JPS6367823B2 - - Google Patents
Info
- Publication number
- JPS6367823B2 JPS6367823B2 JP58046888A JP4688883A JPS6367823B2 JP S6367823 B2 JPS6367823 B2 JP S6367823B2 JP 58046888 A JP58046888 A JP 58046888A JP 4688883 A JP4688883 A JP 4688883A JP S6367823 B2 JPS6367823 B2 JP S6367823B2
- Authority
- JP
- Japan
- Prior art keywords
- pullulan
- roasted dextrin
- dextrin
- sizing agent
- present
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 229920001218 Pullulan Polymers 0.000 claims description 28
- 235000019423 pullulan Nutrition 0.000 claims description 28
- 239000004373 Pullulan Substances 0.000 claims description 27
- 239000004375 Dextrin Substances 0.000 claims description 26
- 229920001353 Dextrin Polymers 0.000 claims description 26
- 235000019425 dextrin Nutrition 0.000 claims description 26
- 238000004513 sizing Methods 0.000 claims description 12
- 239000003795 chemical substances by application Substances 0.000 claims description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 9
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 9
- 238000012258 culturing Methods 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 239000000853 adhesive Substances 0.000 description 13
- 230000001070 adhesive effect Effects 0.000 description 13
- 239000000243 solution Substances 0.000 description 9
- 239000003292 glue Substances 0.000 description 7
- 108090000790 Enzymes Proteins 0.000 description 6
- 102000004190 Enzymes Human genes 0.000 description 6
- 229920002472 Starch Polymers 0.000 description 6
- 239000000123 paper Substances 0.000 description 6
- 239000008107 starch Substances 0.000 description 6
- 235000019698 starch Nutrition 0.000 description 6
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 4
- 239000002655 kraft paper Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- 239000002609 medium Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 230000001580 bacterial effect Effects 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000001963 growth medium Substances 0.000 description 3
- 239000003960 organic solvent Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 229920000856 Amylose Polymers 0.000 description 2
- 241000223678 Aureobasidium pullulans Species 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 2
- 229920000881 Modified starch Polymers 0.000 description 2
- 239000004368 Modified starch Substances 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 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 description 2
- 229930006000 Sucrose Natural products 0.000 description 2
- 240000008042 Zea mays Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 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 2
- 235000005822 corn Nutrition 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 2
- 235000019341 magnesium sulphate Nutrition 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 235000019426 modified starch Nutrition 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 235000002639 sodium chloride Nutrition 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000005720 sucrose Substances 0.000 description 2
- 239000006188 syrup Substances 0.000 description 2
- 235000020357 syrup Nutrition 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- LWIHDJKSTIGBAC-UHFFFAOYSA-K tripotassium phosphate Chemical compound [K+].[K+].[K+].[O-]P([O-])([O-])=O LWIHDJKSTIGBAC-UHFFFAOYSA-K 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- WZFUQSJFWNHZHM-UHFFFAOYSA-N 2-[4-[2-(2,3-dihydro-1H-inden-2-ylamino)pyrimidin-5-yl]piperazin-1-yl]-1-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethanone Chemical compound C1C(CC2=CC=CC=C12)NC1=NC=C(C=N1)N1CCN(CC1)CC(=O)N1CC2=C(CC1)NN=N2 WZFUQSJFWNHZHM-UHFFFAOYSA-N 0.000 description 1
