JPH10251402A - Biodegradable water-absorbing resin and its production - Google Patents

Biodegradable water-absorbing resin and its production

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Publication number
JPH10251402A
JPH10251402A JP24068897A JP24068897A JPH10251402A JP H10251402 A JPH10251402 A JP H10251402A JP 24068897 A JP24068897 A JP 24068897A JP 24068897 A JP24068897 A JP 24068897A JP H10251402 A JPH10251402 A JP H10251402A
Authority
JP
Japan
Prior art keywords
glutamic acid
water
poly
absorbent resin
biodegradable
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
Application number
JP24068897A
Other languages
Japanese (ja)
Other versions
JP3715414B2 (en
Inventor
Toshio Hara
敏夫 原
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Idemitsu Kosan Co Ltd
Original Assignee
Idemitsu Kosan Co Ltd
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Filing date
Publication date
Application filed by Idemitsu Kosan Co Ltd filed Critical Idemitsu Kosan Co Ltd
Priority to JP24068897A priority Critical patent/JP3715414B2/en
Publication of JPH10251402A publication Critical patent/JPH10251402A/en
Application granted granted Critical
Publication of JP3715414B2 publication Critical patent/JP3715414B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Polyamides (AREA)
  • Biological Depolymerization Polymers (AREA)

Abstract

PROBLEM TO BE SOLVED: To obtain a biodegradable water-absorbing resin which has a high gelation ratio, absorbs water even from an aq. or salt soln., and absorbs ethanol by forming a cross-linked poly-γ-glutamic acid having a specified gelation ratio. SOLUTION: This water-absorbing resin, a crosslinked poly-γ-glutamic acid, is obtd. by dissolving poly-γ-glutamic acid in a solvent (e.g. water) to give a soln. with a concn. of 2-15wt.%, exposing the soln. to a radiation, and separating and purifying the resultant cross-linked polymer. Poly-γ-glutamic acid used as the raw material is obtd. e.g. by culturing with Bacillus subtilis, by culturing with gene recombination microorganisms, or by chemical synthesis. The polymn. of poly-γ-glutamic acid is pref. conducted by free-radical polymn. with a radiation. Pref. the dose rate is 1.0-20kGy/hr, and the dosage is pref. 30kGy or higher. After the exposure to radiation, water is removed to obtain a solid biodegradable resin, a crosslinked poly-γ-glutamic acid, having a gelation ratio of 91-100%.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、生分解性吸水性樹
脂およびその製造方法に関するものである。さらに詳し
くは、吸水能力に優れ、かつ、生分解性を有する吸水性
樹脂およびその製造方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a biodegradable water-absorbent resin and a method for producing the same. More specifically, the present invention relates to a water-absorbent resin having excellent water-absorbing ability and having biodegradability, and a method for producing the same.

【0002】[0002]

【従来の技術】近年、吸水性樹脂は、紙オムツ等の用途
のみならず、体液吸収体等の医療分野、建築分野、鮮度
保持剤等の食料分野、緑化等の農業・園芸分野等の多く
の分野において用いられている。この吸水性樹脂は、各
分野に応じた様々な種類の吸水性樹脂が知られている。
この様々な吸水性樹脂のうち、アクリル酸系の吸水性樹
脂は、ある程度の吸水能力を有し、かつ、安価であるた
め、幅広く用いられている。しかし、生分解性を殆ど有
していないため、土中の細菌等により分解されないの
で、環境汚染等の環境問題を引き起こすことが知られて
いる。また、アクリル酸系の吸水性樹脂は塩溶液に対す
る給水率やエタノールに対する吸収率が著しく低く実用
上満足のいくものではなかった。この問題を解決するた
めに、生分解性を有する吸水性樹脂として、デンプン系
吸水性樹脂、ヒアルロン酸系吸水性樹脂等が知られてい
る。これらの吸水性樹脂として、特に生分解性に有する
吸水性樹脂として、ポリ−γ−グルタミン酸系架橋体等
が知られている(例えば、特開平6−322358、特
開平7−300563等)。しかしながら、ポリ−γ−
グルタミン酸等のゲル化率は90%までであった。ま
た、塩溶液に対する給水率やエタノールに対する吸収率
の向上が望まれていた。
2. Description of the Related Art In recent years, water-absorbent resins have been used not only in applications such as disposable diapers, but also in medical fields such as body fluid absorbers, construction fields, food fields such as freshness preserving agents, and agricultural and horticultural fields such as greening. Used in the field. As the water absorbing resin, various kinds of water absorbing resins according to various fields are known.
Among these various water-absorbing resins, acrylic acid-based water-absorbing resins are widely used because they have a certain level of water absorbing ability and are inexpensive. However, since it has almost no biodegradability, it is known that it is not decomposed by bacteria or the like in the soil and causes environmental problems such as environmental pollution. In addition, the acrylic acid-based water-absorbing resin has a remarkably low water supply rate with respect to a salt solution and an absorptivity with respect to ethanol, and is not practically satisfactory. In order to solve this problem, starch-based water-absorbent resins, hyaluronic acid-based water-absorbent resins, and the like are known as biodegradable water-absorbent resins. As these water-absorbing resins, in particular, poly-γ-glutamic acid-based crosslinked products and the like are known as biodegradable water-absorbing resins (for example, JP-A-6-322358 and JP-A-7-300563). However, poly-γ-
The gelation ratio of glutamic acid and the like was up to 90%. Further, it has been desired to improve the water supply rate for salt solutions and the absorption rate for ethanol.

【0003】[0003]

【発明が解決しようとする課題】この発明の目的は、よ
り高いゲル化率を有するポリ−γ−グルタミン酸架橋体
からなる生分解生吸水性樹脂を提供することである。ま
た、水または塩溶液に対して吸水性能を有し、かつ、エ
タノールに対しても高い吸収性能を有するポリ−γ−グ
ルタミン酸架橋体からなる生分解生吸水性樹脂を提供す
ることである。さらに、より高いゲル化率を有するポリ
−γ−グルタミン酸架橋体からなる生分解性吸水性樹脂
の製造方法を提供することである。
SUMMARY OF THE INVENTION An object of the present invention is to provide a biodegradable bioabsorbable resin comprising a crosslinked poly-γ-glutamic acid having a higher gelation ratio. Another object of the present invention is to provide a biodegradable bioabsorbent resin comprising a crosslinked poly-γ-glutamic acid having a water absorbing property for water or a salt solution and having a high absorbing property for ethanol. Another object of the present invention is to provide a method for producing a biodegradable water-absorbent resin comprising a crosslinked poly-γ-glutamic acid having a higher gelation ratio.

