JP3417460B2 - Hypochlorous acid proportional mixing water purifier - Google Patents

Hypochlorous acid proportional mixing water purifier

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Publication number
JP3417460B2
JP3417460B2 JP28435897A JP28435897A JP3417460B2 JP 3417460 B2 JP3417460 B2 JP 3417460B2 JP 28435897 A JP28435897 A JP 28435897A JP 28435897 A JP28435897 A JP 28435897A JP 3417460 B2 JP3417460 B2 JP 3417460B2
Authority
JP
Japan
Prior art keywords
water
cotton
raw water
activated carbon
hypochlorous acid
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.)
Expired - Fee Related
Application number
JP28435897A
Other languages
Japanese (ja)
Other versions
JPH11104620A (en
Inventor
滋夫 栃窪
敏正 石松
竜次 鶴
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.)
TYK Corp
Original Assignee
TYK Corp
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Filing date
Publication date
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Priority to JP28435897A priority Critical patent/JP3417460B2/en
Publication of JPH11104620A publication Critical patent/JPH11104620A/en
Application granted granted Critical
Publication of JP3417460B2 publication Critical patent/JP3417460B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、主に航空機、船舶
など不特定多数の年齢、人種を対象とし、又、取扱い
者、地域、配管、水栓の衛生管理状態が異なる場合にお
いても、飲料水中に含まれる病原性細菌、微生物、一般
細菌などの殺菌あるいは増殖を抑制し、安全、衛生的且
つ清浄度の高い水を確保する浄水器に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention is mainly intended for an unspecified number of ages and races such as airplanes and ships, and also when the hygiene control conditions of the handler, region, piping, and faucet are different. The present invention relates to a water purifier that suppresses sterilization or growth of pathogenic bacteria, microorganisms, general bacteria and the like contained in drinking water and ensures safe, hygienic and highly clean water.

【0002】[0002]

【従来の技術】従来、航空機などでは、円筒ブロック状
のフィルター、粒状活性炭をカートリッジ化したものが
カルキ臭、カビ臭の除去の用に供されている。
2. Description of the Related Art Conventionally, in an aircraft or the like, a cylindrical block-shaped filter and a granular activated carbon cartridge are provided for removing odors of scaly and musty.

【0003】しかし、浄水器中の雑菌が配管路に流出し
たものあるいは水栓から侵入する雑菌が駐機中に増殖
し、入国と同時に検疫により見つかり問題を起こすこと
が多く、航空会社では水の浄化サービスのための浄水器
設置を止めざるを得なかった。
However, the bacteria in the water purifier that have flowed out into the pipeline or the bacteria that invade from the faucet multiply during the parking and are often found by quarantine upon entry into the country, causing problems. I had no choice but to stop installing water purifiers for purification services.

【0004】また、こうした浄水器設置故の雑菌の増殖
を防ぐため、微小径のバイパスによるものがなされた
り、充填密度を下げて次亜塩素酸の除去率を下げ、浄水
中に低濃度の次亜塩素酸を確保しようとする策も検討さ
れた経緯もあるが、航空機では、駐機中、飛行中の速度
などの違いによっても、原水圧力が一定でなく、混合濃
度が変化するため、汎用性を持たず、実用化されていな
い。
Further, in order to prevent the growth of various bacteria due to the installation of such a water purifier, a bypass with a small diameter is used, or the packing density is reduced to reduce the hypochlorous acid removal rate, so that the purified water has a low concentration Although there has been a history of studying measures to secure chlorous acid, in aircraft, the raw water pressure is not constant and the mixed concentration changes due to differences in speed during parking and flight. It has no property and has not been put to practical use.

