JPH04210292A - Bactericidal filtering device and production of bactericidal filter bed used therefor - Google Patents

Bactericidal filtering device and production of bactericidal filter bed used therefor

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Publication number
JPH04210292A
JPH04210292A JP2401896A JP40189690A JPH04210292A JP H04210292 A JPH04210292 A JP H04210292A JP 2401896 A JP2401896 A JP 2401896A JP 40189690 A JP40189690 A JP 40189690A JP H04210292 A JPH04210292 A JP H04210292A
Authority
JP
Japan
Prior art keywords
filter
silver chloride
silver
water
filter bed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2401896A
Other languages
Japanese (ja)
Inventor
Toshihide Maeda
俊秀 前田
Masashi Yamaguchi
雅司 山口
Masahide Iura
井浦 征英
Yasushi Takahara
高原 康
Takamitsu Nakayama
中山 隆充
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP2401896A priority Critical patent/JPH04210292A/en
Publication of JPH04210292A publication Critical patent/JPH04210292A/en
Pending legal-status Critical Current

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  • Coating By Spraying Or Casting (AREA)

Abstract

PURPOSE:To be porous the Ag carried on a resin filter, to be easily chlorinated and to make it favorable as a bactericidal filter bed by carrying silver chloride on the filter bed consisting of a porous ceramic plate or the resin filter, etc., or a filter material consisting of ceramic particles, etc. CONSTITUTION:Warm water being flowed in from a raw water inflow pipe 7 is eliminated large dusts, etc., with a flow straighting plate 17 consisting of the porous ceramic plate to simultaneously distribute the raw water on the filter material 16 consisting of ceramic particles or glass carried with silver chloride distributed on the bed 17 without carrying silver chloride, to almost uniformly supply the water to eliminate small dusts and scales, etc., and simultaneously to sterilize the water. The purified warm water is cycled from a purification discharge pipe 8 to a water bath 1. When the filter bed 17 is made from the resin filter or the porous ceramic plate carried with silver chloride, even though the particles such as ceramic particles of glass beads, not carrying silver chloride are used for the filter material 16, the water is sterilized and purified as well. The silver carried on the resin filter is porous and it is easily chlorinated and it becomes suitable as a bactericidal filter bed.

Description

【発明の詳細な説明】[Detailed description of the invention]