- 244000215068 Acacia senegal Species 0.000 description 1
- 229920000945 Amylopectin Polymers 0.000 description 1
- 241000223651 Aureobasidium Species 0.000 description 1
- 108010010803 Gelatin Proteins 0.000 description 1
- 229920000084 Gum arabic Polymers 0.000 description 1
- 244000017020 Ipomoea batatas Species 0.000 description 1
- 235000002678 Ipomoea batatas Nutrition 0.000 description 1
- 240000003183 Manihot esculenta Species 0.000 description 1
- 235000016735 Manihot esculenta subsp esculenta Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- 239000004372 Polyvinyl alcohol Substances 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 235000021307 Triticum Nutrition 0.000 description 1
- 244000098338 Triticum aestivum Species 0.000 description 1
- 235000010489 acacia gum Nutrition 0.000 description 1
- 239000000205 acacia gum Substances 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 235000008504 concentrate Nutrition 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000008121 dextrose Substances 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000002036 drum drying Methods 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- BXKDSDJJOVIHMX-UHFFFAOYSA-N edrophonium chloride Chemical compound [Cl-].CC[N+](C)(C)C1=CC=CC(O)=C1 BXKDSDJJOVIHMX-UHFFFAOYSA-N 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000004744 fabric 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
- 238000002523 gelfiltration Methods 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910000358 iron sulfate Inorganic materials 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 235000010755 mineral Nutrition 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000002772 monosaccharides Chemical class 0.000 description 1
- 239000001254 oxidized starch Substances 0.000 description 1
- 235000013808 oxidized starch Nutrition 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 229910000160 potassium phosphate Inorganic materials 0.000 description 1
- 235000011009 potassium phosphates Nutrition 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005215 recombination Methods 0.000 description 1
- 230000006798 recombination Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 238000006276 transfer reaction Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01K—ANIMAL HUSBANDRY; AVICULTURE; APICULTURE; PISCICULTURE; FISHING; REARING OR BREEDING ANIMALS, NOT OTHERWISE PROVIDED FOR; NEW BREEDS OF ANIMALS
- A01K87/00—Fishing rods
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Environmental Sciences (AREA)
- Marine Sciences & Fisheries (AREA)
- Animal Husbandry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Polysaccharides And Polysaccharide Derivatives (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Adhesives Or Adhesive Processes (AREA)
- General Preparation And Processing Of Foods (AREA)
- Jellies, Jams, And Syrups (AREA)
Description
本発明は焙焼デキストリンを炭素源として含有
する培地にプルラン生産菌を培養することによつ
て得られる組成物を主成分とする再湿性接着剤、
粘結剤、繊維用糊剤等に好適に用いられる接着
力、粘結力、皮膜性優れた糊剤およびその製造法
に関するものである。
従来より、焙焼デキストリンは糊液の粘性が著
しく低い、糊液の安定性は分解度に応じ非常に良
くなり、高分解度のものは完全に冷水可溶性であ
る、接着力、粘結力は高濃度において強い。とい
う特徴を生かし、紙工、切手、レツテル、ガムテ
ープ、転写紙、鋳物の砂型、電気溶接棒、砥石、
石膏ボード、絵具などの接着剤、医薬、染料、酵
素などの希釈剤、繊維の仕上用あるいは捺染用の
糊剤として用いられている。
また、焙焼デキストリンは上記の性質に加え
て、他の糊剤(例えば、ポリビニルアルコール、
ゼラチン、にかわ、アラビアガム、プルラン)に
比べ安価であるというコスト面での利点がある
が、耐黴性、皮膜の耐湿性および脆さ、塗布紙の
カール性等に問題がある。
一方、プルランは糊液の粘度が低い、冷水に非
常に良く溶解する、接着力、粘結力が良好、皮膜
に耐湿性があり、脆さがない。という特徴がある
