JPS6313831Y2 - - Google Patents
Info
- Publication number
- JPS6313831Y2 JPS6313831Y2 JP1981066686U JP6668681U JPS6313831Y2 JP S6313831 Y2 JPS6313831 Y2 JP S6313831Y2 JP 1981066686 U JP1981066686 U JP 1981066686U JP 6668681 U JP6668681 U JP 6668681U JP S6313831 Y2 JPS6313831 Y2 JP S6313831Y2
- Authority
- JP
- Japan
- Prior art keywords
- outer cylinder
- flow path
- path switching
- water
- switching port
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 70
- 239000008399 tap water Substances 0.000 claims description 21
- 235000020679 tap water Nutrition 0.000 claims description 21
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical class C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 13
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 9
- 229910052709 silver Inorganic materials 0.000 claims description 9
- 239000004332 silver Substances 0.000 claims description 9
- 238000003780 insertion Methods 0.000 claims description 5
- 230000037431 insertion Effects 0.000 claims description 5
- 230000002093 peripheral effect Effects 0.000 claims 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 34
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 11
- 229910052801 chlorine Inorganic materials 0.000 description 11
- 239000000460 chlorine Substances 0.000 description 11
- 229920000049 Carbon (fiber) Polymers 0.000 description 10
- 239000006260 foam Substances 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 238000010612 desalination reaction Methods 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000006298 dechlorination reaction Methods 0.000 description 2
- 239000003566 sealing material Substances 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- 229920002972 Acrylic fiber Polymers 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 235000013361 beverage Nutrition 0.000 description 1
- 238000010000 carbonizing Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 235000012489 doughnuts Nutrition 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000005180 public health Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 238000007740 vapor deposition Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Description
【考案の詳細な説明】
本考案は水道水中の残留塩素を除去した脱塩素
水、シヤワー水などを簡単な操作で任意に切替え
て流出する機能を有し、かつ水道水蛇口に直結す
るタイプの小型の浄水器に関するものである。[Detailed description of the invention] This invention is a type that can be connected directly to a tap water faucet, and has the function of freely switching and discharging dechlorinated water, shower water, etc. that removes residual chlorine from tap water, with a simple operation. This relates to a small water purifier.
水道水はその衛生的見地から供給末端におい
て、残留塩素が0.1ppm以上保持されることが定
められているが、実際はもつと多量に存在し、特
に夏場などはその塩素臭のため飲料時に不快感を
与えている。したがつて近年になつてレストラ
ン、喫茶店、各家庭などにおいて、残留塩素を除
去するための浄水器が用いられるようになつてき
た。 From a hygienic standpoint, tap water is required to contain at least 0.1 ppm of residual chlorine at the supply end, but in reality, a large amount of residual chlorine is present, and the chlorine odor can cause discomfort when drinking, especially in the summer. is giving. Therefore, in recent years, water purifiers for removing residual chlorine have come into use in restaurants, coffee shops, households, and the like.
これらの従来の浄水器は一般に粒状活性炭を脱
塩素材として用い、たとえば筒状の容器内に粒状
活性炭を充填し、当該粒状活性炭層に水道水を通
過させることによつて水中の残留塩素を除去する
ものであるが、以下のような欠点を有している。 These conventional water purifiers generally use granular activated carbon as a desalination material; for example, by filling a cylindrical container with granular activated carbon and passing tap water through the granular activated carbon layer, residual chlorine in the water is removed. However, it has the following drawbacks.
すなわち浄水器に用いられる粒状活性炭の粒径
は通常0.3〜2mm程度のものであるので脱塩素反
応が遅く、したがつてたとえば水道水蛇口から流
出する通常の流量で脱塩素処理するためには浄水
器そのものの容量が比較的大きくなる。浄水器の
容量が比較的大きくなるとこれを水道水蛇口に直
結して用いることができず、たとえば壁あるいは
洗し台などに浄水器を付設し、浄水器の流入口と
水道水蛇口とをビニールホースなどの配管で連結
せねばならず、したがつて浄水器の設置場所を確
保する必要があり、また配管により浄水器回りが
繁雑となる。 In other words, the particle size of granular activated carbon used in water purifiers is usually about 0.3 to 2 mm, so the dechlorination reaction is slow. The capacity of the container itself is relatively large. When the capacity of a water purifier is relatively large, it is not possible to connect it directly to a tap water faucet. The water purifier must be connected with piping such as a hose, so it is necessary to secure a place to install the water purifier, and the piping makes the area around the water purifier complicated.