【0004】[0004]

【課題を解決しようとする手段】本発明者は、生分解性
を有するポリ−γ−グルタミン酸架橋体からなる吸水性
樹脂を開発するために種々研究を重ねた結果、より高い
ゲル化率を有するポリ−γ−グルタミン酸架橋体からな
る吸水性樹脂を得ることに成功し、この架橋体が生分解
性を失うことことなく吸水性を有することを見いだし、
この知見に基づき本発明を完成するに至った。また、ポ
リ−γ−グルタミン酸の濃度と照射する放射線の線量率
が特定の範囲にある場合にゲル化率91〜100%のポ
リ−γ−グルタミン酸架橋体からなる吸水性樹脂を得る
ことができることを見いだし、この知見に基づき本発明
を完成するに至った。
The present inventors have conducted various studies to develop a water-absorbent resin comprising a crosslinked product of poly-γ-glutamic acid having biodegradability, and as a result, it has a higher gelation ratio. Succeeded in obtaining a water-absorbent resin comprising a cross-linked poly-γ-glutamic acid, and found that this cross-linked body has water absorbability without losing biodegradability,
Based on this finding, the present invention has been completed. Further, when the concentration of poly-γ-glutamic acid and the radiation dose rate are within a specific range, it is possible to obtain a water-absorbent resin comprising a crosslinked poly-γ-glutamic acid having a gelation rate of 91 to 100%. The present inventors have completed the present invention based on this finding.

【0005】すなわち、本発明は、以下の生分解性吸水
性樹脂およびその製造方法を提供するものである。 (1)ゲル化率91〜100%のポリ−γ−グルタミン
酸架橋体からなる生分解性吸水性樹脂。 (2)ゲル化率94〜100%のポリ−γ−グルタミン
酸架橋体からなる生分解性吸水性樹脂。 (3)ポリ−γ−グルタミン酸架橋体からなる生分解性
吸水性樹脂を製造する方法において、ポリ−γ−グルタ
ミン酸をその濃度が2〜15重量%になるように溶解し
た後、放射線を照射線量30kGy以上照射し、ゲル化
率91〜100%のポリ−γ−グルタミン酸架橋体を得
ることを特徴とする生分解性吸水性樹脂の製造方法。 (4)ポリ−γ−グルタミン酸架橋体からなる生分解性
吸収性樹脂を製造する方法において、ポリ−γ−グルタ
ミン酸をその濃度が2〜8重量%になるように溶解した
後、放射線を線量率1.0〜1.4kGy/時間で照射
し、ゲル化率91〜100%のポリ−γ−グルタミン酸
架橋体を得ることを特徴とする生分解性吸水性樹脂の製
造方法。 (5)ポリ−γ−グルタミン酸架橋体からなる生分解性
吸収性樹脂を製造する方法において、ポリ−γ−グルタ
ミン酸をその濃度が4〜7重量%になるように溶解した
後、放射線を線量率1.0〜1.4kGy/時間で照射
し、ゲル化率94〜100%のポリ−γ−グルタミン酸
架橋体を得ることを特徴とする生分解性吸水性樹脂の製
造方法。 (6)放射線が、γ線であることを特徴とする上記
(3)乃至(5)のいずれかに記載の生分解性吸水性樹
脂の製造方法。
That is, the present invention provides the following biodegradable water-absorbent resin and a method for producing the same. (1) A biodegradable water-absorbent resin comprising a crosslinked poly-γ-glutamic acid having a gelation ratio of 91 to 100%. (2) A biodegradable water-absorbing resin comprising a crosslinked poly-γ-glutamic acid having a gelation ratio of 94 to 100%. (3) In a method for producing a biodegradable water-absorbent resin comprising a cross-linked poly-γ-glutamic acid, radiation is irradiated after dissolving poly-γ-glutamic acid so that its concentration becomes 2 to 15% by weight. A method for producing a biodegradable water-absorbent resin, which comprises irradiating at least 30 kGy to obtain a crosslinked poly-γ-glutamic acid having a gelation ratio of 91 to 100%. (4) In a method for producing a biodegradable absorbent resin comprising a cross-linked poly-γ-glutamic acid, poly-γ-glutamic acid is dissolved so that its concentration becomes 2 to 8% by weight, and then radiation is dosed. A method for producing a biodegradable water-absorbent resin, which comprises irradiating at 1.0 to 1.4 kGy / hour to obtain a crosslinked poly-γ-glutamic acid having a gelation ratio of 91 to 100%. (5) In a method for producing a biodegradable absorbent resin comprising a cross-linked poly-γ-glutamic acid, poly-γ-glutamic acid is dissolved so that its concentration becomes 4 to 7% by weight, and then radiation is dosed. A method for producing a biodegradable water-absorbent resin, which comprises irradiating at 1.0 to 1.4 kGy / hour to obtain a crosslinked poly-γ-glutamic acid having a gelation ratio of 94 to 100%. (6) The method for producing a biodegradable water-absorbent resin according to any one of the above (3) to (5), wherein the radiation is gamma rays.

【0006】[0006]

【発明の実施の形態】本発明のポリ−γ−グルタミン酸
架橋体からなる吸水性樹脂は、ポリ−γ−グルタミン酸
をその濃度が2〜15重量%、好ましくは2〜8重量
%、さらに好ましくは4〜7重量%になるように水等の
溶媒に溶解し、次いでこの溶液に放射線を照射したの
ち、生成した架橋体を分離生成等をすることにより得る
ことができる。2重量%以下であれば、吸水率が低く、
15重量%以上であれば、ゲル化率が低くなり、収率の
点から好ましくない。
BEST MODE FOR CARRYING OUT THE INVENTION The water-absorbent resin comprising a crosslinked poly-γ-glutamic acid of the present invention has a poly-γ-glutamic acid concentration of 2 to 15% by weight, preferably 2 to 8% by weight, more preferably It can be obtained by dissolving it in a solvent such as water so as to have a concentration of 4 to 7% by weight, and then irradiating the solution with radiation, and then separating and producing the resulting crosslinked product. If it is 2% by weight or less, the water absorption is low,
If it is 15% by weight or more, the gelation rate is low, which is not preferable in terms of yield.

