JPH04131111A - Preparation of sterilization filter medium - Google Patents
Preparation of sterilization filter mediumInfo
- Publication number
- JPH04131111A JPH04131111A JP25328390A JP25328390A JPH04131111A JP H04131111 A JPH04131111 A JP H04131111A JP 25328390 A JP25328390 A JP 25328390A JP 25328390 A JP25328390 A JP 25328390A JP H04131111 A JPH04131111 A JP H04131111A
- Authority
- JP
- Japan
- Prior art keywords
- silver chloride
- substrate
- filter medium
- organic vehicle
- hot water
- 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
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 31
- 238000004659 sterilization and disinfection Methods 0.000 title abstract description 10
- 229910021607 Silver chloride Inorganic materials 0.000 claims abstract description 47
- HKZLPVFGJNLROG-UHFFFAOYSA-M silver monochloride Chemical compound [Cl-].[Ag+] HKZLPVFGJNLROG-UHFFFAOYSA-M 0.000 claims abstract description 47
- 239000000758 substrate Substances 0.000 claims abstract description 21
- 239000000919 ceramic Substances 0.000 claims abstract description 9
- 239000011976 maleic acid Substances 0.000 claims abstract description 9
- 239000000203 mixture Substances 0.000 claims abstract description 9
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 7
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 claims abstract description 7
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 claims abstract description 7
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 claims abstract description 7
- 238000002156 mixing Methods 0.000 claims abstract description 6
- 239000011347 resin Substances 0.000 claims abstract description 5
- 229920005989 resin Polymers 0.000 claims abstract description 5
- 239000000843 powder Substances 0.000 claims description 10
- 238000004519 manufacturing process Methods 0.000 claims description 7
- 239000012784 inorganic fiber Substances 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 42
- 230000000694 effects Effects 0.000 abstract description 8
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 241000894006 Bacteria Species 0.000 description 12
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 12
- 229910052709 silver Inorganic materials 0.000 description 12
- 239000004332 silver Substances 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 10
- 239000010410 layer Substances 0.000 description 9
- 238000002474 experimental method Methods 0.000 description 7
- 238000001914 filtration Methods 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 230000000844 anti-bacterial effect Effects 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 239000011230 binding agent Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 239000011247 coating layer Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 239000004793 Polystyrene Substances 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 229920002223 polystyrene Polymers 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 229920001817 Agar Polymers 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000008272 agar Substances 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002070 germicidal effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 230000036962 time dependent Effects 0.000 description 1
- -1 ultraviolet rays Chemical compound 0.000 description 1
Landscapes
- Filtering Materials (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、浴用循環温水器等に用いられる殺菌濾材の製
造方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for manufacturing a sterilizing filter medium used in bath circulating water heaters and the like.
従来の技術 近年、浴用循環温水器の需要が高まっている。Conventional technology In recent years, demand for circulating water heaters for baths has been increasing.
第2図は一般的な浴用循環温水器を示す概略図である。FIG. 2 is a schematic diagram showing a general bath circulation water heater.
第2図において、1は浴槽で、浴槽1には吐水管2及び
吸水管3がそれぞれ設けられている。4は吸水管3に設
けられたフィルターで、フィルター2は髪の毛等の大き
なゴミを濾過する。In FIG. 2, 1 is a bathtub, and the bathtub 1 is provided with a water discharge pipe 2 and a water intake pipe 3, respectively. 4 is a filter provided in the water suction pipe 3, and the filter 2 filters out large particles such as hair.
