JPH07328418A - Catalytic reaction method using activated mineral water and device therefor - Google Patents

Catalytic reaction method using activated mineral water and device therefor

Info

Publication number
JPH07328418A
JPH07328418A JP12254394A JP12254394A JPH07328418A JP H07328418 A JPH07328418 A JP H07328418A JP 12254394 A JP12254394 A JP 12254394A JP 12254394 A JP12254394 A JP 12254394A JP H07328418 A JPH07328418 A JP H07328418A
Authority
JP
Japan
Prior art keywords
water
activated mineral
mineral water
pressurized
treated
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
JP12254394A
Other languages
Japanese (ja)
Other versions
JP3561532B2 (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 JP12254394A priority Critical patent/JP3561532B2/en
Publication of JPH07328418A publication Critical patent/JPH07328418A/en
Application granted granted Critical
Publication of JP3561532B2 publication Critical patent/JP3561532B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Abstract

PURPOSE:To subject an activated mineral water to an efficient catalytic reaction without changing the shape of a material to be treated by utilizing an activated mineral water produced by repeatedly passing water through a specified inorg. material in contact with each other and passing the activated mineral water pressurized to a specified pressure through the solid material to be treated. CONSTITUTION:A catalytic reaction is conducted by utilizing an activated mineral water provided with high permeability, antibacterial activity, etc., as a processing water. Namely, a water pressurized to 5-30atm is passed through a specified inorg. material in contact with each other, and then the pressurized water is stored in an atmosphere kept at a pressure lower than the specified atm. The pressurized water is circulated to alternately repeat the processes, and an activated mineral water is produced. The activated mineral water is pressurized to 2-30-atm and brought into efficient contact with a solid material to be treated. Meanwhile, the catalytic reactor is constituted of a water permeating device A for producing the activated mineral water, a drainage bypass B furnished with an intervening pressure tank 1 storing a material to be extracted together with the activated mineral water and a drainage bypass C having an intervening water permeating device 3 to bring the solid material 2 to be treated into contact with a water current.

Description

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

【0001】[0001]

【産業上の利用分野】この発明は高浸透性や抗菌性等が
認められる活性化鉱水を処理用水として利用する活性化
鉱水を用いた接触反応方法および装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a catalytic reaction method and apparatus using activated mineral water, which uses activated mineral water having high permeability and antibacterial property as treatment water.

【0002】[0002]

【従来の技術】一般に、水は、通常、5分子以上が水素
結合によって集団(クラスター)を形成していることが
知られているが、このようなクラスターが崩壊するか、
または昇降圧、無機物質からの2価、3価イオンなどイ
オンを中心に水が小分子集団となった水には、例えば浸
透性が増したり、繊維加工水として用いた場合に染着性
が改善されたり、また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, in water, generally five or more molecules form a group (cluster) by hydrogen bonds.
Alternatively, water having a small molecule group mainly composed of ions such as buck-boost, divalent and trivalent ions from an inorganic substance has an increased permeability, or has a dyeing property when used as fiber processing water. It is also known to have various effects such as improvement or suppression of growth of various bacteria.

【0003】この発明の出願人も、食品加工用水や繊維
加工用水として活性化鉱水の製造方法を開示し(特公平
4−74074号)、その中で加圧水を所定の無機物質
に接触通過させる工程と、この工程を経た加圧水を常圧
下に曝す工程とから製造された活性化鉱水には、微生物
の増殖抑制などの有用性のあることを明らかにした。
The applicant of the present invention also discloses a method for producing activated mineral water as water for food processing and water for fiber processing (Japanese Patent Publication No. 4-74074), in which pressurized water is brought into contact with a predetermined inorganic substance. It was clarified that the activated mineral water produced by the step of exposing the pressurized water to the atmospheric pressure after this step has usefulness such as inhibiting the growth of microorganisms.