【0007】本発明に用いるポリ−γ−グルタミン酸に
ついては、特に制限はなく、種々の製造方法によるもの
が用いられる。例えば、微生物、例えば枯草菌による培
養法、遺伝子組換微生物による培養法、納豆より調整す
る方法、または化学合成法等が様々考えられる。微生物
による培養法によりポリ−γ−グルタミン酸を製造する
場合には、ポリ−γ−グルタミン酸を菌体外に生成する
菌株であればいずれも使用可能であるが、特にバチラス
属菌種が望ましい。具体的な例としては、バチラス・ズ
ブチルス、バチラス・アントラシス、バチラス・ナット
ウなどが用いられる。特に、バチラス・ズブチリスのよ
うな微生物により産生される数百万以上の分子量を有す
るものが好ましい。(特開平1−174397)なお、
重合反応に影響がない場合には、ポリ−γ−グルタミン
酸のカルボキシル基等にアルキル基等を修飾した誘導体
を用いることができる。
[0007] The poly-γ-glutamic acid used in the present invention is not particularly limited, and those produced by various production methods are used. For example, various methods such as a culture method using a microorganism, for example, Bacillus subtilis, a culture method using a genetically modified microorganism, a method using natto, or a chemical synthesis method are considered. In the case of producing poly-γ-glutamic acid by a culture method using a microorganism, any strain can be used as long as it produces poly-γ-glutamic acid outside the cells, but a Bacillus species is particularly desirable. Specific examples include Bacillus subtilis, Bacillus anthracis, and Bacillus natto. In particular, those having a molecular weight of several millions or more produced by a microorganism such as Bacillus subtilis are preferable. (Japanese Unexamined Patent Publication No. 1-174397)
When the polymerization reaction is not affected, a derivative in which a carboxyl group or the like of poly-γ-glutamic acid is modified with an alkyl group or the like can be used.

【0008】本発明で使用する微生物の培養法において
は、菌株や培地等はポリ−γ−グルタミン酸が生産され
るものならどのようなものでもよい。例えば、培地とし
ては、炭素源、窒素源、無機物その他の栄養物を適当に
含有する培地ならば、合成培地、天然培地いずれでも用
いることができる。添加アミノ酸としては、L−グルタ
ミン酸、アスパラギン酸、アラニン、ロイシン、フェニ
ルアラニン、ヒスチジンなどまたはこれらの塩を用いる
ことができ、好ましくはL−グルタミン酸であり、2〜
12%、好ましくは3〜10%である。
[0008] In the method for culturing microorganisms used in the present invention, any strain, medium, etc. may be used as long as poly-γ-glutamic acid is produced. For example, any of a synthetic medium and a natural medium may be used as long as the medium appropriately contains a carbon source, a nitrogen source, inorganic substances, and other nutrients. As the added amino acid, L-glutamic acid, aspartic acid, alanine, leucine, phenylalanine, histidine or the like or a salt thereof can be used, and preferably L-glutamic acid,
It is 12%, preferably 3 to 10%.

【0009】炭素源としては、グルコ−ス、シュクロ−
ス、クエン酸またはキシロースなどを用いることができ
るが、好ましくはクエン酸またはグルコースである。窒
素源としては、ペプトンまたは酵母エキスなどの有機栄
養源、硫酸アンモニウム等の無機栄養源などを用いるこ
とができる。 培養は、振とう培養または攪拌培養など
の好気的条件下で行い、培養温度は25〜45℃、好ま
しくは30〜40℃である。培養時のpHは5〜9、好
ましくは6〜8であり、培養時のpH調整は水酸化ナト
リウム、水酸化カリウムなどにより行う。
As a carbon source, glucose, sucrose,
, Citric acid or xylose can be used, but preferably citric acid or glucose. As a nitrogen source, an organic nutrient such as peptone or yeast extract, an inorganic nutrient such as ammonium sulfate, or the like can be used. The culture is performed under aerobic conditions such as shaking culture or stirring culture, and the culture temperature is 25 to 45 ° C, preferably 30 to 40 ° C. The pH during the culture is 5 to 9, preferably 6 to 8, and the pH during the culture is adjusted with sodium hydroxide, potassium hydroxide or the like.

【0010】培養時間は通常48〜72時間でポリ−γ
−グルタミン酸は、菌体外に蓄積される。培養終了後の
培養液中のポリ−γ−グルタミン酸は、従来から行われ
ている方法により回収することができる。すなわち、遠
心分離、濾過助剤または微細孔を有するフィルター濾過
により菌体を除去し、限外濾過することによりポリ−γ
−グルタミン酸を回収することができる。また、3〜4
倍量のエタノールなどを添加してポリ−γ−グルタミン
酸を沈殿させる。沈殿物を水に溶解させ不溶物を除去
し、透析または限外濾過などにより低分子量物を除き、
エタノ−ルなどにより再沈殿を繰り返してポリ−γ−グ
ルタミン酸を回収することができる。
The cultivation time is usually 48 to 72 hours and the poly-γ
-Glutamic acid is accumulated extracellularly. The poly-γ-glutamic acid in the culture solution after completion of the culture can be recovered by a conventional method. That is, the cells are removed by centrifugation, filtration aid or filter filtration having micropores, and poly-γ is obtained by ultrafiltration.
-Glutamic acid can be recovered. Also, 3-4
A double amount of ethanol or the like is added to precipitate poly-γ-glutamic acid. Dissolve the precipitate in water to remove insolubles, remove low molecular weight substances such as dialysis or ultrafiltration,
Poly-γ-glutamic acid can be recovered by repeating reprecipitation with ethanol or the like.

【0011】本発明において、ポリ−γ−グルタミン酸
を重合させる方法としては、遊離基重合による。この
際、遊離基反応形式は様々で、また、反応の開始剤は過
酸化物、アゾ化合物等が考えられる。本発明の場合には
特に限定されないが、放射線による遊離基重合が好まし
い。放射線による場合には、ポリ−γ−グルタミン酸を
溶解させるのは、ポリ−γ−グルタミン酸を溶解させる
ことができれば特に限定されず、例えば、水、メチルア
ルコール水溶液、エチルアルコール水溶液等であるが、
特に水が好ましい。
In the present invention, the method for polymerizing poly-γ-glutamic acid is by free radical polymerization. At this time, the type of free radical reaction varies, and the initiator of the reaction may be a peroxide, an azo compound or the like. Although not particularly limited in the case of the present invention, free radical polymerization by radiation is preferred. In the case of radiation, the dissolution of poly-γ-glutamic acid is not particularly limited as long as poly-γ-glutamic acid can be dissolved, and examples thereof include water, a methyl alcohol aqueous solution, and an ethyl alcohol aqueous solution.
Water is particularly preferred.

