JPH05271425A - Production of pva gel molding - Google Patents

Production of pva gel molding

Info

Publication number
JPH05271425A
JPH05271425A JP10166592A JP10166592A JPH05271425A JP H05271425 A JPH05271425 A JP H05271425A JP 10166592 A JP10166592 A JP 10166592A JP 10166592 A JP10166592 A JP 10166592A JP H05271425 A JPH05271425 A JP H05271425A
Authority
JP
Japan
Prior art keywords
pva
aqueous solution
spherical
water
polyvinyl alcohol
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.)
Pending
Application number
JP10166592A
Other languages
Japanese (ja)
Inventor
Hiroaki Fujii
弘明 藤井
Toshihiro Hamada
敏裕 浜田
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.)
Kuraray Co Ltd
Original Assignee
Kuraray Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP10166592A priority Critical patent/JPH05271425A/en
Publication of JPH05271425A publication Critical patent/JPH05271425A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain the title molding having high strengths, water resistance and chemical resistance and a high affinity for a biocatalyst by bringing a mixed aqueous solution of PVA and a water-soluble polysaccharide into contact with a liquid containing borate ions and cations to form particles and treating the particles for insolubilizing the PVA. CONSTITUTION:A spherical polyvinyl alcohol gel molding is produced by bringing an aqueous solution containing polyvinyl alcohol and a water-soluble polysaccharide capable of gelling upon contact with cations into contact with a liquid containing borate ions and cations to form spherical particles and treating the particles for insolubilizing the PVA. According to this process, the spherical polyvinyl alcohol gel molding can be easily obtained, has a high affinity for a biocatalyst, and therefore can be used as a bioreactor, a carrier for wastewater treatment, a water retentive, a low-temperature insulation, etc.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、酵素および微生物等の
生体触媒との親和性の高いポリビニルアルコール系ゲル
成形物の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polyvinyl alcohol gel molding having a high affinity with biocatalysts such as enzymes and microorganisms.

【0002】[0002]

【従来の技術】高分子含水ゲルは生体触媒の固定化担
体、保水材、保冷材、眼・皮膚・関節などの生体ゲルの
代替、薬物の徐放材、アクチュエーターの基材として、
近年、その研究が盛んである。これらの含水ゲルの原料
となる高分子素材として、寒天、アルギン酸塩、カラギ
ーナン、ポリアクリルアミド、ポリビニルアルコール、
光硬化性樹脂等がある。このうち、ポリビニルアルコー
ル(以下PVAと略記する)含水ゲルは、含水率が高
く、酸素・基質の透過性に優れ、生体との親和性が高
く、高分子含水ゲル中でも特に優れている。このPVA
系含水ゲルの形状としては、流動性、充填効果、取扱性
を考慮した場合、球状が要求される場合が多い。
Polymer hydrogels are used as a carrier for immobilizing biocatalysts, water retention materials, cold insulation materials, substitutes for biogels for eyes, skin, joints, etc.
In recent years, research has been active. As a polymer material which is a raw material of these hydrogels, agar, alginate, carrageenan, polyacrylamide, polyvinyl alcohol,
There are photo-curable resins and the like. Among these, polyvinyl alcohol (hereinafter abbreviated as PVA) hydrogel has a high water content, excellent oxygen / substrate permeability, high affinity with living organisms, and is particularly excellent among high molecular hydrogels. This PVA
The shape of the hydrous gel is often required to be spherical in consideration of fluidity, filling effect, and handleability.

【0003】従来、PVAゲルを球状に成形する方法と
して、PVA水溶液を飽和ホウ酸水溶液と接触させゲル
化する方法(下水道協会誌、23、41(1986)、
用水と廃水、30、36(1986).);PVAとア
ルギン酸ナトリウムの混合水溶液を塩化カルシウムおよ
びホウ酸の混合水溶液に接触させて球状ゲル化させる方
法(特開昭62−138193);PVAとアルギン酸
ナトリウムの混合水溶液を塩化カルシウム水溶液に接触
させて球状成形した後、凍結・解凍することにより、P
VAをゲル化させる方法(特開昭64−43188)が
知られている。
Conventionally, as a method of forming PVA gel into a spherical shape, a method of bringing an aqueous solution of PVA into contact with a saturated aqueous solution of boric acid to form a gel (Sewerage Society, 23, 41 (1986),
Irrigation and wastewater, 30, 36 (1986). ); Method of contacting a mixed aqueous solution of PVA and sodium alginate with a mixed aqueous solution of calcium chloride and boric acid to form a spherical gel (JP-A-62-138193); Contacting a mixed aqueous solution of PVA and sodium alginate with an aqueous calcium chloride solution After spherical molding, freeze and thaw
A method for gelating VA (Japanese Patent Laid-Open No. 64-43188) is known.