本考案は従来の浄水器におけるかかる欠点を解
決するもので、水道水蛇口に直結し得るような小
型で高性能の残留塩素除去能力を有し、かつ脱塩
素水、シヤワー水、通常の流下水などを任意に切
替えることができる水流切替機能を併せて有する
浄水器に関するものである。 The present invention solves the drawbacks of conventional water purifiers, and is compact and capable of removing residual chlorine with high performance and can be connected directly to tap water faucets. The present invention relates to a water purifier that also has a water flow switching function that allows the water flow to be switched arbitrarily.
以下に本考案を図面に基づいて詳細に説明す
る。 The present invention will be explained in detail below based on the drawings.
第1図は本考案の実施態様の一例の切欠縦断面
図であつて、上部および下部に多数の通水孔1を
有する中空円盤状の充填ケース2内に活性炭素繊
維3を充填し、当該充填ケース2を中空円盤状の
外筒4に収納する。当該活性炭素繊維3はアクリ
ル繊維などの合成繊維や羊毛などの動物性繊維や
綿などの植物性繊維を炭化して活性化したもの
で、直径10〜100μmの単繊維を1m2あたり50〜
500gの目付けをしたフエルト状のものを用いる
とよい。第1図に示した活性炭素繊維3は当該フ
エルト状の活性炭素繊維をドーナツ状に形成し、
これを6層に充填したものである。このような活
性炭素繊維はヨー素価が1.5g/g以上、比表面
積1000〜1550m2/g、平均細孔直径14Å以上の性
能を有し、特に当該活性炭素繊維の外表面積は
1.5〜2.0m2/gであり、粒状活性炭の外表面積の
0.01m2/g前後と比較して100倍以上も大きい。
したがつて当該活性炭素繊維を脱塩素材として用
いることにより、粒状活性炭を用いる場合と比較
して、その充填容量を約1/10とすることができ
る。 FIG. 1 is a cutaway vertical cross-sectional view of an example of an embodiment of the present invention, in which activated carbon fibers 3 are filled in a hollow disc-shaped filling case 2 having a large number of water passage holes 1 in the upper and lower parts. A filling case 2 is housed in a hollow disc-shaped outer cylinder 4. The activated carbon fiber 3 is made by carbonizing and activating synthetic fibers such as acrylic fibers, animal fibers such as wool, and vegetable fibers such as cotton.
It is best to use a felt-like material with a basis weight of 500g. The activated carbon fiber 3 shown in FIG. 1 is formed by forming the felt-like activated carbon fiber into a donut shape,
This is packed in 6 layers. Such activated carbon fibers have an iodine value of 1.5 g/g or more, a specific surface area of 1000 to 1550 m 2 /g, and an average pore diameter of 14 Å or more. In particular, the outer surface area of the activated carbon fibers is
1.5~2.0m 2 /g, which is the outer surface area of granular activated carbon.
It is more than 100 times larger than around 0.01m 2 /g.
Therefore, by using the activated carbon fiber as a desalination material, the filling capacity can be reduced to about 1/10 compared to the case where granular activated carbon is used.