5は温水を循環させるためのポンプ、6はポンプ5から
送られてきた温水の細かなゴミを濾過したり、殺菌を行
なう濾過装置である。浴槽1の中の温水はポンプ5によ
って濾過装置6に送られて、濾過及び殺菌されて吐水管
2を通して再び浴槽の中に返される。従来この濾過装置
6は中にゼオライトや活性炭等が封入されて細菌を吸着
したり、また濾過装置6の中でオゾン、紫外線または塩
素によって細菌を死滅させて温水の殺菌を行なっていた
。しかしながらオゾンや塩素による殺菌では温水中にそ
れらの残留物が残り人体への悪影響が懸念される。また
ゼオライトや活性炭への細菌の吸着及び紫外線照射によ
る殺菌は、温水の循環を停止してしまうとその殺菌作用
を全く示さない。5 is a pump for circulating hot water, and 6 is a filtration device that filters fine dust from the hot water sent from the pump 5 and sterilizes it. Hot water in the bathtub 1 is sent to a filter device 6 by a pump 5, filtered and sterilized, and returned to the bathtub through the water discharge pipe 2. Conventionally, this filtration device 6 has zeolite, activated carbon, etc. sealed therein to adsorb bacteria, and bacteria have been killed by ozone, ultraviolet rays, or chlorine inside the filtration device 6 to sterilize hot water. However, there is concern that sterilization using ozone or chlorine may leave residues in hot water and have an adverse effect on the human body. Furthermore, sterilization by adsorption of bacteria to zeolite or activated carbon and irradiation with ultraviolet rays does not exhibit any sterilization effect if the circulation of hot water is stopped.
この対策として近年、殺菌作用のある金属(例えば銀)
を温水中に溶出させて細菌の繁殖を抑える方法が開発さ
れた。この方法を用いると、浴用循環温水器の動作を停
止させても温水中に溶出した金属イオンが殺菌効果を示
し、湯垢や悪臭の発生を防止する。従来、バインダーと
塩化銀粉末を混合したものを濾材に塗布して、濾材に塩
化銀層を形成し、その濾材を濾過装置の中に配置する事
によって温水中に銀を溶出させて、温水の殺菌を行なっ
ていた。As a countermeasure against this problem, in recent years metals with bactericidal properties (such as silver) have been
A method has been developed to suppress the growth of bacteria by eluting it into warm water. When this method is used, the metal ions eluted into the hot water exhibit a bactericidal effect even when the operation of the bath circulation water heater is stopped, preventing the generation of scale and bad odors. Conventionally, a mixture of a binder and silver chloride powder was applied to a filter medium to form a silver chloride layer on the filter medium, and the filter medium was placed in a filtration device to elute silver into hot water. It was being sterilized.
発明が解決しようとする課題
しかしながら前記従来の構成では、バインダーと塩化銀
粉末を混合して濾材に塗布して塩化銀層を形成している
ために、塩化銀粉末がバインダーにコーティングされた
状態となっているので、塩化銀層表面の塩化銀しか温水
中に溶出しない。従って非常に効率が悪く、温水中の銀
濃度を所定値にするためには大きな濾材に塩化銀層を設
ける必要があり、濾過装置が大型になるという問題点を
有していた。また塩化銀層と濾材の接合強度があまり強
くないために、濾材に衝撃を加えると塩化銀層が脱落し
てしまうので、濾材の取り扱いを慎重に行なわなければ
ならないという問題点を有していた。Problems to be Solved by the Invention However, in the conventional configuration, the binder and silver chloride powder are mixed and applied to the filter medium to form a silver chloride layer, so the silver chloride powder is coated on the binder. Therefore, only the silver chloride on the surface of the silver chloride layer is eluted into the hot water. Therefore, the efficiency is extremely low, and in order to maintain the silver concentration in hot water at a predetermined value, it is necessary to provide a silver chloride layer on a large filter medium, resulting in a large filtration device. Furthermore, since the bonding strength between the silver chloride layer and the filter medium was not very strong, the silver chloride layer would fall off if the filter medium was subjected to impact, so there was a problem in that the filter medium had to be handled carefully. .
本発明は前記従来の問題点を解決するもので、濾材が小
さくても所定の銀濃度を得る事ができ、しかも塩化銀が
濾材から脱落しにくい殺菌濾材の製造方法を提供する事
を目的としている。The present invention solves the above-mentioned conventional problems, and aims to provide a method for producing a sterilizing filter medium that can obtain a predetermined silver concentration even if the filter medium is small, and in which silver chloride is difficult to fall off from the filter medium. There is.
課題を解決するための手段
この目的を達成するために、塩化銀粉末と、少なくとも
アルコール系オイルとマレイン酸系樹脂よりなる有機ビ
ヒクルを混合し、その混合物を基板に塗布し、その後に
基板に熱処理を施した。Means for Solving the Problem To achieve this objective, silver chloride powder is mixed with an organic vehicle consisting of at least an alcohol-based oil and a maleic acid-based resin, the mixture is applied to a substrate, and the substrate is then heat-treated. was applied.