【0005】[0005]

【発明が解決しようとする課題】そこで本発明は、活性
炭層を通過し、次亜塩素酸が除去され、殺菌効果を全く
失った浄水に、人間が味覚として感ぜず、尚、殺菌効果
を維持出来る所期の濃度となるよう、活性炭層を通過し
ない次亜塩素酸を含む微量の原水を織布、不織布あるい
はそれらを開砕して綿状にし、カートリッジキャップに
より挟み込み、圧縮して毛細管現象による原水の滲透層
を設け、且つ、環状の開砕綿などを内側にはみ出させ
て、活性炭中央の貫通路から流出する浄水と接触させ、
浄水に原水中の次亜塩素酸を混合することが出来る浄水
カートリッジを提供することを目的とする。
Therefore, according to the present invention, human beings do not perceive the taste of the purified water that has passed through the activated carbon layer to remove hypochlorous acid and lose the bactericidal effect. Capillary phenomenon by crushing a small amount of raw water containing hypochlorous acid that does not pass through the activated carbon layer into woven or non-woven fabric or crushing them into cotton, sandwiching them with a cartridge cap, and compressing to achieve the desired concentration that can be maintained. By providing a permeation layer of raw water by, and making the ring-shaped crushed cotton etc. protrude inside, contact with purified water flowing out from the through passage in the center of activated carbon,
An object of the present invention is to provide a water purification cartridge capable of mixing purified water with hypochlorous acid in raw water.

【0006】本発明の他の目的とするところは、次亜塩
素酸の濃度は原水の圧力に左右されない毛細管現象のみ
によって開砕綿などの層を滲透する原水を、浄水の流量
に比例混合し、原水の圧力が変化しても常に次亜塩素酸
の所期の濃度範囲を保持できる浄水カートリッジを提供
するものである。
Another object of the present invention is that the concentration of hypochlorous acid is not affected by the pressure of the raw water, and the raw water that permeates a layer such as crushed cotton only by capillary action is mixed in proportion to the flow rate of the purified water. The present invention provides a water purification cartridge that can always maintain a desired concentration range of hypochlorous acid even if the pressure of raw water changes.

【0007】また、本発明の他の目的とするところは、
原水中のきょう雑物による通過層の閉塞を防ぐため、圧
縮繊維層に熱溶着せず、綿状品をニードルパンチングし
た不織布などの開砕品を用いることにより、長期間、原
水の圧力に拘らず、安定滲透させることが出来、原水中
の次亜塩素酸を所期量、浄水に混合することが出来る浄
水カートリッジを提供するものである。
Another object of the present invention is to:
In order to prevent clogging of the passage layer due to foreign matter in the raw water, use a crushed product such as a nonwoven fabric obtained by needle punching a cotton-like product without heat welding to the compressed fiber layer. The present invention provides a water purification cartridge that can be stably permeated and that can mix a desired amount of hypochlorous acid in raw water with purified water.

【0008】さらにまた、本発明の他の目的とするとこ
ろは、原水中の次亜塩素酸の影響を受けて、膨潤、腐食
しない化学繊維綿を圧縮、原水の滲透層とした浄水カー
トリッジを提供するものである。
Still another object of the present invention is to provide a water purification cartridge in which a chemical fiber cotton which does not swell or corrode under the influence of hypochlorous acid in the raw water is compressed and used as a permeation layer of the raw water. To do.

【0009】さらにまた、本発明の他の目的とするとこ
ろは、プラスに帯電した繊維を用いることで、一般的に
マイナスに帯電するきょう雑物を吸着あるいは濾過する
ことが出来、浄水に混入するのを防ぐことが出来る浄水
カートリッジを提供するものである。
Still another object of the present invention is to use a positively charged fiber to adsorb or filter foreign matters that are generally negatively charged, and mix it into purified water. This is to provide a water purification cartridge that can prevent

【0010】[0010]