[00011 [00011

【産業上の利用分野]本発明は、浴用等の循環温水器に
用いられる温水浄化用の殺菌濾過装置及びそれに使用す
る殺菌濾床の製造方法に関するものである。 [0002] 【従来の技術】近年、バスライフへの関心が高まり常時
入浴できる浴槽システムとして浴用温水循環装置が開発
されている。浴用温水循環装置はその性格上、温水浄化
用の殺菌濾過装置が必要とされ種々提案されている。 [0003]以下に従来の殺菌濾過装置について説明す
る。図3は一般的な浴用の温水循環装置の概略構成図で
あり、図4は従来の殺菌濾過装置の要部断面図である。 1は浴槽、2は髪毛等大きなゴミを濾過するフィルタを
備えた吸込口、3は浄化された温水の吐出口、4は吸込
管、5は温水を循環させるためのポンプ、6はポンプ5
から送られた温水の微細なゴミや湯垢を濾過したり殺菌
する温水浄化用の殺菌濾過装置、7はポンプ5の吐出側
と殺菌濾過装置6の原水入口側とを接続する原水流入管
、8は浄化水吐出管である。図4において、9は殺菌濾
過槽、10はオゾン等の発生器や紫外線殺菌灯等の殺菌
手段、11はゼオライト、活性炭等からなる濾材、12
は濾材11を保持する多孔質セラミック板や樹脂フィル
タからなる濾床、13は水の流れを制御する分流板であ
る。 [0004]以上のように構成された従来の殺菌濾過装
置について、以下その殺菌濾過方法を説明する。原水流
入管7より流入した温水は、分流板13である程度整流
さねゼオライト等の濾材11上に給水され、濾材11で
細菌を吸着したり微細なゴミや湯垢を濾過し、また、濾
槽内にオゾン、紫外線の殺菌手段10で殺菌し、浄化水
吐出管8から浴槽1へ浄化され殺菌された温水を供給し
、衛生的に保つようになっている。 [00051次に、従来の銀の担持方法について説明す
る。図5は従来のアーク溶射装置の要部断面図である。 20.21は銀ワイヤでこれら各々に電圧がかけられて
いる。22は空気吹き出しノズル、23はアーク溶射装
置である。 [0006]以上のように構成された従来のアーク溶射
装置による銀の担持方法について説明する。銀ワイヤ2
0.21はアーク溶射装置23の先端で接触し、各々に
電圧がかかっているため接点が高温になり溶融銀24が
できる。この溶融銀24をノズル22からの空気流で被
射体25に吹き付けて担持させていた。 [0007]
[Field of Industrial Application] The present invention relates to a sterilizing filtration device for purifying hot water used in circulating water heaters for baths and the like, and a method for manufacturing a sterilizing filter bed used therein. [0002] In recent years, interest in bath life has increased, and hot water circulation devices for baths have been developed as bathtub systems that allow bathing at all times. Due to its nature, hot water circulation devices for baths require a sterilizing filtration device for hot water purification, and various proposals have been made. [0003] A conventional sterilizing filtration device will be explained below. FIG. 3 is a schematic configuration diagram of a general bath hot water circulation device, and FIG. 4 is a sectional view of a main part of a conventional sterilizing filtration device. 1 is a bathtub, 2 is a suction port equipped with a filter for filtering out large debris such as hair, 3 is a discharge port for purified hot water, 4 is a suction pipe, 5 is a pump for circulating hot water, and 6 is a pump 5
7 is a raw water inflow pipe connecting the discharge side of the pump 5 and the raw water inlet side of the sterilizing filtration device 6; 8; is the purified water discharge pipe. In FIG. 4, 9 is a sterilizing filter tank, 10 is a sterilizing means such as an ozone generator or an ultraviolet germicidal lamp, 11 is a filter material made of zeolite, activated carbon, etc., and 12 is a sterilizing filter tank.
1 is a filter bed made of a porous ceramic plate or a resin filter that holds the filter medium 11, and 13 is a flow dividing plate that controls the flow of water. [0004] The sterilizing filtration method of the conventional sterilizing filtration device configured as described above will be explained below. Hot water flowing in from the raw water inflow pipe 7 is rectified to some extent by a flow divider plate 13 and is supplied onto a filter medium 11 such as zeolite, which adsorbs bacteria and filters fine dust and scale. The water is then sterilized by ozone and ultraviolet sterilization means 10, and purified and sterilized hot water is supplied from the purified water discharge pipe 8 to the bathtub 1 to maintain sanitary conditions. [00051] Next, a conventional method for supporting silver will be explained. FIG. 5 is a sectional view of a main part of a conventional arc thermal spraying apparatus. 20 and 21 are silver wires, each of which is energized. 22 is an air blowing nozzle, and 23 is an arc spraying device. [0006] A method of supporting silver using the conventional arc spraying apparatus configured as described above will be described. silver wire 2
0.21 contacts at the tip of the arc spraying device 23, and since a voltage is applied to each, the contact points become high temperature and molten silver 24 is formed. This molten silver 24 was blown onto the target object 25 with an air flow from the nozzle 22 to be carried thereon. [0007]

【発明が解決しようとする課題】しかしながら上記従来
の構成では、温水の循環を停止すると、ゼオライトや活
性炭への細菌の吸着は当然のことながら全く行われず、
また、紫外線やオゾンは濾槽内を殺菌しても浴槽内の温
水は殺菌することができず、その結果、浴槽内に細菌が
繁殖し、湯垢が溜まりヌメリ等が生じ、悪臭を発生させ
るという問題点を有していた。 [0008]また、浴槽内の温水を排水させた際、温水
循環システムの保護のため、また凍結により濾槽が破壊
されるのを防止するため濾槽内に濾材が浸漬する程度に
湯水を残存させるようになっているが、この際、残存水
に細菌が繁殖し、湯垢や悪臭が発生するという問題点が
あった。更に、オゾンや塩素等による殺菌では、温水中
のそれらの残存物の人体やシステム機器への悪影響が懸
念されるという問題点を有していた。 [0009]また、従来の銀の担持方法による殺菌濾床
の製造方法では、溶融された銀は、搬送空気流で冷却さ
れるので、溶融部分の温度を高温にする必要がある。耐
熱性のない易燃性の樹脂製フィルタに銀を担持させる場
合、溶融された銀を適度に冷却するため溶射ガンと被射
体との間に所定の距離を保ちながら溶射しなければなら
なかった。その結果、銀の均一な担持膜を得ることが不
可能で、かつ、銀の温度が高すぎたり冷却されすぎたり
して密着性にむらができ、担持した銀が剥離するという
問題点を有し、特に、耐熱性に乏しい樹脂製フィルタに
は摘要が困難であった。従って、銀を担持した樹脂製フ
ィルタを塩素化処理して殺菌濾床を工業的に製造するこ
とは不可能であった。 [00101本発明は上記従来の問題点を解決するもの
で、殺菌効果を持続させた衛生的で快適なパスライフを
約束する殺菌濾過装置及びそれに使用する殺菌濾床の製
造方法を提供することを目的とする。 [0011]
[Problems to be Solved by the Invention] However, in the above conventional configuration, when the circulation of hot water is stopped, bacteria are naturally not adsorbed to the zeolite or activated carbon at all.
Furthermore, even if ultraviolet rays and ozone sterilize the inside of the filter tank, they cannot sterilize the hot water in the bathtub, and as a result, bacteria breed in the bathtub, causing scale to build up, slime, etc., and a bad odor. It had some problems. [0008] Also, when the hot water in the bathtub is drained, the hot water remains in the bathtub to the extent that the filter material is immersed in the filter tank in order to protect the hot water circulation system and to prevent the filter tank from being destroyed by freezing. However, when doing so, there was a problem in that bacteria grew in the remaining water, causing scale and bad odors. Furthermore, sterilization using ozone, chlorine, etc. has a problem in that there is concern that residual substances in hot water may have an adverse effect on the human body and system equipment. [0009] Furthermore, in the method for manufacturing a sterilizing filter bed using the conventional silver supporting method, the molten silver is cooled by the conveying air flow, so it is necessary to raise the temperature of the molten part to a high temperature. When silver is supported on a flammable resin filter that is not heat resistant, it is necessary to maintain a predetermined distance between the spray gun and the object in order to cool the molten silver appropriately. Ta. As a result, it is impossible to obtain a uniform silver support film, and the silver temperature becomes too high or the silver is cooled too much, resulting in uneven adhesion and peeling of the supported silver. However, it has been particularly difficult to summarize the results for resin filters that have poor heat resistance. Therefore, it has been impossible to industrially produce a sterilizing filter bed by chlorinating a resin filter carrying silver. [00101 The present invention solves the above-mentioned conventional problems, and aims to provide a sterilizing filtration device that promises a hygienic and comfortable pass life with a sustained sterilizing effect, and a method for manufacturing a sterilizing filter bed used therein. purpose. [0011]