【0012】ポリ−γ−グルタミン酸を溶解した溶液
は、放射線透過性容器、例えばガラス製バイアル瓶等が
用いられる。放射線については、特に制限なく、例え
ば、α線、β線、γ線、電子線、中性子線、X線等があ
るが、好ましくはγ線である。γ線は、特に制限はない
が、例えば、コバルト60を線源とする照射装置などに
より発生させたものが用いられる。この場合、線量率
1.0〜20kGy/時間が好ましい。さらに好ましく
は、線量率1.0〜1.4kGy/時間である。照射時
間は、特に制限されないが、照射線量30kGy以上と
なるようにすることが好ましい。
The solution in which the poly-γ-glutamic acid is dissolved is used in a radiolucent container such as a glass vial. The radiation is not particularly limited, and includes, for example, α-rays, β-rays, γ-rays, electron beams, neutron rays, X-rays, etc., and preferably γ-rays. The γ-rays are not particularly limited, but, for example, those generated by an irradiation device using cobalt 60 as a radiation source are used. In this case, the dose rate is preferably 1.0 to 20 kGy / hour. More preferably, the dose rate is 1.0 to 1.4 kGy / hour. The irradiation time is not particularly limited, but is preferably set to an irradiation dose of 30 kGy or more.

【0013】この後、水を除去することにより固形物で
ある吸水性樹脂を得ることができる。この吸水性樹脂
は、無色透明であり、吸水性に優れ、生分解性も有して
いる。以上の方法により得られる吸水性樹脂は、所定形
状に造粒されていてもよく、また、不定形破砕状、球状
等であってもよい。この吸水性樹脂は、衛生分野のみな
らず、多種多様な分野において利用可能である。例え
ば、微生物培養液に本発明吸水性樹脂を添加し、培養液
をゲル化し、その後の微生物添加等の適当な処理によ
り、効率的な堆肥化を図ることができる。また、本発明
の吸水性樹脂は食用可能であり、成形加工することによ
り食用可能な各種容器を製造可能で、ゴミ問題などの環
境問題を解決できる。さらに、本発明の吸水性樹脂の接
着性を利用し、吸湿剤の不要な接着剤として利用するこ
ともできる。
Thereafter, water is removed to obtain a solid water-absorbing resin. This water-absorbent resin is colorless and transparent, has excellent water absorbability, and has biodegradability. The water-absorbent resin obtained by the above method may be granulated into a predetermined shape, or may be irregularly crushed, spherical, or the like. This water-absorbent resin can be used not only in the hygiene field but also in various fields. For example, by adding the water-absorbent resin of the present invention to a microorganism culture solution, gelling the culture solution, and then appropriately processing such as addition of microorganisms, efficient composting can be achieved. In addition, the water-absorbent resin of the present invention is edible, and various edible containers can be manufactured by molding to solve environmental problems such as dust. Further, by utilizing the adhesiveness of the water-absorbent resin of the present invention, the water-absorbent resin can be used as an adhesive which does not require a moisture absorbent.

【0014】なお、本発明で用いるゲル化率とは、ポリ
−γ−グルタミン酸架橋体からなる吸水性樹脂の乾燥重
量を用いたポリ−γ−グルタミン酸の量で割った数値、
すなわち、仕込みポリ−γ−グルタミン酸量に対するポ
リ−γ−グルタミン酸架橋体からなる吸水性樹脂の乾燥
重量の百分率を意味する。
The gelation ratio used in the present invention is a value obtained by dividing the dry weight of the water-absorbent resin composed of the crosslinked poly-γ-glutamic acid by the amount of poly-γ-glutamic acid using the dry weight.
That is, it means the percentage of the dry weight of the water-absorbent resin composed of the crosslinked poly-γ-glutamic acid to the amount of the charged poly-γ-glutamic acid.

【0015】[0015]

【実施例】以下に、実施例等によって、本発明をさらに
詳細に説明するが、本発明はこれらにより何ら制限され
るものではない。 実施例1〜3 明治γ−PGA(明治製菓(株)製ポリ−γ−グルタミ
ン酸)を4重量%濃度になるように水に溶解させ、窒素
によりバブリングした後、蓋付き10mlサンプル瓶に
それぞれ2ml入れ、蓋を閉めた。このサンプル瓶に、
線源としてコバルト60を用いるγ線照射装置により、
γ線を線量率1.2kGy/時間で室温にて、照射線量
20kGy、50kGy、110kGyとなるように照
射した。得られた処理物を蓋付き10mlサンプル瓶か
ら取り出し、一週間4℃の水に浸漬し、未架橋のポリ−
γ−グルタミン酸を除去した。水を吸収して膨潤したポ
リ−γ−グルタミン酸ハイドロゲルを80メッシュの金
網で濾過後、凍結乾燥し、ポリ−γ−グルタミン酸架橋
体として得た。この架橋体の吸水性樹脂について、ゲル
化率と吸水率を測定し、その結果を表1に示した。ゲル
化率は、仕込みポリ−γ−グルタミン酸量に対するポリ
−γ−グルタミン酸架橋体からなる吸水性樹脂の乾燥重
量の百分率で求めた。吸水率は、ポリ−γ−グルタミン
酸架橋体からなる吸水性樹脂を大過剰の蒸留水に浸漬し
て十分膨潤させた後、80メッシュの金網で水切りした
後の重量(湿重量)を測定し吸水重量(湿重量から乾燥
重量を引いた量)を乾燥重量により割った数値により求
めた。
The present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the present invention. Examples 1 to 3 Meiji γ-PGA (poly-γ-glutamic acid manufactured by Meiji Seika Co., Ltd.) was dissolved in water to a concentration of 4% by weight, bubbled with nitrogen, and then 2 ml each in a 10 ml sample bottle with a lid. Put in and close the lid. In this sample bottle,
With a gamma irradiation device using cobalt 60 as a radiation source,
Irradiation was performed at room temperature at a dose rate of 1.2 kGy / hour at a dose rate of 20 kGy, 50 kGy, and 110 kGy. The treated product was taken out of a 10 ml sample bottle with a lid, immersed in water at 4 ° C. for one week, and the uncrosslinked poly-
γ-glutamic acid was removed. The poly-γ-glutamic acid hydrogel swollen by absorbing water was filtered through an 80-mesh wire gauze and freeze-dried to obtain a cross-linked poly-γ-glutamic acid. The gelation rate and the water absorption rate of the water-absorbent resin of this crosslinked body were measured, and the results are shown in Table 1. The gelation ratio was determined as a percentage of the dry weight of the water-absorbent resin composed of the crosslinked poly-γ-glutamic acid based on the amount of the charged poly-γ-glutamic acid. The water absorption was determined by immersing a water-absorbent resin composed of a cross-linked poly-γ-glutamic acid in a large excess of distilled water to sufficiently swell, and then measuring the weight (wet weight) after draining with a 80-mesh wire gauze. The weight (the amount obtained by subtracting the dry weight from the wet weight) was divided by the dry weight to obtain a numerical value.