【課題を解決するための手段】即ち、固形円筒ブロック
に成形した活性炭フィルターの上下に極細、円盤状の開
砕綿、不織布などを設置、上下のキャップ、フィルター
を貫通する吐水パイプのネジにより締め付けて圧縮し、
原水の圧力に影響されない毛細管現象のみの滲透層を形
成し、滲透層を浄水のながれに浸漬、接触させて、原水
の滲透水を浄水に混入させ、浄水の流量が変化しても比
例、一定した原水中の次亜塩素酸濃度を得ることが出
来、浄水として味覚を向上させながら、浄水器内部、配
管路、水栓に至るまで、殺菌効果を得ることを特徴とし
たことを要旨とする。
[Means for solving the problem] That is, extra fine, disk-shaped crushed cotton, non-woven fabric, etc. are installed on the top and bottom of an activated carbon filter molded in a solid cylindrical block, and tightened with screws on the upper and lower caps and the water discharge pipe that penetrates the filter. Compress it,
By forming a permeation layer that is not affected by the pressure of raw water by only a capillary phenomenon, immersing the permeation layer in the flow of purified water and contacting it, mixing the permeation water of the raw water into the purified water, and proportional and constant even if the flow rate of the purified water changes It is characterized in that the concentration of hypochlorous acid in the raw water can be obtained, and while improving the taste as purified water, it has a sterilizing effect on the inside of the water purifier, the pipeline and the faucet. .

【0011】[0011]

【実施例】本発明を実施例に基づいて、図面を参考にし
ながら詳細を説明する。図1は、本発明のカートリッジ
全体を示すものであり、活性炭フィルター1は100メ
ッシュアンダーの微粉末活性炭と木節粘土、水をそれぞ
れ1/3づつとして、ハイスピードミキサーにて混練、
造粒の上、プレス成形、焼成して得た素焼き状の円筒形
のフィルターである。キャップ2、3は、中心部にネジ
4、5を切り、活性炭フィルター1の上下にはめ込んで
いる。開砕綿6、7は活性炭フィルター1の上下端面に
キャップ2、3の形状に合わせ、中心をくり抜いて円形
とし、接着剤を使用せずに吐水パイプ8のネジ9、10
とキャップ2、3のネジ4、5とにより締め付け、図示
していない狭い間隙の原水通路に圧縮保持されている。
また、吐水パイプ8には浄水の流入口11を開口してい
る。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail based on embodiments with reference to the drawings. FIG. 1 shows the entire cartridge of the present invention, in which an activated carbon filter 1 is a fine mesh of activated carbon of 100 mesh under, Kobushi clay and 1/3 each of which is kneaded in a high speed mixer,
It is a unglazed cylindrical filter obtained by granulation, press molding and firing. The caps 2 and 3 are formed by cutting screws 4 and 5 in the central part and fitting them into the upper and lower sides of the activated carbon filter 1. The crushed cottons 6 and 7 match the shapes of the caps 2 and 3 on the upper and lower end surfaces of the activated carbon filter 1, and the center is hollowed out into a circular shape.
And the caps 2 and 3 are tightened by screws 4 and 5, and compressed and held in a raw water passage having a narrow gap (not shown).
Further, the water discharge pipe 8 has an opening 11 for purified water.

【0012】水道水は活性炭フィルター1の外側全外周
12から入り、円筒13に至り、流入口11を経て、流
出口14から吐水される。
Tap water enters from the entire outer circumference 12 of the activated carbon filter 1, reaches the cylinder 13, passes through the inflow port 11, and is discharged from the outflow port 14.

【0013】その時、開砕綿6,7にも原水圧がかかっ
ているが、キャップ2、3とネジ9、10とにより強く
圧縮され、且つ、含水した活性炭フィルター1の膨張に
より、繊維密度は極限まで上がって、原水の透過損失が
大きすぎ、繊維間の毛細管現象による滲透量以上吐出す
ることはない。活性炭フィルター1を細孔を持たない樹
脂に置き換え、原水圧を掛け、吐水の可否を確認した
が、量の測定は不可能であった。
At that time, the raw water pressure is also applied to the crushed cottons 6 and 7, but the fiber density is increased by the expansion of the activated carbon filter 1 which is strongly compressed by the caps 2 and 3 and the screws 9 and 10. The permeation loss of the raw water is so high that it is not discharged more than the permeation amount due to the capillary phenomenon between the fibers. The activated carbon filter 1 was replaced with a resin having no pores, and the raw water pressure was applied to check whether or not water was discharged, but the amount could not be measured.

