JPH0959402A - Method for activating resin material - Google Patents

Method for activating resin material

Info

Publication number
JPH0959402A
JPH0959402A JP7214632A JP21463295A JPH0959402A JP H0959402 A JPH0959402 A JP H0959402A JP 7214632 A JP7214632 A JP 7214632A JP 21463295 A JP21463295 A JP 21463295A JP H0959402 A JPH0959402 A JP H0959402A
Authority
JP
Japan
Prior art keywords
resin material
water
activated
pressurized
inorganic substance
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
JP7214632A
Other languages
Japanese (ja)
Other versions
JP3634021B2 (en
Inventor
Kenji Hatanaka
賢爾 畑中
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.)
SHINKI SANGYO KK
Original Assignee
SHINKI SANGYO KK
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 SHINKI SANGYO KK filed Critical SHINKI SANGYO KK
Priority to JP21463295A priority Critical patent/JP3634021B2/en
Publication of JPH0959402A publication Critical patent/JPH0959402A/en
Application granted granted Critical
Publication of JP3634021B2 publication Critical patent/JP3634021B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for activating resin material by treatment with an activated water, whereby the resin material is subjected to physicochemical action to form an activated material which can give for example a container which can markedly retard the lowering of the freshness of perishables and can make the taste of the perishables mellow. SOLUTION: This method for activating resin material comprises immersing or passing a monomer the resin material a polymer (resin material itself) or a catalyst to be fed together with the monomer of the resin material into a polymerizer under agitation to polymerize the monomer in or through an activated water prepared by a step of passing water pressurized to 5-30atm. Through an inorganic substance and a step of storing the pressurized water in an atmosphere under a pressure of 5 to below 30atm. or the activated water prepared by repeating these steps. The polymer is subjected to the activation treatment in the form of pellets or flakes. As for the catalyst, the activated catalyst is fed into the polymerizer and agitated together with the monomer to obtain an activated resin material. The inorganic substance is desirably a ferroelectric mineral.

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、高浸透性や抗菌性
等が認められる活性化水を処理用水として利用する樹脂
材の活性処理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 method for active treatment of a resin material, which uses activated water, which has high permeability and antibacterial properties, as treatment water.

【0002】[0002]

【従来の技術】一般に、水は複数の水分子が水素結合に
よってクラスターを形成してなることは知られてはいる
が、このクラスターの形成度合が水の腐敗の速度に多大
な影響を及ぼすことも近年多くの学者等の実験研究によ
って解明され、更にこのクラスターを崩壊させるか、又
は昇降圧、無機物質からの2価、3価イオン等、イオン
を中心に小分子集団となった水には、例えば物質への浸
透性が増したり、繊維加工水として用いた場合には、染
着性が改善されたり、又は雑菌の増殖を抑制するといっ
た種々の効用があることも知られている。
2. Description of the Related Art Generally, it is known that a plurality of water molecules form clusters by hydrogen bonds, but the degree of formation of these clusters has a great influence on the decay rate of water. In recent years, it has been clarified by experimental research by many scholars, etc., and this cluster is further collapsed, or water that has become a small molecule group centered on ions such as buck-boost, divalent and trivalent ions from inorganic substances It is also known that, for example, it has various effects such as increased permeability to substances, improved dyeability when used as fiber processing water, or suppression of growth of various bacteria.

【0003】本発明の出願人も、特公平4−74074
号で食品加工用や繊維加工用として小分子集団又は単分
子化された活性化水の微生物の増殖抑制等の有用性や、
特願平4−282904号では活性化水を抽出溶媒とし
て果実その他の抽出物から比較的短時間で濃厚なエキス
が得られる等の提案をした。
The applicant of the present invention is also the Japanese Patent Publication No. 4-74074.
In the No. issue, usefulness such as suppressing the growth of microorganisms of small molecules or activated water of monomolecularized activated water for food processing and fiber processing,
Japanese Patent Application No. 4-282904 proposes that a concentrated extract can be obtained from fruits and other extracts in a relatively short time using activated water as an extraction solvent.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、活性化
水の利用分野は、前記食品用等のエキスの溶媒や繊維加
工用水に限られており、特に世界的にみても利用分野、
用途が広範囲にわたる樹脂材(天然樹脂及び合成樹脂の
双方を含む)と活性化水とを反応させて該樹脂材に物理
化学的作用を及ぼす試みはこれまで全くなされてはいな
い。
However, the field of use of the activated water is limited to the solvent of the extract for foods and the like and the water for fiber processing.
Until now, no attempt has been made to react a resin material (including both natural resin and synthetic resin) having a wide range of applications with activated water to exert a physicochemical action on the resin material.

【0005】又、活性化水を抽出溶媒として果実その他
の抽出物から得られたエキス成分を樹脂材と反応させる
試みについても同様である。
The same applies to an attempt to react an extract component obtained from fruits or other extracts with a resin material using activated water as an extraction solvent.

【0006】然して、本発明は、活性化水を樹脂材と反
応させることにより、樹脂材に物理化学的作用を及ぼす
ことを課題するものである。
However, the present invention has an object to exert a physicochemical action on a resin material by reacting activated water with the resin material.

【0007】[0007]

【課題を解決するための手段】本発明は、上記の課題を
解決するために、全く新しい樹脂材の活性処理方法を発
明したものである。
In order to solve the above problems, the present invention invents a completely new method for active treatment of a resin material.

【0008】即ち、本発明は、樹脂材のモノマー又はポ
リマーを、5〜30気圧に加圧された水を所定の無機物
質に接触通過させる工程と、無機物質を接触通過した加
圧水を5〜30気圧未満の雰囲気下にて貯留する工程と
から得られた活性化水に所定時間浸漬させて活性処理す
る方法にある。
That is, according to the present invention, a step of bringing water pressurized to 5 to 30 atmospheres into contact with a predetermined inorganic substance through a monomer or polymer of a resin material and 5 to 30 times of pressurized water having passed through contact with the inorganic substance. There is a method of activating by immersing the activated water obtained from the step of storing in an atmosphere of less than atmospheric pressure for a predetermined time.

【0009】更に、本発明は、樹脂材のモノマー又はポ
リマーを、5〜30気圧に加圧された水を所定の無機物
質に接触通過させる工程と、無機物質を接触通過した加
圧水を5〜30気圧未満の雰囲気下にて貯留する工程と
を交互に繰り返し循環させて得られた活性化水に所定時
間浸漬させて活性処理する方法にある。
Further, in the present invention, the step of bringing the monomer or polymer of the resin material into contact with water pressurized to 5 to 30 atm to a predetermined inorganic substance, and the pressurized water having passed through the inorganic substance to 5 to 30 This is a method of activating by immersing in activated water obtained by repeatedly circulating the step of storing under an atmosphere of less than atmospheric pressure for a predetermined time.