が他の糊剤に比べ高価であるため、工業的分野で
は実際にはほとんど使用されていないのが現状で
ある。
通常、プルランは生産菌株を炭素源として蔗
糖、ぶどう糖、または湿式において酵素または酸
加水分解された澱粉部分加水分解物(特願昭46―
79413)を含む液体培地に5〜8日間通気培養し、
その培養液より生成したプルランを分離精製する
ことによつて得られている。
しかしながら、短時間の培養で高収率にプルラ
ンを得ることは困難であり、しかも、培養終了後
加熱して酵素を失活させ、菌体を除去し、メタノ
ール等の有機溶媒を等量以上加えプルランを沈殿
を沈殿させ、これを集め水に溶解して同様に沈殿
を繰返して精製後、乾燥することによりプルラン
粉末を得ていたため非常に高価なものとなつてい
た。
本発明者らは良好な接着力、粘結力、皮膜性、
耐湿性を有し、かつ安価な糊剤を得るべく鋭意研
究を重ねた結果、焙焼デキストリンを炭素源とし
て含有する培地にプルラン生産菌を培養すること
によつて得られる組成物を主成分とする糊剤が最
適であり、単にプルランと焙焼デキストリンを混
合したものより優れていることを見出し本発明を
完成するに至つた。
培地の炭素源として用いる焙焼デキストリンは
馬鈴薯、甘藷、トウモロコシ、高アミローストウ
モロシ、小麦、米、タピオカ、サゴ等から得られ
る天然澱粉、アミロースやアミロペクチン分画
物、架橋澱粉、エーテル化澱粉、エステル化澱
粉、酸化澱粉、酸処理化澱粉等を原料とし、わず
かの鉱酸と共に加熱して得られる白色および黄色
デキストリンと無酸またはアルカリ性で焙焼され
たブリテイシユガムが用いられる。
焙焼デキストリンは湿式による酸加水分解物、
酵素変性デキストリンのような単なる加水分解反
応のみでなく、転移反応と切断分子の再結合反応
を経て得られるところに大きな特徴があり、湿式
による酸加水分解物、酵素変性デキストリンとは
分子構造および性質が異つている。
本発明に用いられる焙焼デキストリンはその加
水分解度(以後DEと略称し、還元糖値をデキス
トロースに換算した値で表わす)が0.5〜20のも
のが利用し得る。この焙焼デキストリンが培地に
用いられる濃度は5〜40%好ましくは15〜30%の
範囲である。
培地として必要な他の窒素源は通常使用せられ
る有機または無機窒素が用いられる。また無機塩
類も公知の塩類が使用される。即ち燐酸カリウ
ム、塩化ナトリウム、硫酸マグネシウム、硫酸鉄
等を用いる。
プルラン生産菌株はプルラン生産能を有する菌
株であれば何れも用いられるが、例えば、
Pullularia Pulluans AHU9553、Pullularia
Pullulans IFO6353、Dematium Pullulans
IFO4464 Aureobasidium PullulansIFO6401,
6402,6353等多数の菌株が用いられる。
培養に際しては、最初のPHは5.0〜7.5、焙養温
度は22〜30℃に調整し、常法により通気撹拌す
る。所要培養時間は通常5〜8日間必要とする
が、本発明においては通常より高濃度で培養し、
残存する焙焼デキストリンも有効に利用しうるた
め培養所要時間を3〜5日に短縮することができ
る。
培養終了後は、通常、培養液を加熱して酵素を
失活させ、菌体を除去、脱色、濃縮、有機溶媒に
よる分別精製が必要であるが、本発明の糊剤にお
いては、糊液として用いる場合は培養液を加熱し
て酵素を失活し、滅菌しそのままあるいは必要に
よりろ過、濃縮してドラム乾燥、噴霧乾燥あるい
は有機溶媒による沈殿などの手段により粉末化す
ることができる。
本発明の糊剤溶液のPHは3〜8、粘度は103〜
105cps(15%水溶液、30℃、B型回転粘度計)、生
産されるプルランの分子量は103〜106である。
本発明の糊剤における成分は生産されるプルラ
ン、残存する焙焼デキストリンおよびそれら以外
のもの(菌体により変性され、培地に使用された
焙焼デキストリンと構造の異つたデキストリンお
よび、単糖、酵素変性デキストリン、酸糖化水飴
を炭素源とした場合に生産されるプルランと構造
が異つたプルランが副生されていると考えられ
る。)であり、主成分のプルランと焙焼デキスト
リンの比率は培養条件により、変わるがプルラ
ン:焙焼デキストリン=7:3〜3:7(重量比)
の範囲に入る。しかも、これらの比率でプルラン
と焙焼デキストリンを混合したものよりも本発明
の糊剤の方が接着力、粘結力が優り、しかも製造
コストが低くなることが見出された。
本発明の糊剤は良好な接着力、粘結力、皮膜
性、耐湿性等を有するため紙工、切手、レツテ
ル、ガムテープ、転写紙、鋳物の砂型、電気溶接
棒、砥石、セラミツク、石膏ボード、絵具などの
接着剤、繊維の仕上用あるいはサイジング用糊
剤、製紙のコーテイングバインダー、として有効
に使用することができる。
次に実施例により本発明を更に詳しく説明す
る。
実施例 1
本発明の糊剤の製造においてDematium
Pullulans IFO4464菌株に対して炭素源として蔗
糖、グルコース、酸糖化水飴(DE45)、焙焼デキ
ストリン(DE0.7、5、10、17)を用いて炭素源
の種類と培養時間の影響を検討した。
使用培地の組成は炭素源20.0%、K2HPO40.2
%、Nac10.2%、ペプトン0.4%、MgSO4、
7H2O0.04%、FeSO4.7H2O0.001%であり、最初
のPH7.5、焙養温度28℃、培養時間3、4、5日
間、ロータリーシエーカー使用。
生産されたプルランの収量(g/)を表1に
示す。また、ゲル濾過法により得られたプルラン
の分子量を測定した結果、表1の試料番号1、
2、6より得られたものはおよそ103、試料番号
5のものはおよそ104、試料番号4のものはおよ
そ106、試料番号3のものは105であつた。
The present invention provides a rewetting adhesive mainly comprising a composition obtained by culturing pullulan-producing bacteria in a medium containing roasted dextrin as a carbon source;
The present invention relates to a sizing agent with excellent adhesive strength, caking strength, and film properties, which is suitably used as a binder, a sizing agent for fibers, etc., and a method for producing the same. Conventionally, roasted dextrin has a significantly low viscosity of the size liquid, the stability of the size liquid improves depending on the degree of decomposition, and those with a high degree of decomposition are completely soluble in cold water, and the adhesive strength and caking strength are Strong at high concentrations. Taking advantage of this feature, we are able to produce paper products, stamps, stamps, gummed tape, transfer paper, foundry sand molds, electric welding rods, whetstones,