【0004】[0004]

【発明が解決しようとする課題】PVA水溶液をホウ酸
水溶液に滴下する方法は、滴下した液滴どうしが膠着を
起こし球状の成形物を得ることはできない。また、PV
Aとアルギン酸ナトリウムの混合水溶液を塩化カルシウ
ムおよびホウ酸の混合水溶液に滴下し、その後の処理を
行わない方法は、滴下物をホウ酸水溶液に長時間接触さ
せ、球状の成形物の中心部までゲル化させなければなら
ないため、生体触媒を固定した場合にはホウ酸が生体触
媒に悪影響を与え、生体触媒の活性が発現しない。ま
た、ホウ酸によるゲル化は可逆反応のため、pHの変化
などにより容易にゲルが溶解してしまうことから、実用
化は困難である。また、PVAとアルギン酸ナトリウム
の混合水溶液を塩化カルシウム水溶液に接触させて球状
に成形した後、凍結・解凍することにより、PVAをゲ
ル化させる方法は、球状に成形する際、アルギン酸塩の
みがゲル化しPVAはゲル化しないため、塩化カルシウ
ム水溶液中にPVAが溶出し、塩化カルシウム水溶液が
汚染され、粘度が上昇するために塩化カルシウム水溶液
を繰り返し使用することができない。また、凍結する際
にもPVAが表面にしみ出し、球状のゲルどうしが膠着
してしまうという問題点があった。
In the method of dropping the PVA aqueous solution into the boric acid aqueous solution, the dropped droplets stick to each other and a spherical molded article cannot be obtained. Also, PV
A method of dropping a mixed aqueous solution of A and sodium alginate into a mixed aqueous solution of calcium chloride and boric acid, and performing no subsequent treatment is to bring the dropped product into contact with the aqueous boric acid solution for a long time, and to form a gel up to the center of the spherical molded article. Therefore, when the biocatalyst is immobilized, boric acid adversely affects the biocatalyst and the activity of the biocatalyst does not appear. Further, gelation with boric acid is a reversible reaction, and the gel is easily dissolved due to a change in pH, etc., which makes practical application difficult. In addition, a method of gelating PVA by contacting a mixed aqueous solution of PVA and sodium alginate with a calcium chloride aqueous solution to form a spherical shape, and then freezing and thawing, is a method in which only the alginate is gelated when forming the spherical shape. Since PVA does not gel, PVA is eluted into the calcium chloride aqueous solution, the calcium chloride aqueous solution is contaminated, and the viscosity increases, so that the calcium chloride aqueous solution cannot be repeatedly used. Further, there was a problem that the PVA exudes to the surface even when it is frozen, and the spherical gels stick to each other.

【0005】[0005]

【課題を解決するための手段】上記課題を解決するため
に鋭意検討の結果、PVA(A)および陽イオンとの接
触によりゲル化する能力のある水溶液多糖類(B)を含
む混合水溶液(以下、PVA混合水溶液と略称する)
を、ホウ酸イオンおよび陽イオンを含む液体(以下、凝
固液と略称する)に接触させることにより球状に成形し
た後、PVAの不溶化処理を行うことを特徴とする球状
のPVA系ゲル成形物の製造方法を見出し本発明を完成
させるに至った。
Means for Solving the Problems As a result of intensive studies to solve the above problems, a mixed aqueous solution containing an aqueous solution polysaccharide (B) capable of gelling upon contact with PVA (A) and a cation (hereinafter , Abbreviated as PVA mixed aqueous solution)
Is formed into a spherical shape by contacting with a liquid containing borate ions and cations (hereinafter abbreviated as coagulation liquid), and then PVA insolubilization treatment is carried out. The manufacturing method was found and the present invention was completed.