【課題を解決するための手段】この目的を達成するため
に本発明の殺菌濾過装置及びそれに使用する殺菌濾床の
製造方法は、温水中に溶存し殺菌効果を継続発揮する塩
化銀を多孔質セラミック板や樹脂製フィルタ等からなる
濾床やセラミック粒状物等からなる濾材に担持させたも
のを殺菌濾過装置に使用するようにしたものである。ま
た、低温熔射法を用いることにより耐熱性に欠ける樹脂
製フィルタ上に銀を担持させ、次いで担持した銀を塩素
化させて殺菌濾床を製造することからなる構成を有して
いる。 [0012]
[Means for Solving the Problems] In order to achieve this object, the sterilizing filtration device of the present invention and the method for manufacturing the sterilizing filter bed used therein provide a method for manufacturing a sterilizing filter bed using silver chloride dissolved in hot water and continuously exhibiting a sterilizing effect. The filter is supported on a filter bed made of a ceramic plate, a resin filter, etc., or a filter medium made of ceramic particles, etc., and is used in a sterilizing filtration device. Further, it has a structure in which silver is supported on a resin filter lacking in heat resistance by using a low-temperature spraying method, and then the supported silver is chlorinated to produce a sterilizing filter bed. [0012]

【作用】この構成によって、濾床や濾材に塩化銀を担持
しているので、循環温水器の運転の有無にかかわらず、
塩化銀が温水中に溶出し、銀イオンが雑菌を殺菌するの
で浴槽内は常に清潔に保たれる。また、耐熱性に欠は銀
の担持が不可能であった樹脂製フィルタに低温熔射法を
用いることにより、必要量の銀を樹脂製フィルタの表面
全面に均一に担持することが可能となった。樹脂製フィ
ルタ上に担持された銀はポーラスなので、容易に塩素化
ができ、殺菌濾床として好適な樹脂製フィルタを得るこ
とができた。 [0013]
[Operation] With this configuration, silver chloride is supported on the filter bed and filter medium, so regardless of whether the circulating water heater is operating or not,
Silver chloride is eluted into the hot water, and the silver ions kill germs, keeping the bathtub clean at all times. In addition, by using a low-temperature spraying method on resin filters, which were unable to support silver due to their lack of heat resistance, it became possible to uniformly support the required amount of silver over the entire surface of the resin filter. Ta. Since the silver supported on the resin filter is porous, it can be easily chlorinated, making it possible to obtain a resin filter suitable as a sterilizing filter bed. [0013]