【0010】更に、本発明は、樹脂材のモノマー又はポ
リマーを、5〜30気圧に加圧された水を所定の無機物
質に接触通過させる工程と、無機物質を接触通過した加
圧水を5〜30気圧未満の雰囲気下にて貯留する工程と
から得られた活性化水に接触通過させて活性処理する方
法にある。
Further, in the present invention, a step of bringing water pressurized to 5 to 30 atmospheres into contact with a predetermined inorganic substance through a monomer or polymer of a resin material, and 5 to 30 times of pressurized water having passed through contact with the inorganic substance. There is a method of performing activation treatment by bringing the activated water obtained through the step of storing under an atmosphere of less than atmospheric pressure into contact with the activated water.

【0011】又、本発明は、樹脂材のモノマー又はポリ
マーを、5〜30気圧に加圧された水を所定の無機物質
に接触通過させる工程と、無機物質を接触通過した加圧
水を5〜30気圧未満の雰囲気下にて貯留する工程とを
交互に繰り返し循環させて得られた活性化水に接触通過
させて活性処理する方法にある。
In the present invention, the step of bringing the monomer or polymer of the resin material into contact with water pressurized to 5 to 30 atmospheres with a predetermined inorganic substance, and the pressurized water having passed through the inorganic substance to 5 to 30 It is a method of performing active treatment by contacting and passing activated water obtained by repeatedly circulating the step of storing under an atmosphere of less than atmospheric pressure.

【0012】更に、本発明は、前記ポリマーがペレット
状又はフレーク状で活性処理される方法にある。
Furthermore, the present invention resides in a method wherein the polymer is activated in the form of pellets or flakes.

【0013】更に、本発明は、樹脂材を高分子化させる
べく、該樹脂材と共に攪拌重合装置に投入される触媒
を、5〜30気圧に加圧された水を所定の無機物質に接
触通過させる工程と、無機物質を接触通過した加圧水を
5〜30気圧未満の雰囲気下にて貯留する工程とから得
られた活性化水に所定時間浸漬させることにより活性処
理し、その後活性処理された触媒を前記攪拌重合装置に
投入して樹脂材と共に攪拌することで高分子化樹脂材を
活性処理する方法にある。
Further, in the present invention, in order to polymerize the resin material, the catalyst charged into the stirring polymerization apparatus together with the resin material is contacted with water pressurized to 5 to 30 atm to a predetermined inorganic substance. And the activated water obtained by the step of storing the pressurized water that has passed through the contact with the inorganic substance under the atmosphere of 5 to less than 30 atm for a predetermined time, and then activated the catalyst. In the stirring polymerization apparatus and stirred with the resin material to activate the polymerized resin material.

【0014】更に、本発明は、樹脂材を高分子化させる
べく、該樹脂材と共に攪拌重合装置に投入される触媒
を、5〜30気圧に加圧された水を所定の無機物質に接
触通過させる工程と、無機物質を接触通過した加圧水を
5〜30気圧未満の雰囲気下にて貯留する工程とを交互
に繰り返し循環させて得られた活性化水に所定時間浸漬
させることにより活性処理し、その後活性処理された触
媒を前記攪拌重合装置に投入して樹脂材と共に攪拌する
ことで高分子化樹脂材を活性処理する方法にある。
Further, in the present invention, in order to polymerize the resin material, the catalyst charged into the stirring polymerization apparatus together with the resin material is brought into contact with water pressurized to 5 to 30 atm to a predetermined inorganic substance. And the step of storing the pressurized water that has passed through the contact with the inorganic substance under the atmosphere of 5 to less than 30 atmospheres are alternately and repeatedly circulated to obtain the activated water obtained by activating treatment for a predetermined time, Then, the activated polymer is charged into the stirring polymerization apparatus and stirred with the resin material to activate the polymerized resin material.

【0015】又、本発明は、樹脂材を高分子化させるべ
く、該樹脂材と共に攪拌重合装置に投入される触媒を、
5〜30気圧に加圧された水を所定の無機物質に接触通
過させる工程と、無機物質を接触通過した加圧水を5〜
30気圧未満の雰囲気下にて貯留する工程とから得られ
た活性化水に接触通過させることにより活性処理し、そ
の後活性処理された触媒を前記攪拌重合装置に投入して
樹脂材と共に攪拌することで高分子化樹脂材を活性処理
する方法にある。
The present invention further comprises a catalyst which is charged into a stirring polymerization apparatus together with the resin material in order to polymerize the resin material.
The step of bringing water pressurized to 5 to 30 atm into contact with a predetermined inorganic substance and the pressurized water having passed through the inorganic substance to 5
Activated by contacting and passing through activated water obtained from the step of storing under an atmosphere of less than 30 atm, and then adding the activated catalyst to the stirring polymerization apparatus and stirring with the resin material. There is a method of activating the polymerized resin material with.

【0016】更に、本発明は、樹脂材を高分子化させる
べく、該樹脂材と共に攪拌重合装置に投入される触媒
を、5〜30気圧に加圧された水を所定の無機物質に接
触通過させる工程と、無機物質を接触通過した加圧水を
5〜30気圧未満の雰囲気下にて貯留する工程とを交互
に繰り返し循環させて得られた活性化水に接触通過させ
ることにより活性処理し、その後活性処理された触媒を
前記攪拌重合装置に投入して樹脂材と共に攪拌すること
で高分子化樹脂材を活性処理する方法にある。
Further, in the present invention, in order to polymerize the resin material, the catalyst charged into the stirring polymerization apparatus together with the resin material is contacted with water pressurized to 5 to 30 atm to a predetermined inorganic substance. And a step of storing the pressurized water that has passed through the contact with the inorganic substance under an atmosphere of less than 5 to 30 atmospheres are alternately and repeatedly circulated, and the activated water obtained by contact is passed through the activated water. There is a method of activating the polymerized resin material by introducing the activated catalyst into the stirring polymerization apparatus and stirring it together with the resin material.

【0017】更に、本発明は、前記活性化水が、水蒸気
として用いられる方法にある。
Furthermore, the present invention resides in a method wherein the activated water is used as steam.

【0018】又、本発明は、前記工程にて得られた活性
化水を、該活性化水に樹脂材を浸漬させる前工程又は樹
脂材を接触通過させる前工程において再度2〜30気圧
に加圧し、その後この活性化水に樹脂材を浸漬させるか
又は接触通過させる方法にある。
Further, in the present invention, the activated water obtained in the above step is applied again to 2 to 30 atm in the step before the resin material is immersed in the activated water or the step before the resin material is brought into contact with the activated water. In this method, the resin material is dipped in the activated water or is then passed through contact with the activated water.

【0019】更に、本発明は、前記工程にて得られた活
性化水を、該活性化水に樹脂材を浸漬させる前工程又は
樹脂材を接触通過させる前工程の段階で抽出溶媒として
動植物等の被抽出物よりエキスを抽出し、その後抽出さ
れたエキスを前記活性化水に添加した後、該活性化水を
2〜30気圧に加圧し、その後この活性化水に樹脂材を
浸漬させるか又は接触通過させる方法にある。
Further, according to the present invention, the activated water obtained in the above-mentioned step is used as an extraction solvent at the stage of the pre-step of immersing the resin material in the activated water or the step of contact-passing the resin material with animals and plants. Is extracted from the substance to be extracted, and then the extracted extract is added to the activated water, the activated water is pressurized to 2 to 30 atm, and then the resin material is immersed in the activated water. Alternatively, there is a method of passing through contact.

