃度を 3.4%に調整し、オートクレープで滅 菌することで、培地を得た。  [0045] Next, a culture medium is prepared by squeezing a stone tip. After harvesting the bamboo shoots, the stone bumps remaining on the fungus bed were crushed with a mixer. The crushed stone bump was squeezed to obtain a squeezed liquid. The obtained compressed solution was filtered, the Brix concentration was adjusted to 3.4%, and sterilized with an autoclave to obtain a medium.
[0046] 最後に、子実体を水煮することによって培地を調製した場合である。タモギタケを水 煮加工した際に生じた煮汁を得た。得られた煮汁をろ過し、ブリックス濃度を 3.4%に 調整し、オートクレープで滅菌することで、培地を得た。  [0046] Finally, a case where the medium is prepared by boiling the fruit body in water. Boiled soup produced when boiled tamamotake was obtained. The resulting broth was filtered, the Brix concentration was adjusted to 3.4%, and sterilized with an autoclave to obtain a medium.
[0047] 図 1は、各培地についての糖分析の結果を示すグラフである。高速液体クロマトダラ フィー(HPLC)による糖分析の結果、各培地には、マン-トール、グリセロール、ダル コース、フルクトース、トレハロース、ァラビトール、イノシトールなどが含まれていること がわかった。廃棄物の種類および処理方法によって、各糖および糖アルコールの濃 度は多少異なっていたが、組成はほぼ共通であった。全ての培地において最も含有 割合が大き力つたのはマン-トールであった。ブリックス濃度を等しく調整した各培地 における上記 7種の糖類の合計含有割合は、 1.2% (菌床圧搾)、 1.0% (冷水抽出) 、 1.1% (熱水抽出)、 0.9% (石突圧搾)および 1.1% (水煮残渣液)であった。対照と して、カラマッォガ粉のみの抽出液についても糖分析を行った力 前記各処理物で 含有量が多力つたグリセロールでも 0.03%し力含まれていなかった。  FIG. 1 is a graph showing the results of sugar analysis for each medium. As a result of sugar analysis by high performance liquid chromatography (HPLC), it was found that each medium contained mannitol, glycerol, dalcose, fructose, trehalose, arabitol, inositol and the like. Depending on the type of waste and the treatment method, the concentration of each sugar and sugar alcohol was slightly different, but the composition was almost the same. In all the media, mannitol had the largest content. The total content of the above seven sugars in each medium adjusted to the same Brix concentration is 1.2% (bacteria bed press), 1.0% (cold water extraction), 1.1% (hot water extraction), 0.9% (stone bump press) and 1.1% (boiled residue liquid). As a control, the strength of the sugar analysis was also obtained for the extract of only kala maggot powder.
[0048] (培養)  [0048] (culture)
セルロース生産菌として、ダルコノアセトバクタ^ ~ ·キシリヌス(Gluconacetobacter xyl inus)ATCC—10245株を用いた。前培養は HS寒天培地を用いて行い、次いで、 深底シャーレ(直径 9cm)中の 40mLの前記各培地に前記前培養液を 1白金耳接種 した。また、対照実験として HS培地における培養を行うため、深底シャーレ(直径 9c m)中の 40mLの HS培地(グルコース 2.0%、ペプトン 0.5%、イースト抽出物 0.5%、 リン酸 2ナトリウム 0.15%およびクェン酸 0.27%を滅菌水に溶解したもの: pH = 6.0) にも接種した。培養温度は 29°C、培養期間は 1週間とし、静置培養を行った。  As a cellulose-producing bacterium, darconoacetobacter xylinus ATCC-10245 strain was used. Pre-culture was performed using HS agar medium, and then one platinum loop of the pre-culture liquid was inoculated into 40 mL of each medium in a deep bottom petri dish (diameter 9 cm). As a control experiment, 40 mL of HS medium (glucose 2.0%, peptone 0.5%, yeast extract 0.5%, disodium phosphate 0.15%, and ken Acid 0.27% dissolved in sterile water: pH = 6.0) was also inoculated. The culture temperature was 29 ° C, the culture period was 1 week, and stationary culture was performed.
[0049] (バクテリアセルロースの定量) [0049] (Quantification of bacterial cellulose)
培地の表面に生成されたバクテリアセルロース膜を分離し、 1M水酸ィ匕ナトリウム水 溶液で煮沸処理後中和し、 105°Cのオーブンで 15時間かけて乾燥させ、重量を測 定した。図 2はその結果を示すグラフである。前記各培地で培養したシャーレにおけ るバクテリアセルロースの収量は、対照実験で行った HS培地のシャーレにおける収 量の 1.2倍 (菌床圧搾)、 1.2倍 (冷水抽出)、 1.1倍 (熱水抽出)、 2.8倍 (石突圧搾) および 1.7倍 (水煮残渣液)であった。これらのデータから、残渣 1トン力 0.2〜2.0k gのバクテリアセルロースを製造できることが試算された。 Bacterial cellulose membrane formed on the surface of the culture medium is separated, and 1M sodium hydroxide The solution was neutralized after boiling, dried in an oven at 105 ° C for 15 hours, and weighed. Figure 2 is a graph showing the results. The yield of bacterial cellulose in petri dishes cultured in the above media was 1.2 times (bacterial bed press), 1.2 times (cold water extraction), 1.1 times (hot water extraction) of the HS medium petri dishes in the control experiments. ), 2.8 times (stone squeezed) and 1.7 times (boiled residue). From these data, it was estimated that bacterial cellulose having a residue 1 ton force of 0.2 to 2.0 kg could be produced.