【実施例】以下本発明の一実施例について、図面を参照
しながら説明する。 [00141図1は殺菌濾過装置の要部断面図である。 7は原水流入管、8は浄化水流出管、9は殺菌濾過槽、
13は分流板であり、これらは従来例と同様のものであ
るので、同一の番号を付し説明を省略する。14は原水
流入管7からの温水を整流分配するとともに、大小のゴ
ミや湯垢を濾過する多孔質セラミック板からなる整流板
である。尚、整流板14に必要により銀を担持させたも
のを用いてもよい。15は整流板14の固定具、16は
塩化銀が担持された、又は担持されていないセラミック
粒状物やガラスピーズ等の細粒状物からなる濾材、17
は濾材16を保持するための濾床で塩化銀を担持した多
孔質セラミック板や樹脂製フィルタ等からなる。多孔質
セラミック板や樹脂フィルタへの塩化銀の担持量は多け
れば多い程殺菌効果が持続し耐久性が増すので好ましい
が、反面多すぎると孔隙率が低下し、圧損が大きくなり
、濾槽等に過大の圧力が加わり破損の虞があるので、殺
菌濾過装置の大小等に応じて適宜選択されるが一般的に
は0. 1 g/cm2〜10 g/cm2程度が望ま
しい。また、セラミック粒状物等への銀の担持は、セラ
ミック粒状物を銀イオン含有溶液中に浸漬後、これに塩
素イオンを反応させる化学的方法やセラミック粒状物や
ガラスピーズを展着オイル(例えば、スキージ−オイル
(末筆色素化学工業(株)製)と塩化銀粉末の所定量を
混合したペーストでコーテイング後焼成して塩化銀膜を
表面に融着させてもよい(以下、焼成法という)。 [0015]次に、樹脂製フィルタからなる殺菌濾床の
製造方法について説明する。図2は本発明の製造方法の
一実施例における低温溶射装置の要部断面図である。2
0.21は電圧をかけられた銀ワイヤ、24は溶融銀、
25は樹脂製フィルタからなる被射体であり、26は低
温溶射装置、27は低温溶射装置26の先端部に嵌装さ
れた空気噴出用のノズルである。銀ワイヤ20.21が
接触すると電圧がかかっているため接点が高温になり溶
融銀24ができる。これにノズル27から空気を噴出す
ると、溶融銀24の前方で円錐状の減圧層(一般的には
0.7kg/cm2が形成され、溶融銀24は減圧層に
吸弓され、5〜150μmに粉砕微粒子化される。そし
てこの瞬間に銀の粒子温度は平均溶融温度の約1/10
程度に冷却されて、更に被射体25までの距離を移動す
る間に冷却されて被射体25に吹き付けられ担持される
。 [0016]次に、銀を担持した樹脂製フィルタは塩素
化工程で塩素化される。塩素化工程としては、例えば、
銀を担持した樹脂製フィルタを6%次亜塩素酸ナトリウ
ム溶液に約1時間攪拌浸漬し、溶射銀の塩素化を行った
後、充分乾燥するか、または、溶射銀を塩素ガス雰囲気
下にさらして行う等により行われる。 [0017]尚、多孔質セラミック板への塩化銀の担持
は、前述したセラミック粒状物への担持法、すなわち焼
成法等でもよいが、アーク溶射法や低温熔射法により直
接銀を担持した後塩素化してもよい。 [0018]以上のように構成された本実施例の殺菌濾
過装置について、以下その使用方法を説明する。原水流
入管7より流入した温水は、多孔質セラミック板からな
る整流板14で大きなゴミ等を濾過すると共に、塩化銀
を担持しない濾床17上に敷設散布された塩化銀を担持
したセラミック粒やガラスピーズ等からなる濾材16上
に原水を分配して略均−に給水し、小さなゴミや湯垢等
を濾過すると共に、殺菌し、浄化水吐出管8から浴槽1
へ浄化された温水を循環する。濾床17が塩化銀で担持
された樹脂製フィルタや多孔質セラミック板であるとき
は、濾材16は塩化銀を担持しないセラミック粒やガラ
スピーズ等の粒状物を使用しても同様に殺菌浄化される
。 [00191次に、本発明の殺菌濾過装置と、従来例の
ものとを、実施例及び比較例に基づいて説明する。 [00201 (実施例1) 多孔質セラミック円板(岩尾磁器工業(株)製平均孔径
11001L、直径150mm)に、スキージ−オイル
(末筆色素化学工業(株)製)と塩化銀粉末(山中貴金
属(株)製)を各々20g混合し、作成したペーストを
多孔質セラミック板にコーティングし、常温で10分間
放置後、600℃で30分間焼成処理を行った。その結
果スキージ−オイルは完全に分解し、多孔質セラミック
板上に略均−に塩化銀が融着した殺菌濾床が得られた。 この殺菌濾床を図1に示す殺菌濾過装置に装着し、次い
で、平均粒径190μmのガラスピーズ1. 5kgを
前記殺菌濾床上に均一に散布敷設した。濾槽の上部には
、直径が100nunの多孔質セラミック円板からなる
整流板を配設した。二の殺菌濾過装置を浴用循環温水シ
ステムの系内に組み込み、実験を行った。実験条件は、
浴槽に2001の水を注入し、40℃に加熱保温し、次
いで一般細菌を注入し、240時間にわたり温水を連続
的に循環させた。その間、一定時間毎に検水を採取し、
濾過器内の細菌数(一般細菌テスト:普通寒天培地 栄
研化学(株)製)及び銀イオンの溶出量(原子吸光光度
計:日本Jarre I I  Ash  AA−86
0)を測定し、経時変化を求めた。その結果を(表1)
に示す。 [00211 (実施例2) 型枠に張設された樹脂製フィルタの表面に低温熔射法に
より銀17gを均一に溶射させ、室温に冷却後、6%次
亜塩素酸ナトリウム溶液に60分攪拌浸漬し、溶射銀の
塩素化を行った後、60℃の温度で180分間乾燥した
。塩化銀の担持量は20 gであった。この塩化銀を担
持した樹脂製フィルタを実施例1の塩化銀を担持した多
孔質セラミック板と代えて殺菌濾床とした他は、実施例
1と同一の条件で実験を行った。その結果を表1に示す
。 [0022] (比較例1) 実施例1で用いた多孔質セラミック円板を塩化銀の担持
処理をしないで濾床とし、濾槽内に紫外線殺菌灯を設置
した他は実施例1と同一の条件で実験を行った。その結
果を(表1)に示す。 [0023] (比較例2) 実施例1で用いた多孔質セラミック円板を塩化銀の担持
処理をしないて濾床とした他は実施例1と同一の条件で
実験を行った。その結果を(表1)に示す。 [0024]
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings. [00141 FIG. 1 is a sectional view of the main parts of the sterilizing filtration device. 7 is a raw water inflow pipe, 8 is a purified water outflow pipe, 9 is a sterilization filter tank,
Reference numeral 13 denotes a flow divider plate, which is the same as in the conventional example, so the same number will be given and the explanation will be omitted. Reference numeral 14 denotes a rectifier plate made of a porous ceramic plate that rectifies and distributes hot water from the raw water inflow pipe 7 and filters large and small dust and scale. Note that the current plate 14 may be supported with silver if necessary. 15 is a fixing device for the rectifying plate 14; 16 is a filter medium made of fine particles such as ceramic particles or glass beads on which silver chloride is supported or not; 17
A filter bed for holding the filter medium 16 is made of a porous ceramic plate carrying silver chloride, a resin filter, or the like. The larger the amount of silver chloride supported on the porous ceramic plate or resin filter, the better the sterilizing effect will last and the durability will increase, but on the other hand, if it is too large, the porosity will decrease, pressure loss will increase, and the filter tank etc. There is a risk of damage due to excessive pressure being applied to the filter, so the selection is made appropriately depending on the size of the sterilizing filtration device, but generally 0. Approximately 1 g/cm2 to 10 g/cm2 is desirable. Silver can also be supported on ceramic granules by a chemical method in which the ceramic granules are immersed in a silver ion-containing solution and then reacted with chlorine ions, or by spreading the ceramic granules or glass beads with oil (e.g. The silver chloride film may be fused to the surface by coating after coating with a paste made by mixing a predetermined amount of squeegee oil (manufactured by Suefushi Shiki Kagaku Kogyo Co., Ltd.) and silver chloride powder (hereinafter referred to as the baking method). [0015] Next, a method for manufacturing a sterilizing filter bed made of a resin filter will be described. FIG. 2 is a sectional view of a main part of a low temperature thermal spraying apparatus in an embodiment of the manufacturing method of the present invention. 2
0.21 is a voltage applied silver wire, 24 is molten silver,