外筒4はネジ込みなどによつて上部外筒4aと
下部外筒4bとに分割できるようにし、使用済み
の活性炭素繊維3を充填ケース2とともに交替で
きるように構成する。また外筒4の下方部に多数
のシヤワー穴5を有する円盤状のシヤワー板6を
付設し、当該外筒4の中空部に、上部に水道水蛇
口の差し込み口19を有する内筒7を回転滑動自
在に貫装し、外筒4の内壁と内筒7の外壁とが密
着して水が漏れないように構成する。内筒7は第
2図に示したように下端部のみをのこして他は空
洞とし、上方部の空洞部に位置する側部滑動面に
流路切替口8を設け、さらに下方の非空洞部に位
置する側部滑動面に、空洞部と連通する切欠流路
切替口9と、空洞部と連通することなく下端が開
放した切欠流路切替口11と、空洞部と下端とが
貫通する切欠流路切替口10をそれぞれ角度をず
らして付設する。なお流路切替口8、切欠流路切
替口9,10,11はそれぞれの対称の位置にも
付設し、それぞれ2ケ所づつ設ける。 The outer cylinder 4 can be divided into an upper outer cylinder 4a and a lower outer cylinder 4b by screwing or the like, and is configured so that the used activated carbon fibers 3 can be replaced together with the filling case 2. Further, a disc-shaped shower plate 6 having a large number of shower holes 5 is attached to the lower part of the outer cylinder 4, and an inner cylinder 7 having a tap water faucet insertion port 19 at the upper part is rotated in the hollow part of the outer cylinder 4. It is slidably inserted, and the inner wall of the outer cylinder 4 and the outer wall of the inner cylinder 7 are in close contact with each other to prevent water from leaking. As shown in FIG. 2, the inner cylinder 7 leaves only the lower end and is hollow, with a flow passage switching port 8 provided on the side sliding surface located in the upper hollow part, and a non-hollow part further below. A notched passage switching port 9 that communicates with the cavity, a notched passage switching opening 11 whose lower end is open without communicating with the cavity, and a notch that penetrates the cavity and the lower end on the side sliding surface located at The flow path switching ports 10 are attached at different angles. Note that the channel switching port 8 and the notched channel switching ports 9, 10, and 11 are also provided at symmetrical positions, and two locations each are provided.
一方外筒4については第3図に示したように外
筒4上方の内壁の側部滑動面12に、内筒7ある
いは外筒4を相対的に回転させることにより、前
記切替口8と合致する流路切替口13を、また外
筒4上方の内壁の滑動面12に内筒7あるいは外
筒4を相対的に回転させることにより、前記切欠
流路切替口9あるいは10とそれぞれ単独で合致
する流路切替口14を、また外筒4の底部滑動面
に内筒7あるいは外筒4を相対的に回転すること
により、前記切欠流路切替口10あるいは11と
それぞれ単独で合致する流路切替口15を付設す
る。なおこれらの流路切替口13,14,15も
同じようにそれぞれの対称の位置に付設し、それ
ぞれ2ケ所づつ設ける。 On the other hand, as for the outer cylinder 4, by rotating the inner cylinder 7 or the outer cylinder 4 relatively to the side sliding surface 12 of the inner wall above the outer cylinder 4, as shown in FIG. By rotating the inner tube 7 or the outer tube 4 relative to the sliding surface 12 of the inner wall above the outer tube 4, the channel switching port 13 can be aligned with the notched channel switching port 9 or 10, respectively. By rotating the inner cylinder 7 or the outer cylinder 4 relative to the bottom sliding surface of the outer cylinder 4, a flow path can be formed that individually matches the notched flow path switching opening 10 or 11, respectively. A switching port 15 is provided. Note that these flow path switching ports 13, 14, and 15 are similarly provided at symmetrical positions, and are provided at two locations each.
また第1図に示したごとく内筒7の差し込み口
19にゴムなどのシール材16を接着し、内筒7
の差し込み口19と水道水蛇口とを直結したとき
このシール材16によつて強く固定できるように
構成する。さらに前述の流路切替口15の下部に
前記シヤワー板6の圧力損失により極めて小さい
圧力損失を有する焼結金属などの泡沫板17を付
設し、内筒7の下部であつて、外筒4の底部滑動
面の下方に水の流出口18を開口する。 Further, as shown in FIG. 1, a sealant 16 such as rubber is glued to the insertion port 19 of the inner cylinder 7,
When the insertion port 19 and the tap water faucet are directly connected, they can be firmly fixed by the sealing material 16. Further, a foam plate 17 made of sintered metal or the like which has an extremely small pressure loss due to the pressure loss of the shower plate 6 is attached to the lower part of the flow path switching port 15 described above, and a foam plate 17 is attached to the lower part of the inner cylinder 7 and A water outlet 18 is opened below the bottom sliding surface.
本考案の浄水器は以上説明したような構造から
なり、内筒7の差し込み口19を水道栓蛇口に直
結して用いるものであり、本実施態様においては
外筒4を回転滑動させることにより脱塩素水、シ
ヤワー水などを任意に切替えて流出させるもので
ある。以下にその使用形態を説明する。 The water purifier of the present invention has the structure as explained above, and is used by directly connecting the insertion port 19 of the inner cylinder 7 to a water faucet.In this embodiment, the water purifier can be removed by rotating and sliding the outer cylinder 4. It allows you to switch between chlorinated water, shower water, etc. as you like. The usage pattern will be explained below.