【0004】また、この発明の出願人は、特願平4−2
82904号で活性化鉱水を加熱加圧して、これを抽出
溶媒として果実その他の抽出物を浸漬すれば、抽出効率
が良く比較的短時間で濃厚なエキスが得られることを提
案した。
Further, the applicant of the present invention is the Japanese Patent Application No. 4-2.
It was proposed in No. 82904 that activated mineral water was heated and pressurized, and when this was used as an extraction solvent to immerse fruits and other extracts, a good extract was obtained and a concentrated extract could be obtained in a relatively short time.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、活性化
鉱水の利用分野は、前記したような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、このような活性化
鉱水を、その他の固体状の物質に接触させて、これらに
何らかの物理化学的作用を及ぼす可能性を発見するため
の方法はこれまでに開発されていない。
However, the field of use of activated mineral water is limited to the solvent for the extract for foods and the water for fiber processing as described above. No method has so far been developed for contacting solid substances and discovering the possibility of exerting some physicochemical effect on them.

【0006】また、前記したエキスの製造方法によって
抽出されたエキス成分を添加した活性化鉱水についても
同様である。
The same applies to the activated mineral water to which the extract component extracted by the above-mentioned method for producing an extract is added.

【0007】さらにまた、前記したエキスの製造方法に
おいては、被処理物は細粒化されてしまうので、固体状
の物質の形を変えずに、効率良くこのような接触反応方
法を適用することはできないという問題点もある。
Furthermore, in the above-mentioned method for producing an extract, since the object to be treated is finely divided, it is necessary to efficiently apply such a catalytic reaction method without changing the shape of the solid substance. There is also the problem that it cannot be done.

【0008】そこで、この発明の課題は、上記した問題
点を解決し、活性化鉱水を、固形状の被処理物に接触さ
せる場合に被処理物の形状を変化させないようにして接
触反応させることを可能にすると共に、その場合の被処
理物に対する接触効率を可及的に高めることである。
Therefore, an object of the present invention is to solve the above-mentioned problems and to carry out a catalytic reaction without changing the shape of the object to be treated when the activated mineral water is brought into contact with the solid object to be treated. And the contact efficiency with respect to the object to be treated in that case is increased as much as possible.

【0009】[0009]

【課題を解決するための手段】上記の課題を解決するた
め、この発明においては、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、この工程を
経た加圧水を前記所定の気圧未満の雰囲気に貯留する工
程とを設け、これらの工程を交互に繰り返すように前記
加圧水を循環させて活性化鉱水を製造した後、この活性
化鉱水を2〜30気圧に加圧して固形状被処理物に接触
通過させる活性化鉱水を用いた接触反応方法としたので
ある。
In order to solve the above problems, in the present invention, a step of bringing water pressurized to 5 to 30 atm into contact with a predetermined inorganic substance and a pressurized water which has been subjected to this step are provided. The step of storing in an atmosphere of less than the predetermined atmospheric pressure is provided, and after the activated mineral water is produced by circulating the pressurized water so as to alternately repeat these steps, the activated mineral water is pressurized to 2 to 30 atmospheric pressure. In this way, the catalytic reaction method using activated mineral water that is passed through a solid object to be contacted is used.

【0010】また、前記の活性化鉱水を抽出溶媒として
被抽出物を浸漬し、分取した抽出液を別途製造した活性
化鉱水に添加し、これを2〜30気圧に加圧して固形状
被処理物に接触通過させることからなる活性化鉱水を用
いた接触反応方法としたのである。この場合、前記被抽
出物が竹である手段を採用することもできる。
Further, the material to be extracted is immersed in the activated mineral water as an extraction solvent, and the separated extract is added to the separately prepared activated mineral water, which is pressurized to 2 to 30 atm. The contact reaction method using the activated mineral water consists of contacting and passing the treated material. In this case, it is also possible to employ a means in which the substance to be extracted is bamboo.

【0011】または、原料水を貯留するタンクから通水
される送水路に5〜30気圧の加圧水を送出するポンプ
を設け、前記送水路のポンプの下流には加圧水を無機物
質に接触通過させる透水装置を設け、この透水装置には
通過水を前記貯留タンクに返送する返送路を連結して設
け、前記ポンプ下流の送水路または返送路には操作弁付
きの複数のバイパス配水路を開閉可能に設け、一つのバ
イパス配水路には固形状被処理物を水流に接触通過させ
る透水装置を介在させ、他の一つのバイパス配水路には
被抽出物を収容する圧力タンクを介在させてなる活性化
鉱水を用いた接触反応装置としたのである。
Alternatively, a pump for delivering pressurized water of 5 to 30 atm is provided in a water passage through which water is stored from a tank for storing raw water, and a water permeate for passing the pressurized water into contact with an inorganic substance is provided downstream of the pump in the water passage. A device is provided, and a return passage for returning the passing water to the storage tank is connected to the water permeation device, and a plurality of bypass distribution passages with operation valves can be opened and closed in the water passage or the return passage downstream of the pump. An activation system is provided in which one bypass distribution channel has a water-permeable device that allows solid substances to come into contact with the water stream to pass through, and the other bypass distribution channel has a pressure tank that contains the extraction target substance. It was a catalytic reactor using mineral water.