Reference numeral 25 is a target object made of a resin filter, 26 is a low-temperature spraying device, and 27 is a nozzle fitted to the tip of the low-temperature spraying device 26 for ejecting air. When the silver wires 20, 21 make contact, the contact becomes hot and molten silver 24 is formed due to the voltage applied thereto. When air is ejected from the nozzle 27, a conical reduced pressure layer (generally 0.7 kg/cm2) is formed in front of the molten silver 24, and the molten silver 24 is absorbed by the reduced pressure layer and has a thickness of 5 to 150 μm. At this moment, the silver particle temperature is about 1/10 of the average melting temperature.
It is cooled to a certain extent, and further cooled while traveling the distance to the object 25, and is blown onto the object 25 and carried there. [0016] Next, the resin filter carrying silver is chlorinated in a chlorination step. As the chlorination step, for example,
A resin filter carrying silver is stirred and immersed in a 6% sodium hypochlorite solution for about 1 hour to chlorinate the sprayed silver, and then dried thoroughly, or the sprayed silver is exposed to a chlorine gas atmosphere. This is done by, for example, [0017] Silver chloride may be supported on the porous ceramic plate by the above-mentioned method of supporting on ceramic granules, that is, the firing method, but it is also possible to support silver chloride directly on the porous ceramic plate by an arc spraying method or a low-temperature spraying method. May be chlorinated. [0018] The method of using the sterilizing filtration device of this embodiment configured as described above will be explained below. The hot water that flows in from the raw water inlet pipe 7 is filtered to remove large particles and the like by a rectifying plate 14 made of a porous ceramic plate, and is also filtered with ceramic grains carrying silver chloride and spread over a filter bed 17 that does not carry silver chloride. The raw water is distributed over a filter medium 16 made of glass beads, etc., and the water is supplied approximately evenly, filtering out small dirt, scales, etc., and sterilizing the water.
circulates purified hot water to When the filter bed 17 is a resin filter or porous ceramic plate supported with silver chloride, the filter medium 16 can be sterilized and purified in the same way even if granules such as ceramic grains or glass beads that do not support silver chloride are used. Ru. [00191] Next, the sterilizing filtration device of the present invention and a conventional example will be explained based on Examples and Comparative Examples. [00201 (Example 1) Squeegee oil (manufactured by Suefushi Shiki Kagaku Kogyo Co., Ltd.) and silver chloride powder (Yamanaka Kikinzoku (Yamanaka Kikinzoku) Co., Ltd.) were mixed, and the prepared paste was coated on a porous ceramic plate, left at room temperature for 10 minutes, and then fired at 600° C. for 30 minutes. As a result, the squeegee oil was completely decomposed, and a sterilized filter bed in which silver chloride was fused approximately evenly on the porous ceramic plate was obtained. This sterilizing filter bed was attached to the sterilizing filtration device shown in FIG. 1, and then glass beads 1. 5 kg was evenly spread and laid on the sterilized filter bed. A rectifier plate made of a porous ceramic disk with a diameter of 100 nm was placed above the filter tank. The second sterilizing filtration device was installed in a bath circulation hot water system and an experiment was conducted. The experimental conditions were
2001 water was injected into the bathtub, heated and kept at 40°C, then common bacteria were injected, and the hot water was continuously circulated for 240 hours. During that time, water samples are taken at regular intervals.
The number of bacteria in the filter (general bacteria test: ordinary agar medium, manufactured by Eiken Kagaku Co., Ltd.) and the amount of silver ions eluted (atomic absorption spectrophotometer: Japan Jarre II Ash AA-86)
0) was measured and the change over time was determined. The results (Table 1)
Shown below. [00211 (Example 2) 17 g of silver was uniformly sprayed on the surface of a resin filter stretched over a mold using a low-temperature spraying method, and after cooling to room temperature, it was stirred in a 6% sodium hypochlorite solution for 60 minutes. After immersion and chlorination of the sprayed silver, it was dried at a temperature of 60° C. for 180 minutes. The amount of silver chloride supported was 20 g. An experiment was conducted under the same conditions as in Example 1, except that this silver chloride-supported resin filter was used as a sterilizing filter bed in place of the silver chloride-supported porous ceramic plate of Example 1. The results are shown in Table 1. [0022] (Comparative Example 1) Same as Example 1 except that the porous ceramic disc used in Example 1 was used as a filter bed without being treated to support silver chloride, and an ultraviolet germicidal lamp was installed in the filter tank. The experiment was conducted under the following conditions. The results are shown in (Table 1). [0023] (Comparative Example 2) An experiment was conducted under the same conditions as in Example 1, except that the porous ceramic disc used in Example 1 was used as a filter bed without being subjected to silver chloride support treatment. The results are shown in (Table 1). [0024]