It is used as an adhesive for plasterboard and paint, a diluent for medicines, dyes, enzymes, etc., and a sizing agent for finishing textiles and printing. In addition to the above-mentioned properties, roasted dextrin also has other sizing agents (e.g., polyvinyl alcohol,
Although it has the advantage of being cheaper than gelatin, glue, gum arabic, and pullulan), it has problems with mold resistance, moisture resistance and brittleness of the film, and curling of coated paper. On the other hand, pullulan has a low viscosity in the size liquid, dissolves very well in cold water, has good adhesion and cohesive strength, has a moisture-resistant film, and is not brittle. However, because it is more expensive than other adhesives, it is currently hardly used in the industrial field. Usually, pullulan is produced using sucrose, glucose, or a starch partial hydrolyzate (patent application 1973-
79413) for 5 to 8 days,
It is obtained by separating and purifying pullulan produced from the culture solution. However, it is difficult to obtain pullulan in high yield through short-term cultivation, and furthermore, after the cultivation is completed, the enzymes are inactivated by heating, the bacterial cells are removed, and more than an equal amount of an organic solvent such as methanol is added. Pullulan powder was obtained by precipitating pullulan, collecting the precipitate, dissolving it in water, repeating the same precipitation, and then drying to obtain pullulan powder, making it very expensive. The present inventors have found that good adhesive strength, caking strength, film properties,
As a result of extensive research in order to obtain a glue that is both moisture-resistant and inexpensive, we have developed a composition whose main ingredient is a composition obtained by culturing pullulan-producing bacteria in a medium containing roasted dextrin as a carbon source. The present inventors have discovered that a sizing agent based on the present invention is optimal and is superior to a simple mixture of pullulan and roasted dextrin, leading to the completion of the present invention. The roasted dextrin used as a carbon source for the culture medium is natural starch obtained from potatoes, sweet potatoes, corn, high amylose corn, wheat, rice, tapioca, sago, etc., amylose and amylopectin fractions, cross-linked starch, etherified starch, and esters. White and yellow dextrins obtained by heating modified starch, oxidized starch, acid-treated starch, etc. with a small amount of mineral acid, and British gum roasted in an acid-free or alkaline environment are used. Roasted dextrin is a wet acid hydrolyzate,
The major feature of enzyme-modified dextrin is that it is obtained not only through a simple hydrolysis reaction, but also through a transfer reaction and a recombination reaction of cut molecules. are different. The roasted dextrin used in the present invention may have a degree of hydrolysis (hereinafter abbreviated as DE, expressed as a reducing sugar value converted to dextrose) of 0.5 to 20. The concentration of this torrefied dextrin used in the culture medium ranges from 5 to 40%, preferably from 15 to 30%. Other nitrogen sources necessary for the medium include commonly used organic or inorganic nitrogen. Also, known inorganic salts may be used. That is, potassium phosphate, sodium chloride, magnesium sulfate, iron sulfate, etc. are used. Any strain capable of producing pullulan can be used as the pullulan-producing strain, but for example,
Pullularia Pulluans AHU9553, Pullularia
Pullulans IFO6353, Dematium Pullulans
IFO4464 Aureobasidium PullulansIFO6401,