作 用
この構成により、多孔質セラミックの中に塩化銀を三次
元的に保持させる事ができる。Function: With this configuration, silver chloride can be held three-dimensionally within the porous ceramic.
実施例
以下本発明の一実施例における殺菌濾材の製造方法につ
いて説明する。EXAMPLE A method for producing a sterilizing filter medium according to an example of the present invention will be described below.
まず有機ビヒクルとしてアルコール系オイルとマレイン
酸系樹脂を混合したスキージ−オイル(アルコールマレ
イン系 東華色素化学工業(株)製)と、塩化銀粉末(
日中貴金属(株)製 粒径75μm以下)を重量比でl
: 1の割合で配合し、アジテータを用いて混合して塗
布剤を作成する。次に第1図(a)に示す様に多孔質セ
ラミック(アルミナ−シリカ系 孔径100μm 岩屋
磁器工業(株)製)でできた基板7の周縁部に枠8を立
設し、枠8で囲まれた基板7の表面に塗布剤を流し込む
。そして常温で10分〜60分乾燥させ、第1図(b)
の様に塗布層9を形成する。First, as an organic vehicle, squeegee oil (alcohol maleic, manufactured by Toka Shiki Kagaku Kogyo Co., Ltd.), which is a mixture of alcohol oil and maleic acid resin, and silver chloride powder (
Made by Nichi Kikinzoku Co., Ltd. Particle size: 75 μm or less) by weight
: Blend in a ratio of 1:1 and mix using an agitator to create a coating agent. Next, as shown in FIG. 1(a), a frame 8 is erected on the periphery of the substrate 7 made of porous ceramic (alumina-silica type, pore diameter 100 μm, manufactured by Iwaya Porcelain Industry Co., Ltd.), and the frame 8 surrounds the substrate 7. A coating agent is poured onto the surface of the substrate 7. Then, dry at room temperature for 10 to 60 minutes, as shown in Figure 1(b).
A coating layer 9 is formed as shown in FIG.
この乾燥の工程中では塗布剤は基板7の中に浸透してい
く。乾燥させた後に基板7を炉等の加熱手段によって4
00℃〜600℃の温度で約30分熱処理する。この熱
処理によって塗布層9に含まれていたスキージ−オイル
はほぼ完全に水と炭酸ガスに分解してしまい、第1図(
C)に示す様に塩化銀層10が形成される。この時有機
ビヒクルとしてアルコールマレイン酸系を用いたのは熱
処理を行なう際に塩化銀が還元されて銀化しないように
するためである。During this drying process, the coating agent permeates into the substrate 7. After drying, the substrate 7 is heated by a heating means such as a furnace.
Heat treatment is performed at a temperature of 00°C to 600°C for about 30 minutes. As a result of this heat treatment, the squeegee oil contained in the coating layer 9 is almost completely decomposed into water and carbon dioxide gas, as shown in Figure 1 (
A silver chloride layer 10 is formed as shown in C). The reason why alcohol maleic acid was used as the organic vehicle was to prevent silver chloride from being reduced and turned into silver during heat treatment.
この様に形成した殺菌濾材は塩化銀が多孔質セラミック
の多数の孔に入り込んで三次元的に保持されるので、従
来の殺菌濾材の様に衝撃等によって塩化銀の膜が脱落す
る事がない。また塩化銀と渇水の接触面積が非常に大き
くなるので、小さな殺菌濾材でも十分に温水のなかの銀
濃度を大きくする事ができる。このように本実施例の殺
菌濾材は濾材の大きさを小さくできるので、第2図に示
す浴用循環温水器に用いた場合、濾過装置をコンパクト
にする事ができる。In the sterilizing filter media formed in this way, the silver chloride enters the many pores of the porous ceramic and is held three-dimensionally, so unlike conventional sterilizing filter media, the silver chloride film does not fall off due to impact etc. . Furthermore, since the contact area between silver chloride and dry water becomes very large, even a small sterilizing filter medium can sufficiently increase the silver concentration in hot water. As described above, since the sterilizing filter medium of this embodiment can be made small in size, when used in the bath circulation water heater shown in FIG. 2, the filtration device can be made compact.