【0016】[0016]

【表1】 [Table 1]

【0017】実施例4〜7 明治γ−PGA(明治製菓(株)製)を2、5、7、8
重量%濃度になるように水に溶解させ、窒素によりバブ
リングした後、蓋付き10mlサンプル瓶に2ml入
れ、蓋を閉めた。このサンプル瓶に、線源としてコバル
ト60を用いるγ線照射装置により、γ線を線量率1.
2kGy/時間で室温にて、照射線量20kGyとなる
ように照射した。得られた処理物を蓋付き10mlサン
プル瓶から取り出し、一週間4℃の水に浸漬し、未架橋
のポリ−γ−グルタミン酸を除去した。水を吸収して膨
潤したポリ−γ−グルタミン酸ハイドロゲルを80メッ
シュの金網で濾過後、凍結乾燥し、ポリ−γ−グルタミ
ン酸架橋体として得た。この架橋体の吸水性樹脂につい
て、ゲル化率と吸水率を測定し、その結果を表2に示し
た。ゲル化率は及び吸水率は実施例1と同様にして測定
した。
Examples 4 to 7 Meiji γ-PGA (Meiji Seika Co., Ltd.) was prepared using 2, 5, 7, 8
After dissolving in water to a concentration of weight% and bubbling with nitrogen, 2 ml was put into a 10 ml sample bottle with a lid, and the lid was closed. The sample bottle was irradiated with γ-rays at a dose rate of 1.
Irradiation was performed at room temperature at 2 kGy / hour so that the irradiation dose was 20 kGy. The treated product was taken out of a 10 ml sample bottle with a lid and immersed in water at 4 ° C. for one week to remove uncrosslinked poly-γ-glutamic acid. The poly-γ-glutamic acid hydrogel swollen by absorbing water was filtered through an 80-mesh wire gauze and freeze-dried to obtain a cross-linked poly-γ-glutamic acid. The gelation rate and the water absorption rate of the water-absorbent resin of this crosslinked body were measured, and the results are shown in Table 2. The gelation ratio and the water absorption were measured in the same manner as in Example 1.

【0018】[0018]

【表2】 [Table 2]

【0019】実施例8〜13 使用菌株としてバチルス・ズブチリスIFO3335株
を用い、表3の培地を3ml試験管に入れ37℃で1晩
振とう培養を行い前培養液とした。次に500ml容坂
口フラスコに表2の培地を100ml入れ、前培養液1
mlを加え37℃で振とう培養を行い、72時間後培養
液を回収した。回収した培養液に水を4倍量添加し、p
Hを2.5に調整した。この培養液を4℃で12,00
0r.p.m、30分間遠心分離し、遠心分離後の培養
液上清を限外濾過し、濃縮したポリ−γ−グルタミン酸
溶液を凍結乾燥した。この操作により1.5g/100
ml培養液のポリ−γ−グルタミン酸を得ることができ
た。
Examples 8 to 13 Bacillus subtilis IFO3335 strain was used as a strain to be used, and the medium shown in Table 3 was placed in a 3 ml test tube and shake-cultured at 37 ° C. overnight to prepare a preculture solution. Next, 100 ml of the medium shown in Table 2 was placed in a 500 ml Sakaguchi flask, and the preculture liquid 1 was added.
The resulting mixture was shake-cultured at 37 ° C., and the culture solution was recovered after 72 hours. Four times the amount of water is added to the collected culture solution, and p
H was adjusted to 2.5. This culture was incubated at 4 ° C. for 12,000 hours.
0r. p. After centrifugation for 30 minutes, the culture supernatant after centrifugation was ultrafiltered, and the concentrated poly-γ-glutamic acid solution was lyophilized. By this operation, 1.5 g / 100
Thus, poly-γ-glutamic acid in the ml culture solution was obtained.

【0020】上記の製造方法を数回行うことにより得ら
れたポリ−γ−グルタミン酸を2、5、7、8、10、
15重量%濃度になるように水に溶解させ、窒素により
バブリングした後、蓋付き10mlサンプル瓶に2ml
入れ、蓋を閉めた。このサンプル瓶に、線源としてコバ
ルト60を用いるγ線を線量率10kGy/時間で室温
にて、照射線量30kGyとなるように照射した。得ら
れた処理物を蓋付き10mlサンプル瓶から取り出し、
一週間4℃の水に浸漬し、未架橋のポリ−γ−グルタミ
ン酸を除去した。水を吸収して膨潤したポリ−γ−グル
タミン酸ハイドロゲルを80メッシュの金網で濾過後、
凍結乾燥し、ポリ−γ−グルタミン酸架橋体として得
た。この架橋体の吸水性樹脂について、ゲル化率と吸水
率を測定し、その結果を表4に示した。ゲル化率は及び
吸水率は実施例1と同様にして測定した。
The poly-γ-glutamic acid obtained by performing the above-mentioned production method several times is 2,5,7,8,10,
After dissolving in water to a concentration of 15% by weight and bubbling with nitrogen, 2 ml was placed in a 10 ml sample bottle with a lid.
Put in and close the lid. The sample bottle was irradiated with gamma rays using cobalt 60 as a radiation source at a dose rate of 10 kGy / hour at room temperature so as to have an irradiation dose of 30 kGy. Take out the obtained processed product from the 10 ml sample bottle with a lid,
It was immersed in water at 4 ° C. for one week to remove uncrosslinked poly-γ-glutamic acid. After filtering the water-swollen poly-γ-glutamic acid hydrogel through an 80 mesh wire mesh,
It was freeze-dried to obtain a cross-linked poly-γ-glutamic acid. The gelation rate and water absorption rate of the water-absorbent resin of this crosslinked body were measured, and the results are shown in Table 4. The gelation ratio and the water absorption were measured in the same manner as in Example 1.