【0006】以下、本発明の球状のPVA系ゲル成形物
の製造方法についてより詳細に説明する。まず、本発明
に使用する成分について説明する。本発明に使用するP
VA(A)は平均重合度が1000以上が好ましく、1
700以上がより好ましい。PVAのケン化度は98.
5モル%以上が好ましく、99.85モル%以上の完全
ケン化PVAがゲルの形成上からより好ましい。また本
発明のPVAとしては、本発明の目的を阻害しない範囲
において、公知の種々の変性PVAを用いることができ
る。PVAの濃度が高いほど強固なゲルが生成するが、
必要なゲル強度が得られれば、PVA濃度が低い方が原
料コスト面から有利である。PVA以外の添加成分の種
類や濃度、PVA混合水溶液の液温および液滴形成法に
よって、適切な濃度を選定する必要はあるが、常温でP
VA混合水溶液を滴下する場合は、PVA濃度0.3〜
40wt%が球状化が容易であり、実用上充分なゲル強
度が得られる。本発明に使用する陽イオンとの接触によ
りゲル化する能力のある水溶液多糖類(B)としては、
アルギン酸塩、カラギーナン、マンナン、キトサンなど
が挙げられるが、とりわけアルギン酸ナトリウムが好ま
しい。本発明における陽イオンとしては、カルシウムイ
オン、マグシウムイオン、ストロンチウムイオン、バリ
ウムイオン、アルミニウムイオン、カリウムイオン、セ
リウムイオン、ニッケルイオンなどの金属イオン、アン
モニウムイオンなどの陽イオンが挙げられ、特に多価金
属陽イオンが好ましい。これらの陽イオンのうち少なく
とも1種を含有する化合物とりわけ塩化カルシウムが好
ましい。陽イオンの濃度は、0.1〜10重量%が好ま
しい。本発明におけるホウ酸イオンを含有する化合物と
してはホウ酸、ホウ酸塩、ホウ酸エステルが挙げられ
る。ホウ酸イオンの濃度は1g/リットル以上が好まし
く、10g/リットル以上がより好ましく、飽和溶液で
も差し支えない。また、このホウ酸イオン含有水溶液に
アルカリ性物質を添加しpHを調節してもよい。
The method for producing the spherical PVA-based gel molded article of the present invention will be described in more detail below. First, the components used in the present invention will be described. P used in the present invention
The average degree of polymerization of VA (A) is preferably 1000 or more, and 1
700 or more is more preferable. The degree of saponification of PVA is 98.
5 mol% or more is preferable, and 99.85 mol% or more of completely saponified PVA is more preferable from the viewpoint of gel formation. Further, as the PVA of the present invention, various known modified PVA can be used as long as the object of the present invention is not impaired. The higher the concentration of PVA, the stronger the gel formed,
If the required gel strength can be obtained, it is advantageous from the viewpoint of raw material cost that the PVA concentration is low. Although it is necessary to select an appropriate concentration depending on the type and concentration of the additive component other than PVA, the liquid temperature of the PVA mixed aqueous solution, and the droplet formation method, P at room temperature
When dropping the VA mixed aqueous solution, the PVA concentration is 0.3 to
40 wt% is easy to be spheroidized, and practically sufficient gel strength can be obtained. The aqueous solution polysaccharide (B) having the ability to gel upon contact with a cation used in the present invention includes:
Examples thereof include alginate, carrageenan, mannan, chitosan, etc., and sodium alginate is particularly preferable. Examples of the cations in the present invention include calcium ions, magnesium ions, strontium ions, barium ions, aluminum ions, potassium ions, cerium ions, metal ions such as nickel ions, and cations such as ammonium ions. Metal cations are preferred. Compounds containing at least one of these cations, especially calcium chloride, are preferred. The cation concentration is preferably 0.1 to 10% by weight. Examples of the compound containing a borate ion in the present invention include boric acid, borate, and borate ester. The borate ion concentration is preferably 1 g / liter or more, more preferably 10 g / liter or more, and a saturated solution may be used. Further, the pH may be adjusted by adding an alkaline substance to the borate ion-containing aqueous solution.

