JPH0838894A - Treatment of adsorbent, filter agent and mineral ellution agent used in water purifier - Google Patents
Treatment of adsorbent, filter agent and mineral ellution agent used in water purifierInfo
- Publication number
- JPH0838894A JPH0838894A JP19907194A JP19907194A JPH0838894A JP H0838894 A JPH0838894 A JP H0838894A JP 19907194 A JP19907194 A JP 19907194A JP 19907194 A JP19907194 A JP 19907194A JP H0838894 A JPH0838894 A JP H0838894A
- Authority
- JP
- Japan
- Prior art keywords
- adsorbent
- mineral
- heating
- zeolite
- stones
- 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
Links
Landscapes
- Water Treatment By Sorption (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
【産業上の利用分野】本発明は、浄水機等に用いる吸着
剤、濾過剤、ミネラル溶出剤の処理方法に関するもので
あり、詳しくは、浄水機、精水機、ミネラル水製造機等
に用いられる活性炭、ゼオライト、セラミック、貝化
石、サンゴ石、麦飯石等からなる吸着剤、濾過剤、ミネ
ラル溶出剤の使用前の処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating an adsorbent, a filtering agent and a mineral eluent used in a water purifier, etc., and more specifically, it is used in a water purifier, a water purifier, a mineral water producing machine and the like. The present invention relates to a treatment method before use of an adsorbent composed of activated carbon, zeolite, ceramic, shell fossil, coral stone, barley stone, etc., a filtering agent, and a mineral eluent.
【従来の技術】従来、活性炭、ゼオライト、セラミッ
ク、貝化石、麦飯石等を吸着剤、濾過剤、ミネラル溶出
剤として用いつつこれらを装置内に収納した諸種の形式
の浄水機、精水機、ミネラル水製造機が存在する。従来
においては、上記吸着剤、濾過剤、ミネラル溶出剤とし
て用いられている活性炭、ゼオライト、セラミック、貝
化石、サンゴ石、麦飯石等に対して低温殺菌や水洗等を
行っているが、雑菌の繁殖防止や雑菌の排出防止等の処
理を何ら施すことなく、活性炭、ゼオライト、セラミッ
ク、貝化石、サンゴ石、麦飯石等をそのまま浄水機等に
内蔵し使用しているのが実情である。2. Description of the Related Art Conventionally, various types of water purifiers, water purifiers, in which activated carbon, zeolite, ceramics, shell fossils, barley stones, etc. are used as adsorbents, filtration agents, mineral eluents and are housed in the equipment, There is a mineral water maker. Conventionally, the adsorbent, the filtering agent, activated carbon used as a mineral eluent, zeolite, ceramic, shell fossil, coral stone, barley stone, etc. are subjected to pasteurization and water washing, etc. The actual situation is that activated carbon, zeolite, ceramics, fossil shells, coral stones, barley stones, etc. are used as they are as they are by incorporating them into a water purifier, etc. without any processing such as breeding prevention and discharge prevention of miscellaneous bacteria.
【発明が解決しようとする課題】しかしながら、前記従
来における吸着剤、濾過剤、ミネラル溶出剤として用い
られている活性炭、ゼオライト、セラミック、貝化石、
サンゴ石、麦飯石などは、未燃焼物などの有機物やガス
体（特に有害ガス体）が含まれている。同時に、時間の
経過とともに浄水機、精水機、ミネラル水製造機等には
種々の有害物質が吸着されるため、上記各剤を浄水機、
精水機などの吸着剤、濾過剤等に使用したままにする
と、経時的に未燃焼物の有機物から雑菌などが繁殖して
くる。従って、このような状況から、浄水機等の使用開
始後には、常に雑菌の溶出或いは繁殖があるために、安
定した浄水、精水、ミネラル水が得られないのが実情で
ある。特に、真夏の気温の高い時期は、高温度との関係
上、上記現象が顕著に表れる。本発明は、このような従
来の実情に鑑み開発されたもので、その目的とするとこ
ろは、吸着剤、濾過剤、ミネラル溶出剤として浄水機、
精水機、ミネラル水製造機などに用いられる活性炭、ゼ
オライト、セラミック、貝化石、サンゴ石、麦飯石等に
含有される未燃焼物等の有機物の発生を減少させ、当該
有機物から発生する種々の雑菌を溶出させることなく、
長期にわたって安定した吸着剤、濾過剤、ミネラル溶出
剤等として使用することができる浄水機等に用いる吸着
剤、濾過剤、ミネラル溶出剤の処理方法を提供すること
にある。However, activated carbon, zeolite, ceramics, fossil shells, which are used as the above-mentioned conventional adsorbents, filter agents, and mineral eluents,
Coral stones, bakuhanseki, etc. contain organic substances such as unburned substances and gas bodies (particularly harmful gas bodies). At the same time, since various harmful substances are adsorbed to the water purifier, the water purifier, the mineral water production machine, etc. with the passage of time,
If it is used as an adsorbent for a water purification machine, a filter, etc., various bacteria will grow from organic matter of unburned substances over time. Therefore, from such a situation, after the start of use of the water purifier or the like, stable purification water, purified water, and mineral water cannot be obtained because various bacteria are always eluted or propagated. In particular, during the high temperature of midsummer, the above phenomenon is prominent due to the high temperature. The present invention has been developed in view of such conventional circumstances, and an object thereof is an adsorbent, a filtering agent, a water purifier as a mineral eluent,
Activated carbon, zeolite, ceramics, shellfish fossils, coral stones, used in a water purification machine, mineral water production machine, etc. to reduce the generation of organic substances such as unburned substances contained in, etc., and to generate various organic substances. Without eluting miscellaneous bacteria
An object of the present invention is to provide a method for treating an adsorbent, a filter agent, and a mineral eluent used in a water purifier or the like that can be used as a stable adsorbent, a filter agent, a mineral eluent, etc. for a long period of time.