【0021】[0021]

【表3】 [Table 3]

【0022】[0022]

【表4】 [Table 4]

【0023】実施例14 実施例12により得られた架橋体の吸水性樹脂につい
て、各塩溶液に対する吸収率を測定し、その結果を表5
に示した。吸収率は、ポリ−γ−グルタミン酸架橋体か
らなる吸水性樹脂を大過剰の各塩溶液に浸漬して十分膨
潤させたのち、80メッシュの金網で水切りした後重量
(湿重量)を測定し、吸収重量(湿重量から乾燥重量を
引いた量)を乾燥重量により割ることにより求めた。
Example 14 With respect to the water-absorbent resin of the crosslinked product obtained in Example 12, the absorptance of each salt solution was measured.
It was shown to. Absorbance was measured by immersing a water-absorbent resin composed of cross-linked poly-γ-glutamic acid in a large excess of each salt solution to sufficiently swell, then draining with a 80-mesh wire net, and measuring the weight (wet weight). It was determined by dividing the absorbed weight (wet weight minus dry weight) by dry weight.

【0024】[0024]

【表5】 [Table 5]

【0025】実施例15 実施例12により得られた架橋体の吸水性樹脂につい
て、各種アルコール水溶液に対する吸収率を測定し、そ
の結果を表6に示した。吸収率は、ポリ−γ−グルタミ
ン酸架橋体からなる吸水性樹脂を大過剰の各種アルコー
ル水溶液に浸漬して十分膨潤させたのち、80メッシュ
の金網で水切りした後重量(湿重量)を測定し、吸収重
量(湿重量から乾燥重量を引いた量)を乾燥重量により
割ることにより求めた。
Example 15 The water-absorbent resin of the crosslinked product obtained in Example 12 was measured for the absorptivity to various alcohol aqueous solutions, and the results are shown in Table 6. Absorbance was measured by immersing a water-absorbent resin composed of a cross-linked poly-γ-glutamic acid in a large excess of various alcohol aqueous solutions to sufficiently swell, then draining with a 80-mesh wire net, and measuring the weight (wet weight). It was determined by dividing the absorbed weight (wet weight minus dry weight) by dry weight.

【0026】なお、実施例により得られた架橋体の吸水
性樹脂は2−プロパノール、3−メチル−1−ブタノー
ル、1−ブタノールの20%水溶液および40%水溶液
でも膨潤し、吸収能を有することを確認した。
The crosslinked water-absorbent resin obtained in the examples swells even in a 20% aqueous solution and a 40% aqueous solution of 2-propanol, 3-methyl-1-butanol, and 1-butanol, and has an absorbing ability. It was confirmed.

【0027】[0027]

【表6】 [Table 6]

【0028】実施例16 実施例12により得られた架橋体の吸水性樹脂につい
て、各種溶液に対する吸収能力について検討し、その結
果を表7に示した。吸収能力については、各種溶液20
mlを入れた溶液に0.05gの吸水性樹脂を添加し、
各種溶液の状態を検討した。
Example 16 The water-absorbent resin of the crosslinked product obtained in Example 12 was examined for its absorption capacity in various solutions, and the results are shown in Table 7. For the absorption capacity, various solutions 20
Add 0.05 g of water-absorbent resin to the solution containing
The state of various solutions was examined.

【0029】[0029]

【表7】 [Table 7]

【0030】参考例1〜5 明治γ−PGA(明治製菓(株)製ポリ−γ−グルタミ
ン酸)を5、9、15、20、25重量%濃度になるよ
うに水に溶解させ、窒素によりバブリングした後、蓋付
き10mlサンプル瓶にそれぞれ2ml入れ、蓋を閉め
た。このサンプル瓶に、線源としてコバルト60を用い
るγ線照射装置により、γ線を線量率1.2kGy/時
間で室温にて、照射線量20kGyとなるように照射し
た。得られた処理物を蓋付き10mlサンプル瓶から取
り出し、一週間4℃の水に浸漬し、未架橋のポリ−γ−
グルタミン酸を除去した。水を吸収して膨潤したポリ−
γ−グルタミン酸ハイドロゲルを80メッシュの金網で
濾過後、凍結乾燥し、ポリ−γ−グルタミン酸架橋体体
として得た。この架橋体の吸水性樹脂について、ゲル化
率と吸水率を測定し、その結果を表8に示した。ゲル化
率は及び吸水率は実施例1と同様にして測定した。
Reference Examples 1 to 5 Meiji γ-PGA (poly-γ-glutamic acid manufactured by Meiji Seika Co., Ltd.) was dissolved in water so as to have a concentration of 5, 9, 15, 20, or 25% by weight, and bubbling was performed with nitrogen. After that, 2 ml each was placed in a 10 ml sample bottle with a lid, and the lid was closed. The sample bottle was irradiated with γ-rays at a dose rate of 1.2 kGy / hour at room temperature to give an irradiation dose of 20 kGy by a γ-ray irradiator using cobalt 60 as a radiation source. The treated product was taken out of a 10 ml sample bottle with a lid, immersed in water at 4 ° C. for one week, and subjected to uncrosslinked poly-γ-
Glutamic acid was removed. Poly swelled by absorbing water
The γ-glutamic acid hydrogel was filtered through an 80-mesh wire gauze and freeze-dried to obtain a cross-linked poly-γ-glutamic acid. The gelation rate and the water absorption rate of the water-absorbent resin of this crosslinked body were measured, and the results are shown in Table 8. The gelation ratio and the water absorption were measured in the same manner as in Example 1.

【0031】[0031]

【表8】 [Table 8]

【0032】参考例6 明治γ−PGA(明治製菓(株)製ポリ−γ−グルタミ
ン酸)を10重量%濃度になるように水に溶解させ、窒
素によりバブリングした後、蓋付き10mlサンプル瓶
にそれぞれ2ml入れ、蓋を閉めた。このサンプル瓶
に、線源としてコバルト60を用いるγ線照射装置によ
り、γ線を線量率1.2kGy/時間で室温にて、照射
線量20kGyとなるように照射した。得られた処理物
を蓋付き10mlサンプル瓶から取り出し、一週間4℃
の水に浸漬し、未架橋のポリ−γ−グルタミン酸を除去
した。水を吸収して膨潤したポリ−γ−グルタミン酸ハ
イドロゲルを80メッシュの金網で濾過後、凍結乾燥
し、ポリ−γ−グルタミン酸架橋体として得た。この架
橋体の吸水性樹脂について、実施例1と同様にしてゲル
化率と吸水率を測定したところ、ゲル化率は86%で、
吸水率は5000であった。
Reference Example 6 Meiji γ-PGA (poly-γ-glutamic acid manufactured by Meiji Seika Co., Ltd.) was dissolved in water to a concentration of 10% by weight, bubbled with nitrogen, and placed in a 10 ml sample bottle with a lid. 2 ml was put and the lid was closed. The sample bottle was irradiated with γ-rays at a dose rate of 1.2 kGy / hour at room temperature to give an irradiation dose of 20 kGy by a γ-ray irradiator using cobalt 60 as a radiation source. The obtained processed product was taken out of a 10 ml sample bottle with a lid and kept at 4 ° C for one week.
In water to remove uncrosslinked poly-γ-glutamic acid. The poly-γ-glutamic acid hydrogel swollen by absorbing water was filtered through an 80-mesh wire gauze and freeze-dried to obtain a cross-linked poly-γ-glutamic acid. The gelation rate and the water absorption rate of this crosslinked water-absorbent resin were measured in the same manner as in Example 1, and the gelation rate was 86%.
The water absorption was 5000.