【0007】このPVA混合水溶液には、PVAのゲル
化を阻害しない範囲で、微生物・酵素などの生体触媒、
微生物の培地、球状ゲルの強度を上げるための補強材、
ゲル成形物の比重を調整する充填材などを添加してもよ
い。上記の方法により得られたPVA混合水溶液を例え
ば、管状の口金から滴下させるか、または噴霧口金から
噴霧させることによって液滴を形成させ、次いで凝固液
に接触させる。PVA混合水溶液の液滴は、凝固液に接
触すると表面張力によって球状となる。球状の成形物の
直径は、口金の直径、噴霧圧力、PVA水溶液の粘度を
調整することによって任意に変えられる。凝固液は静置
でもよいが、スターラー等で強制攪拌することによっ
て、PVA混合水溶液と凝固液との反応を促進し、球状
の成形物どうしの膠着を完全に防止できる。実用上、多
量のPVA系ゲル成形物を製造する場合、PVA混合水
溶液を滴下させるための押し出しにポンプ等を用いるこ
とにより、球状の成形物の直径を揃えることができる。
凝固液中で球状化したPVA系成形物は凝固液と分離
後、PVAの不溶化処理を行なう。PVAの不溶化処理
は次の2つの方法が好ましい。 −5℃以下、好ましくは−10℃で凍結し、少なくと
も1時間以上、好ましくは10時間以上保持後、解凍す
る操作を少なくとも1回以上、好ましくは2回以上繰り
返す。 PVAの離液作用のある化合物を含有する液体に接触
させる。浸漬時間は、10分以上、好ましくは30分以
上がよい。PVAの離液作用のある化合物としては、硫
酸ナトリウム、硫酸アンモニウム、硫酸カリウム、硫酸
マグネシウム、硫酸アルミニウム、クエン酸ナトリウ
ム、クエン酸アンモニウム、クエン酸カリウム、クエン
酸マグネシウム、クエン酸アルミニウム、酒石酸ナトリ
ウム、酒石酸アンモニウム、酒石酸カリウム、酒石酸マ
グネシウム、酒石酸アルミニウム等の化合物のうちの少
なくとも1種を含有する液体が挙げられるが、とりわけ
硫酸ナトリウム水溶液が好ましい。濃度は100g/リ
ットル以上、特に飽和水溶液が好ましい、また、上記の
およびの方法を併用してもよい。このようにして得
られた球状のPVA系ゲル成形物は、長期間にわたっ
て、変形、損壊しない強度を有し、水や各種薬液に対し
ても侵されることなく、連続使用が可能となり、実用性
が発現する。
This PVA mixed aqueous solution contains biocatalysts such as microorganisms and enzymes within a range that does not inhibit gelation of PVA.
Microbial medium, reinforcing material to increase the strength of spherical gel,
You may add the filler etc. which adjust the specific gravity of a gel molding. For example, the PVA mixed aqueous solution obtained by the above method is dropped from a tubular die or sprayed from a spray die to form droplets, which are then brought into contact with a coagulating liquid. The droplets of the PVA mixed aqueous solution become spherical due to the surface tension when they come into contact with the coagulating liquid. The diameter of the spherical molded product can be arbitrarily changed by adjusting the diameter of the die, the spraying pressure, and the viscosity of the PVA aqueous solution. The coagulation liquid may be allowed to stand still, but by forcibly stirring it with a stirrer or the like, the reaction between the PVA mixed aqueous solution and the coagulation liquid can be promoted, and the sticking of the spherical molded products can be completely prevented. In practice, when a large amount of PVA-based gel molded product is produced, the diameter of the spherical molded product can be made uniform by using a pump or the like for the extrusion for dropping the PVA mixed aqueous solution.
The PVA-based molded product spheroidized in the coagulating liquid is subjected to insolubilization treatment of PVA after being separated from the coagulating liquid. The following two methods are preferable for the insolubilization treatment of PVA. The operation of freezing at −5 ° C. or lower, preferably −10 ° C., holding for at least 1 hour or longer, preferably 10 hours or longer, and then thawing is repeated at least once or more, preferably 2 or more times. The PVA is brought into contact with a liquid containing a compound having a syneresis action. The immersion time is 10 minutes or longer, preferably 30 minutes or longer. Examples of the compound having a synergic action of PVA include sodium sulfate, ammonium sulfate, potassium sulfate, magnesium sulfate, aluminum sulfate, sodium citrate, ammonium citrate, potassium citrate, magnesium citrate, aluminum citrate, sodium tartrate, and ammonium tartrate. Examples include liquids containing at least one of compounds such as potassium tartrate, magnesium tartrate, and aluminum tartrate, with sodium sulfate aqueous solution being particularly preferable. The concentration is 100 g / liter or more, and a saturated aqueous solution is particularly preferable, and the above methods and may be used in combination. The spherical PVA-based gel molded product thus obtained has strength that does not deform or damage over a long period of time, and can be continuously used without being attacked by water or various chemicals. Is expressed.

【0008】[0008]

【作用】PVA混合水溶液が凝固液に接触する際、凝固
液へのPVA溶出がなくなったのは、水溶性多糖類が陽
イオンによりゲル化すると同時にPVAがホウ酸架橋
し、PVAが一時的に不溶化されるためと考えられる。
また、球状の成形物どうしの膠着がなくなったのは、ホ
ウ酸架橋によるPVAの一時的な不溶化のためと考えら
れる。さらに、ホウ酸架橋だけでは不完全であったゲル
が、上記のまたはの不溶化処理により、強度・耐久
性が向上するものと考えられる。
When the PVA mixed aqueous solution comes into contact with the coagulation liquid, the elution of PVA into the coagulation liquid disappeared because the water-soluble polysaccharide was gelated by the cations and at the same time the PVA was cross-linked with boric acid and the PVA was temporarily suspended. It is thought that this is due to insolubilization.
Further, it is considered that the reason why the spherical molded articles disappeared from each other was due to the temporary insolubilization of PVA due to the cross-linking with boric acid. Further, it is considered that the gel, which was incomplete by only boric acid crosslinking, is improved in strength and durability by the insolubilization treatment of or.