まず脱塩素水を所望する場合は外筒4を回転滑
動させ、内筒7の流路切替口8に外筒7の流路切
替口13を合致させるとともに、外筒7の切欠流
路切替口11に外筒4の流路切替口14と流路切
替口15合致させる。このようにすると他の流路
切替口は外筒4の内壁および内筒7の外壁の滑動
面によつてシールされるので、第4図に示した矢
印のように内筒7の上部より流入する水道水は内
筒7の空洞部から流路切替口8,13を径て外筒
4内の上部に流入し、次いで活性炭素繊維3を通
過して水中の遊離塩素を除去し、脱塩素水が流路
切替口14および切欠流路切替口11を経てふた
たび内筒7内に流入し、そして流路切替口15か
ら泡沫板17を経て流出口18より流出する。 First, when dechlorinated water is desired, the outer cylinder 4 is rotated and slid, and the flow path switching port 13 of the outer cylinder 7 is aligned with the flow path switching port 8 of the inner cylinder 7, and the notched flow path switching port of the outer cylinder 7 is 11 and the flow path switching port 14 of the outer cylinder 4 and the flow path switching port 15 are made to match. In this way, the other flow path switching ports are sealed by the sliding surfaces of the inner wall of the outer cylinder 4 and the outer wall of the inner cylinder 7, so that the flow of water flows from the upper part of the inner cylinder 7 as shown by the arrow in FIG. The tap water flows from the cavity of the inner cylinder 7 through the flow path switching ports 8 and 13 into the upper part of the outer cylinder 4, and then passes through the activated carbon fibers 3 to remove free chlorine in the water and dechlorinate it. Water flows into the inner cylinder 7 again through the flow path switching port 14 and the notched flow path switching port 11, and then flows out from the flow path switching port 15, through the foam plate 17, and from the outlet 18.
なお充填ケース2の下部に達した脱塩素水はシ
ヤワー板6のシヤワー穴5からも流出しようとす
るが、しかし当該シヤワー板6の圧力損失により
泡沫板17の圧力損失の方が極めて小さいので脱
塩水は優先的に流出口18より流出することとな
る。 The dechlorinated water that has reached the lower part of the filling case 2 also tries to flow out from the shower hole 5 of the shower plate 6, but since the pressure loss of the foam plate 17 is extremely small due to the pressure loss of the shower plate 6, the dechlorinated water does not escape. Salt water preferentially flows out from the outlet 18.
次に水道水のシヤワー水を所望する場合は外筒
4を回転滑動させ、内筒7の切欠流路切替口9を
外筒4内壁の流路切替口14に合致させる。この
ようにすると他の流路切替口は前述と同じように
それぞれの滑動面によつてシールされ、第5図に
示した矢印のごとく内筒7の上部より流入する水
道水は内筒7を流下して切欠流路切替口9、流路
切替口14を経て充填ケース2の下部に流入し、
次いでシヤワー板6の多数のシヤワー穴5より流
出する。さらに水道水の通常の流下水を所望する
場合は外筒4を回転させ、流路切替口8、切欠流
路切替口9,11および流路切替口13,14を
それぞれの滑動面でシールし、切欠流路切替口1
0と流路切替口15を合致させる。このようにす
ると第6図に示した矢印のごとく内筒7の上部よ
り流下する水道水は内筒7を流下し、流路切替口
10,15および泡沫板17を経て流出口18よ
り流出する。 Next, when a shower of tap water is desired, the outer cylinder 4 is rotated and slid so that the notched flow path switching port 9 of the inner cylinder 7 matches the flow path switching port 14 on the inner wall of the outer cylinder 4. In this way, the other flow path switching ports are sealed by their respective sliding surfaces in the same way as described above, and the tap water flowing from the upper part of the inner cylinder 7 as shown by the arrow in FIG. It flows down and flows into the lower part of the filling case 2 through the notched flow path switching port 9 and the flow path switching port 14,
The water then flows out from the shower holes 5 of the shower plate 6. Furthermore, when a normal flow of tap water is desired, the outer cylinder 4 is rotated and the flow path switching ports 8, notched flow path switching ports 9, 11, and flow path switching ports 13, 14 are sealed with their respective sliding surfaces. , notch flow path switching port 1
0 and the flow path switching port 15. In this way, the tap water flowing down from the upper part of the inner cylinder 7 as shown by the arrow in FIG. .