【0014】従って、原水の圧力の高低による浄水量の
変化、フィルター閉塞による浄水量の変化によっても、
滲透量は変化することはない。
Therefore, even if the amount of purified water changes depending on the pressure of raw water and the amount of purified water changes due to filter clogging,
The amount of penetration does not change.

【0015】浄水への原水の混入は円筒13の上下の端
末15、15に滲透してきた原水が大きく取った間隙部
16、16の浄水の乱流に接触、巻き込まれる状態で浄
水とともに流入口11、11から流出口14に至る。
When the raw water is mixed with the purified water, the raw water that has permeated the upper and lower terminals 15, 15 of the cylinder 13 comes into contact with the turbulent flow of the purified water in the gaps 16, 16 in which the raw water has taken a large amount, and is caught in the turbulent flow, together with the purified water. , 11 to the outlet 14.

【0016】円筒13内部に乱流もしくは吸入流を起こ
すため、吐水パイプ8の流入口11は上下の端末15、
15に近接させ、間隙16、16にある浄水は必ず対流
し、間隙部16、16にはみ出した開砕綿6、7からの
滲透原水を引き出す効果を得た。
Since a turbulent flow or a suction flow is generated inside the cylinder 13, the inlet 11 of the water discharge pipe 8 has upper and lower terminals 15,
The purified water in the gaps 16 and 16 was surely convected to be close to the gap 15, and the effect of extracting the permeated raw water from the crushed cottons 6 and 7 protruding into the gaps 16 and 16 was obtained.

【0017】原水中の次亜塩素酸の一般的濃度は、世界
的に見ても0.1ppmから2.0ppm程度であり、
0.4ppmを超えると著しく味を損ない、臭気をもた
らすことがある。国内外の殺菌効果を保持する目的での
規制値は0.1ppm以上であって、この程度の濃度に
あっては、殆ど味覚として感じることがないため、殺菌
効果と味覚を両立させるためには、この濃度に近似であ
ればよい。しかしながら、航空機にあっては原水圧力が
変化するため、微小な開口を経由させても比例混合させ
ることは困難であり、且つ、きょう雑物による閉塞が起
こりやすい。
The general concentration of hypochlorous acid in raw water is about 0.1 ppm to 2.0 ppm in the world,
If it exceeds 0.4 ppm, the taste may be significantly impaired and odor may be caused. The regulation value for the purpose of maintaining the bactericidal effect at home and abroad is 0.1 ppm or more, and at such a concentration, almost no taste is felt, so in order to achieve both the bactericidal effect and the taste. , It suffices if it is close to this concentration. However, in an aircraft, since the raw water pressure changes, it is difficult to perform proportional mixing even through a minute opening, and clogging by foreign matter is likely to occur.

【0018】そこで実施例においては、原水の凡そ10
%の次亜塩素酸濃度となり、きょう雑物の閉塞がさほど
なく、長期安定的に透過量が変化せず、浄水の透過量の
幅にも十分な滲透量を補給出来ることを確認した、ポリ
プロピレンの不織布を開砕、ニードルパンチングして綿
状の厚さ約1mm、繊維の太さが1.5から2.0デニ
ール、重量は平方メートル当たり100gで、きょう雑
物の閉塞の心配がなく、毛細管現象に阻害要素とならな
い、熱溶着していないものを用い、活性炭フィルター1
の端面にあわせて打ち抜き、上下に設置の上、キャップ
2、3を吐水パイプ8により手で目一杯に締め付けた。
Therefore, in the embodiment, the raw water is approximately 10
It was confirmed that the concentration of hypochlorous acid was%, clogging of foreign matters was not so large, the permeation amount did not change stably for a long period of time, and sufficient permeation amount could be supplied to the range of permeation amount of purified water. The non-woven fabric is crushed and needle punched to a cotton-like thickness of about 1 mm, the fiber thickness is 1.5 to 2.0 denier, and the weight is 100 g per square meter. Activated carbon filter 1 that uses a non-heat-welded material that does not become an obstacle to the phenomenon
It was punched out according to the end face of the above, installed up and down, and caps 2 and 3 were tightly tightened by hand with the water discharge pipe 8.