以下具体的例を挙げて本実施例の効果を説明する。The effects of this embodiment will be explained below with specific examples.
(実施例1)
上記方法すなわち第1図(a)(b)(c)で説明した
殺菌濾材を第2図に示す濾過装置6内に収納した。(Example 1) The sterilizing filter medium described in the above method, that is, in FIGS. 1(a), (b), and (c), was housed in the filtration device 6 shown in FIG. 2.
(比較例1) 紫外線殺菌燈を第2図に示す濾過装置θ内に設けた。(Comparative example 1) An ultraviolet germicidal lamp was installed in the filter device θ shown in FIG.
(比較例2)
多孔質セラミック板にポリスチレンをコーティングして
、その上に塩化銀の粉末をスプレーして乾燥させて殺菌
濾材を作成した。この殺菌濾材を第2図に示す濾過装置
6内に設けた。(Comparative Example 2) A sterilizing filter medium was prepared by coating a porous ceramic plate with polystyrene, spraying silver chloride powder thereon, and drying it. This sterilizing filter medium was installed in a filter device 6 shown in FIG.
第1の試験は第2図に示す浴槽1の中の温水に細菌を混
入し、40℃で1000時間温水を循環させて温水中の
細菌数(一般細菌テスト:普通寒天培地 栄研化学(株
)製)及び銀検出量の経時変化を原子吸光光度計(日本
Jarrell AshAA−860)によって検査
した。その結果を第1表に示す。In the first test, bacteria were mixed into the hot water in the bathtub 1 shown in Figure 2, and the hot water was circulated at 40°C for 1000 hours to determine the number of bacteria in the hot water (general bacteria test: ordinary agar medium). ) and the time-dependent change in the detected amount of silver was examined using an atomic absorption spectrophotometer (Jarrell AshAA-860, Japan). The results are shown in Table 1.
(以 下 余 白 )
第
表
(以下余白)
第1表かられかる様に実施例1は温水を循環させて4時
間後には細菌は検出できなかった。また比較例1の紫外
線灯を用いたものは2時間後には細菌は検出できなかっ
た。また比較例2は500時間後に細菌を検出する事が
できなかった。この第1の実験から実施例1および比較
例1のどちらも殺菌作用を呈する事がわかる。また比較
例2ではポリスチレンによって塩化銀がコーティングさ
れているために他の例よりも殺菌効果を発揮する時間が
長くかかったのだと考えられる。(Margin below) Table 1 (Margin below) As can be seen from Table 1, in Example 1, no bacteria could be detected 4 hours after circulating hot water. Further, in Comparative Example 1 using an ultraviolet lamp, no bacteria could be detected after 2 hours. Moreover, in Comparative Example 2, no bacteria could be detected after 500 hours. This first experiment shows that both Example 1 and Comparative Example 1 exhibit bactericidal action. Furthermore, in Comparative Example 2, it is thought that because the silver chloride was coated with polystyrene, it took a longer time to exhibit the bactericidal effect than in the other examples.
又第2の実験として40℃で24時間温水を循環させて
、その後に温水の循環をやめ、温水中の細菌の数及び銀
濃度の経時変化を上記第1の実験と同じ様に検査し、そ
の結果を第2表に示す。In a second experiment, hot water was circulated at 40°C for 24 hours, then the circulation of hot water was stopped, and the number of bacteria and silver concentration in the hot water were examined over time in the same manner as in the first experiment. The results are shown in Table 2.
(以 下 余 白 )
第
表
(以下余白)
この第2表かられかるように、比較例1ては温水の循環
をやめると、再び細菌が増殖しだす事がわかる。これは
紫外線による殺菌の場合、常に温水を循環させて、温水
を紫外線にさらさなければならない事がわかる。他の例
では銀が温水中に溶けているので、細菌の増殖はなかっ
た。しかし比較例2については、実施例1よりもはるか
に殺菌効果を発揮する時間がかかることがわかる。(Margins below) Table 2 (Margins below) As can be seen from Table 2, in Comparative Example 1, when the hot water circulation was stopped, bacteria began to grow again. This means that in the case of sterilization using ultraviolet rays, it is necessary to constantly circulate hot water and expose the hot water to ultraviolet rays. In other cases, the silver was dissolved in the hot water, so there was no bacterial growth. However, it can be seen that in Comparative Example 2, it takes much longer to exhibit the bactericidal effect than in Example 1.