【0020】[0020]

【実施例】以下、本発明の樹脂材の活性処理方法を実施
する場合に於ける樹脂材の活性処理装置の実施形態を詳
述する。
Embodiments of the resin material activation treatment apparatus for carrying out the resin material activation treatment method of the present invention will be described in detail below.

【0021】[0021]

【発明の実施の形態】BEST MODE FOR CARRYING OUT THE INVENTION

<第一実施形態>図1に示す様に、一実施形態としての
樹脂材の活性処理装置は、活性化水の製造に用いる透水
装置Aと、被抽出物を活性化水と共に収容する圧力タン
ク1を介在したバイパス配水路Bと、樹脂材(ここでは
AS樹脂を使用)のペレット2を水流に接触通過させる
透水装置3を介在したバイパス配水路Cを有してなる。
<First Embodiment> As shown in FIG. 1, a resin material activation treatment apparatus according to an embodiment includes a water permeation apparatus A used for production of activated water and a pressure tank for accommodating an extract together with the activated water. 1 and a bypass water distribution channel C having a water permeation device 3 for passing the pellets 2 of a resin material (AS resin here) in contact with the water flow.

【0022】尚、上記活性処理装置には、原料水を貯留
するタンク4から通水される送水路5に5〜30気圧の
加圧水を送出するポンプ6を取付けると共に、その下流
には加圧水を無機物質(例えば、自然残留磁気を有する
と共に、マグネシウム、鉄等の所謂ミネラルを含んだ玄
武岩、安山岩、磁鉄鉱等の強磁性鉱物が特に好ましい
が、ゲルマニウム等の半導体物質を添加した場合もより
好ましく、又金属酸化物若しくはこれらを焼結したセラ
ミックス又は鉄鋼、アルミニウム等の精錬した金属でも
好ましい。)に接触通過させる透水装置Aを操作弁7を
介して連結しており、更に透水装置Aの下流には、無機
物質に接触通過した水をタンク4に返送する返送路8を
連結してなると共に、二つのバイパス配水路B,Cは操
作弁7で夫々開閉自在である。
A pump 6 for delivering pressurized water of 5 to 30 atm is attached to the water supply passage 5 which is made to flow from the tank 4 for storing the raw material water, and the activated water is supplied to the downstream of the active treatment apparatus. Substances (e.g., ferritic minerals such as basalt, andesite, magnetite, etc., which have so-called minerals such as magnesium, iron, etc., in addition to having a natural remanence, are particularly preferable, but semiconductor substances such as germanium are more preferable, It is also preferable to use a metal oxide or ceramics obtained by sintering these or a refined metal such as steel and aluminum.) A water permeation device A for contacting and passing through is connected through an operation valve 7, and further downstream of the water permeation device A. , The return passage 8 for returning the water that has passed through the contact with the inorganic substance to the tank 4 is connected, and the two bypass water passages B and C are opened and closed by the operation valve 7, respectively. It is.

【0023】貯水タンク4は、原料水を貯留する上部開
口の蓋付のステンレス製で、これに温度指示調節計9aを
具備した電熱による加熱器9を付設すると共に、タンク
4の下部の送水路5に連通して5〜30気圧の加圧水を
送出する片吸入渦巻方式のポンプ6を設けてなる。
The water storage tank 4 is made of stainless steel with an upper opening lid for storing the raw material water. An electric heater 9 equipped with a temperature indicating controller 9a is attached to the water storage tank 4, and a water supply passage under the tank 4 is provided. A single-suction-vortex-type pump 6 that communicates with 5 and delivers pressurized water of 5 to 30 atmospheres is provided.

【0024】活性化水の製造に用いる透水装置Aは、5
本の金属製筒状の耐圧容器10を直列に連結し、夫々の内
部に上下一対のステンレス製多孔板11を配置し、且つそ
の間に粒径約5ミリの玄武岩を主要成分とする無機物質
12を充填してなる。
The water permeation apparatus A used for the production of activated water is 5
A series of metal cylindrical pressure-resistant containers 10 are connected in series, and a pair of upper and lower stainless steel perforated plates 11 are placed inside each of them, and an inorganic substance mainly composed of basalt with a grain size of about 5 mm is placed between them.
Filled with 12.

【0025】返送路8には、この透水装置Aを通過した
水を濾過する2基の高力フィルター13を直列に設けてな
る。
The return path 8 is provided with two high-strength filters 13 in series for filtering the water that has passed through the water permeation apparatus A.

【0026】尚、バイパス配水路B,Cは、送水路5か
ら別れて再び送水路5に連結してなるが、前記透水装置
Aの上流と返送路8との間には、夫々を直結するバイパ
ス配水路Dを設けている。
The bypass water distribution paths B and C are separated from the water supply path 5 and connected to the water supply path 5 again, but the upstream side of the water permeation apparatus A and the return path 8 are directly connected to each other. A bypass water distribution channel D is provided.

【0027】上記バイパス配水路Cに介設した透水装置
3は、耐圧容器の両端に網又は多孔性素材からなるフィ
ルタ14を有してなる他は、前記透水装置Aと同様の耐圧
構造を有するものである。
The water permeation device 3 provided in the bypass water passage C has the same pressure resistance structure as that of the water permeation device A except that it has filters 14 made of a net or porous material at both ends of the pressure container. It is a thing.

【0028】又、バイパス配水路Bについては、透水装
置3と同様の構造の耐圧容器を有するが、この場合は抽
出するエキスを所望の程度に濾過するためフィルタ15を
取付けてなり、しかもフィルタ5は適宜取り外すか、又
は網目の大きいものを選択使用してもよい。
Further, the bypass water distribution passage B has a pressure resistant container having the same structure as the water permeation device 3, but in this case, a filter 15 is attached in order to filter the extract to be extracted to a desired degree, and the filter 5 May be appropriately removed or a large mesh may be selected and used.

【0029】これらのバイパス配水路B,C,Dは、夫
々の両端に操作弁7を有しており、これを開閉操作して
夫々単独使用したり又は併用することが出来る。尚、図
中16は圧力計を示す。
Each of these bypass water distribution channels B, C, D has an operation valve 7 at each end, which can be used independently or in combination by opening and closing the operation valve 7. In the figure, 16 indicates a pressure gauge.

【0030】本発明の樹脂材の活性処理方法を実施する
場合に於ける一実施形態としての樹脂材の活性処理装置
は以上の構成からなるが、次に係る装置を用いて樹脂材
を活性処理する方法について説明する。
The apparatus for activating a resin material as one embodiment for carrying out the method for activating a resin material according to the present invention has the above-mentioned structure. The method for doing so will be described.