【0019】開砕綿は繊維太さ1.0から5.0デニー
ル、平方メートル当たり重量50〜300gまでを試験
したが、実用的には太さ1.0から3.0デニール、重
量は平方メートル当たり50〜200gまでにおいて効
果を確認した。
Crushed cotton was tested for a fiber thickness of 1.0 to 5.0 denier and a weight per square meter of 50 to 300 g, but practically 1.0 to 3.0 denier and a weight per square meter. The effect was confirmed up to 50 to 200 g.

【0020】本来、締め付けにはトルク管理が必要であ
るが、活性炭フィルター1は通水後、含水して膨張する
ため、正確なトルクの測定が困難であり、且つ、トルク
管理をせずも、活性炭の膨張による追加的圧縮で開砕綿
の繊維密度変化は次亜塩素酸濃度の測定によってさほど
バラツキをみることはなかった。
Originally, torque control is required for tightening, but since the activated carbon filter 1 expands after being impregnated with water, it is difficult to measure the torque accurately, and even without torque control, The change in fiber density of the crushed cotton due to the additional compression due to the expansion of activated carbon did not vary so much when the concentration of hypochlorous acid was measured.

【0021】表1は、原水圧力、浄水量と浄水に於ける
次亜塩素酸濃度の相関をみたものである。
Table 1 shows the correlation between the raw water pressure, the amount of purified water and the concentration of hypochlorous acid in the purified water.

【0022】[0022]

【表1】 [Table 1]

【0023】この結果、原水の低濃度から試料水の平均
濃度に至るまで、所期値を得ることが出来た。下限の規
制値は0.1ppmとなっているが、滞留時間が長けれ
ば0.01ppmでも殺菌効果は期待出来る。
As a result, desired values could be obtained from low concentration of raw water to average concentration of sample water. The lower limit value is 0.1 ppm, but if the residence time is long, 0.01 ppm can be expected to have a bactericidal effect.

【0024】表2は、一般細菌、大腸菌への効果を時間
毎の試料から見たものである。
Table 2 shows the effects on general bacteria and Escherichia coli from the samples taken every hour.

【0025】[0025]

【表2】 [Table 2]

【0026】この場合、0.01ppmを限界として是
とすることが出来た。即ち、航空機に補給される水は常
に水道水であり、且つ、水栓により密閉され空気から遮
断されているため、通常数時間の経過によっては雑菌は
繁殖しないと想定出来、さらに時間が経過すれば低濃度
の浄水であっても殺菌効果が生じてくるからである。
In this case, the limit could be set to 0.01 ppm. In other words, the water supplied to the aircraft is always tap water, and since it is sealed by a water faucet and shielded from the air, it can be assumed that various bacteria will not normally grow over the course of several hours. This is because even if the concentration of purified water is low, a bactericidal effect will be produced.

【0027】織布を用いた場合には、薄手よりも厚手、
繊維は縒って細いものが制御しやすい結果を得た。
When woven cloth is used, it is thicker than thin,
The fiber was twisted, and the result that the thin one was easy to control was obtained.

【0028】熱溶着した類似の不織布にては、懸濁物が
多い原水を使った促進試験では積算量の増加に連れ、目
詰まりを起こし、原水混合が比例しなくなり効果を減じ
た。
In a similar non-woven fabric that was heat-welded, in an accelerated test using raw water containing a large amount of suspended solids, as the integrated amount increased, clogging occurred, and the mixing of raw water became non-proportional, reducing the effect.

【0029】不織布などによらず、単純にキャップ2、
3を圧着固定したものでは、圧力毎の制御が困難で、汎
用性が乏しいことが判明した。
The cap 2 is simply used regardless of the non-woven fabric or the like.
It was found that the one in which 3 was fixed by crimping was difficult to control for each pressure and the versatility was poor.

【0030】図2は、圧縮された粒状活性炭によるカー
トリッジのケースの応用例であり、上下いずれかからの
原水の流入に対し、円筒内面に不織布を当てることによ
っても同様な効果が期待できる。
FIG. 2 is an application example of a case of a cartridge made of compressed granular activated carbon, and the same effect can be expected by applying a nonwoven fabric to the inner surface of the cylinder against the inflow of raw water from above or below.