【課題を解決するための手段】請求項１記載の処理方法
は、浄水機、精水機、ミネラル水製造機等に用いられる
活性炭、ゼオライト、セラミック、貝化石、サンゴ石、
麦飯石等からなる吸着剤、濾過剤、ミネラル溶出剤の使
用前の処理方法であって、原料１、即ち、活性炭、ゼオ
ライト、セラミック、貝化石、麦飯石等からなる吸着
剤、濾過剤、ミネラル溶出剤を加熱及び／又は焼成する
工程からなるものである。請求項２記載の処理方法は、
前記請求項１記載の処理工程中の加熱及び／又は焼成温
度、加熱及び／又は焼成時間、加熱及び／又は焼成の回
数が、吸着剤、濾過剤、ミネラル溶出剤として用いられ
る活性炭、ゼオライト、セラミック、貝化石、サンゴ
石、麦飯石等が有する吸着特性、溶出特性等を最大限に
引き出すことが可能な範囲から選ばれるものである。請
求項３記載の処理方法は、前記請求項１記載の処理工程
中の加熱及び／又は焼成温度を３００℃乃至５００℃、
加熱及び／又は焼成時間を１５分乃至３０分間、加熱及
び／又は焼成の回数を１回乃至３回としたものである。
請求項４記載の処理方法は、浄水機、精水機、ミネラル
水製造機等に用いられる活性炭、ゼオライト、セラミッ
ク、貝化石、サンゴ石、麦飯石等からなる吸着剤、濾過
剤、ミネラル溶出剤の使用前の処理方法であって、原料
１、即ち、活性炭、ゼオライト、セラミック、貝化石、
サンゴ石、麦飯石等からなる吸着剤、濾過剤、ミネラル
溶出剤を加熱及び／又は焼成する第１工程と、次に、活
性炭、ゼオライト、セラミック、貝化石、サンゴ石、麦
飯石等からなる吸着剤、濾過剤、ミネラル溶出剤を再加
熱する第２工程と、最後に、活性炭、ゼオライト、セラ
ミック、貝化石、サンゴ石、麦飯石等からなる吸着剤、
濾過剤、ミネラル溶出剤をオゾン零囲気中で冷却する第
３工程とを具備してなるものである。請求項５記載の処
理方法は、前記請求項４記載の第１工程における加熱及
び／又は焼成温度、加熱及び／又は焼成時間、加熱及び
／又は焼成の回数が、吸着剤、濾過剤、ミネラル溶出剤
として用いられる活性炭、ゼオライト、セラミック、貝
化石、サンゴ石、麦飯石等が有する吸着特性、溶出特性
等を最大限に引き出すことが可能な範囲から選ばれるも
のである。請求項６記載の処理方法は、前記請求項４記
載の第１工程における加熱及び／又は焼成温度を３００
℃乃至５００℃、加熱及び／又は焼成時間を１５分乃至
３０分間とし、加熱及び／又は焼成の回数を１回乃至３
回としたものである。請求項７記載の処理方法は、前記
請求項４記載の第２工程における再加熱温度が、吸着
剤、濾過剤、ミネラル溶出剤として用いられる活性炭、
ゼオライト、セラミック、貝化石、サンゴ石、麦飯石等
の悪臭分子、成分、ガスを追い出すことが可能範囲から
選ばれるものである。請求項８記載の処理方法は、前記
請求項４記載の第２工程における再加熱温度を３００℃
乃至５００℃としたものである。請求項９記載の処理方
法は、前記請求項４記載の第３工程が、吸着剤、濾過
剤、ミネラル溶出剤として用いられる活性炭、ゼオライ
ト、セラミック、貝化石、サンゴ石、麦飯石等を冷却し
ながら電磁波の照射及び／又は適宜オゾン発生器からオ
ゾンを採取して処理するものであり、この場合の冷却温
度を、１００℃乃至５０℃としたものである。The treatment method according to claim 1 is an activated carbon, a zeolite, a ceramic, a shell fossil, a coral stone, which is used in a water purifier, a water purifier, a mineral water production machine or the like.
What is claimed is: 1. A treatment method of an adsorbent composed of barley stone, etc., a filtering agent, a mineral eluent, which is a raw material 1, namely, an adsorbent composed of activated carbon, zeolite, ceramic, shell fossil, barley stone, etc., a filtering agent, mineral It comprises a step of heating and / or calcining the eluent. The processing method according to claim 2 is
The heating and / or calcination temperature, the heating and / or calcination time, and the number of times of heating and / or calcination during the treatment step according to claim 1, are used as an adsorbent, a filter agent, a mineral eluent, activated carbon, zeolite, or ceramic. , The fossil shellfish, the coral stone, the barley stone, and the like, are selected from the range that can maximize the adsorption characteristics and elution characteristics. The treatment method according to claim 3 is such that the heating and / or firing temperature during the treatment step according to claim 1 is 300 ° C to 500 ° C.
The heating and / or firing time is 15 to 30 minutes, and the number of heating and / or firing is 1 to 3 times.
The treatment method according to claim 4 is an adsorbent composed of activated carbon, zeolite, ceramic, shellfish fossil, coral stone, barley stone, etc. used in a water purifier, a water purifier, a mineral water producing machine, etc., a filtering agent, a mineral eluent. A method for treating a raw material 1, that is, activated carbon, zeolite, ceramics, fossil shells,
The first step of heating and / or firing an adsorbent composed of coral stone, barley stone, etc., a filtering agent, a mineral eluent, and then an adsorption composed of activated carbon, zeolite, ceramic, shell fossil, coral stone, barley stone, etc. The second step of reheating the agent, filter agent, mineral eluent, and finally, an adsorbent consisting of activated carbon, zeolite, ceramics, fossil shells, coral stones, barley stones, etc.