【0031】先ず、圧力タンク1及び透水装置3に水が
流入しないように、これらの上流側及び下流側の操作弁
を閉じた状態として所定量の原料水をタンク4からポン
プ6で25気圧に加圧して送水し、玄武岩粒を収容した
透水装置A、高力フィルタ13、返送路8から貯水タンク
4に至る経路を約24時間連続して循環させ原料水の全
てを活性化処理する。
First, in order to prevent water from flowing into the pressure tank 1 and the water permeation apparatus 3, the upstream and downstream operation valves are closed and a predetermined amount of raw water is pumped from the tank 4 to 25 atm. Water is pressurized and sent, and the path from the water permeable device A containing the basalt grains, the high-strength filter 13, and the return path 8 to the water storage tank 4 is continuously circulated for about 24 hours to activate all the raw water.

【0032】次に、上記工程によって得られた活性化水
のうち約半分の量をタンク4に貯留すると共に、残りを
バルブ17を開けて取り出し、別途設けたタンク(図示せ
ず)に貯留する。尚、タンク4内の活性化水は反応効率
を上げるため、加熱器9にて水温95℃に加熱し、しか
も圧力タンク1には、乾留により調整された竹の粉末か
らなる被抽出物を所定量収容し、その後前記閉じていた
操作弁13を開けてバイパス配水路Bを送水路5に開通さ
せる。
Next, about half of the activated water obtained by the above process is stored in the tank 4, and the rest is taken out by opening the valve 17 and stored in a separately provided tank (not shown). . In order to increase the reaction efficiency, the activated water in the tank 4 is heated to a water temperature of 95 ° C. by the heater 9, and the pressure tank 1 contains an extract made of bamboo powder adjusted by carbonization. A fixed amount is stored, and then the closed operation valve 13 is opened to open the bypass water distribution passage B to the water supply passage 5.

【0033】一方、透水装置Aの上・下流の操作弁7を
閉じると共に、透水装置Aの上流と返送路8を直結する
ようにバイパス配水路Dを操作弁7で開通させ、ポンプ
6で5気圧の加圧活性化水を送出し、ポンプ6、圧力タ
ンク1、バイパス配水路D、高力フィルター13、返送路
8、タンク4を循環する経路に12時間通水して抽出操
作を行い所定量の抽出竹エキスを得ることが出来る。
On the other hand, the bypass valve D is opened by the operation valve 7 so that the upstream and downstream operation valves 7 of the water permeation apparatus A are closed, and the upstream of the water permeation apparatus A and the return path 8 are directly connected, and the pump 6 is used to The pressurized activated water of atmospheric pressure is sent out, and water is passed through the pump 6, the pressure tank 1, the bypass water distribution channel D, the high-strength filter 13, the return channel 8, and the tank 4 for 12 hours to perform the extraction operation. It is possible to obtain a fixed amount of extracted bamboo extract.

【0034】次に、バイパス配水路Bを操作弁7で閉
じ、透水装置3にAS樹脂のペレット2を収容し、タン
ク4に別途貯留してなる活性化水を追加してバイパス配
水路Cの上・下流の操作弁7を開栓すると共に、ポンプ
6で5気圧の抽出竹エキス含有の加圧活性化水を送出
し、タンク4、ポンプ6、バイパス配水路C、バイパス
配水路D、高力フィルター13、返送路8を順に経由して
タンク4に至る経路に水流を12時間循環して抽出竹エ
キス含有の加圧活性化水によりAS樹脂のペレット2を
活性処理した。
Next, the bypass water distribution passage B is closed by the operation valve 7, the AS resin pellets 2 are stored in the water permeation device 3, and the activated water separately stored in the tank 4 is added to the bypass water distribution passage C. The upstream and downstream operation valves 7 are opened, and the pump 6 sends pressurized activated water containing the extracted bamboo extract at 5 atm to the tank 4, the pump 6, the bypass distribution channel C, the bypass distribution channel D, and the high level. The AS resin pellets 2 were activated by the pressurized activated water containing the extracted bamboo extract by circulating a water stream for 12 hours in the route from the force filter 13 and the return passage 8 to the tank 4.

【0035】よって、上記工程を介して活性処理された
AS樹脂のペレット2は、クラスターを形成する水分子
の固まりを、分子レベルにおいて超高速で振動可能な個
々の単分子又は極めて小数の集団へと分解された水分子
と、該水分子を介して高効率で抽出された抽出竹エキス
の成分である糖、酢酸、グルタミン酸との夫々を介して
変質することとなる。
Therefore, the AS resin pellets 2 which have been activated through the above-mentioned steps, the clusters of water molecules forming clusters are separated into individual single molecules or extremely small populations capable of vibrating at the molecular level at an extremely high speed. And the decomposed water molecules, and sugar, acetic acid, and glutamic acid, which are the components of the extracted bamboo extract with high efficiency through the water molecules, cause deterioration.

【0036】従って、上記の如く変質したAS樹脂のペ
レット2で所望形状の液体や固体の収容容器(図示せ
ず)を各種成形方法により成形し、その中に、例えば生
鮮食品を収容した場合には、活性処理を行わないAS樹
脂のペレット2で成形した収容容器に生鮮食品を収容し
た場合と比べ鮮度の低下が極めて緩やかな収容容器を提
供することが出来るだけでなく、収容物の味自体も円や
かになるといった種々の特異な物理化学的作用を有する
こととなった。
Therefore, when a container (not shown) of liquid or solid having a desired shape is molded by various molding methods with the pellet 2 of the AS resin which has been modified as described above, for example, when fresh food is contained therein. Is not only capable of providing a container in which the freshness is much less deteriorated than the case where fresh food is contained in a container formed of AS resin pellets 2 which is not subjected to activation treatment, but also the taste itself of the contained product. It also has various peculiar physicochemical effects such as becoming round.

【0037】<第二実施形態>更に、本発明に於ける樹
脂材の活性処理方法は、必ずしも第一実施形態に限ら
ず、例えば、図2に示す様に、エチレン樹脂材を高分子
化(ポリマー化)させるべく、溶媒が含有された所定量
のエチレン18と共に攪拌重合装置19に投入される酸化ク
ロムや酸化モリブデン等の触媒20を、前記第一実施形態
と同様の工程を介して活性処理し、その後活性処理され
た触媒20を前記攪拌重合装置19に投入してエチレン18と
共に攪拌した後、未反応のエチレン21を蒸発させ、その
後残った溶媒22を冷却すると、ポリエチレン23が固体に
なって分かれ、このポリエチレン23を乾燥工程23a を介
して活性処理されたポリエチレン樹脂のペレット2を製
造し、各種成形方法によって前記同様の容器を成形して
もよく、この場合であっても前記同様の種々の特異な物
理化学的作用を有することとなる。
<Second Embodiment> Furthermore, the method of active treatment of a resin material according to the present invention is not necessarily limited to that of the first embodiment. For example, as shown in FIG. The catalyst 20 such as chromium oxide or molybdenum oxide, which is charged into the stirring polymerization apparatus 19 together with a predetermined amount of ethylene 18 containing a solvent, is activated through the same steps as in the first embodiment. After that, the activated catalyst 20 is charged into the stirring polymerization apparatus 19 and stirred with ethylene 18, the unreacted ethylene 21 is evaporated, and then the remaining solvent 22 is cooled, so that the polyethylene 23 becomes solid. In this case, the polyethylene 23 pellets obtained by subjecting the polyethylene 23 to the activation treatment through the drying step 23a may be manufactured, and the same container as described above may be molded by various molding methods. Serial will have a variety of unique physicochemical action similar.