次に第3の実験として、実施例1及び比較例2で作成し
た殺菌濾材30Cm2を、それぞれ40℃の水道水(塩
素イオン濃度: 10ppm)1リツトル中に浸漬し、
24時間経過した後の銀濃度を測定した。これを132
0時間まで測定し、この結果を第3表にまとめた。Next, as a third experiment, 30 cm2 of the sterilizing filter media prepared in Example 1 and Comparative Example 2 were each immersed in 1 liter of tap water (chloride ion concentration: 10 ppm) at 40°C.
The silver concentration was measured after 24 hours had elapsed. This is 132
Measurements were made up to 0 hours, and the results are summarized in Table 3.
(以 下 余 白 )
第
表
(以下余白)
第3表かられかるように、比較例2では塩化銀濃度が0
.O7ppmを超えるのは720時間後であるが、実施
例1においては24時間後にはもう0.O7ppmを超
えている。この実験かられかるように実施例1では塩化
銀層と水との接触面積が非常に大きい事がわかる。(Margin below) Table 3 (Margin below) As can be seen from Table 3, in Comparative Example 2, the silver chloride concentration was 0.
.. O exceeds 7ppm after 720 hours, but in Example 1 it is already 0.0 after 24 hours. O exceeds 7ppm. As can be seen from this experiment, in Example 1, the contact area between the silver chloride layer and water was extremely large.
これらの実験より本実施例の殺菌濾材は非常に殺菌効果
が早く現われる事がわかる。These experiments show that the sterilizing filter medium of this example exhibits a sterilizing effect very quickly.
つぎにアルコールマレイン酸系の有機ビヒクルと塩化銀
粉末の混合割合に付いて説明する。Next, the mixing ratio of the alcohol maleic acid-based organic vehicle and the silver chloride powder will be explained.
第4の実験として重量比で塩化銀粉末工の割合に対して
アルコールマレイン酸系有機ビヒクルを0〜3の割合で
混合したサンプルを複数作成し、そのサンプルを熱処理
して、その熱処理した後の塩化銀に対する銀の割合を求
めた。As a fourth experiment, multiple samples were prepared by mixing an alcohol-maleic acid-based organic vehicle in a weight ratio of 0 to 3 with respect to the proportion of silver chloride powder, and the samples were heat-treated. The ratio of silver to silver chloride was determined.
(以下余白)
第
表
(以下余白)
第4表かられかるように有機ビヒクルの割合が1.5以
上になると、急激に塩化銀が銀と塩素に分解する割合が
大きくなる。従って有機ビヒクルの混合割合は塩化銀]
の割合に対して1.5以下にすると基板により効率よく
塩化銀を担持させる事ができる。(Hereafter the margin) Table 4 (Hereafter the margin) As can be seen from Table 4, when the ratio of the organic vehicle becomes 1.5 or more, the ratio of silver chloride decomposing into silver and chlorine increases rapidly. Therefore, the mixing ratio of the organic vehicle is silver chloride]
When the ratio is 1.5 or less, silver chloride can be more efficiently supported on the substrate.
以上の様に本実施例では、アルコールマレイン酸系の有
機ビヒクルと塩化銀を混合して塗布剤を形成し、その塗
布剤を多孔質セラミックスでできた基板に塗布し、乾燥
させて、熱処理する事によって、従来のように濾材に衝
撃を加えても濾材が脱落する事がないので、殺菌作用が
長持ちする。As described above, in this example, a coating agent is formed by mixing an alcohol-maleic acid-based organic vehicle and silver chloride, and the coating agent is applied to a substrate made of porous ceramics, dried, and heat-treated. As a result, the filter material does not fall off even if a shock is applied to it like in the past, so the sterilization effect lasts for a long time.