And a third step of cooling the filtering agent and the mineral eluent in an atmosphere of zero ozone. In the treatment method according to claim 5, the heating and / or calcination temperature, the heating and / or calcination time, and the number of times of heating and / or calcination in the first step according to claim 4 are an adsorbent, a filtering agent, and a mineral elution. The active carbon, zeolite, ceramics, shell fossils, coral stones, barley stones, etc. used as agents are selected from the range that can maximize the adsorption properties and elution properties. According to a treatment method of claim 6, the heating and / or firing temperature in the first step of claim 4 is 300.
C. to 500.degree. C., heating and / or firing time is 15 minutes to 30 minutes, and heating and / or firing is performed once to 3 times.
It is a time. The treatment method according to claim 7, wherein the reheating temperature in the second step according to claim 4 is an activated carbon used as an adsorbent, a filtering agent, a mineral eluent,
It is selected from the range capable of expelling malodorous molecules, components, and gases such as zeolite, ceramics, fossil shells, coral stones, and barley stones. In the treatment method according to claim 8, the reheating temperature in the second step according to claim 4 is 300 ° C.
To 500 ° C. In the treatment method according to claim 9, the third step of claim 4 is to cool activated carbon, zeolite, ceramics, shell fossil, coral stone, barley stone, etc. used as an adsorbent, a filtering agent, a mineral eluent. However, it is intended to irradiate electromagnetic waves and / or appropriately collect ozone from an ozone generator for processing, and the cooling temperature in this case is 100 ° C. to 50 ° C.
【作用】請求項１乃至３記載の処理方法によれば、浄水
機、精水機、ミネラル水製造機等に吸着剤、濾過剤、ミ
ネラル溶出剤として用いられる活性炭、ゼオライト、セ
ラミック、貝化石、サンゴ石、麦飯石等が有する吸着特
性、溶出特性等を最大限に引き出すことができるととも
に、これらの各剤に含有されている未燃焼物などの有機
物を２乃至５重量％以下に減少できるので、活性炭、ゼ
オライト、セラミック、貝化石、サンゴ石、麦飯石等に
含有されている有機物から発生する種々の雑菌の溶出現
象を解消することができることから、活性炭、ゼオライ
ト、セラミック、貝化石、サンゴ石、麦飯石等の各剤を
長期にわたって安定、安心した吸着剤、濾過剤、ミネラ
ル溶出剤等として浄水機、精水機、ミネラル水製造機等
に使用できる。請求項４乃至９記載の処理方法によれ
ば、前記請求項１乃至３記載の作用を発揮できるととも
に、浄水機等に吸着剤、濾過剤、ミネラル溶出剤として
用いられる活性炭、ゼオライト、セラミック、貝化石、
サンゴ石、麦飯石などの悪臭分子、成分、ガスを追い出
すことができ、しかも、活性炭、ゼオライト、セラミッ
ク、貝化石、サンゴ石、麦飯石等にオゾンを効果的に吸
着させることができ、当該各剤の細孔中にオゾンを長期
間保持させることが可能であるので、活性炭、ゼオライ
ト、セラミック、貝化石、サンゴ石、麦飯石等を浄水機
等に入れて使用した場合、殺菌又は除菌効果を発揮させ
ることができる結果、浄水機、精水機、ミネラル水製造
機の中で雑菌の発生、増加を抑え、且つ、悪臭の発生を
防ぐ事ができることから、活性炭、ゼオライト、セラミ
ック、貝化石、サンゴ石、麦飯石等の各剤を長期にわた
って安定、安心した吸着剤、濾過剤、ミネラル溶出剤等
として浄水機、精水機、ミネラル水製造機等に使用でき
る。According to the treatment method according to claims 1 to 3, an adsorbent, a filter, an activated carbon used as a mineral eluent for a water purifier, a water purifier, a mineral water producing machine, a zeolite, a ceramic, a shell fossil, Since it is possible to maximize the adsorption and elution characteristics of coral stones and boiled stones, the organic substances such as unburned substances contained in these agents can be reduced to 2 to 5% by weight or less. , Activated carbon, zeolite, ceramics, fossil shells, coral stones, barley stones, etc., because it is possible to eliminate the elution phenomenon of various bacteria generated from organic substances contained in activated carbon, zeolites, ceramics, shell fossils, coral stones. Each agent such as barley stone can be used for water purifiers, water purifiers, mineral water producing machines, etc. as adsorbents, filters, mineral eluents, etc. that are stable and reliable for a long period of time. According to the treatment method of claims 4 to 9, the functions of claims 1 to 3 can be exhibited, and activated carbon, zeolite, ceramics, shellfish used as adsorbents, filter agents, mineral eluents in water purifiers and the like. fossil,
Malodorous molecules, components and gases such as coral stone and barley stone can be expelled, and ozone can be effectively adsorbed to activated carbon, zeolite, ceramics, shell fossils, coral stone, barley stone, etc. Since it is possible to retain ozone in the pores of the agent for a long time, when using activated carbon, zeolite, ceramic, shell fossil, coral stone, barley stone, etc. in a water purifier, etc., sterilizing or sterilizing effect As a result, activated carbon, zeolite, ceramics, fossil shells can be prevented because the generation and increase of bacteria in the water purifier, water purifier, and mineral water production machine can be suppressed and the generation of malodor can be prevented. , Coral stone, barley stone, etc. can be used as a stable and reliable adsorbent, filter, mineral eluent, etc. for water purifiers, water purifiers, mineral water production machines, etc.