【0038】<第三実施形態>更に、本発明に於ける樹
脂材の活性処理方法は、必ずしもポリマーがペレット状
である必要はなく、例えば、ポリエチレンテレフタレー
トのフレーク状(薄片)であってもよく、この場合に
は、ポリエチレンテレフタレートを材料とする容器の成
形又は再生時に於けるフレークを、フレーク洗浄工程又
は比重分離工程等に使用するアルカリ性洗剤溶液又は水
を5〜30気圧に加圧して所定の無機物質に接触通過さ
せる工程と、無機物質を接触通過した溶液又は水を5〜
30気圧未満の雰囲気下にて貯留する工程とから得られ
た活性化溶液又は水に所定時間浸漬させて活性処理する
ことも出来る。
<Third Embodiment> Furthermore, in the method for active treatment of a resin material according to the present invention, the polymer does not necessarily have to be in the form of pellets, and may be, for example, flakes (thin flakes) of polyethylene terephthalate. In this case, the flakes at the time of molding or regeneration of the container made of polyethylene terephthalate are pressurized to a predetermined pressure of 5 to 30 atmospheres with alkaline detergent solution or water used in the flake washing step or the specific gravity separation step. The step of bringing the inorganic substance into contact with and passing through the solution or the water which has passed the inorganic substance into contact with
The activation treatment can also be performed by immersing it in the activation solution or water obtained from the step of storing under an atmosphere of less than 30 atm for a predetermined time.

【0039】更に、本発明に於ける樹脂材の活性処理方
法は、樹脂材のモノマー又はポリマーを、5〜30気圧
に加圧された水を所定の無機物質に接触通過させる工程
と、無機物質を接触通過した加圧水を5〜30気圧未満
の雰囲気下にて貯留する工程とを交互に繰り返し循環さ
せて得られた活性化水に所定時間浸漬させて活性処理し
てもよく、この場合には、被抽出物から抽出されたエキ
スを全く用いる必要もなく、水だけで活性処理された樹
脂材を介して成形された容器に生鮮食品を収容した際、
活性処理していない樹脂材から成形された容器に生鮮食
品を収容した場合と比べ鮮度の低下が極めて緩やかな収
容容器を提供することが出来るだけでなく、収容物の味
自体も円やかになるといった種々の特異な物理化学的作
用を有する。
Further, the method for active treatment of a resin material according to the present invention comprises a step of allowing water pressurized under a pressure of 5 to 30 atm to pass through a predetermined inorganic material through a monomer or polymer of the resin material, and an inorganic material. May be immersed in activated water obtained by repeatedly circulating the pressurized water that has passed through contact with the water under an atmosphere of 5 to less than 30 atm for a predetermined time, and in this case, When storing fresh food in a container molded through a resin material that has been activated only with water, it is not necessary to use an extract extracted from the substance to be extracted,
Not only can it provide a container whose freshness is much less declining compared to the case where fresh food is contained in a container molded from a resin material that has not been activated, but the taste of the container itself is also gentle. It has various unique physicochemical effects such as

【0040】更に、本発明に於ける樹脂材の活性処理方
法は、樹脂材のモノマー又はポリマーを、5〜30気圧
に加圧された水を所定の無機物質に接触通過させる工程
と、無機物質を接触通過した加圧水を5〜30気圧未満
の雰囲気下にて貯留する工程とから得られた活性化水に
接触通過させたり、又樹脂材のモノマー又はポリマー
を、5〜30気圧に加圧された水を所定の無機物質に接
触通過させる工程と、無機物質を接触通過した加圧水を
5〜30気圧未満の雰囲気下にて貯留する工程とを交互
に繰り返し循環させて得られた活性化水に接触通過させ
て活性処理してもよく、この場合における樹脂材の活性
化水への接触通過は、単に活性化水に瞬間的に浸す工程
のみならず、例えば、水蒸気となった活性化水に樹脂材
を通過させる工程であってもよいのは言うまでもない。
Further, the method of active treatment of a resin material according to the present invention comprises a step of allowing water pressurized under a pressure of 5 to 30 atm to pass through a predetermined inorganic substance through a monomer or polymer of the resin material, and an inorganic substance. And the activated water obtained from the step of storing the pressurized water that has passed through the contact point under an atmosphere of less than 5 to 30 atm, or the monomer or polymer of the resin material is pressurized to 5 to 30 atm. Activated water obtained by alternately repeating a step of contacting and passing water with a predetermined inorganic substance and a step of storing pressurized water contacting and passing the inorganic substance under an atmosphere of less than 5 to 30 atm. It may be activated by contact passing, and in this case, contact passing of the resin material to the activated water is not limited to the step of instantaneously immersing the resin material in the activated water. In the process of passing the resin material It may be me of course.

【0041】更に、本発明に於ける樹脂材の活性処理方
法は、樹脂材を高分子化させるべく、該樹脂材と共に攪
拌重合装置に投入される触媒を、5〜30気圧に加圧さ
れた水を所定の無機物質に接触通過させる工程と、無機
物質を接触通過した加圧水を5〜30気圧未満の雰囲気
下にて貯留する工程とから得られた活性化水に所定時間
浸漬させることにより活性処理し、その後活性処理され
た触媒を前記攪拌重合装置に投入して樹脂材と共に攪拌
するか、又は樹脂材と共に攪拌重合装置に投入される触
媒を、5〜30気圧に加圧された水を所定の無機物質に
接触通過させる工程と、無機物質を接触通過した加圧水
を5〜30気圧未満の雰囲気下にて貯留する工程とを交
互に繰り返し循環させて得られた活性化水に所定時間浸
漬させることにより活性処理し、その後活性処理された
触媒を前記攪拌重合装置に投入して樹脂材と共に攪拌す
ることで高分子化樹脂材を活性処理してもよく、この場
合にも、被抽出物から抽出されたエキスを全く用いる必
要もなく、水だけで活性処理された樹脂材を介して成形
された容器に生鮮食品を収容した際、活性処理していな
い樹脂材から成形された容器に生鮮食品を収容した場合
と比べ鮮度の低下が極めて緩やかな収容容器を提供する
ことが出来るだけでなく、収容物の味自体も円やかにな
るといった種々の特異な物理化学的作用を有する。
Further, in the method for active treatment of a resin material according to the present invention, the catalyst charged into the stirring polymerization apparatus together with the resin material is pressurized to 5 to 30 atm in order to polymerize the resin material. Activated by immersing in activated water obtained for a predetermined time from the step of bringing water into contact with a predetermined inorganic substance and the step of storing the pressurized water having passed through the inorganic substance in an atmosphere of less than 5 to 30 atm. The catalyst that has been treated and then activated is charged into the stirring polymerization apparatus and stirred with the resin material, or the catalyst that is charged with the resin material into the stirring polymerization apparatus is treated with water pressurized to 5 to 30 atmospheres. Immersion in activated water for a predetermined period of time by alternately circulating a step of contacting and passing a predetermined inorganic substance and a step of storing pressurized water contacting and passing the inorganic substance under an atmosphere of less than 5 to 30 atm. By letting The polymerized resin material may be subjected to activation treatment, and then the activation-treated catalyst may be put into the stirring polymerization apparatus and stirred with the resin material to activate the polymerized resin material. When you store fresh food in a container molded through a resin material that has been activated only with water, you do not need to use any extract, and you can store the fresh food in a container molded from a resin material that has not been activated. In addition to providing a container in which the degree of freshness is extremely gentle compared to the case described above, it has various unique physicochemical actions such that the taste of the container itself becomes round.