【0012】[0012]

【作用】この発明に用いる活性化鉱水が、どのような作
用で固形状被処理物と接触反応するのか、その作用機構
は明らかではない。しかし、活性化鉱水は分子レベルで
水の状態が変化し、すなわち、無機物質から溶出した2
価、3価イオンなどによって、これらのイオンを中心に
水が小分子集団化していると考えられるので、固体状被
処理物内に効率良く浸透し、少なくともその表面に何ら
かの物理化学的作用を及ぼしていると考えられる。
The action mechanism of the activated mineral water used in the present invention for the catalytic reaction with the solid object to be treated is not clear. However, the state of water in activated mineral water changes at the molecular level, that is, it is eluted from inorganic substances.
Water is considered to be a group of small molecules centering around these ions due to valent and trivalent ions, so that water efficiently permeates into the solid object to be treated and exerts some physicochemical action on at least its surface. It is thought that

【0013】また、このような活性化鉱水に被抽出物を
浸漬すれば、抽出能力およびその効率が良く、前記浸漬
を繰り返して比較的短時間で濃厚なエキスが得られる。
When the substance to be extracted is dipped in such activated mineral water, the extraction ability and its efficiency are good, and the dipping can be repeated to obtain a concentrated extract in a relatively short time.

【0014】接触反応装置においては、適宜に連通する
複数のバイパス配水路を設けており、一つのバイパス配
水路に被抽出物を収容する圧力タンクを介在させて前記
バイパス配水路を閉じて活性化鉱水を製造し、その後、
当該バイパス配水路を開通させ、ポンプでもって加圧さ
れた活性化鉱水を圧力タンク内に収容して、抽出処理を
循環状態で行なう。そして、前記一つのバイパス配水路
を閉じるか、または所要量の流量に調節して、固体状被
処理物を収容した透水装置を介在した他の一つのバイパ
ス配水路を開けることにより、活性化鉱水と前記した抽
出液が混合された液を、固形状被処理物に効率よく接触
させることができる。
The contact reactor is provided with a plurality of bypass water passages that communicate with each other as appropriate, and one bypass water passage is closed and activated by interposing a pressure tank for containing the substance to be extracted. Producing mineral water, then
The bypass water passage is opened, the activated mineral water pressurized by the pump is stored in the pressure tank, and the extraction process is performed in a circulating state. Then, the activated mineral water is activated by closing the one bypass water passage or by adjusting the flow rate to a required amount and opening the other one bypass water passage having the water permeation device containing the solid object to be processed. The liquid in which the above-mentioned extraction liquid is mixed can be efficiently brought into contact with the solid object.

【0015】[0015]

【実施例】この発明の接触反応方法または接触反応装置
に用いる無機物質は、例えば鉱物性無機物質、金属酸化
物もしくはこれらを焼結したセラミックスまたは鉄鋼、
アルミニウムなどの精錬した金属等であって、特にその
種類を限定することなく採用できる。
Examples The inorganic substance used in the catalytic reaction method or catalytic reactor of the present invention is, for example, a mineral inorganic substance, a metal oxide, or ceramics or steel obtained by sintering these,
It is a refined metal such as aluminum, which can be adopted without any particular limitation.

【0016】前記した鉱物性無機物質としては、自然残
留磁気を有し、かつマグネシウム、鉄などのいわゆるミ
ネラルを含んだ玄武岩、安山岩、磁鉄鉱などの強磁性鉱
物が特に好ましいものとして挙げられる。また、ゲルマ
ニウム等の半導体物質を添加した場合にも好ましい結果
を得ている。
As the above-mentioned mineral inorganic substance, ferromagnetic minerals such as basalt, andesite and magnetite, which have natural remanence and contain so-called minerals such as magnesium and iron, are particularly preferable. Also, favorable results are obtained when a semiconductor material such as germanium is added.