Many strains such as 6402 and 6353 are used. During cultivation, the initial pH is adjusted to 5.0 to 7.5, the roasting temperature is adjusted to 22 to 30°C, and the mixture is aerated and stirred using a conventional method. The required culture time is usually 5 to 8 days, but in the present invention, the culture is carried out at a higher concentration than usual,
Since the remaining roasted dextrin can also be effectively utilized, the time required for culturing can be shortened to 3 to 5 days. After culturing, it is usually necessary to heat the culture solution to inactivate enzymes, remove bacterial cells, decolorize, concentrate, and separate and purify using an organic solvent. When used, the culture solution can be heated to inactivate the enzyme, sterilized, and left as is, or if necessary, filtered, concentrated, and powdered by means such as drum drying, spray drying, or precipitation with an organic solvent. The PH of the glue solution of the present invention is 3 to 8, and the viscosity is 10 3 to 8.
10 5 cps (15% aqueous solution, 30° C., B-type rotational viscometer), and the molecular weight of the pullulan produced is 10 3 to 10 6 . The ingredients in the glue of the present invention are the produced pullulan, the remaining roasted dextrin, and other things (dextrin that has been modified by bacterial cells and has a different structure from the roasted dextrin used in the culture medium, monosaccharides, and enzymes). It is thought that pullulan, which has a different structure from the pullulan produced when modified dextrin or acid-saccharified starch syrup is used as a carbon source, is produced as a by-product.) The ratio of the main component pullulan to roasted dextrin varies depending on the culture conditions. Depending on the situation, pullulan: roasted dextrin = 7:3 to 3:7 (weight ratio)
falls within the range of Moreover, it has been found that the sizing agent of the present invention has superior adhesive strength and caking strength, and has a lower manufacturing cost than a mixture of pullulan and roasted dextrin in these ratios. The adhesive of the present invention has good adhesive strength, caking strength, film properties, moisture resistance, etc., and is therefore used in paper making, stamps, labels, gummed tape, transfer paper, foundry sand molds, electric welding rods, grindstones, ceramics, gypsum boards, etc. It can be effectively used as an adhesive for paints, a sizing agent for finishing or sizing fibers, and a coating binder for paper manufacturing. Next, the present invention will be explained in more detail with reference to Examples. Example 1 In the production of the sizing agent of the present invention, Dematium
Using sucrose, glucose, acid-saccharified starch syrup (DE45), and roasted dextrin (DE0.7, 5, 10, and 17) as carbon sources for the Pullulans IFO4464 strain, the effects of the type of carbon source and culture time were investigated. The composition of the medium used is carbon source 20.0%, K 2 HPO 4 0.2
%, Nac10.2%, Peptone 0.4%, MgSO4 ,
7H 2 O 0.04%, FeSO 4 .7H 2 O 0.001%, initial pH 7.5, roasting temperature 28°C, culture time 3, 4, 5 days, using rotary shaker. Table 1 shows the yield (g/) of pullulan produced. In addition, as a result of measuring the molecular weight of pullulan obtained by gel filtration method, sample number 1 in Table 1,
The amount obtained from samples No. 2 and 6 was approximately 10 3 , the amount obtained from sample number 5 was approximately 10 4 , the amount obtained from sample number 4 was approximately 10 6 , and the amount obtained from sample number 3 was 10 5 .