【0033】また、この架橋体の吸水性樹脂について、
実施例14と同様にして各塩溶液に対する吸吸率を測定
し、その結果を表9に示した。
The crosslinked water-absorbent resin is
The absorption rate of each salt solution was measured in the same manner as in Example 14, and the results are shown in Table 9.

【0034】[0034]

【表9】 [Table 9]

【0035】参考例7〜10 使用菌株としてバチルスズブチリスIFO3335株を
用い、表2の培地を3ml試験管に入れ37℃で1晩振
とう培養を行い前培養液とした。次に500ml容坂口
フラスコに表2の培地を100ml入れ、前培養液1m
lを加え37℃で振とう培養を行い、72時間後培養液
を回収した。回収した培養液は4℃で12,000r.
p.m、30分間遠心分離を行い、遠心分離後の培養液
上清に3倍量のエチルアルコールを加えて生じる沈殿物
を遠心分離にて回収し、凍結乾燥することにより1.5
g/100ml培養液のポリ−γ−グルタミン酸を得る
ことができた。
Reference Examples 7 to 10 Bacillus subtilis IFO3335 strain was used as a strain to be used, and the medium shown in Table 2 was placed in a 3 ml test tube and shake-cultured at 37 ° C. overnight to obtain a preculture solution. Next, 100 ml of the medium of Table 2 was placed in a 500 ml Sakaguchi flask, and 1 m of the preculture liquid was added.
and shaking culture was performed at 37 ° C., and a culture solution was collected after 72 hours. The recovered culture solution was 12,000 r.
p. m, centrifugation for 30 minutes, and adding a three-fold amount of ethyl alcohol to the culture supernatant after centrifugation, collects the precipitate by centrifugation, and freeze-drys to obtain a precipitate.
g / 100 ml of the culture solution was able to obtain poly-γ-glutamic acid.

【0036】上記の製造方法を数回行うことにより得ら
れたポリ−γ−グルタミン酸を9、15、20、25重
量%濃度になるように水に溶解させ、窒素によりバブリ
ングした後、蓋付き10mlサンプル瓶に2ml入れ、
蓋を閉めた。このサンプル瓶に、線源としてコバルト6
0を用いるγ線を線量率1.2kGy/時間で室温に
て、照射線量20kGyとなるように照射した。得られ
た処理物を蓋付き10mlサンプル瓶から取り出し、一
週間4℃の水に浸漬し、未架橋のポリ−γ−グルタミン
酸を除去した。水を吸収して膨潤したポリ−γ−グルタ
ミン酸ハイドロゲルを80メッシュの金網で濾過後、凍
結乾燥し、ポリ−γ−グルタミン酸架橋体として得た。
この架橋体の吸水性樹脂について、実施例1と同様にし
てゲル化率と吸水率を測定し、その結果を表10に示し
た。
The poly-γ-glutamic acid obtained by performing the above-mentioned production method several times is dissolved in water so as to have a concentration of 9, 15, 20, and 25% by weight, bubbled with nitrogen, and then 10 ml with a lid. Put 2 ml in the sample bottle,
The lid was closed. In this sample bottle, cobalt 6 was used as a radiation source.
Irradiation was carried out at room temperature at a dose rate of 1.2 kGy / hour using γ-rays using 0 at an irradiation dose of 20 kGy. The treated product was taken out of a 10 ml sample bottle with a lid and immersed in water at 4 ° C. for one week to remove uncrosslinked poly-γ-glutamic acid. The poly-γ-glutamic acid hydrogel swollen by absorbing water was filtered through an 80-mesh wire gauze and freeze-dried to obtain a cross-linked poly-γ-glutamic acid.
The gelation rate and water absorption rate of the water-absorbent resin of this crosslinked body were measured in the same manner as in Example 1, and the results are shown in Table 10.

【0037】[0037]

【表10】 [Table 10]

【0038】[0038]