【0042】又、本発明に於ける樹脂材の活性処理方法
は、活性化水に樹脂材を浸漬させる前工程又は樹脂材を
接触通過させる前工程において再度2〜30気圧に加圧
し、その後この活性化水に樹脂材を浸漬させるか又は接
触通過させても前記同様の種々の特異な物理化学的作用
を有するが、上記第一実施形態で述べた様に、活性化水
に樹脂材を浸漬させる前工程又は樹脂材を接触通過させ
る前工程の段階で抽出溶媒として動植物等の被抽出物よ
りエキスを抽出し、その後抽出されたエキスを前記活性
化水に添加した後、該活性化水を2〜30気圧に加圧
し、その後この活性化水に樹脂材を浸漬させるか又は接
触通過させてもよく、この場合には、分子レベルにおい
て超高速で振動可能な個々の単分子又は極めて小数の集
団へと分解された水分子の作用のみならず、該水分子を
介して高効率で抽出された被抽出物のエキスの成分の夫
々を介して樹脂材の性質を変質させることが出来る。
Further, in the method for active treatment of a resin material according to the present invention, pressure is again applied to 2 to 30 atm in the step before immersing the resin material in the activated water or the step before contacting the resin material, and thereafter, Although the resin material has various unique physicochemical effects similar to the above even when the resin material is immersed in the activated water or passed through contact therewith, as described in the first embodiment, the resin material is immersed in the activated water. Extract the extract from the extract such as animals and plants as an extraction solvent in the step of the previous step or contact step with the resin material, after adding the extracted extract to the activated water, the activated water The pressure may be increased to 2 to 30 atmospheres, and then the resin material may be dipped in or contacted with the activated water. Water broken down into groups Not only the action of the child, can be altered the nature of the resin material through to the respective components of the extract of the extract extracted with high efficiency through the water molecules.

【0043】尚、上記各実施形態に於いて、活性処理さ
れる樹脂材は熱可塑性や熱硬化性の一切を問わず、又具
体的な樹脂材の種類もポリエチレン、ポリスチレン、ポ
リプロピレン、塩化ビニル樹脂、塩化ビニルコンパウン
ド、メタクリル樹脂、不飽和ポリエステル樹脂、フェノ
ール樹脂、ユリア・メラミン樹脂、再生品プラスチック
樹脂等の何れであってもよく、更に天然樹脂や合成樹脂
の限定もなく、又活性処理された樹脂材によって成形さ
れた容器の種類もボトル型、トレー型、蓋付容器等の何
れであってもよく、更に樹脂材が発泡材として容器を形
成すべく用いられるものであってもよいのは言うまでも
ない。
In each of the above-mentioned embodiments, the resin material to be activated does not matter whether it is thermoplastic or thermosetting, and the specific type of resin material is polyethylene, polystyrene, polypropylene or vinyl chloride resin. , Vinyl chloride compound, methacrylic resin, unsaturated polyester resin, phenol resin, urea / melamine resin, recycled plastic resin, etc., and there is no limitation of natural resin or synthetic resin, and it is activated. The type of the container formed of the resin material may be any of a bottle type, a tray type, a container with a lid, etc., and the resin material may be used as a foam material to form the container. Needless to say.

【0044】[0044]

【発明の効果】叙上のように、本発明は、樹脂材のモノ
マー又はポリマーを、5〜30気圧に加圧された水を所
定の無機物質に接触通過させる工程と、無機物質を接触
通過した加圧水を5〜30気圧未満の雰囲気下にて貯留
する工程とから得られた活性化水に所定時間浸漬させて
活性処理した後、活性処理された樹脂材によって所望形
状の液体や固体の収容容器等を各種成形方法により成形
し、その中に、例えば生鮮食品を収容した場合に、活性
処理を行わない樹脂材で成形した収容容器に生鮮食品を
収容した場合と比べ鮮度の低下が極めて緩やかで、しか
も収容物の味自体も円やかになるといった種々の特異な
物理化学的作用を有する極めて優れた樹脂材の活性処理
方法を提供することが出来るという格別な効果を有する
に至った。
As described above, according to the present invention, the monomer or polymer of the resin material is passed through a step of bringing water pressurized to 5 to 30 atm into contact with a predetermined inorganic substance, and the inorganic substance is passed through by contact. The pressurized water is stored in an atmosphere of 5 to less than 30 atm for immersion for a predetermined time in the activated water, and after the activation treatment, the activated resin material stores a liquid or solid in a desired shape. A container is molded by various molding methods, and when fresh food is stored in it, for example, the deterioration of freshness is extremely gentle compared to the case where fresh food is stored in a storage container that is molded from a resin material that does not undergo activation treatment. In addition, it has a special effect that it is possible to provide an extremely excellent method for active treatment of a resin material having various peculiar physicochemical actions such that the taste itself of the contained object becomes round.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明における樹脂材の活性処理方法に用いる
活性処理装置を説明する模式図。
FIG. 1 is a schematic diagram illustrating an activation processing apparatus used in an activation processing method for a resin material according to the present invention.

【図2】樹脂材の高分子化装置を説明する模式図。FIG. 2 is a schematic diagram illustrating a polymerizing device for a resin material.

【符号の説明】[Explanation of symbols]

A…透水装置 B…バイパス配水路 C…バイパス配水路 D…バイパス配水路 1…圧力タンク 2…樹脂材のペレット 4…タンク 5…送水路 6…ポンプ 7…操作弁 8…返送路 A ... Water permeation device B ... Bypass water channel C ... Bypass water channel D ... Bypass water channel 1 ... Pressure tank 2 ... Resin material pellet 4 ... Tank 5 ... Water channel 6 ... Pump 7 ... Operation valve 8 ... Return channel

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C08G 85/00 NUZ C08G 85/00 NUZ ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical indication C08G 85/00 NUZ C08G 85/00 NUZ

Claims (12)