【0009】[0009]

【実施例】以下、実施例により本発明を具体的に説明す
るが、本発明はこれらの実施例により限定されるもので
はない。 実施例1 (株)クラレ製のPVA(平均重合度4100、ケン化
度99.85モル%)を40℃の温水で約1時間洗浄
後、PVA濃度10wt%になるようにPVAに水を加
え全量を500gにし、これを攪拌しながら110℃、
2時間処理してPVAを溶解し、室温まで放冷した。こ
れに4wt%アルギン酸ナトリウム水溶液250gを加
えて混合し、さらに(株)クラレ岡山工場(岡山県岡山
市海岸通り1丁目2番1号)の排水処理槽より採取し、
濃縮操作を施して得られた活性汚泥(MLSS 800
00mg/リットル 250gを加え、十分に攪拌し
た。この混合液を先端に内径1mmの注射針を取り付け
た内径2mmφのビニル管1本を使用したローラーポン
プで1ミリリットル/分で送液し、スターラーで攪拌し
pH7に調整した10g/リットルのホウ酸および30
g/リットルの塩化カルシウムの混合水溶液(凝固液)
10リットルに水表面5cmの高さより滴下した。滴下
した液滴は凝固液中で直ちに球状化した。全量滴下後、
これらの球状化した成形物を凝固液と分離し、スターラ
ーで攪拌した飽和Na↓2SO↓4水溶液に90分浸漬す
ることによって、不透明な褐色の柔軟性に富んだ球状の
ゲルが得られた。このゲルは球状に成形化され、粘着性
もなかった。粒径は3〜3.5mmφであった。凝固液
の全有機炭素量(TOC)を測定したところ4ppmで
あり、PVAの凝固液への溶出は非常に少なかった。こ
のようにして得られたPVAゲルについて水中での耐久
性を調べた。ゲル30gに対して水300gを加え、3
0℃にて攪拌した。1か月経過後も粒径、強度ともに変
化は見られなかった。
EXAMPLES The present invention will be specifically described below with reference to examples, but the present invention is not limited to these examples. Example 1 PVA (average polymerization degree: 4100, saponification degree: 99.85 mol%) manufactured by Kuraray Co., Ltd. was washed with warm water at 40 ° C. for about 1 hour, and water was added to PVA so that the PVA concentration became 10 wt%. The total amount is 500 g, and while stirring this, 110 ° C,
It was treated for 2 hours to dissolve PVA and allowed to cool to room temperature. To this, 250 g of 4 wt% sodium alginate aqueous solution was added and mixed, and further collected from the wastewater treatment tank of the Kuraray Okayama Plant (1-2-1, Kaigandori, Okayama City, Okayama Prefecture).
Activated sludge obtained by subjecting to concentration operation (MLSS 800
250 mg of 00 mg / liter was added and sufficiently stirred. This mixed solution was fed at a rate of 1 ml / min by a roller pump using one vinyl tube having an inner diameter of 2 mmφ with an injection needle having an inner diameter of 1 mm attached to the tip, and stirred with a stirrer to pH 7 to adjust the pH to 7 g of boric acid. And 30
g / l calcium chloride mixed aqueous solution (coagulation liquid)
Water was added dropwise to 10 liters from a height of 5 cm on the water surface. The dropped droplets were immediately spherical in the coagulating liquid. After dropping the whole amount,
These spheroidized molded products were separated from the coagulating liquid and immersed in a saturated Na ↓ 2SO ↓ 4 aqueous solution stirred with a stirrer for 90 minutes to obtain an opaque brown flexible spherical gel. This gel was formed into a spherical shape and was not tacky. The particle size was 3 to 3.5 mmφ. The total organic carbon content (TOC) of the coagulation liquid was measured to be 4 ppm, and the elution of PVA into the coagulation liquid was very small. The PVA gel thus obtained was examined for durability in water. Add 300g of water to 30g of gel and add 3
Stirred at 0 ° C. No change in particle size or strength was observed even after 1 month.