【発明の効果】本発明のポリ−γ−グルタミン酸架橋体
の吸水性樹脂は、より高いゲル化率を達成することがで
き、(製造上有利に製造できるだけでなく)優れた吸水
性能を有し、生分解性も有する。上記の吸水性樹脂は、
紙オムツ等の衛生分野としての利用のみでなく、医療分
野、建築分野、食品分野、農業・園芸分野等への幅広い
分野へ応用可能である。また、生分解性に優れているこ
とから、廃棄処分が安全・簡便であるという効果も有し
ている。また、本発明の製造方法によれば、ゲル化率の
より高く、優れた吸水性能を有する吸水性能を製造する
ことができる。
EFFECT OF THE INVENTION The water-absorbent resin of the crosslinked poly-γ-glutamic acid of the present invention can achieve a higher gelation rate and has excellent water absorption performance (not only can be advantageously produced in production). It also has biodegradability. The above water absorbent resin,
It can be applied not only to sanitary fields such as disposable diapers, but also to a wide range of fields such as the medical field, the construction field, the food field, and the agriculture and horticulture fields. In addition, because of its excellent biodegradability, it has the effect that disposal is safe and simple. Further, according to the production method of the present invention, it is possible to produce water absorption performance having a higher gelation rate and excellent water absorption performance.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 ゲル化率91〜100%のポリ−γ−グ
ルタミン酸架橋体からなる生分解性吸水性樹脂。
1. A biodegradable water-absorbing resin comprising a crosslinked poly-γ-glutamic acid having a gelation ratio of 91 to 100%.
【請求項2】 ゲル化率94〜100%のポリ−γ−グ
ルタミン酸架橋体からなる生分解性吸水性樹脂。
2. A biodegradable water-absorbent resin comprising a crosslinked poly-γ-glutamic acid having a gelation ratio of 94 to 100%.
【請求項3】 ポリ−γ−グルタミン酸架橋体からなる
生分解性吸水性樹脂を製造する方法において、ポリ−γ
−グルタミン酸をその濃度が2〜15重量%になるよう
に溶解した後、放射線を照射線量30kGy以上照射
し、ゲル化率91〜100%のポリ−γ−グルタミン酸
架橋体を得ることを特徴とする生分解性吸水性樹脂の製
造方法
3. A method for producing a biodegradable water-absorbent resin comprising a cross-linked poly-γ-glutamic acid, comprising the steps of:
-Dissolving glutamic acid so that its concentration becomes 2 to 15% by weight, and then irradiating it with an irradiation dose of 30 kGy or more to obtain a crosslinked poly-γ-glutamic acid having a gelation ratio of 91 to 100%. Method for producing biodegradable water absorbent resin
【請求項4】 ポリ−γ−グルタミン酸架橋体からなる
生分解性吸収性樹脂を製造する方法において、ポリ−γ
−グルタミン酸をその濃度が2〜8重量%になるように
溶解した後、放射線を線量率1.0〜1.4kGy/時
間で照射し、ゲル化率91〜100%のポリ−γ−グル
タミン酸架橋体を得ることを特徴とする生分解性吸水性
樹脂の製造方法。
4. A method for producing a biodegradable absorbent resin comprising a cross-linked poly-γ-glutamic acid, comprising the steps of:
After dissolving glutamic acid so that its concentration becomes 2 to 8% by weight, irradiation with radiation is performed at a dose rate of 1.0 to 1.4 kGy / hour to crosslink poly-γ-glutamic acid having a gelation rate of 91 to 100%. A method for producing a biodegradable water-absorbent resin, comprising obtaining a body.
【請求項5】 ポリ−γ−グルタミン酸架橋体からなる
生分解性吸収性樹脂を製造する方法において、ポリ−γ
−グルタミン酸をその濃度が4〜7重量%になるように
溶解した後、放射線を線量率1.0〜1.4kGy/時
間で照射し、ゲル化率94〜100%のポリ−γ−グル
タミン酸架橋体を得ることを特徴とする生分解性吸水性
樹脂の製造方法。
5. A method for producing a biodegradable absorbent resin comprising a cross-linked poly-γ-glutamic acid, comprising the steps of:
-Dissolving glutamic acid to a concentration of 4 to 7% by weight, and then irradiating with radiation at a dose rate of 1.0 to 1.4 kGy / hour to crosslink poly-γ-glutamic acid having a gelation rate of 94 to 100%. A method for producing a biodegradable water-absorbent resin, comprising obtaining a body.
【請求項6】 放射線が、γ線であることを特徴とする
請求項3乃至5のいずれかに記載の生分解性吸水性樹脂
の製造方法。
6. The method for producing a biodegradable water-absorbent resin according to claim 3, wherein the radiation is gamma rays.
JP24068897A 1997-01-07 1997-09-05 Biodegradable water absorbent resin Expired - Fee Related JP3715414B2 (en)

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JP85097 1997-01-07
JP85197 1997-01-07
JP9-851 1997-01-07
JP9-850 1997-01-07
JP24068897A JP3715414B2 (en) 1997-01-07 1997-09-05 Biodegradable water absorbent resin

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WO2002051907A1 (en) * 2000-12-22 2002-07-04 Microorganism Science Laboratory Incorporated Biodegradable plastics
JP2005314489A (en) * 2004-04-27 2005-11-10 Idemitsu Technofine Co Ltd MANUFACTURING METHOD OF CROSSLINKED PRODUCT OF POLY-gamma-GLUTAMIC ACID AND CROSSLINKED PRODUCT OF POLY-gamma-GLUTAMIC ACID OBTAINED BY THE SAME
JP2005348881A (en) * 2004-06-09 2005-12-22 Meiji Seika Kaisha Ltd Wound dressing
WO2007135801A1 (en) 2006-05-23 2007-11-29 Toyo Boseki Kabushiki Kaisha MICROORGANISM CAPABLE OF PRODUCING γ-L-PGA, METHOD FOR PRODUCTION OF γ-L-PGA USING THE MICROORGANISM, CROSSLINKED PRODUCT, AND AGENT FOR EXTERNAL APPLICATION TO THE SKIN
JP2009089837A (en) * 2007-10-05 2009-04-30 Idemitsu Technofine Co Ltd Wound covering material
DE102010002146A1 (en) 2009-02-20 2010-11-25 Idemitsu Technofine Co. Ltd. Crosslinked fiber body and production process for cross-linked fiber bodies
US8916141B2 (en) 2005-10-20 2014-12-23 Bioleaders Corporation Hyaluronidase inhibitor containing poly-gamma-glutamic acid as an effective component

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002051907A1 (en) * 2000-12-22 2002-07-04 Microorganism Science Laboratory Incorporated Biodegradable plastics
JP2005314489A (en) * 2004-04-27 2005-11-10 Idemitsu Technofine Co Ltd MANUFACTURING METHOD OF CROSSLINKED PRODUCT OF POLY-gamma-GLUTAMIC ACID AND CROSSLINKED PRODUCT OF POLY-gamma-GLUTAMIC ACID OBTAINED BY THE SAME
JP4574214B2 (en) * 2004-04-27 2010-11-04 出光テクノファイン株式会社 Method for producing poly-γ-glutamic acid crosslinked product
JP2005348881A (en) * 2004-06-09 2005-12-22 Meiji Seika Kaisha Ltd Wound dressing
US8916141B2 (en) 2005-10-20 2014-12-23 Bioleaders Corporation Hyaluronidase inhibitor containing poly-gamma-glutamic acid as an effective component
WO2007135801A1 (en) 2006-05-23 2007-11-29 Toyo Boseki Kabushiki Kaisha MICROORGANISM CAPABLE OF PRODUCING γ-L-PGA, METHOD FOR PRODUCTION OF γ-L-PGA USING THE MICROORGANISM, CROSSLINKED PRODUCT, AND AGENT FOR EXTERNAL APPLICATION TO THE SKIN
US8703443B2 (en) 2006-05-23 2014-04-22 Toyo Boseki Kabushiki Kaisha γ-L-PGA producing microorganism, method of producing γ-L-PGA using the microorganism, crosslinked substance produced using the microorganism, and external dermal agent produced using the microorganism
JP2009089837A (en) * 2007-10-05 2009-04-30 Idemitsu Technofine Co Ltd Wound covering material
DE102010002146A1 (en) 2009-02-20 2010-11-25 Idemitsu Technofine Co. Ltd. Crosslinked fiber body and production process for cross-linked fiber bodies

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