【表1】 [0025]この(表1)から明らかなように、実施例
1、実施例2では温水循環後2時間で細菌は検出されな
かった。尚、比較例1では1時間で細菌は検出されなか
った。比較例2では4時間以降急速に増加した。 [o o 26] (実施例3) 実施例1の実験装備で、かつ同一の条件で、循環温水器
を24時間運転し、た後、72時間運転を停止し、放置
して、その間所定時間待に実施例1と同様に細菌数及び
銀イオンの溶出量を測定し7、その経時変化を求めた。 その結果を(表2)に示す。 [0027] (実施例4) 実施例2の実験装備で、かつ同一の条件で、実施例3と
同様の実験を行った。その結果を(表2)に示す。 [0028] (比較例3) 比較例1の実験装備で、かつ同一の条件で、実施例3と
同様の実験を行った。その結果を(表2)に示す。 [0029] (比較例4) 比較例2の実験装備で、かつ同一の条件で実施例3と同
様の実験を行なった。その結果を(表2)に示す。 [00301 (実施例5) 平均粒径が2mmのセラミック粒1. 5kgを準備し
、実施例1と同様に調整して塩化銀を20g担持させた
ものを濾材として用い、比較例4と同一の条件で実験を
行なった。その結果実施例3と路間−の結果が得られた
。 [00311
[Table 1] [0025] As is clear from this (Table 1), in Examples 1 and 2, no bacteria were detected 2 hours after hot water circulation. In addition, in Comparative Example 1, no bacteria were detected within 1 hour. In Comparative Example 2, it increased rapidly after 4 hours. [o o 26] (Example 3) Using the experimental equipment of Example 1 and under the same conditions, a circulating water heater was operated for 24 hours, and then stopped for 72 hours and left to stand for a specified period of time. First, the number of bacteria and the amount of silver ions eluted were measured in the same manner as in Example 17, and their changes over time were determined. The results are shown in (Table 2). [0027] (Example 4) An experiment similar to Example 3 was conducted using the experimental equipment of Example 2 and under the same conditions. The results are shown in (Table 2). [0028] (Comparative Example 3) Using the experimental equipment of Comparative Example 1 and under the same conditions, an experiment similar to that of Example 3 was conducted. The results are shown in (Table 2). [0029] (Comparative Example 4) An experiment similar to Example 3 was conducted using the experimental equipment of Comparative Example 2 and under the same conditions. The results are shown in (Table 2). [00301 (Example 5) Ceramic grains with an average grain size of 2 mm 1. An experiment was conducted under the same conditions as in Comparative Example 4, using 5 kg of filter material prepared in the same manner as in Example 1 and supporting 20 g of silver chloride as a filter medium. As a result, results similar to those of Example 3 were obtained. [00311