【特許請求の範囲】[Claims] 【請求項1】 樹脂材のモノマー又はポリマーを、5〜
30気圧に加圧された水を所定の無機物質に接触通過さ
せる工程と、無機物質を接触通過した加圧水を5〜30
気圧未満の雰囲気下にて貯留する工程とから得られた活
性化水に所定時間浸漬させることにより活性処理するこ
とを特徴とする樹脂材の活性処理方法。
1. A resin material containing a monomer or polymer
The step of bringing water pressurized to 30 atm into contact with a predetermined inorganic substance and the pressurized water having passed through the inorganic substance by 5 to 30
A method for activating a resin material, which comprises immersing in activated water obtained from the step of storing under an atmosphere of less than atmospheric pressure for a predetermined time to carry out an activation treatment.
【請求項2】 樹脂材のモノマー又はポリマーを、5〜
30気圧に加圧された水を所定の無機物質に接触通過さ
せる工程と、無機物質を接触通過した加圧水を5〜30
気圧未満の雰囲気下にて貯留する工程とを交互に繰り返
し循環させて得られた活性化水に所定時間浸漬させるこ
とにより活性処理することを特徴とする樹脂材の活性処
理方法。
2. The monomer or polymer of the resin material is 5 to
The step of bringing water pressurized to 30 atm into contact with a predetermined inorganic substance and the pressurized water having passed through the inorganic substance by 5 to 30
A method for active treatment of a resin material, which comprises performing an active treatment by immersing in activated water obtained by repeatedly circulating the step of storing under an atmosphere of less than atmospheric pressure for a predetermined time.
【請求項3】 樹脂材のモノマー又はポリマーを、5〜
30気圧に加圧された水を所定の無機物質に接触通過さ
せる工程と、無機物質を接触通過した加圧水を5〜30
気圧未満の雰囲気下にて貯留する工程とから得られた活
性化水に接触通過させることにより活性処理することを
特徴とする樹脂材の活性処理方法。
3. The monomer or polymer of the resin material is 5 to
The step of bringing water pressurized to 30 atm into contact with a predetermined inorganic substance and the pressurized water having passed through the inorganic substance by 5 to 30
An activation treatment method for a resin material, characterized in that activation treatment is carried out by bringing the activated water obtained through the step of storing under an atmosphere of less than atmospheric pressure into contact with the activated water.
【請求項4】 樹脂材のモノマー又はポリマーを、5〜
30気圧に加圧された水を所定の無機物質に接触通過さ
せる工程と、無機物質を接触通過した加圧水を5〜30
気圧未満の雰囲気下にて貯留する工程とを交互に繰り返
し循環させて得られた活性化水に接触通過させることに
より活性処理することを特徴とする樹脂材の活性処理方
法。
4. The resin material monomer or polymer is
The step of bringing water pressurized to 30 atm into contact with a predetermined inorganic substance and the pressurized water having passed through the inorganic substance by 5 to 30
A method for active treatment of a resin material, characterized in that the active treatment is carried out by bringing the activated water obtained by contacting and passing the activated water obtained by repeatedly circulating the step of storing under an atmosphere of less than atmospheric pressure.
【請求項5】 前記ポリマーがペレット状又はフレーク
状である請求項1乃至4の何れかに記載の樹脂材の活性
処理方法。
5. The method for active treatment of a resin material according to claim 1, wherein the polymer is in the form of pellets or flakes.
【請求項6】 樹脂材を高分子化させるべく、該樹脂材
と共に攪拌重合装置に投入される触媒を、5〜30気圧
に加圧された水を所定の無機物質に接触通過させる工程
と、無機物質を接触通過した加圧水を5〜30気圧未満
の雰囲気下にて貯留する工程とから得られた活性化水に
所定時間浸漬させることにより活性処理し、その後活性
処理された触媒を前記攪拌重合装置に投入して樹脂材と
共に攪拌することで高分子化樹脂材を活性処理すること
を特徴とする樹脂材の活性処理方法。
6. A step of bringing water pressurized to 5 to 30 atm into contact with a predetermined inorganic substance through a catalyst charged into a stirring polymerization apparatus together with the resin material in order to polymerize the resin material, The pressurized water that has passed through the contact with the inorganic substance is subjected to an activation treatment by immersing it in the activation water obtained from the step of storing in an atmosphere of 5 to less than 30 atm for a predetermined time, and then the activated catalyst is subjected to the stirring polymerization. A method for active treatment of a resin material, characterized in that the polymerized resin material is activated by being placed in an apparatus and stirred with the resin material.
【請求項7】 樹脂材を高分子化させるべく、該樹脂材
と共に攪拌重合装置に投入される触媒を、5〜30気圧
に加圧された水を所定の無機物質に接触通過させる工程
と、無機物質を接触通過した加圧水を5〜30気圧未満
の雰囲気下にて貯留する工程とを交互に繰り返し循環さ
せて得られた活性化水に所定時間浸漬させることにより
活性処理し、その後活性処理された触媒を前記攪拌重合
装置に投入して樹脂材と共に攪拌することで高分子化樹
脂材を活性処理することを特徴とする樹脂材の活性処理
方法。
7. A step of bringing water pressurized to 5 to 30 atm into contact with a predetermined inorganic substance through a catalyst charged into a stirring polymerization apparatus together with the resin material in order to polymerize the resin material, An activated treatment is carried out by immersing the activated water obtained by repeatedly circulating the pressurized water which has passed through the contact with the inorganic substance in an atmosphere of less than 5 to 30 atm for a predetermined time, and then activated. A method for active treatment of a resin material, characterized in that the polymerized resin material is activated by introducing the catalyst into the stirring polymerization apparatus and stirring it together with the resin material.
【請求項8】 樹脂材を高分子化させるべく、該樹脂材
と共に攪拌重合装置に投入される触媒を、5〜30気圧
に加圧された水を所定の無機物質に接触通過させる工程
と、無機物質を接触通過した加圧水を5〜30気圧未満
の雰囲気下にて貯留する工程とから得られた活性化水に
接触通過させることにより活性処理し、その後活性処理
された触媒を前記攪拌重合装置に投入して樹脂材と共に
攪拌することで高分子化樹脂材を活性処理することを特
徴とする樹脂材の活性処理方法。
8. A step of bringing water, which has been pressurized to 5 to 30 atm, into contact with a predetermined inorganic substance through a catalyst which is put into a stirring polymerization apparatus together with the resin material in order to polymerize the resin material, Activated water obtained by contacting the activated water obtained from the step of storing pressurized water, which has passed through contact with the inorganic substance, in an atmosphere of less than 5 to 30 atm, and then the activated catalyst is subjected to the stirring polymerization apparatus. A method for active treatment of a resin material, which comprises subjecting the polymerized resin material to an active treatment by charging the polymerized resin material and stirring it together with the resin material.
【請求項9】 樹脂材を高分子化させるべく、該樹脂材
と共に攪拌重合装置に投入される触媒を、5〜30気圧
に加圧された水を所定の無機物質に接触通過させる工程
と、無機物質を接触通過した加圧水を5〜30気圧未満
の雰囲気下にて貯留する工程とを交互に繰り返し循環さ
せて得られた活性化水に接触通過させることにより活性
処理し、その後活性処理された触媒を前記攪拌重合装置
に投入して樹脂材と共に攪拌することで高分子化樹脂材
を活性処理することを特徴とする樹脂材の活性処理方
法。
9. A step of bringing water pressurized to 5 to 30 atm into contact with a predetermined inorganic substance through a catalyst charged into a stirring polymerization apparatus together with the resin material in order to polymerize the resin material, Activated water was obtained by contacting and passing activated water obtained by repeatedly circulating the pressurized water that passed through the contact with the inorganic substance under an atmosphere of less than 5 to 30 atmospheres, and then activated. A method for active treatment of a resin material, characterized in that a polymerized resin material is activated by introducing a catalyst into the stirring polymerization apparatus and stirring it together with the resin material.
【請求項10】 前記活性化水が、水蒸気である請求項
3、4、8又は9の何れかに記載の樹脂材の活性処理方
法。
10. The method of active treatment of a resin material according to claim 3, wherein the activated water is steam.
【請求項11】 前記工程にて得られた活性化水を、該
活性化水に樹脂材を浸漬させる前工程又は樹脂材を接触
通過させる前工程において再度2〜30気圧に加圧し、
その後この活性化水に樹脂材を浸漬させるか又は接触通
過させることを特徴とする請求項1乃至10の何れかに
記載の樹脂材の活性処理方法。
11. The activated water obtained in the above step is pressurized again to 2 to 30 atm in the step of immersing the resin material in the activated water or the step of contacting the resin material with the activated water,
The resin material activation treatment method according to any one of claims 1 to 10, wherein the resin material is then immersed in or contacted with the activated water.
【請求項12】 前記工程にて得られた活性化水を、該
活性化水に樹脂材を浸漬させる前工程又は樹脂材を接触
通過させる前工程の段階で抽出溶媒として動植物等の被
抽出物よりエキスを抽出し、その後抽出されたエキスを
前記活性化水に添加した後、該活性化水を2〜30気圧
に加圧し、その後この活性化水に樹脂材を浸漬させるか
又は接触通過させることを特徴とする請求項1乃至10
の何れかに記載の樹脂材の活性処理方法。
12. The activated water obtained in the above step is used as an extraction solvent in the step of pre-immersing the resin material in the activated water or in the step of passing the resin material in contact with the activated water to be extracted such as animals and plants. The extract is further extracted, and then the extracted extract is added to the activated water, the activated water is pressurized to 2 to 30 atm, and then the resin material is immersed in or contacted with the activated water. 11. The method according to claim 1, wherein
The method for active treatment of a resin material according to any one of 1.
JP21463295A 1995-08-23 1995-08-23 Resin material activation treatment method Expired - Lifetime JP3634021B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21463295A JP3634021B2 (en) 1995-08-23 1995-08-23 Resin material activation treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21463295A JP3634021B2 (en) 1995-08-23 1995-08-23 Resin material activation treatment method