また塩化銀と温水の接触面積が大きくなるので、従来よ
り小さな殺菌濾材でも同等の殺菌効果を得る事ができる
。Furthermore, since the contact area between silver chloride and hot water is increased, the same sterilizing effect can be obtained even with a smaller sterilizing filter medium than before.
なお本実施例において温水を用いたけれども、室温の水
や、冷水でも同様の効果を得る事ができる。Although warm water was used in this embodiment, the same effect can be obtained with water at room temperature or cold water.
発明の効果
本発明は、塩化銀粉末と、少なくともアルコール系オイ
ルとマレイン酸系樹脂よりなる有機ビヒクルを混合し、
その混合物を基板に塗布し、その後に基板に熱処理を施
した事により、多孔質セラミックの中に塩化銀を三次元
的に保持させる事ができるので、温水と塩化銀の接触面
積を大きくする事ができ、従来より小さな殺菌濾材でも
、十分に従来と同じ殺菌効果を得る事ができる。また接
合強度も大きくなるので、従来のように衝撃によって塩
化銀の膜が脱落する事がない。Effects of the Invention The present invention mixes silver chloride powder and an organic vehicle consisting of at least alcoholic oil and maleic acid resin,
By applying the mixture to the substrate and then heat-treating the substrate, silver chloride can be held three-dimensionally within the porous ceramic, increasing the contact area between hot water and silver chloride. Even with a smaller sterilizing filter medium than before, it is possible to obtain the same sterilizing effect as before. Furthermore, since the bonding strength is increased, the silver chloride film does not fall off due to impact as in the conventional method.
【図面の簡単な説明】
第1図(a)(b)(c)は本発明の位置実施例におけ
る殺菌濾材の製造方法を示す工程図、第2図は一般的な
浴用循環温水器を示す概略図である。
7・・・・・・基板 8・・・・・・枠 9・・
・・・・塗布層10・・・・・・塩化銀層[Brief Description of the Drawings] Figure 1 (a), (b), and (c) are process diagrams showing a method for manufacturing a sterilizing filter medium in an embodiment of the present invention, and Figure 2 shows a general circulating water heater for baths. It is a schematic diagram. 7... Board 8... Frame 9...
... Coating layer 10 ... Silver chloride layer
Claims (3)
マレイン酸系樹脂よりなる有機ビヒクルを混合し、前記
混合物を基板に塗布し、その後に前記基板に熱処理を施
し、前記基板に塩化銀を担持させる事を特徴とする殺菌
濾材の製造方法。(1) Mixing silver chloride powder with an organic vehicle consisting of at least alcohol-based oil and maleic acid-based resin, applying the mixture to a substrate, and then heat-treating the substrate to support silver chloride on the substrate. A method for producing a sterilizing filter medium, which is characterized by:
よって構成されている事を特徴とする請求項第1項記載
の殺菌濾材の製造方法。(2) The method for producing a sterilizing filter medium according to claim 1, wherein the substrate is made of porous ceramic or inorganic fiber.
を1.5以下(0を含まず)の割合で混合した事を特徴
とする殺菌濾材の製造方法。(3) A method for producing a sterilizing filter medium, characterized in that an organic vehicle is mixed in a weight ratio of 1 part silver chloride to 1.5 or less (excluding 0) of an organic vehicle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25328390A JPH04131111A (en) | 1990-09-21 | 1990-09-21 | Preparation of sterilization filter medium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25328390A JPH04131111A (en) | 1990-09-21 | 1990-09-21 | Preparation of sterilization filter medium |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04131111A true JPH04131111A (en) | 1992-05-01 |
Family
ID=17249130
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25328390A Pending JPH04131111A (en) | 1990-09-21 | 1990-09-21 | Preparation of sterilization filter medium |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04131111A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6551609B2 (en) * | 1997-10-24 | 2003-04-22 | Joseph A. King | Water treatment composition |
US7168574B2 (en) | 1999-04-22 | 2007-01-30 | King Technology | Dual filter |
-
1990
- 1990-09-21 JP JP25328390A patent/JPH04131111A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6551609B2 (en) * | 1997-10-24 | 2003-04-22 | Joseph A. King | Water treatment composition |
US7168574B2 (en) | 1999-04-22 | 2007-01-30 | King Technology | Dual filter |
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