【表】【table】
【表】
実施例 2
実施例1で得られた培養液(試料番号1〜6)
を加熱し、酵素を失活し、滅菌し、ろ過、濃縮し
て25%糊液にしたもの、およびこれらと比較する
ため市販プルラン(分子量30万)、焙焼デキスト
リン(DE3)および前記プルランと焙焼デキスト
リンを7:3の割合で混合したものの25%糊液を
用いて以下の条件で接着力試験を行つた。
各糊液を上質クラフト紙を30mm×60mmに切断
し、一端の30mm×3mmにm2当り30gの糊固形分が
付着するように塗布した。
塗布後5、30、120秒放置し、30mm×60mmのク
ラフト紙の一端を糊部に重ねて接着し、接着後
10、20秒放置して接着力を測定した。結果を表2
に示す。[Table] Example 2 Culture solution obtained in Example 1 (sample numbers 1 to 6)
was heated to deactivate the enzyme, sterilized, filtered, and concentrated to make a 25% paste solution, and for comparison with these, commercially available pullulan (molecular weight 300,000), roasted dextrin (DE3), and the above-mentioned pullulan. An adhesion test was conducted under the following conditions using a 25% glue solution made by mixing roasted dextrin at a ratio of 7:3. Each size solution was applied to a piece of high-quality kraft paper cut into 30 mm x 60 mm so that 30 g solid glue per m 2 was applied to one end of 30 mm x 3 mm. After application, leave for 5, 30, and 120 seconds, overlap one end of 30mm x 60mm kraft paper on the glue part, and adhere.
The adhesive force was measured after being left for 10 or 20 seconds. Table 2 shows the results.
Shown below.
【表】【table】
【表】
実施例 3
実施例2の糊液サンプルを用いて、上質クラフ
ト紙に40g/m2の固形分になるように塗布し、70
℃で1時間乾燥後、20℃、65%RHの恒温恒湿室
内で1昼夜平衡状態に保つた後、実施例2と同様
に30mm×60mmに切断し、その一端の糊面30mm×30
mmを濡水後2、5、10秒放置し、同形のクラフト
紙の一端30mm×30mmに重ねて500gの荷重で圧着
し、5、10秒放置して接着力を測定した。結果を
表3に示す。[Table] Example 3 Using the size liquid sample of Example 2, it was coated on high-quality kraft paper to a solid content of 40 g/m 2 .
After drying at ℃ for 1 hour, and keeping it in an equilibrium state for one day and night in a constant temperature and humidity room at 20℃ and 65% RH, it was cut to 30 mm x 60 mm in the same way as in Example 2, and the glued side of one end was 30 mm x 30 mm.
After wetting the sheets with water, they were allowed to stand for 2, 5, and 10 seconds, and one end of the same-shaped kraft paper was stacked on 30 mm x 30 mm and pressed together with a load of 500 g, and left for 5 and 10 seconds to measure the adhesive strength. The results are shown in Table 3.