【実施例】以下、添付した図面を参照して本発明に係る
浄水機等に用いる吸着剤、濾過剤、ミネラル溶出剤の処
理方法の実施例を説明する。本発明は、浄水機、精水
機、ミネラル水製造機等に用いられる活性炭、ゼオライ
ト、セラミック、貝化石、サンゴ石、麦飯石等からなる
吸着剤、濾過剤、ミネラル溶出剤を、図１又は図２に示
すような工程でもって処理する方法である。本実施例に
おいては、浄水機に用いる場合の活性炭、ゼオライト、
セラミック、貝化石、サンゴ石、麦飯石等からなる吸着
剤、濾過剤、ミネラル溶出剤の処理方法について説明す
る。図１は、浄水機に用いる場合の活性炭、ゼオライ
ト、セラミック、貝化石、サンゴ石、麦飯石等からなる
吸着剤、濾過剤、ミネラル溶出剤の処理工程を示すブロ
ック図である。即ち、本実施例の処理方法は、原料１、
即ち、活性炭、ゼオライト、セラミック、貝化石、サン
ゴ石、麦飯石等からなる吸着剤、濾過剤、ミネラル溶出
剤を加熱及び／又は焼成する工程からなる。この処理工
程の後、活性炭、ゼオライト、セラミック、貝化石、サ
ンゴ石、麦飯石等からなる製品としての吸着剤、濾過
剤、ミネラル溶出剤２を得ることができる。前記処理工
程中の加熱及び／又は焼成温度、加熱及び／又は焼成時
間、加熱及び／又は焼成の回数は、吸着剤、濾過剤、ミ
ネラル溶出剤として用いられる活性炭、ゼオライト、セ
ラミック、貝化石、サンゴ石、麦飯石などが有する吸着
特性、溶出特性等を最大限に引き出すことが可能な範囲
から選ばれ、特に限定されるものではない。但し、上記
処理工程中における加熱及び／又は焼成温度は５００
℃、加熱及び／又は焼成時間は１５分間、加熱及び／又
は焼成の回数は１回が適当である。これにより、浄水
機、精水機、ミネラル水製造機等に吸着剤、濾過剤、ミ
ネラル溶出剤として用いられる活性炭、ゼオライト、セ
ラミック、貝化石、サンゴ石、麦飯石等が有する吸着特
性、溶出特性等を最大限に引き出すことができるととも
に、これらの各剤に含有されている未燃焼物などの有機
物を２重量％以下に減少できることが判明した。従っ
て、活性炭、ゼオライト、セラミック、貝化石、サンゴ
石、麦飯石等に含有されている有機物から発生する種々
雑菌の溶出現象を解消することができ、活性炭、ゼオラ
イト、セラミック、貝化石、サンゴ石、麦飯石等の各剤
を長期にわたって安定、安心した吸着剤、濾過剤、ミネ
ラル溶出剤等として浄水機、精水機、ミネラル水製造機
等に使用できることが判明した。図２は、前記図１に示
す処理方法と異なる実施例の処理方法に係る処理工程を
示すブロック図である。本実施例の処理方法は、先ず、
原料１、即ち、活性炭、ゼオライト、セラミック、貝化
石、サンゴ石、麦飯石等からなる吸着剤、濾過剤、ミネ
ラル溶出剤を加熱及び／又は焼成する第１工程と、次
に、活性炭、ゼオライト、セラミック、貝化石、サンゴ
石、麦飯石等からなる吸着剤、濾過剤、ミネラル溶出剤
を再加熱する第２工程と、活性炭、ゼオライト、セラミ
ック、貝化石、サンゴ石、麦飯石等からなる吸着剤、濾
過剤、ミネラル溶出剤をオゾン零囲気中で冷却する第３
工程とを具備してなるものである。これらの処理工程の
後、活性炭、ゼオライト、セラミック、貝化石、サンゴ
石、麦飯石などからなる製品としての吸着剤、濾過剤、
ミネラル溶出剤３を得ることができる。前記第１工程中
の加熱及び／又は焼成温度、加熱及び／又は焼成時間、
加熱及び／又は焼成の回数は、吸着剤、濾過剤、ミネラ
ル溶出剤として用いられる活性炭、ゼオライト、セラミ
ック、貝化石、サンゴ石、麦飯石などが有する吸着特
性、溶出特性等を最大限に引き出すことが可能な範囲か
ら選ばれ、特に限定されるものではない。但し、上記処
理工程中における加熱及び／又は焼成温度は５００℃、
加熱及び／又は焼成時間は１５分間、加熱及び／又は焼
成の回数は１回が適当である。また、前記第２工程にお
ける再加熱温度は、吸着剤、濾過剤、ミネラル溶出剤と
して用いられる活性炭、ゼオライト、セラミック、貝化
石、サンゴ石、麦飯石等の悪臭分子、成分、ガスを追い
出すことが可能範囲から選ばれ、特に限定するものでは
ないが、この場合、３５０℃が適当である。更に、前記
第３工程においては、吸着剤、濾過剤、ミネラル溶出剤
として用いられる活性炭、ゼオライト、セラミック、貝
化石、サンゴ石、麦飯石等を冷却しながら電磁波の照射
及び／又は適宜のオゾン発生器からオゾンを採取して処
理する。この場合の冷却温度は、５０℃が適当である。
前記第１工程の処理後、前記図１に示す実施例において
説明したと同様に、浄水機、精水機、ミネラル水製造機
等に吸着剤、濾過剤、ミネラル溶出剤として用いられる
活性炭、ゼオライト、セラミック、貝化石、サンゴ石、
麦飯石等が有する吸着特性、溶出特性等を最大限に引き
出すことができるとともに、これらの各剤に含有されて
いる未燃焼物などの有機物を２重量％以下に減少できる
ので、活性炭、ゼオライト、セラミック、貝化石、サン
ゴ石、麦飯石等に含有されている有機物から発生する種
々の雑菌の溶出現象を解消することができ、活性炭、ゼ
オライト、セラミック、貝化石、サンゴ石、麦飯石等の
各剤を長期にわたって安定、安心した吸着剤、濾過剤、
ミネラル溶出剤等として浄水機、精水機、ミネラル水製
造機等に使用できることが判明した。次に、前記第２工
程の処理後、浄水機等に吸着剤、濾過剤、ミネラル溶出
剤として用いられる活性炭、ゼオライト、セラミック、
貝化石、サンゴ石、麦飯石等の悪臭分子、成分、ガスを
追い出すことができ、前記第３工程の処理後、活性炭、
ゼオライト、セラミック、貝化石、サンゴ石、麦飯石等
にオゾンを効果的に吸着させることができ、当該各剤の
細孔中にオゾンを長期間保持させることが可能で、これ
らの処理が施された活性炭、ゼオライト、セラミック、
貝化石、サンゴ石、麦飯石等を浄水機などに入れて使用
した場合、殺菌、除菌効果を発揮させることができる結
果、浄水機、精水機、ミネラル水製造機の中で雑菌の発
生、増加を抑え、且つ、悪臭の発生を防ぐ事ができるこ
とから、活性炭、ゼオライト、セラミック、貝化石、サ
ンゴ石、麦飯石等の各剤を長期にわたって安定、安心し
た吸着剤、濾過剤、ミネラル溶出剤等として浄水機、精
水機、ミネラル水製造機等に使用できることが判明し
た。本発明は、上述した各実施例に限定されるものでは
なく、その要旨の範囲内で種々の変形が可能である。EXAMPLES Examples of a method for treating an adsorbent, a filtering agent and a mineral eluent used in a water purifier according to the present invention will be described below with reference to the accompanying drawings. The present invention provides an adsorbent, a filter agent, and a mineral eluent composed of activated carbon, zeolite, ceramics, fossil shells, coral stones, barley stones, etc., used in water purifiers, water purifiers, mineral water producing machines, etc., as shown in FIG. This is a method of processing through the steps shown in FIG. In the present embodiment, activated carbon when used in a water purifier, zeolite,
A method of treating an adsorbent made of ceramics, fossil shells, coral stones, barley stones, etc., a filtering agent, and a mineral eluent will be described. FIG. 1 is a block diagram showing a treatment process of an adsorbent made of activated carbon, zeolite, ceramics, fossil shells, coral stone, barley stone, etc., a filtering agent, and a mineral eluent when used in a water purifier. That is, the treatment method of the present embodiment is based on the raw material 1,