【0017】この発明に用いる活性化鉱水は、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、この工程を経た加圧水を前記所定の気圧未満の
雰囲気に貯留する工程とを2つの工程を交互に繰り返し
て得られ、特に加圧水を数時間から24時間または、そ
れ以上の長時間連続的に循環させて製造することが好ま
しい。この場合、製造直後の活性化鉱水の水温は、ヒー
タ等の加熱装置を使用せずとも70〜80℃程度に上昇
するので、そのまま接触反応に用いることでより反応性
が高くなって好ましい。
The activated mineral water used in the present invention is 5 to 30.
Obtained by alternately repeating two steps, a step of bringing water pressurized to atmospheric pressure into contact with a predetermined inorganic substance and a step of storing the pressurized water that has passed through this step in an atmosphere of less than the predetermined atmospheric pressure, in particular, It is preferable that the pressurized water is continuously circulated for several hours to 24 hours or more for a long time. In this case, the water temperature of the activated mineral water immediately after production rises to about 70 to 80 ° C. without using a heating device such as a heater. Therefore, it is preferable to use the activated mineral water as it is for the catalytic reaction because the reactivity becomes higher.

【0018】活性化鉱水の製造に用いる加圧水を、5〜
30気圧に限定する理由は、5気圧未満の低圧では生成
された活性化鉱水の微生物の増殖抑制効果が劣り、被抽
出物への浸透力も劣ることとなり、逆に30気圧以上の
高圧では製造装置が大型化して実用性に欠ける点で好ま
しくないからである。
The pressurized water used for the production of activated mineral water is 5 to
The reason for limiting the pressure to 30 atm is that at a low pressure of less than 5 atm, the effect of suppressing the growth of microorganisms of the activated mineral water produced is inferior and the infiltration power to the substance to be extracted is inferior. Is unfavorable in that it becomes large and lacks practicality.

【0019】固形状被処理物に接触通過させる場合に用
いる活性化鉱水は、2〜30気圧に加圧して用いる。な
ぜなら、所定範囲未満の加圧条件では接触効率が充分で
なく、30気圧を越えると固形状被処理物が物理的に崩
壊する場合が多くなるからである。
The activated mineral water used when it is brought into contact with the solid object to be treated is pressurized to 2 to 30 atm. This is because the contact efficiency is not sufficient under a pressurizing condition below a predetermined range, and the solid object to be treated is often physically collapsed above 30 atm.

【0020】この発明で処理対象となる固形状被処理物
は、前記した所定圧力の活性化鉱水を接触させても破壊
されない程度のものであれば、特に限定することなく種
々の物質を採用できる。具体例としては、炭化ケイ素系
等の任意の成分からなるセラミックス、ガラス、酸化ア
ルミニウム(アルミナ)、鉄、鋼、銅その他の金属、黒
鉛・グラファイト等の炭素その他の無機物質、アクリロ
ニトリル・ブタジエン・スチレン共重合体樹脂(ABS
樹脂)、塩化ビニル樹脂、ポリアミド樹脂、ポリエステ
ル樹脂その他の樹脂、または水に不溶または難溶性の植
物質として、大豆、米、麦などが挙げられる。
The solid object to be treated in the present invention is not particularly limited as long as it is not destroyed even when it is contacted with the activated mineral water having the above-mentioned predetermined pressure, and various substances can be adopted. . Specific examples include ceramics made of arbitrary components such as silicon carbide, glass, aluminum oxide (alumina), iron, steel, copper and other metals, carbon and other inorganic substances such as graphite and graphite, acrylonitrile, butadiene and styrene. Copolymer resin (ABS
Examples of the resin), vinyl chloride resin, polyamide resin, polyester resin and other resins, and water-insoluble or sparingly soluble plant material include soybean, rice and wheat.

【0021】そして、前記した所定の圧力範囲内で処理
を行なう場合には、例えば無機物質を処理する際には、
比較的高圧域の圧力条件を設定し、植物体等を処理する
にはその原形を損なわないように、低圧域の処理条件を
採用する。
When the treatment is performed within the above-mentioned predetermined pressure range, for example, when treating an inorganic substance,
To set the pressure conditions in a relatively high pressure range, and to treat plants, etc., adopt the processing conditions in a low pressure range so as not to impair the original shape.