【表2] (0032]  (表2)から明らかなように、実施例
3、実施例4では温水の循環を停止し放置しておいても
細菌は認められない。これは、溶出した銀イオンの殺菌
効果が持続しているためである。比較例3では循環温水
機の運転停止後4時間で細菌の繁殖が認められ、以後等
比級数的に増加していた。これは、紫外線の照射が循環
温水機の運転停止とともに停止し、紫外線による殺菌効
果がなくなったためである。従って、紫外線による殺菌
では、浴槽を使用していなくても常に温水を循環させ紫
外線にさらしておく必要があり著しくエネルギーを消費
することがわかる。 [0033]また、浴槽の温水を排水したとき、循環温
水器は通常、システムの保護、及び、凍結による濾槽の
破壊防止のため濾槽内の温水を濾床が浸漬する程度に水
を残して放置するが、実施例3.4. 5かられかるよ
うに溶出した銀イオンにより細菌の繁殖を防ぐことがで
き、ヌメリの防止、悪臭の防止を図ることができ、再度
浴槽に水を張り入浴しても何ら支障がないことが判る。 [0034]尚、浴槽が大型のときや、入浴者の多い場
合には、整流板に塩化銀を担持した多孔質セラミック板
を使用すると循環温水器使用中は銀イオンの溶出量を飛
躍的に増加させ効果的である。また、塩化銀の担持量が
少ないときは、塩化銀を担持した濾床及び濾材を使用す
ることにより同様の効果が得られる。 [0035] 【発明の効果】以上のように本発明は、濾床又は濾材に
塩化銀を担持させることにより、浴槽の使用中は、大小
のゴミや湯垢等を濾過するだけでなく殺菌効果の高い銀
イオンをエネルギーを消費しないで効率よく浴槽中に供
給することにより細菌の発生を防止し、極めて衛生的で
あり、かつヌメリがないことから浴槽中で滑って事故を
起こすこともなく極めて安全である。 [0036]また、浴槽の湯水の排水時や、湯水を張っ
たまま浴槽を長時間使用しないときでも殺菌性を持続し
、浴槽内等にヌメリや浴室に悪臭を発生することもなく
快適なパスライフを提供できる優れた殺菌濾過装置を実
現できるものである。 [00371更に、低温熔射法と塩素化工程の組合せに
より極めて安定した品質の樹脂製フィルタからなる殺菌
濾床を作業性よく高い生産効率で提供できるようになっ
た。
[Table 2] (0032) As is clear from (Table 2), in Examples 3 and 4, no bacteria were observed even if the circulation of hot water was stopped and the water was left standing. This is because the bactericidal effect of UV irradiation continues.In Comparative Example 3, bacterial growth was observed 4 hours after the circulating water heater was stopped, and the number increased exponentially thereafter. This is because the sterilization effect of ultraviolet rays stopped when the circulating water heater stopped operating, and the sterilizing effect of ultraviolet rays disappeared.Therefore, with sterilizing with ultraviolet rays, it is necessary to constantly circulate hot water and expose it to ultraviolet rays even when the bathtub is not in use, which significantly It can be seen that energy is consumed. [0033] Also, when the hot water in the bathtub is drained, the circulating water heater usually drains the hot water in the filter tank to the filter bed to protect the system and prevent the filter tank from being destroyed by freezing. However, the silver ions eluted from Examples 3, 4, and 5 can prevent bacterial growth, prevent slime, and prevent bad odors. It can be seen that there is no problem even if the bathtub is filled with water and bathed again. Using a ceramic plate is effective because it dramatically increases the amount of silver ions eluted while using a circulating water heater.Also, when the amount of supported silver chloride is small, use a filter bed and filter medium that support silver chloride. [0035] [Effects of the Invention] As described above, the present invention allows silver chloride to be supported on the filter bed or filter medium, thereby preventing large and small dust and scale from being removed while the bathtub is in use. It not only filters the bacteria, but also efficiently supplies silver ions with high sterilization effect into the bathtub without consuming energy, preventing the growth of bacteria. It is extremely safe and does not cause slipping and accidents. [0036] It also maintains its sterilizing properties even when draining hot water from the bathtub or when the bathtub is not used for a long time with hot water in it, and does not cause slime inside the bathtub. This makes it possible to realize an excellent sterilizing filtration device that can provide a comfortable pass life without producing bad odors in the bathroom or bathroom. It is now possible to provide a sterilizing filter bed made of manufactured filters with good workability and high production efficiency.