That is, it comprises a step of heating and / or firing an adsorbent composed of activated carbon, zeolite, ceramics, shell fossil, coral stone, barley stone, etc., a filtering agent, and a mineral eluent. After this treatment step, an adsorbent, a filtering agent, a mineral eluent 2 as a product made of activated carbon, zeolite, ceramics, fossil shells, coral stones, barley stones, etc. can be obtained. The heating and / or calcination temperature, the heating and / or calcination time, and the number of times of the heating and / or calcination during the treatment step are as follows: adsorbent, filtering agent, activated carbon used as a mineral eluent, zeolite, ceramic, shell fossil, coral. It is selected from the range capable of maximizing the adsorption characteristics, elution characteristics, etc. possessed by stones, barley stones, etc., and is not particularly limited. However, the heating and / or firing temperature in the above treatment step is 500.
It is suitable that the temperature is 15 ° C., the heating and / or firing time is 15 minutes, and the heating and / or firing is once. As a result, the adsorption characteristics and elution characteristics of adsorbents, filtration agents, activated carbon used as mineral eluents, zeolites, ceramics, shell fossils, coral stones, barley stones, etc. in water purifiers, water purifiers, mineral water production machines, etc. It has been found that the organic substances such as unburned substances contained in each of these agents can be reduced to 2% by weight or less, while maximizing the above. Therefore, activated carbon, zeolite, ceramics, shell fossils, coral stones, it is possible to eliminate the elution phenomenon of various miscellaneous bacteria generated from organic matter contained in barite, activated carbon, zeolite, ceramics, shell fossils, coral stone, It was found that each agent such as barley stone can be used as a stable and reliable adsorbent, filter, mineral eluent, etc. for a water purifier, a water purifier, a mineral water production machine, etc. FIG. 2 is a block diagram showing processing steps according to a processing method of an embodiment different from the processing method shown in FIG. The processing method of this embodiment is as follows.
The first step of heating and / or calcining the raw material 1, that is, an adsorbent composed of activated carbon, zeolite, ceramic, shell fossil, coral stone, barley stone, etc., a filtering agent, a mineral eluent, and then activated carbon, zeolite, The second step of reheating the adsorbent made of ceramics, shell fossils, coral stones, barley stones, etc., the filtering agent, the mineral eluent, and the adsorbent made of activated carbon, zeolite, ceramics, shell fossils, coral stones, barley stones, etc. Cooling filters, filters and mineral eluents in zero ozone atmosphere
And a process. After these treatment steps, activated carbon, zeolite, ceramics, fossil shells, coral stone, adsorbent as a product made of barite stone, filter agent,
The mineral eluent 3 can be obtained. Heating and / or firing temperature, heating and / or firing time during the first step,
The number of times of heating and / or calcination should maximize the adsorption and elution characteristics of adsorbents, filtration agents, activated carbon used as mineral eluents, zeolites, ceramics, shell fossils, coral stones, barley stones, etc. Is selected from the range that is possible, and is not particularly limited. However, the heating and / or firing temperature during the above treatment step is 500 ° C.,
It is suitable that the heating and / or firing time is 15 minutes and the heating and / or firing is performed once. Further, the reheating temperature in the second step may drive off the malodorous molecules, components and gases such as adsorbents, filtering agents, activated carbon used as mineral eluents, zeolites, ceramics, fossil shells, coral stones and barley stones. It is selected from the possible range and is not particularly limited, but in this case, 350 ° C. is suitable. Further, in the third step, while adsorbent, filtering agent, activated carbon used as a mineral eluent, zeolite, ceramic, shell fossil, coral stone, barley stone, etc. are irradiated with electromagnetic waves and / or appropriate ozone generation. Ozone is collected from the container and processed. A suitable cooling temperature in this case is 50 ° C.