【0022】また、抽出液を別途製造した活性化鉱水に
添加して接触反応する発明に係る被抽出物としては、有
害な成分を含まない動・植物体であれば、特に限定する
ことなくこれを採用できる。
The extract to be subjected to the catalytic reaction by adding the extract to the separately prepared activated mineral water is not particularly limited as long as it is an animal or plant body containing no harmful components. Can be adopted.

【0023】このような植物体としては、キュウリ、ニ
ンジン、レタス、トマト、大豆、ごま、ニンニク、銀
杏、トウガラシなどの野菜類、食用藻類として、クロレ
ラ、コンブ、ワカメなどが挙げられる。また、植物成分
由来の薬効を期待する場合には、梅の実、ココ椰子、松
や杉の葉や種子、孟宗竹などの竹、もしくは檜またはこ
れらの乾留物(活性炭)等であってよい。動物体として
は、鶏卵など鳥類の卵、羊毛、絹糸、動物の角、甲殻
(キチン、キトサン)等の硬蛋白質が挙げられる。
Examples of such plants include vegetables such as cucumber, carrot, lettuce, tomato, soybean, sesame, garlic, ginkgo, and pepper, and edible algae such as chlorella, kelp and wakame. When a medicinal effect derived from a plant component is expected, it may be ume fruit, coco palm, pine or cedar leaf or seed, bamboo such as Menso bamboo, or cypress or a dry distillation product thereof (activated carbon). Examples of the animal body include avian eggs such as chicken eggs, wool, silk thread, animal horns, and hard proteins such as shells (chitin and chitosan).

【0024】抽出液を活性化鉱水に添加する割合は、特
に限定されるものでなく、被抽出物に対応した抽出液の
濃度と処理目的に応じて適宜対応すればよい。
The ratio of the extract added to the activated mineral water is not particularly limited, and may be appropriately adjusted depending on the concentration of the extract corresponding to the substance to be extracted and the purpose of treatment.

【0025】この発明の実施例である活性化鉱水を用い
た接触反応方法および装置を、さらに、添付図面に基づ
いて説明する。図1に示すように、実施例の接触反応装
置は、活性化鉱水の製造に用いる透水装置Aと、被抽出
物を活性化鉱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、固形状被処理物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
ている。
A catalytic reaction method and apparatus using activated mineral water according to an embodiment of the present invention will be further described with reference to the accompanying drawings. As shown in FIG. 1, the catalytic reactor of the embodiment comprises a water permeation apparatus A used for production of activated mineral water, a bypass water distribution channel B having a pressure tank 1 for accommodating a substance to be extracted together with the activated mineral water, It has a bypass water distribution channel C in which a water permeation device 3 for allowing the shaped object 2 to pass in contact with a water flow is interposed.

【0026】この接触反応装置は、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、その下流には加圧水を無
機物質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、さらに透水装置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
ている。そして、二つのバイパス配水路B,Cは操作弁
7でそれぞれ開閉可能である。
In this contact reaction apparatus, a pump 6 for delivering pressurized water of 5 to 30 atm is attached to a water passage 5 which is passed from a tank 4 for storing raw material water, and the pressurized water is brought into contact with an inorganic substance downstream thereof. The water permeation apparatus A is connected via the operation valve 7, and further downstream of the water permeation apparatus A is connected a return passage 8 for returning the water that has passed through contact with the inorganic substance to the tank 4. The two bypass distribution channels B and C can be opened and closed by the operation valve 7, respectively.

【0027】貯水タンク4は、原料水を貯留する上面開
口の蓋付きのステンレス製のものであり、これに温度指
示調節計9aを備えた電熱による加熱器9を付設し、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(三和ハイドロテ
ック社製)6を設けている。
The water storage tank 4 is made of stainless steel with a lid having an opening on the upper surface 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 single suction spiral pump (manufactured by Sanwa Hydrotech Co., Ltd.) 6 that communicates with the water supply passage 5 and delivers pressurized water of 5 to 30 atm is provided.

【0028】活性化鉱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、それ
ぞれの内部に上下一対のステンレス製多孔板11を配置
し、その間に粒径約5mmの玄武岩を主要成分とする無
機物質12を充填している。
The water permeation apparatus A used for producing activated mineral water is
Five metal cylindrical pressure-resistant containers 10 are connected in series, and a pair of upper and lower stainless perforated plates 11 are arranged inside each of them, and an inorganic substance 12 mainly composed of basalt having a particle diameter of about 5 mm is placed between them. Filling.