【0010】実施例2 実施例1と同様のPVAを40℃の温水で約1時間洗浄
後、PVA濃度10wt%になるようにPVAに水を加
え全量を500gにし、これを攪拌しながら110℃、
2時間処理してPVAを溶解し、室温まで放冷した。こ
れに4wt%アルギン酸ナトリウム水溶液250gを加
えて混合し、さらに実施例1と同じ排水処理槽より採取
し、濃縮操作を施して得られた活性汚泥(MLSS 8
0000mg/リットル)250gを加え、十分に攪拌
した。この混合液を先端に内径1mmの注射針を取り付
けた内径2mmφのビニル管1本を使用したローラーポ
ンプて1ミリリットル/分で送液し、スターラーで攪拌
しpH7に調整した10g/リットルのホウ酸および3
0g/リットルの塩化カルシウムの混合水溶液(凝固
液)10リットルに水表面5cmの高さより滴下した。
滴下した液滴は凝固液中で直ちに球状化した。全量滴下
後、これらの球状化した成形物を凝固液と分離し、−2
0℃で24時間凍結し室温で解凍した。さらにこの凍結
解凍操作を2回繰り返し、不透明な褐色の柔軟性に富ん
だ球状のゲルが得られた。このゲルは球状に成形化さ
れ、粘着性もない。粒径は3〜3.5mmφであった。
凝固液の全有機炭素量(TOC)を測定したところ3p
pmであり、PVAの凝固液への溶出は非常に少なかっ
た。このようにして得られたPVAゲルについて水中で
の耐久性を調べた。ゲル30gに対して水300gを加
え30℃にて攪拌した。1か月経過後も粒径、強度とも
変化は見られなかった。
Example 2 The same PVA as in Example 1 was washed with warm water of 40 ° C. for about 1 hour, water was added to PVA so that the concentration of PVA was 10 wt%, and the total amount was 500 g. ,
It was treated for 2 hours to dissolve PVA and allowed to cool to room temperature. To this, 250 g of 4 wt% sodium alginate aqueous solution was added and mixed, and the sludge was collected from the same wastewater treatment tank as in Example 1 and concentrated to obtain activated sludge (MLSS 8).
250 g (0000 mg / liter) was added and sufficiently stirred. This mixed solution was sent at 1 ml / min by a roller pump using one vinyl tube having an inner diameter of 2 mmφ with an injection needle having an inner diameter of 1 mm attached to the tip, and was stirred with a stirrer to adjust the pH to 7 g of boric acid of 10 g / liter. And 3
The mixture was added dropwise to 10 liters of a 0 g / liter calcium chloride mixed aqueous solution (coagulation liquid) from a height of 5 cm on the water surface.
The dropped droplets were immediately spherical in the coagulating liquid. After dropping the whole amount, these spheroidized moldings are separated from the coagulating liquid,
It was frozen at 0 ° C. for 24 hours and thawed at room temperature. Further, this freeze-thaw operation was repeated twice to obtain an opaque brown flexible spherical gel. This gel is formed into a spherical shape and is not sticky. The particle size was 3 to 3.5 mmφ.
When the total organic carbon content (TOC) of the coagulation liquid was measured, it was 3p.
pm, and the elution of PVA into the coagulation liquid was very small. The PVA gel thus obtained was examined for durability in water. 300 g of water was added to 30 g of the gel and stirred at 30 ° C. No change in particle size or strength was observed even after 1 month.

【0011】比較例1 実施例1と同様のPVAを40℃の温水で約1時間洗浄
後、PVA濃度10wt%になるようにPVAに水を加
え全量を500gにし、これを攪拌しながら110℃、
2時間処理してPVAを溶解し、室温まで放冷した。こ
れに実施例1と同じ排水処理槽より採取し、濃縮操作を
施して得られた活性汚泥(MLSS 40000mg/
リットル)500gを加え、十分に攪拌した。このこ液
を先端に内径1mmの注射針を取り付けた内径2mmφ
のビニル管1本を使用したローラーポンプで1ミリリッ
トル/分で送液し、スターラーで攪拌しpH7に調整し
た30g/リットルのホウ酸水溶液(凝固液)10リッ
トルに水表面5cmの高さより滴下した。滴下した液滴
は凝固液中で直ちに凝固したが、液滴どうしが膠着をお
こし球状の成形物を得ることはできなかった。
Comparative Example 1 The same PVA as in Example 1 was washed with warm water at 40 ° C. for about 1 hour, then water was added to PVA to a PVA concentration of 10 wt% to make the total amount 500 g, and this was stirred at 110 ° C. ,
It was treated for 2 hours to dissolve PVA and allowed to cool to room temperature. The activated sludge (MLSS 40000 mg / ml) obtained by collecting and collecting the same from the same wastewater treatment tank as in Example 1
Liter) 500 g was added and sufficiently stirred. This liquid has an inner diameter of 2 mm and an injection needle with an inner diameter of 1 mm attached to the tip.
The solution was fed at a rate of 1 ml / min with a roller pump using one vinyl tube of No. 1 and was added dropwise to 10 liters of a 30 g / liter boric acid aqueous solution (coagulation solution) adjusted to pH 7 with a stirrer from a height of 5 cm of water surface. .. The dropped liquid droplets immediately solidified in the solidifying liquid, but the liquid droplets stuck to each other and a spherical molded product could not be obtained.