Publications (2)

Publication Number Publication Date
JPH0959402A true JPH0959402A (en) 1997-03-04
JP3634021B2 JP3634021B2 (en) 2005-03-30

Family

ID=16658960

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21463295A Expired - Lifetime JP3634021B2 (en) 1995-08-23 1995-08-23 Resin material activation treatment method

Country Status (1)

Country Link
JP (1) JP3634021B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013113716A (en) * 2011-11-29 2013-06-10 Shinki Sangyo Kk Method for treating radioactive nuclide contaminant
WO2019088046A1 (en) * 2017-10-30 2019-05-09 株式会社Fig Activated treated water, method for manufacturing activated treated water, method for manufacturing activated treated medium, device for manufacturing activated treated water, method for preserving food product, and activated treated medium

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016014680A (en) * 2015-09-08 2016-01-28 新紀産業株式会社 Treatment method of radioactive nuclide contaminant

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013113716A (en) * 2011-11-29 2013-06-10 Shinki Sangyo Kk Method for treating radioactive nuclide contaminant
WO2019088046A1 (en) * 2017-10-30 2019-05-09 株式会社Fig Activated treated water, method for manufacturing activated treated water, method for manufacturing activated treated medium, device for manufacturing activated treated water, method for preserving food product, and activated treated medium
JPWO2019088046A1 (en) * 2017-10-30 2019-12-26 株式会社Fig Active treated water, method for producing activated treated water, method for producing activated treated medium, apparatus for producing activated treated water, food preservation method, and activated treated medium
CN111655632A (en) * 2017-10-30 2020-09-11 株式会社Fig Activated water, method for producing activated medium, device for producing activated water, method for preserving food, and activated medium
CN111655632B (en) * 2017-10-30 2022-08-30 株式会社Fig Activated water, method for producing activated medium, device for producing activated water, method for preserving food, and activated medium
CN115304146A (en) * 2017-10-30 2022-11-08 株式会社Fig Activated water, method for producing activated medium, method for preserving food, and activated medium
TWI794319B (en) * 2017-10-30 2023-03-01 日商Fig股份有限公司 Active treated water, method for producing active treated water, method for producing active treated water, device for producing active treated water, food preservation method, and active treated medium

Also Published As

Publication number Publication date
JP3634021B2 (en) 2005-03-30

Similar Documents

Publication Publication Date Title
Liu Food and agricultural wastewater utilization and treatment
CA2781708C (en) Process of producing pcr pellets
WO1995029130A1 (en) Oxygen enriched liquids, method and apparatus for making, and applications thereof
JPH0959402A (en) Method for activating resin material
CN112142880B (en) Continuous purification method of polymer polyol
Anirudhan et al. Removal of copper (II) and zinc (II) from aqueous solutions using a lignocellulosic-based polymeric adsorbent containing amidoxime chelating functional groups
Tango et al. A continuous lactic acid production system using an immobilized packed bed of Lactobacillus helveticus
CN105268417B (en) A kind of preparation method of the composite membrane with adsorbing separation heavy metal ion function
Guo et al. Influence of the coagulation‐bath temperature on the phase‐separation process of poly (vinylidene fluoride)‐graft‐poly (N‐isopropylacrylamide) solutions and membrane structures
US3031433A (en) Solid phase polymerization of polyamides
CN113213617B (en) Preparation method of modified magnetic suspension biological carrier for nitrosation process
CN1241844C (en) Apparatus for processing fluids
US6733671B1 (en) Apparatus for treating fluids
McGreavy Polymer reactor engineering
CN103263898A (en) Material of non-woven fabric surface heavy nitrogen coupling gelatin adsorbing material and preparation method thereof
CN107646021A (en) The method for purifying the waste water from ABS emulsion polymerisation process
CN108570147A (en) A kind of 6 coloured slice continuous production device of polyamide fibre and production method
CA1055169A (en) Support medium for biological treatment
Machi Industrial application of radiation processing in Japan
CN217169222U (en) Modified apparatus for producing of abandonment plastics
CN209612935U (en) Processing system for polymer purification
JPH07258331A (en) Removal of volatile substance contained in polymer
DE3841716C2 (en)
CN108568920A (en) A kind of 6 black of polyamide fibre slice continuous production device and production method
CN102796775A (en) Method for extracting lactic acid fermentation product of kitchen waste

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040414

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A132

Effective date: 20040416

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20040608

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040702

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20040830

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20040924

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20040830

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20041217

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20041124

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20041222

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080107

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090107

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100107

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110107

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120107

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120107

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130107

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130107

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140107

Year of fee payment: 9

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term