【0029】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つの高力フイルター13を直列させて設
けている。
In the return path 8, two high-strength filters 13 for filtering the water that has passed through the water permeation apparatus A are provided in series.

【0030】ここで、バイパス配水路はB、Cは、送水
路5から別れて再び送水路5に連結するが、さらに透水
装置Aの上流と返送路8を適宜に直結するバイパス配水
路Dを設けている。
Here, the bypass distribution channels B and C are separated from the water distribution channel 5 and are connected to the water distribution channel 5 again, but a bypass distribution channel D which connects the upstream of the water permeation apparatus A and the return channel 8 is appropriately connected. It is provided.

【0031】このうち、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または多孔性素材から
なるフィルタ14を有している他は、前記した透水装置
Aと同様の耐圧構造を有するものである。
Of these, the water permeation device 3 interposed in the bypass water distribution channel C has the same pressure resistance as the water permeation device A except that it has a filter 14 made of a net or a porous material at both ends of the pressure container. It has a structure.

【0032】また、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ろ過するために、フィル
タ15を取り付けている。フィルタ5は適宜に取り外す
か、また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. The filter 5 may be appropriately removed, or a filter having a large mesh may be selectively used.

【0033】これらのバイパス配水路B、C、Dは、そ
れぞれの両端に操作弁7を有しており、これを開閉操作
してそれぞれ単独使用または併用することができる。な
お、図中番号16は、圧力計を示している。
Each of these bypass water passages B, C, and D has an operation valve 7 at each end, which can be used individually or in combination by opening and closing the operation valve 7. Note that reference numeral 16 in the figure indicates a pressure gauge.

【0034】上記した実施例のエキスの製造装置を用い
た実験例を以下に説明する。まず、圧力タンク1および
透水装置3に水が流入しないように、これらの上流側お
よび下流側の操作弁7を閉じた状態として、原料水60
0リットルをタンク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、600リットルの活性化鉱水を
製造した。
An experimental example using the extract manufacturing apparatus of the above-mentioned embodiment will be described below. 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 7 are closed, and the raw water 60
0 liters of water was pumped from the tank 4 to the pressure of 25 atm with the pump 6, and water was passed through the water permeation apparatus A containing the basalt grains, the high-strength filter 13, and the return path 8 to the water storage tank 4 for about 24 times.
With continuous circulation for 600 hours, 600 liters of activated mineral water were produced.

【0035】この活性化鉱水のうち300リットルをタ
ンク4(容量1000リットル)に貯蔵すると共に、残
量をバルブ17を開けて取り出して別途設けたタンク
(図示せず)に貯蔵し、タンク4内の活性化鉱水は、反
応効率を上げるため、加熱器9にて水温95℃に加熱し
た。そして、圧力タンク1には、乾留により調製された
竹の粉末(竹泉産業社製:きよら)からなる被抽出物4
0kgを収容し、ついで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に開通させた。
300 liters of this activated mineral water is stored in the tank 4 (capacity 1000 liters), and the remaining amount is taken out by opening the valve 17 and stored in a separately provided tank (not shown). The activated mineral water of was heated to a water temperature of 95 ° C. by the heater 9 in order to increase the reaction efficiency. Then, in the pressure tank 1, an extract 4 composed of bamboo powder (manufactured by Takezumi Sangyo Co., Ltd .: Kiyora) prepared by carbonization
0 kg was accommodated, and then the closed operation valve 13 was opened to open the bypass water supply passage B to the water supply passage 5.

【0036】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 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気圧の加圧活性化鉱水を送出して、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
抽出操作を行ない、600リットルの竹抽出液を得た。
この抽出中に、圧力タンク1内の竹の粉末を2回入替え
て、合計80kgの竹の粉末を抽出に用いた。
On the other hand, the operation valves 7 on the upstream and downstream sides of the water permeation apparatus A are closed, and the bypass water distribution channel D is opened by the operation valve 7 so that the upstream side of the water permeation apparatus A and the return path are directly connected. Of the pressurized activated mineral water, the pump 6, the pressure tank 1, the bypass water passage D, the high-strength filter 13,
An extraction operation was performed by passing water through a route circulating through the return path 8 and the tank 4 for 12 hours to obtain 600 liters of bamboo extract.
During this extraction, the bamboo powder in the pressure tank 1 was replaced twice, and a total of 80 kg of bamboo powder was used for the extraction.