After the treatment in the first step, as described in the embodiment shown in FIG. 1, activated carbon and zeolite used as adsorbents, filter agents, mineral eluents in water purifiers, water purifiers, mineral water producing machines, etc. , Ceramic, shell fossil, coral stone,
Since it is possible to maximize the adsorption characteristics, elution characteristics, etc. possessed by barley stone, etc., and the organic substances such as unburned substances contained in each of these agents can be reduced to 2% by weight or less, activated carbon, zeolite, It is possible to eliminate the elution phenomenon of various bacteria generated from organic substances contained in ceramics, shell fossils, coral stones, barley stones, etc., and activated carbon, zeolite, ceramics, shell fossils, coral stones, barley stones, etc. Stable and stable adsorbent, filtration agent,
It has been found that it can be used in water purifiers, water purifiers, mineral water production machines, etc. as a mineral eluent. Next, after the treatment of the second step, an adsorbent, a filtering agent, activated carbon used as a mineral eluent in a water purifier, zeolite, ceramic,
It is possible to drive off malodorous molecules, components and gases such as shellfish fossils, coral stones and barley stones. After the treatment of the third step, activated carbon,
Ozone can be effectively adsorbed on zeolite, ceramics, shell fossils, coral stones, barley stones, etc., and ozone can be retained in the pores of each agent for a long period of time. Activated carbon, zeolite, ceramic,
When fossil shells, coral stones, barley stones, etc. are used in a water purifier, etc., sterilization and sterilization effects can be exhibited.As a result, germs are generated in the water purifier, water purifier, mineral water production machine. Since it can suppress the increase and prevent the generation of bad odor, each agent such as activated carbon, zeolite, ceramics, fossil shells, coral stones, barley stones is stable for a long period of time, and a reliable adsorbent, filtering agent, mineral elution It was found that it can be used as a chemical agent in water purifiers, water purification machines, mineral water production machines, etc. The present invention is not limited to the above-described embodiments, but various modifications can be made within the scope of the invention.
【発明の効果】以上詳述した本発明によれば、以下の各
効果を奏する。請求項１乃至３記載の発明によれば、浄
水機、精水機、ミネラル水製造機等に吸着剤、濾過剤、
ミネラル溶出剤として用いられる活性炭、ゼオライト、
セラミック、貝化石、サンゴ石、麦飯石等が有する吸着
特性、溶出特性等を最大限に引き出すことができると共
に、これらの各剤に含有されている未燃焼物などの有機
物を２乃至５重量％以下に減少できるので、活性炭、ゼ
オライト、セラミック、貝化石、サンゴ石、麦飯石等に
含有されている有機物から発生する種々の雑菌の溶出現
象を解消することができることから、活性炭、ゼオライ
ト、セラミック、貝化石、サンゴ石、麦飯石等の各剤を
長期にわたって安定、安心した吸着剤、濾過剤、ミネラ
ル溶出剤等として浄水機、精水機、ミネラル水製造機等
に使用することができる。請求項４乃至９記載の発明に
よれば、前記請求項１記載の発明の効果とともに、浄水
機等に吸着剤、濾過剤、ミネラル溶出剤として用いられ
る活性炭、ゼオライト、セラミック、貝化石、サンゴ
石、麦飯石等の悪臭分子、成分、ガスを追い出すことが
でき、しかも、活性炭、ゼオライト、セラミック、貝化
石、サンゴ石、麦飯石等にオゾンを効果的に吸着させる
ことができ、当該各剤の細孔中にオゾンを長期間保持さ
せることが可能であるので、活性炭、ゼオライト、セラ
ミック、貝化石、サンゴ石、麦飯石等を浄水機等に入れ
て使用した場合、殺菌、除菌効果を発揮させることがで
きる結果、浄水機、精水機、ミネラル水製造機の中で雑
菌の発生、増加を抑え、且つ、悪臭の発生を防ぐことが
できることから、活性炭、ゼオライト、セラミック、貝
化石、サンゴ石、麦飯石等の各剤を長期にわたって安
定、安心した吸着剤、濾過剤及びミネラル溶出剤等とし
て浄水機、精水機、ミネラル水製造機等に使用すること
ができる。According to the present invention described in detail above, the following respective effects are exhibited. According to the inventions of claims 1 to 3, an adsorbent, a filtering agent, a water purifier, a water purifier, a mineral water producing machine, etc.
Activated carbon, zeolite, used as a mineral eluent
It is possible to maximize the adsorption and elution characteristics of ceramics, fossil shells, coral stones, barley stones, etc., and the organic substances such as unburned substances contained in these agents are 2 to 5% by weight. Since it can be reduced to the following, activated carbon, zeolite, ceramics, fossil shells, coral stones, since it is possible to eliminate the elution phenomenon of various miscellaneous bacteria generated from organic matter contained in barite stone, activated carbon, zeolite, ceramic, Each agent such as shellfish fossil, coral stone, and barley stone can be used as a stable and reliable adsorbent, filter agent, mineral eluent, etc. for water purifiers, water purifiers, mineral water production machines, etc. According to the inventions of claims 4 to 9, along with the effect of the invention of claim 1, activated carbon used as an adsorbent, a filtering agent, a mineral eluent for a water purifier, etc., zeolite, ceramics, fossil shells, and coral stones. , It is possible to drive off malodorous molecules, components, gas such as barley stone, and furthermore, it is possible to effectively adsorb ozone to activated carbon, zeolite, ceramics, shell fossils, coral stones, barley stone, etc. Since ozone can be retained in the pores for a long period of time, when activated carbon, zeolite, ceramics, shell fossils, coral stones, barley stones, etc. are used in a water purifier, etc., they show sterilization and sterilization effects. As a result, it is possible to suppress the generation and increase of various bacteria in the water purifier, the water purifier, and the mineral water production machine and prevent the generation of bad odor. It can be used for water purifiers, water purifiers, mineral water production machines, etc. as adsorbents, filters, mineral eluents, etc. that are stable and reliable for a long period of time, such as ku, shell fossil, coral stone, barley stone, etc. .