【0031】[0031]

【発明の効果】本発明によれば、活性炭フィルターとキ
ャップの狭隘な間隙に設定した開砕綿などの圧縮された
滲透層からの毛細管現象のみによる原水を、流出する浄
水に混合することにより原水の圧力如何に拘らず、浄水
の量に比例した原水中の次亜塩素酸濃度を得ることが出
来る実益を要する。また、原水の次亜塩素酸が規定値以
上である場合には浄水に混合される次亜塩素酸濃度が人
間の味覚に感じない低濃度であって、殺菌効果をも保持
出来る浄水を得ることが出来る実益を有する。
EFFECTS OF THE INVENTION According to the present invention, the raw water obtained by mixing only the capillary phenomenon from the compressed permeation layer such as the crushed cotton set in the narrow gap between the activated carbon filter and the cap with the purified water flowing out. Regardless of the pressure, the actual profit is needed to obtain the concentration of hypochlorous acid in the raw water that is proportional to the amount of purified water. In addition, if the hypochlorous acid in the raw water is above the specified value, the concentration of hypochlorous acid mixed in the purified water is low enough to be perceived by human taste, and it is necessary to obtain purified water that can maintain the bactericidal effect. Have the real benefit of being able to

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

【図1】実施例を説明する断面図である。FIG. 1 is a cross-sectional view illustrating an example.

【図2】他の実施例を説明する断面図である。FIG. 2 is a sectional view illustrating another embodiment.

【図3】当実施例での一部欠截部を含む容器との取り合
い図である。
FIG. 3 is an engagement diagram with a container including a partial cutaway portion in the present embodiment.

【符号の説明】[Explanation of symbols]

1 活性炭フィルター 2 キャップ 3 キャップ 4 ネジ 5 ネジ 6 開砕綿 7 開砕綿 8 吐水パイプ 9 ネジ 10 ネジ 11 流入口 12 外側全周面 13 円筒 14 流出口 15 端末 16 間隙部 17 外周不織布 1 activated carbon filter 2 cap 3 caps 4 screws 5 screws 6 crushed cotton 7 Crushed cotton 8 spout pipe 9 screws 10 screws 11 Inlet 12 Outer peripheral surface 13 cylinder 14 Outlet 15 terminals 16 Gap 17 Peripheral nonwoven fabric

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C02F 1/50 550 C02F 1/50 550B 560 560B (56)参考文献 特開 昭61−97095(JP,A) 実開 平4−70186(JP,U) (58)調査した分野(Int.Cl.7,DB名) C02F 1/28 B01J 20/00 - 20/34 B01D 35/00 - 35/04 B01D 35/08 - 35/30 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI C02F 1/50 550 C02F 1/50 550B 560 560B (56) Reference JP-A-61-97095 (JP, A) -70186 (JP, U) (58) Fields surveyed (Int.Cl. 7 , DB name) C02F 1/28 B01J 20/00-20/34 B01D 35/00-35/04 B01D 35/08-35 / 30