【図面の簡単な説明】[Brief explanation of the drawing]

【図1】本発明の一実施例における温水浄化用の殺菌濾
過装置の要部断面図
FIG. 1 is a cross-sectional view of essential parts of a sterilizing filtration device for hot water purification in one embodiment of the present invention.

【図2】本発明の製造方法における低温溶射装置の要部
断面図
[Fig. 2] A cross-sectional view of the main parts of the low-temperature spraying apparatus in the manufacturing method of the present invention

【図3】一般的な浴用の温水循環装置の概略構成図[Figure 3] Schematic diagram of a general bath hot water circulation device

【図
4】従来の殺菌濾過装置の要部断面図
[Figure 4] Cross-sectional view of main parts of a conventional sterilizing filtration device

【図5】従来のア
ーク溶射装置の要部断面図
[Figure 5] Cross-sectional view of main parts of conventional arc thermal spraying equipment

【符号の説明】[Explanation of symbols]

1 浴槽 2 吸込口 3 吐出口 4 吸込管 5 ポンプ 6 殺菌濾過装置 7 原水流入管 8 浄化水吐出管 9 殺菌濾過槽 10 殺菌手段 11 濾材 12 濾床 13 分流板 14 整流板 15 固定具 16 濾材 17 濾床 20.21  銀ワイヤ 22 ノズル 23 アーク溶射装置 24 溶融銀 25 被射体 26 低温溶射装置 27 ノズル 1 Bathtub 2 Suction port 3 Discharge port 4 Suction pipe 5 Pump 6 Sterilization filtration device 7 Raw water inflow pipe 8 Purified water discharge pipe 9 Sterilization filtration tank 10 Sterilization means 11 Filter medium 12 Filter bed 13 Flow divider plate 14 Current plate 15 Fixtures 16 Filter media 17 Filter bed 20.21 Silver wire 22 Nozzle 23 Arc spraying equipment 24 Molten silver 25 Subject 26 Low temperature thermal spraying equipment 27 Nozzle

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】塩化銀を担持した濾床を有することを特徴
とする殺菌濾過装置。
1. A sterilizing filtration device characterized by having a filter bed supporting silver chloride.
【請求項2】塩化銀を担持した濾床と塩化銀を担持した
濾材とを有することを特徴とする殺菌濾過装置。
2. A sterilizing filtration device comprising a filter bed carrying silver chloride and a filter medium carrying silver chloride.
【請求項3】濾床が樹脂製フィルタ又は多孔質セラミッ
ク板であることを特徴とする請求項1又は2の内いずれ
か1に記載の殺菌濾過装置。
3. The sterilizing filtration device according to claim 1, wherein the filter bed is a resin filter or a porous ceramic plate.
【請求項4】塩化銀を担持した樹脂製フィルタからなる
殺菌濾床の製造方法であって、樹脂製フィルタの表面に
銀を低温熔射法により担持させる担持工程と、樹脂製フ
ィルタに担持された銀を塩素化する塩素化工程と、を有
することを特徴とする殺菌濾床の製造方法。
4. A method for producing a sterilizing filter bed made of a resin filter supporting silver chloride, comprising a supporting step of supporting silver on the surface of the resin filter by a low-temperature melting method; A method for producing a sterilizing filter bed, comprising: a chlorination step of chlorinating silver.
JP2401896A 1990-12-13 1990-12-13 Bactericidal filtering device and production of bactericidal filter bed used therefor Pending JPH04210292A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2401896A JPH04210292A (en) 1990-12-13 1990-12-13 Bactericidal filtering device and production of bactericidal filter bed used therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2401896A JPH04210292A (en) 1990-12-13 1990-12-13 Bactericidal filtering device and production of bactericidal filter bed used therefor

Publications (1)

Publication Number Publication Date
JPH04210292A true JPH04210292A (en) 1992-07-31

Family

ID=18511712

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2401896A Pending JPH04210292A (en) 1990-12-13 1990-12-13 Bactericidal filtering device and production of bactericidal filter bed used therefor

Country Status (1)

Country Link
JP (1) JPH04210292A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004004049A1 (en) * 2002-06-28 2004-01-08 Nec Corporation Fuel cell and method of use teereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004004049A1 (en) * 2002-06-28 2004-01-08 Nec Corporation Fuel cell and method of use teereof

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