【図１】本発明の実施例に係る処理方法の処理工程を示
すブロック図である。FIG. 1 is a block diagram showing processing steps of a processing method according to an embodiment of the present invention.
【図２】本発明の異なる実施例に係る処理方法の処理工
程を示すブロック図である。FIG. 2 is a block diagram showing processing steps of a processing method according to another embodiment of the present invention.
１ 原料（活性炭、ゼオライト、セラミック、貝化石、
サンゴ石、麦飯石等） ２ 本発明の処理工程の後、活性炭、ゼオライト、セラ
ミック、貝化石、サンゴ石、麦飯石等からなる製品とし
ての吸着剤、濾過剤、ミネラル溶出剤 ３ 本発明の処理工程の後、活性炭、ゼオライト、セラ
ミック、貝化石、サンゴ石、麦飯石等からなる製品とし
ての吸着剤、濾過剤、ミネラル溶出剤1 Raw materials (activated carbon, zeolite, ceramics, fossil shells,
2 Coral stone, barley stone, etc.) 2 After the treatment step of the present invention, an adsorbent as a product comprising activated carbon, zeolite, ceramics, fossil shells, coral stone, barley stone, etc., a filtering agent, a mineral eluent 3 The treatment of the present invention After the process, adsorbent, filter agent, mineral eluent as a product consisting of activated carbon, zeolite, ceramics, fossil shellfish, coral stone, barite stone, etc.
───────────────────────────────────────────────────── 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 Ｃ０２Ｆ 1/68 ５２０ Ｖ Ｍ Ｐ Ｋ Ｎ ５４０ Ａ Ｚ ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location C02F 1/68 520 V MP K N 540 AZ
Claims (9)
いられる活性炭、ゼオライト、セラミック、貝化石、サ
ンゴ石、麦飯石等からなる吸着剤、濾過剤、ミネラル溶
出剤の使用前の処理方法であって、原料１、即ち、活性
炭、ゼオライト、セラミック、貝化石、サンゴ石、麦飯
石等からなる吸着剤、濾過剤、ミネラル溶出剤を加熱及
び／又は焼成する工程からなる浄水機等に用いる吸着
剤、濾過剤、ミネラル溶出剤の処理方法。1. An adsorbent comprising activated carbon, zeolite, ceramics, shell fossils, coral stones, barley stones, etc. used in water purifiers, water purifiers, mineral water producing machines, etc. A treatment method, which is a water purifier including a step of heating and / or firing a raw material 1, that is, an adsorbent composed of activated carbon, zeolite, ceramic, shell fossil, coral stone, barley stone, etc., a filtering agent, and a mineral eluent A method for treating adsorbents, filters, and mineral eluents used in.
度、加熱及び／又は焼成時間、加熱及び／又は焼成の回
数は、吸着剤、濾過剤、ミネラル溶出剤として用いられ
る活性炭、ゼオライト、セラミック、貝化石、サンゴ
石、麦飯石等が有する吸着特性、溶出特性等を最大限に
引き出すことが可能な範囲から選ばれるものである請求
項１記載の浄水機等に用いる吸着剤、濾過剤、ミネラル
溶出剤の処理方法。2. The heating and / or calcination temperature, the heating and / or calcination time, and the number of times of the heating and / or calcination in the treatment step are as follows: adsorbent, filter agent, activated carbon used as mineral eluent, zeolite, ceramic The adsorbent used in the water purifier or the like according to claim 1, which is selected from the range capable of maximizing the adsorption characteristics, elution characteristics, and the like of shellfish fossils, coral stones, barley stones, and the like. Treatment method of mineral eluent.
は３００℃乃至５００℃で、加熱及び／又は焼成時間は
１５分乃至３０分間で、加熱及び／又は焼成の回数は１
回乃至３回である請求項１記載の浄水機等に用いる吸着
剤、濾過剤、ミネラル溶出剤の処理方法。3. The heating and / or firing temperature in the treatment step is 300 ° C. to 500 ° C., the heating and / or firing time is 15 minutes to 30 minutes, and the number of times of heating and / or firing is 1.
The method for treating an adsorbent, a filtering agent, and a mineral eluent used in a water purifier or the like according to claim 1, which is performed 3 to 3 times.
いられる活性炭、ゼオライト、セラミック、貝化石、サ
ンゴ石、麦飯石等からなる吸着剤、濾過剤、ミネラル溶
出剤の使用前の処理方法であって、原料１、即ち、活性
炭、ゼオライト、セラミック、貝化石、サンゴ石、麦飯
石等からなる吸着剤、濾過剤、ミネラル溶出剤を加熱及
び／又は焼成する第１工程と、次に、活性炭、ゼオライ
ト、セラミック、貝化石、サンゴ石、麦飯石等からなる
吸着剤、濾過剤、ミネラル溶出剤を再加熱する第２工程
と、最後に、活性炭、ゼオライト、セラミック、貝化
石、サンゴ石、麦飯石等からなる吸着剤、濾過剤、ミネ
ラル溶出剤をオゾン零囲気中で冷却する第３工程とを具
備してなる浄水機等に用いる吸着剤、濾過剤、ミネラル
溶出剤の処理方法。4. An adsorbent comprising activated carbon, zeolite, ceramics, shell fossils, coral stones, barley stones, etc. used in water purifiers, water purifiers, mineral water producing machines, etc. A treatment method, which is a first step of heating and / or firing a raw material 1, that is, an adsorbent made of activated carbon, zeolite, ceramic, shell fossil, coral stone, barley stone, etc., a filtering agent, and a mineral eluent, and The second step is to reheat the adsorbent consisting of activated carbon, zeolite, ceramic, shell fossil, coral stone, barley stone, etc., filter agent, mineral eluent, and finally activated carbon, zeolite, ceramic, shell fossil, coral. Adsorbent, filter agent, mineral eluent treatment method used in a water purifier or the like, which comprises a third step of cooling an adsorbent composed of stones, barley stones, etc., in a zero ozone atmosphere .