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 粒状、粉末状、繊維状活性炭を単独、ま
たはそれらの混合物と粘土あるいは樹脂をバインダーと
した混練品又は造粒品を多孔体の活性炭円筒フィルター
に成形し、該活性炭円筒フィルターの上下あるいはいず
れかの一方の端面に、圧迫により繊維密度が可変な円形
の織布、不織布またはそれを開砕した開砕綿にニードル
パンチして構成した綿状品を当てたのち、その綿状品へ
樹脂又は金属のキャップを被せてキャップと活性炭円筒
フィルターの間へ綿状品を挟み込み、圧縮して毛細管現
象による原水の滲透層を設け、かつ活性炭円筒フィルタ
ーの中心をくり抜いた円筒を貫通する流入口を開口した
吐水パイプの両端のネジにより上下のキャップを締め付
綿状品の繊維密度を上げ圧縮させて緻密化した滲透
層と成した環状の開砕綿の末端が間隙部にはみ出し、
要十分な毛細管現象による滲透量のみからの原水を、
パイプの内部に向う間隙部から流出する浄水の吐水パ
イプへ吸い込み流水中に、間隙部にはみ出た環状の開砕
綿を浸漬してきた滲透原水を前記浄水と間隙部に於て接
触混合させ、原水圧力が変化しても常に吐水パイプへの
浄水の吸い込み量に比例一定した原水中の次亜塩素酸を
含有した浄水を得ることができることを特徴とした次亜
塩素酸比例混合浄水器。
1. A granular, powdery or fibrous activated carbon alone or a kneaded product or granulated product using a mixture thereof and clay or a resin as a binder is molded into a porous activated carbon cylindrical filter , and the activated carbon cylindrical filter A circular woven fabric or a nonwoven fabric whose fiber density is variable by pressing is applied to one of the upper and lower ends or one of the end faces with a cotton-like product made by needle punching crushed cotton obtained by crushing it , and then the cotton-like shape. The product and the activated carbon cylinder covered with a resin or metal cap.
Insert a cotton-like product between the filters and compress it to remove the capillary.
Cylindrical filter with activated carbon provided with a permeation layer of raw water
Osmotic was densified by compression to increase the fiber density of the cotton-like product by tightening the upper and lower cap by two screws of the water discharge pipe inlets and opening through the cylinder in which hollow in the center over
The ends of the layered annular crushed cotton squeeze out into the gap, and the raw water from only the permeation amount due to the necessary and sufficient capillary phenomenon is discharged.
Discharge pad of purified water that flows out from the gap facing the inside of the water pipe.
Ring-shaped crushing that spilled into the gap in the running water
The permeated raw water that has been soaked in cotton is mixed with the purified water by contact in the gap, and even if the raw water pressure changes, it always contains a constant amount of hypochlorous acid in the raw water proportional to the suction amount of the purified water into the discharge pipe. A hypochlorous acid proportional mixing water purifier characterized by being able to obtain purified water.
【請求項2】 太さ1.0〜3.0デニール、平方メー
トル当たり50〜200g範囲にあるポリプロピレンの
不織布を開砕して得られた再生不織布を用いることによ
り、長期の使用によっても、閉塞路を形成せず、常に滲
透量が変化せず、所期の原水量を浄水に混合出来ること
を特徴とした請求項1記載の次亜塩素酸比例混合浄水
器。
2. By using a recycled non-woven fabric obtained by crushing a polypropylene non-woven fabric having a thickness of 1.0 to 3.0 denier and a range of 50 to 200 g per square meter, a closed path can be obtained even after long-term use. The hypochlorous acid proportional mixing water purifier according to claim 1, wherein the desired amount of raw water can be mixed with the purified water without forming a permeation amount and without constantly changing the permeation amount.
JP28435897A 1997-09-30 1997-09-30 Hypochlorous acid proportional mixing water purifier Expired - Fee Related JP3417460B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP28435897A JP3417460B2 (en) 1997-09-30 1997-09-30 Hypochlorous acid proportional mixing water purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP28435897A JP3417460B2 (en) 1997-09-30 1997-09-30 Hypochlorous acid proportional mixing water purifier

Publications (2)

Publication Number Publication Date
JPH11104620A JPH11104620A (en) 1999-04-20
JP3417460B2 true JP3417460B2 (en) 2003-06-16

Family

ID=17677566

Family Applications (1)

Application Number Title Priority Date Filing Date
JP28435897A Expired - Fee Related JP3417460B2 (en) 1997-09-30 1997-09-30 Hypochlorous acid proportional mixing water purifier

Country Status (1)

Country Link
JP (1) JP3417460B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100451304B1 (en) * 2001-08-27 2004-10-06 주식회사 동우만앤휴멜 Element of oil filter and its manufacturing method for automobile
CN110357316A (en) * 2019-08-23 2019-10-22 祝汉威 A kind of sanitary wastewater processing automatically cleaning recyclable device

Also Published As

Publication number Publication date
JPH11104620A (en) 1999-04-20

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