[0050] また、培養後に、菌床由来の各培地における前記 7種の糖類の合計含有割合を分 祈したところ、 0.28% (菌床圧搾)、 0.21% (冷水抽出)、 0.19% (熱水抽出)であり、 培養前の培地に比べて各種の糖類が著しく減少していることがわ力つた。さらに、ここ ではデータを示さないが、マン-トール、グルコースおよびイノシトールは、 7日間の 培養でほぼ全量(95%以上)消費されていた。これらのことから、キノコの生産時およ び加工時に生じる廃棄物に残存する水溶性成分は、バクテリアセルロースの生産に 有効であることが示唆された。  [0050] Further, after culturing, when the total content of the seven sugars in each medium derived from the fungus bed was prayed, 0.28% (bacteria bed pressing), 0.21% (cold water extraction), 0.19% (hot water) Extraction), and various sugars were significantly reduced compared to the medium before the culture. Furthermore, although data are not shown here, man-tol, glucose and inositol were consumed almost entirely (over 95%) in 7 days of culture. These results suggest that the water-soluble components remaining in the waste generated during mushroom production and processing are effective for the production of bacterial cellulose.
[0051] 2005年 11月 29曰出願の特願 2005— 344633の曰本出願に含まれる明細書、図 面および要約書の開示内容は、すべて本願に援用される。本願は、当該出願に基 づく優先権を主張する。  [0051] Nov. 29 29, Japanese Patent Application No. 2005-344633 The contents of the description, drawings and abstract contained in this application are all incorporated herein by reference. This application claims priority based on that application.
産業上の利用可能性  Industrial applicability
[0052] 本発明によって、バクテリアセルロースの製造コストを抑えることができるので、分離 膜、医療用'化粧用パッド、スピーカーコーン、セルロース皮膜成形ペイント、増粘剤 、紙、複合材料などの多様な用途に向けて、バクテリアセルロースを安価に提供する ことができる。 [0052] According to the present invention, the production cost of bacterial cellulose can be reduced, so that it can be used in various applications such as separation membranes, medical's cosmetic pads, speaker cones, cellulose film-forming paints, thickeners, paper, and composite materials. Therefore, bacterial cellulose can be provided at a low cost.

Claims

請求の範囲 The scope of the claims
[I] キノコの子実体または菌糸体の処理物を含む培地中でセルロース生産菌を培養す るステップを有するバクテリアセルロースの製造方法。  [I] A method for producing bacterial cellulose comprising a step of culturing a cellulose-producing bacterium in a medium containing a processed product of mushroom fruit bodies or mycelium.
[2] 前記処理物は、キノコの子実体または菌糸体の、圧搾液または抽出液である、請求 項 1記載のバクテリアセルロースの製造方法。  [2] The method for producing bacterial cellulose according to claim 1, wherein the treated product is a pressed or extracted liquid of a fruit body or mycelium of a mushroom.
[3] 前記処理物は、キノコ廃菌床圧搾液、キノコ廃菌床抽出液、キノコ石突圧搾液、ま たは、キノコ水煮残渣液、のいずれかである、請求項 1記載のバクテリアセルロースの 製造方法。 [3] The bacterial cellulose according to claim 1, wherein the treated product is any one of a mushroom waste fungus bed compressed solution, a mushroom waste fungus bed extract, a mushroom stone squeeze solution, or a mushroom boiled residue solution. The manufacturing method.
[4] 前記キノコはタモギタケ(Pleurotus cornucopiae)である、請求項 1記載のバクテリア セルロースの製造方法。  [4] The method for producing bacterial cellulose according to claim 1, wherein the mushroom is Pleurotus cornucopiae.
[5] 前記キノコはタモギタケ(Pleurotus cornucopiae)である、請求項 2記載のバクテリア セルロースの製造方法。  5. The method for producing bacterial cellulose according to claim 2, wherein the mushroom is Pleurotus cornucopiae.
[6] 前記キノコはタモギタケ(Pleurotus cornucopiae)である、請求項 3記載のバクテリア セルロースの製造方法。  6. The method for producing bacterial cellulose according to claim 3, wherein the mushroom is Pleurotus cornucopiae.
[7] 前記セルロース生産菌はダルコノアセトバクタ^ ~ ·キシリヌス(Gluconacetobacter xyli nus)である、請求項 1記載のバクテリアセルロースの製造方法。  [7] The method for producing bacterial cellulose according to [1], wherein the cellulose-producing bacterium is Gluconacetobacter xylinus.
[8] 前記セルロース生産菌はダルコノアセトバクタ^ ~ ·キシリヌス(Gluconacetobacter xyli nus)である、請求項 2記載のバクテリアセルロースの製造方法。 [8] The method for producing bacterial cellulose according to [2], wherein the cellulose-producing bacterium is Gluconacetobacter xylinus.
[9] 前記セルロース生産菌はダルコノアセトバクタ^ ~ ·キシリヌス(Gluconacetobacter xyli nus)である、請求項 3記載のバクテリアセルロースの製造方法。 [9] The method for producing bacterial cellulose according to claim 3, wherein the cellulose-producing bacterium is Gluconacetobacter xylinus.
[10] 前記処理物はマン-トールを含む、請求項 1記載のバクテリアセルロースの製造方 法。 10. The method for producing bacterial cellulose according to claim 1, wherein the treated product contains mannitol.
[I I] 前記処理物はマン-トールを含む、請求項 2記載のバクテリアセルロースの製造方 法。  [I I] The method for producing bacterial cellulose according to claim 2, wherein the treated product contains mannitol.
[12] 前記処理物はマン-トールを含む、請求項 3記載のバクテリアセルロースの製造方 法。  12. The method for producing bacterial cellulose according to claim 3, wherein the treated product contains mannitol.
[13] キノコの子実体または菌糸体の処理物を含むセルロース生産菌培養用培地。  [13] A culture medium for culturing cellulose-producing bacteria, comprising a processed product of mushroom fruit bodies or mycelium.
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