温度、加熱及び／又は焼成時間、加熱及び／又は焼成の
回数は、吸着剤、濾過剤、ミネラル溶出剤として用いら
れる活性炭、ゼオライト、セラミック、貝化石、サンゴ
石、麦飯石等が有する吸着特性、溶出特性等を最大限に
引き出すことが可能な範囲から選ばれるものである請求
項４記載の浄水機等に用いる吸着剤、濾過剤、ミネラル
溶出剤の処理方法。5. The heating and / or calcination temperature, the heating and / or calcination time, and the number of times of the heating and / or calcination in the first step are the adsorbent, the filtering agent, activated carbon used as a mineral eluent, zeolite, and ceramic. 5. An adsorbent used in a water purifier or the like according to claim 4, which is selected from the range capable of maximizing the adsorption characteristics, elution characteristics and the like of shellfish fossils, coral stones, barley stones, etc. Treatment method of mineral eluent.
温度は３００℃乃至５００℃で、加熱及び／又は焼成時
間は１５分乃至３０分間で、加熱及び／又は焼成の回数
は１回乃至３回である請求項４記載の浄水機等に用いる
吸着剤、濾過剤、ミネラル溶出剤の処理方法。6. The heating and / or firing temperature in the first step is 300 ° C. to 500 ° C., the heating and / or firing time is 15 minutes to 30 minutes, and the heating and / or firing times are 1 to 3 times. The method for treating an adsorbent, a filter, and a mineral eluent used in a water purifier according to claim 4, which is a cycle.
剤、濾過剤、ミネラル溶出剤として用いられる活性炭、
ゼオライト、セラミック、貝化石、サンゴ石、麦飯石等
の悪臭分子、成分、ガスを追い出すことが可能範囲から
選ばれるものである請求項４記載の浄水機等に用いる吸
着剤、濾過剤、ミネラル溶出剤の処理方法。7. The reheating temperature in the second step is the adsorbent, the filtering agent, the activated carbon used as a mineral eluent,
The adsorbent, filter agent, mineral elution for use in a water purifier or the like according to claim 4, which is selected from a range capable of expelling malodorous molecules, components, and gases of zeolite, ceramics, fossil shells, coral stones, barley stones, etc. Agent treatment method.
０℃乃至５００℃である請求項４記載の浄水機等に用い
る吸着剤、濾過剤、ミネラル溶出剤の処理方法。8. The reheating temperature in the second step is 30.
The method for treating an adsorbent, a filtering agent, and a mineral eluent used in a water purifier according to claim 4, which has a temperature of 0 ° C to 500 ° C.
ル溶出剤として用いられる活性炭、ゼオライト、セラミ
ック、貝化石、サンゴ石、麦飯石等を冷却しながら電磁
波の照射及び／又は適宜のオゾン発生器からオゾンを採
取して処理するものであり、この場合の冷却温度は、１
００℃乃至５０℃である請求項４記載の浄水機等に用い
る吸着剤、濾過剤、ミネラル溶出剤の処理方法。9. The third step is to irradiate an electromagnetic wave and / or appropriately while cooling an adsorbent, a filtering agent, activated carbon used as a mineral eluent, zeolite, ceramic, shell fossil, coral stone, barley stone, etc. The ozone is collected from the ozone generator and processed. The cooling temperature in this case is 1
The method for treating an adsorbent, a filtering agent, and a mineral eluent used in a water purifier according to claim 4, which has a temperature of 00 ° C to 50 ° C.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19907194A JPH0838894A (en) | 1994-08-01 | 1994-08-01 | Treatment of adsorbent, filter agent and mineral ellution agent used in water purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19907194A JPH0838894A (en) | 1994-08-01 | 1994-08-01 | Treatment of adsorbent, filter agent and mineral ellution agent used in water purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0838894A true JPH0838894A (en) | 1996-02-13 |
Family
ID=16401629
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19907194A Pending JPH0838894A (en) | 1994-08-01 | 1994-08-01 | Treatment of adsorbent, filter agent and mineral ellution agent used in water purifier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0838894A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100402294B1 (en) * | 2001-03-09 | 2003-10-22 | 대한민국 | Bio-media and the production method therefor |
| KR100429915B1 (en) * | 2002-02-01 | 2004-05-03 | 김고정 | Additives for waste-water treatment |
| JP2018123069A (en) * | 2017-01-30 | 2018-08-09 | 葭田 隆治 | Antibacterial active material and fertilizer prepared therewith |
| CN108744728A (en) * | 2018-05-21 | 2018-11-06 | 中国地质大学（武汉） | A kind of natural weak alkali complex mineral sintering activity filtration core and preparation method thereof |
| CN111777199A (en) * | 2020-07-14 | 2020-10-16 | 东莞乔隆家具配件制品有限公司 | Scale-inhibiting sintered carbon rod and preparation method thereof |
-
1994
- 1994-08-01 JP JP19907194A patent/JPH0838894A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100402294B1 (en) * | 2001-03-09 | 2003-10-22 | 대한민국 | Bio-media and the production method therefor |
| KR100429915B1 (en) * | 2002-02-01 | 2004-05-03 | 김고정 | Additives for waste-water treatment |
| JP2018123069A (en) * | 2017-01-30 | 2018-08-09 | 葭田 隆治 | Antibacterial active material and fertilizer prepared therewith |
| CN108744728A (en) * | 2018-05-21 | 2018-11-06 | 中国地质大学（武汉） | A kind of natural weak alkali complex mineral sintering activity filtration core and preparation method thereof |
| CN111777199A (en) * | 2020-07-14 | 2020-10-16 | 东莞乔隆家具配件制品有限公司 | Scale-inhibiting sintered carbon rod and preparation method thereof |
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