【0012】比較例2 実施例1と同様のPVAを40℃の温水で約1時間洗浄
後、PVA濃度10wt%になるようにPVAに水を加
え全量を500gにし、これを攪拌しながら110℃、
2時間処理してPVAを溶解し、室温まで放冷した。こ
れに4wt%アルギン酸ナトリウム水溶液250gを加
えて混合し、さらに実施例1と同じ排水処理槽より採取
し、濃縮操作を施して得られた活性汚泥(MLSS 8
0000mg/リットル)250gを加え、十分に攪拌
した。この混合液を先端に内径1mmの注射針を取り付
けた内径2mmφのビニル管1本を使用したローラーポ
ンプで1ミリリットル/分で送液し、スターラーで攪拌
しpHに調整した10g/リットルのホウ酸および30
g/リットルの塩化カルシウムの混合水溶液(凝固液)
10リットルに水表面5cmの高さより滴下した。滴下
した液滴は凝固液中で直ちに球状化した。全量滴下後、
これらの球状化したPVA混合成形物を凝固液と分離し
た。その後、凍結などの不溶化処理は行わなかった。粒
径3〜3.5mmφであった。凝固液の全有機炭素量
(TOC)を測定したところ3ppmであり、PVAの
凝固液への溶出は非常に少なかった。このようにして得
られたPVAゲルについて水中での耐久性を調べた。ゲ
ル30gに対して水300gを加え、30℃にて攪拌し
た。3日後には、ゲルが溶解してしまい耐久性に問題が
あることがわかった。
Comparative Example 2 The same PVA as in Example 1 was washed with warm water at 40 ° C. for about 1 hour, water was added to PVA so that the concentration of PVA was 10 wt%, and the total amount was adjusted to 500 g. ,
It was treated for 2 hours to dissolve PVA and allowed to cool to room temperature. To this, 250 g of 4 wt% sodium alginate aqueous solution was added and mixed, and the sludge was collected from the same wastewater treatment tank as in Example 1 and concentrated to obtain activated sludge (MLSS 8).
250 g (0000 mg / liter) was added and sufficiently stirred. This mixed solution was fed at a rate of 1 ml / min by a roller pump using one vinyl tube having an inner diameter of 2 mmφ with an injection needle having an inner diameter of 1 mm attached to the tip, and stirred at a stirrer to adjust pH to 10 g / liter boric acid. And 30
g / l calcium chloride mixed aqueous solution (coagulation liquid)
Water was added dropwise to 10 liters from a height of 5 cm on the water surface. The dropped droplets were immediately spherical in the coagulating liquid. After dropping the whole amount,
These spheroidized PVA mixed moldings were separated from the coagulation liquid. After that, insolubilization treatment such as freezing was not performed. The particle size was 3 to 3.5 mmφ. The total organic carbon content (TOC) of the coagulation liquid was measured to be 3 ppm, and the elution of PVA into the coagulation liquid was very small. The PVA gel thus obtained was examined for durability in water. 300 g of water was added to 30 g of the gel, and the mixture was stirred at 30 ° C. It was found that the gel was dissolved after 3 days and there was a problem in durability.

【0013】比較例3 実施例1と同様のPVAを40℃の温水で約1時間洗浄
後、PVA濃度10wt%になるようにPVAに水を加
え全量を500gにし、これを攪拌しながら110℃、
2時間処理してPVAを溶解し、室温まで放冷した。こ
れに4wt%アルギン酸ナトリウム水溶液250gを加
えて混合し、さらに実施例1と同じ排水処理槽より採取
し、濃縮操作を施して得られた活性汚泥(MLSS 8
0000mg/リットル)250gを加え、十分に攪拌
した。この混合液を先端に内径1mmの注射針を取り付
けた内径2mmφのビニル管1本を使用したローラーポ
ンプで1ミリリットル/分で送液し、スターラーで攪拌
しpH7に調整した30g/リットルの塩化カルシウム
水溶液(凝固液)10リットルに水表面5cmの高さよ
り滴下した。滴下した液滴は凝固液中で直ちに球状化し
た。全量滴下後、これらの球状化したPVA混合成形物
を凝固液と分離し、−20℃で24時間凍結し室温で解
凍した。さらにこの凍結解凍操作を2回繰り返し、不透
明な褐色の柔軟性に富んだ球状のゲルが得られた。粒径
は3〜3.5mmφであった。凝固液の全有機炭素量
(TOC)を測定したところ103ppmであり、PV
Aの凝固液中への溶出が多かった。このようにして得ら
れたPVAゲルについて水中での耐久性を調べた。ゲル
30gに対して水300gを加え、30℃にて攪拌し
た。1か月経過後も粒径、強度ともに変化は見られなか
った。
Comparative Example 3 The same PVA as in Example 1 was washed with warm water at 40 ° C. for about 1 hour, water was added to PVA so that the concentration of PVA was 10 wt%, and the total amount was adjusted to 500 g. ,
It was treated for 2 hours to dissolve PVA and allowed to cool to room temperature. To this, 250 g of 4 wt% sodium alginate aqueous solution was added and mixed, and the sludge was collected from the same wastewater treatment tank as in Example 1 and concentrated to obtain activated sludge (MLSS 8).
250 g (0000 mg / liter) was added and sufficiently stirred. This mixed solution was delivered at a rate of 1 ml / min by a roller pump using one vinyl tube having an inner diameter of 2 mmφ with an injection needle having an inner diameter of 1 mm attached to the tip, and stirred with a stirrer to adjust the pH to 30 g / liter calcium chloride. It was added dropwise to 10 liters of the aqueous solution (coagulation liquid) from the height of the water surface of 5 cm. The dropped droplets were immediately spherical in the coagulating liquid. After the entire amount was dropped, these spheroidized PVA-mixed molded products were separated from the coagulating liquid, frozen at -20 ° C for 24 hours, and thawed at room temperature. Further, this freeze-thaw operation was repeated twice to obtain an opaque brown flexible spherical gel. The particle size was 3 to 3.5 mmφ. When the total organic carbon content (TOC) of the coagulation liquid was measured, it was 103 ppm.
The elution of A into the coagulation liquid was large. The PVA gel thus obtained was examined for durability in water. 300 g of water was added to 30 g of the gel, and the mixture was stirred at 30 ° C. No change in particle size or strength was observed even after 1 month.