【0037】次に、バイパス配水路Bを操作弁7で閉
じ、透水装置3にナイロン繊維からなる織布およびセラ
ミックス粒を収容し、タンク4に別途貯蔵していた30
0リットルの活性化鉱水を追加して、バイパス配水路C
の上・下流の操作弁7を開栓した。
Next, the bypass water distribution passage B was closed by the operation valve 7, the woven fabric made of nylon fiber and the ceramic particles were stored in the water permeation device 3, and the water was stored separately in the tank 4.
Add 0 liters of activated mineral water to bypass bypass C
The operation valves 7 on the upper and lower sides of the above were opened.

【0038】そして、ポンプ6で5気圧の竹エキス含有
の加圧活性化鉱水を送出し、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1
3、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、竹エキス含有の加圧活性化鉱水と
固形状被処理物2の接触反応を行なった。
Then, the pump 6 delivers the pressurized activated mineral water containing the bamboo extract at 5 atm, and the tank 4, the pump 6, the bypass distribution channel C, the bypass distribution channel D, and the high-strength filter 1 are supplied.
3, the water flow was circulated for 12 hours in the route from the return passage 8 to the tank 4 in order to carry out the contact reaction between the pressurized activated mineral water containing the bamboo extract and the solid object 2 to be treated.

【0039】得られたナイロン繊維は、活性化鉱水およ
び竹エキスが浸透してこれらの効用が効率よく付加され
ており、特に脱臭性、吸湿性、保温性等に優れていると
共に、肌に馴染みのよい極めて優れた繊維に変性してい
た。
Activated mineral water and bamboo extract permeate the obtained nylon fiber to efficiently add these effects, and in particular, it is excellent in deodorizing property, hygroscopic property, heat retaining property and the like, and is familiar to the skin. It had been modified into a very good fiber with good quality.

【0040】[0040]

【効果】この発明は、以上説明したように、所定の条件
で水を所定の無機物質に繰り返し接触通過させて製造し
た活性化鉱水を用いて、これを所定の圧力に加圧して固
形状被処理物に接触通過させることにより、活性化鉱水
を用い、これを固形状被処理物に対しても接触反応させ
ることが可能となり、その場合の被処理物に対する活性
化鉱水の接触効率を可及的に高めることができるという
利点がある。
As described above, the present invention uses activated mineral water produced by repeatedly contacting and passing water with a predetermined inorganic substance under predetermined conditions. Activated mineral water is used by bringing it into contact with the treated material, and it is possible to react this with the solid object to be treated. In that case, the contact efficiency of the activated mineral water with the object to be treated can be increased. There is an advantage that it can be increased.

【0041】また、前記接触反応において、活性化鉱水
を抽出溶媒として得た抽出液を活性化鉱水に添加混合す
れば、竹などの固形状被処理物に抽出液に固有の物性ま
たは固有の反応性を付加させることもできる利点もあ
る。
In the above catalytic reaction, if an extract obtained by using activated mineral water as an extraction solvent is added to and mixed with the activated mineral water, physical properties unique to the extract or reaction specific to the solid substance to be treated such as bamboo can be obtained. There is also an advantage that it is possible to add sex.

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

【図1】実施例の製造方法および装置を模式化して示す
説明図
FIG. 1 is an explanatory view schematically showing a manufacturing method and an apparatus according to an embodiment.

【符号の説明】[Explanation of symbols]

A 透水装置 B、C、D バイパス配水路 1 圧力タンク 2 固形状被処理物 3 透水装置 4 タンク 5 送水路 6 ポンプ 7 操作弁 8 返送路 A Water permeation system B, C, D Bypass water distribution channel 1 Pressure tank 2 Solid object 3 Water permeation system 4 Tank 5 Water channel 6 Pump 7 Operation valve 8 Return channel