【表】
実施例 4
練炭の素材である炭粉に実施例2で用いたサン
プルを粘結剤として1%添加し、水分17%で圧力
1トンで直径30mm、高さ10mmの円筒形に成型後、
100℃にて1時間乾燥後、20℃、65%RHの恒温
恒湿室内で1昼夜平衡状態に保つた後、テンシロ
ン型試験機で破壊強度を測定した。
結果を表4に示す。[Table] Example 4 1% of the sample used in Example 2 was added as a binder to charcoal powder, which is the raw material for briquettes, and molded into a cylindrical shape with a diameter of 30 mm and a height of 10 mm at a pressure of 1 ton at a moisture content of 17%. rear,
After drying at 100°C for 1 hour, the specimen was kept at equilibrium in a constant temperature and humidity room at 20°C and 65% RH for one day, and then the breaking strength was measured using a Tensilon tester. The results are shown in Table 4.
【表】【table】
【表】
実施例 5
実施例2のサンプル糊液を10%水溶液に調整
し、綿帆布および綿ブロードを浸漬し、マングル
で1回絞り、100℃で5分間乾燥した。
得られた糊付布について剛軟性試験(JIS―L
―1096、A法)を行つた。結果を表5に示す。[Table] Example 5 The sample paste solution of Example 2 was adjusted to a 10% aqueous solution, and cotton canvas and cotton broadcloth were dipped in it, squeezed once with a mangle, and dried at 100°C for 5 minutes. The obtained starched cloth was subjected to a bending test (JIS-L
-1096, Method A). The results are shown in Table 5.
【表】【table】
【表】
以上の実施例の結果から明らかなように本発明
の糊剤はプルラン、焙焼デキストリン、これらの
混合物よりも優れた接着力、粘結力、繊維の堅仕
上効果を有することが示された。[Table] As is clear from the results of the above examples, it is shown that the sizing agent of the present invention has adhesive strength, caking strength, and fiber hardening effect that are superior to pullulan, roasted dextrin, and mixtures thereof. It was done.
Claims (1)
地にプルラン生産菌株を培養することによつて得
られる組成物を主成分とする糊剤。 2 焙焼デキストリンを炭素源として含有する培
地にプルラン生産菌株を培養することを特徴とす
る糊剤の製造方法。[Scope of Claims] 1. A sizing agent whose main component is a composition obtained by culturing a pullulan-producing strain in a medium containing roasted dextrin as a carbon source. 2. A method for producing a sizing agent, which comprises culturing a pullulan-producing strain in a medium containing roasted dextrin as a carbon source.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58046888A JPS59172566A (en) | 1983-03-19 | 1983-03-19 | Paste and production thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58046888A JPS59172566A (en) | 1983-03-19 | 1983-03-19 | Paste and production thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59172566A JPS59172566A (en) | 1984-09-29 |
JPS6367823B2 true JPS6367823B2 (en) | 1988-12-27 |
Family
ID=12759899
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58046888A Granted JPS59172566A (en) | 1983-03-19 | 1983-03-19 | Paste and production thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59172566A (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5411945A (en) * | 1992-08-29 | 1995-05-02 | Kabushiki Kaisha Hayashibara Seibutsu Kagaku Kenkyujo | Pullulan binder and its uses |
JP4817170B2 (en) * | 2004-06-28 | 2011-11-16 | 株式会社林原生物化学研究所 | Starch paste and method for producing the same |
JP5860480B2 (en) | 2011-01-11 | 2016-02-16 | キャプシュゲル・ベルジウム・エヌ・ヴィ | New hard capsule containing pullulan |
JP7222911B2 (en) | 2017-04-14 | 2023-02-15 | カプスゲル・ベルギウム・ナムローゼ・フェンノートシャップ | How to make pullulan |
CN110678170A (en) | 2017-04-14 | 2020-01-10 | 比利时胶囊公司 | Pullulan polysaccharide capsule |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4856239A (en) * | 1971-11-18 | 1973-08-07 |
-
1983
- 1983-03-19 JP JP58046888A patent/JPS59172566A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4856239A (en) * | 1971-11-18 | 1973-08-07 |
Also Published As
Publication number | Publication date |
---|---|
JPS59172566A (en) | 1984-09-29 |
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