【0014】[0014]

【表1】 [Table 1]

【0015】[0015]

【発明の効果】上記の実施例で明らかなとおり、本発明
によると、容易に球状のPVA系ゲル成形物が得られ、
得られたPVA系ゲル成形物は強度が高く十分な耐水性
および耐薬品性を有し、さらに生体触媒との親和性に富
むことから、バイオリアクター・排水処理の担体、保水
材・保冷材などへの利用が可能である。
As is apparent from the above examples, according to the present invention, a spherical PVA-based gel molded product can be easily obtained.
The obtained PVA-based gel molded product has high strength, sufficient water resistance and chemical resistance, and further has a high affinity with biocatalysts, so that it is a bioreactor / wastewater treatment carrier, water retention material / cooling material, etc. Can be used for.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C08L 29/04 LGS 6904−4J LGW 6904−4J (C08L 29/04 5:00) 7415−4J ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 5 Identification code Internal reference number FI Technical display location C08L 29/04 LGS 6904-4J LGW 6904-4J (C08L 29/04 5:00) 7415-4J

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 ポリビニルアルコール(A)および陽イ
オンとの接触によりゲル化する能力のある水溶性多糖類
(B)を含む混合水溶液を、ホウ酸イオンおよび陽イオ
ンを含む液体に接触させることにより球状に成形した
後、ポリビニルアルコールの不溶化処理を行うことを特
徴とする球状のポリビニルアルコール系ゲル成形物の製
造方法。
1. A mixed aqueous solution containing polyvinyl alcohol (A) and a water-soluble polysaccharide (B) capable of gelling upon contact with a cation is brought into contact with a liquid containing borate ions and cations. A method for producing a spherical polyvinyl alcohol-based gel molded article, which comprises performing insolubilization treatment of polyvinyl alcohol after molding into a spherical shape.
【請求項2】 ポリビニルアルコールの不溶化処理の方
法が、−5℃以下で凍結し、解凍する操作を少なくとも
1回以上行う方法またはポリビニルアルコールの離液作
用のある化合物を含有する液体に接触させる方法である
請求項1記載の球状ポリビニルアルコール系ゲル成形物
の製造方法。
2. A method for insolubilizing polyvinyl alcohol is a method of freezing at −5 ° C. or lower and thawing at least once or a method of contacting with a liquid containing a compound having a syneresis function of polyvinyl alcohol. The method for producing a spherical polyvinyl alcohol-based gel molded article according to claim 1, wherein
JP10166592A 1992-03-27 1992-03-27 Production of pva gel molding Pending JPH05271425A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10166592A JPH05271425A (en) 1992-03-27 1992-03-27 Production of pva gel molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10166592A JPH05271425A (en) 1992-03-27 1992-03-27 Production of pva gel molding

Publications (1)

Publication Number Publication Date
JPH05271425A true JPH05271425A (en) 1993-10-19

Family

ID=14306673

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10166592A Pending JPH05271425A (en) 1992-03-27 1992-03-27 Production of pva gel molding

Country Status (1)

Country Link
JP (1) JPH05271425A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998004616A1 (en) * 1996-07-31 1998-02-05 Kanebo Limited Porous spherical polyvinyl acetal particles, process for producing the same, and microbial carriers
CN106543467A (en) * 2015-09-16 2017-03-29 清华大学 A kind of ice glue support and its production and use

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998004616A1 (en) * 1996-07-31 1998-02-05 Kanebo Limited Porous spherical polyvinyl acetal particles, process for producing the same, and microbial carriers
CN106543467A (en) * 2015-09-16 2017-03-29 清华大学 A kind of ice glue support and its production and use
CN106543467B (en) * 2015-09-16 2019-06-18 清华大学 A kind of ice glue bracket and its preparation method and application

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