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 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、この工程を経た加圧水
を前記所定の気圧未満の雰囲気に貯留する工程とを設
け、これらの工程を交互に繰り返すように前記加圧水を
循環させて活性化鉱水を製造した後、この活性化鉱水を
2〜30気圧に加圧して固形状被処理物に接触通過させ
ることからなる活性化鉱水を用いた接触反応方法。
1. A step of bringing water pressurized to 5 to 30 atmospheres into contact with a predetermined inorganic substance to pass therethrough, and a step of storing the pressurized water that has undergone this step in an atmosphere below the predetermined atmospheric pressure are provided. The activated mineral water is produced by circulating the pressurized water so that the steps are alternately repeated to produce activated mineral water, and the activated mineral water is pressurized to 2 to 30 atm to pass through the solid object to be treated. Contact reaction method used.
【請求項2】 請求項1に記載の方法で製造した活性化
鉱水を抽出溶媒として被抽出物を浸漬し、分取した抽出
液を別途製造した活性化鉱水に添加し、これを2〜30
気圧に加圧して固形状被処理物に接触通過させることか
らなる活性化鉱水を用いた接触反応方法。
2. The activated mineral water produced by the method according to claim 1 is used as an extraction solvent to immerse the substance to be extracted, and the fractionated extract is added to the separately prepared activated mineral water.
A catalytic reaction method using activated mineral water comprising pressurizing to atmospheric pressure and allowing it to pass through a solid object to be treated.
【請求項3】 前記被抽出物が竹である請求項2に記載
の活性化鉱水を用いた接触反応方法。
3. The catalytic reaction method using activated mineral water according to claim 2, wherein the substance to be extracted is bamboo.
【請求項4】 原料水を貯留するタンクから通水される
送水路に5〜30気圧の加圧水を送出するポンプを設
け、前記送水路のポンプの下流には加圧水を無機物質に
接触通過させる透水装置を設け、この透水装置には通過
水を前記貯留タンクに返送する返送路を連結して設け、
前記ポンプ下流の送水路または返送路には操作弁付きの
複数のバイパス配水路を開閉可能に設け、一つのバイパ
ス配水路には固形状被処理物を水流に接触通過させる透
水装置を介在させ、他の一つのバイパス配水路には被抽
出物を収容する圧力タンクを介在させてなる活性化鉱水
を用いた接触反応装置。
4. A water supply passage through which a raw water is stored is provided with a pump for delivering pressurized water of 5 to 30 atm, and a water-permeable water passage through which the pressurized water comes into contact with an inorganic substance downstream of the pump of the water delivery passage. A device is provided, and a return path for returning the passing water to the storage tank is connected to the water permeation device,
A plurality of bypass water distribution passages with operation valves are provided in the water supply passage or return passage downstream of the pump so as to be openable and closable, and one bypass water distribution passage is provided with a water permeation device for contacting and passing a solid substance to be treated into a water flow, A catalytic reactor using activated mineral water, in which a pressure tank containing the substance to be extracted is interposed in another bypass water passage.
JP12254394A 1994-06-03 1994-06-03 Contact reaction method and apparatus using activated mineral water Expired - Lifetime JP3561532B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12254394A JP3561532B2 (en) 1994-06-03 1994-06-03 Contact reaction method and apparatus using activated mineral water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12254394A JP3561532B2 (en) 1994-06-03 1994-06-03 Contact reaction method and apparatus using activated mineral water

Publications (2)

Publication Number Publication Date
JPH07328418A true JPH07328418A (en) 1995-12-19
JP3561532B2 JP3561532B2 (en) 2004-09-02

Family

ID=14838480

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP3561532B2 (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012117798A (en) * 2010-11-11 2012-06-21 Assist Tohkei:Kk Organic-matter preservation device and organic-matter preservation system
JP2013113716A (en) * 2011-11-29 2013-06-10 Shinki Sangyo Kk Method for treating radioactive nuclide contaminant
JP2016014680A (en) * 2015-09-08 2016-01-28 新紀産業株式会社 Treatment method of 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
JP2022097914A (en) * 2020-12-21 2022-07-01 日本アガリクス株式会社 Reduced water production method and reduced water production device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012117798A (en) * 2010-11-11 2012-06-21 Assist Tohkei:Kk Organic-matter preservation device and organic-matter preservation system
JP2013113716A (en) * 2011-11-29 2013-06-10 Shinki Sangyo Kk Method for treating radioactive nuclide contaminant
JP2016014680A (en) * 2015-09-08 2016-01-28 新紀産業株式会社 Treatment method of 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
JP2022097914A (en) * 2020-12-21 2022-07-01 日本アガリクス株式会社 Reduced water production method and reduced water production device

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