なお第6図に示したごとく、上記操作位置とし
た場合、切欠流路切替口10が流路切替口14と
も合致し、流下水は流路切替口14から流出して
シヤワー板6のシヤワー穴5からも流出しようと
するが、前述したと同様にシヤワー板6の圧力損
失より泡沫板17の圧力損失の方が極めて小さい
ので脱塩素水は優先的に流出口18より流出する
こととなる。 As shown in FIG. 6, when the operating position is set as above, the notched flow path switching port 10 also matches the flow path switching port 14, and the flowing sewage flows out from the flow path switching port 14 and flows into the shower hole of the shower plate 6. However, as described above, the pressure loss of the foam plate 17 is extremely smaller than the pressure loss of the shower plate 6, so dechlorinated water preferentially flows out from the outlet 18.
このように本考案の浄水器は脱塩素材として反
応速度の極めて速い活性炭素繊維を用いているの
で、浄水器の容量を水道水蛇口に直結し得るよう
な小型のものとすることができる。 As described above, since the water purifier of the present invention uses activated carbon fiber, which has an extremely high reaction rate, as a desalination material, the capacity of the water purifier can be made small enough to be directly connected to a tap water faucet.
たとえば直径10〜20μmの活性炭素単繊維を1
m2あたり約200gの目付をした容量100cm3のフエル
ト状の活性炭素繊維を外筒内に充填し、0.7ppm
の残留塩素を含む水道水を200/Hの流速で通
水したところ処理水の残留塩素は0.04ppmであつ
た。 For example, one activated carbon single fiber with a diameter of 10 to 20 μm is
The outer cylinder is filled with felt-like activated carbon fiber with a capacity of 100cm3 with a basis weight of approximately 200g per m2 , and 0.7ppm
When tap water containing residual chlorine was passed through the tube at a flow rate of 200/H, the residual chlorine in the treated water was 0.04 ppm.
また本考案の浄水器はシヤワー水や通常の流下
水を簡単な操作で任意に得られるので、水道水蛇
口に直結することにより、皿などの比較的大きい
食器の洗浄に便利である。 In addition, the water purifier of the present invention can obtain shower water or ordinary running water at any time with simple operations, so it is convenient for washing relatively large dishes such as dishes by being directly connected to a tap water faucet.
また従来の浄水器においては、浄水器の使用を
中断し、通水を再開する場合、通水当初の処理水
中に一般細菌が含まれるという欠点があつた。こ
れは使用してない間に浄水器内部特に脱塩素材の
内部で一般細菌が増殖することが起因している。 Furthermore, conventional water purifiers have a drawback in that when the water purifier is stopped in use and the water flow is restarted, the treated water that is initially passed through the water contains common bacteria. This is due to the growth of bacteria inside the water purifier, especially inside the desalination material, while the water purifier is not in use.
本考案の浄水器に用いる活性炭素繊維として、
たとえばその表面に金属銀を蒸着した活性炭素繊
維を用いればこの一般細菌の増殖、流出について
も防止することができる。 As activated carbon fiber used in the water purifier of this invention,
For example, by using activated carbon fibers with metal silver deposited on their surfaces, it is possible to prevent the growth and outflow of these common bacteria.
なお金属銀の蒸着については基材の表面に金属
を蒸着させる一般的手法をそのまま応用すればよ
い。 For vapor deposition of metallic silver, a general method for vapor depositing metal on the surface of a base material may be applied as is.
すなわち真空容器内の上方に当該活性炭素繊維
を配置し真空容器内の下方にたとえばルツボなど
に入れた金属銀を加熱などして、金属銀の蒸気を
発生させ、これを活性炭素繊維の表面に析出させ
るのである。 That is, the activated carbon fibers are placed above the vacuum container, and metallic silver placed in a crucible or the like is heated below the vacuum container to generate metallic silver vapor, which is applied to the surface of the activated carbon fibers. It is caused to precipitate.
なお活性炭素繊維の表面に金属銀を蒸着させる
場合、あまり厚く蒸着させると通水性が損なわれ
て脱塩素効果が低下し、またあまり薄いと殺菌能
力およびその持続性が低下するので金属銀の蒸着
の厚みは0.05〜5μmの範囲とすることが好まし
く、より好ましくは0.5〜1μmの範囲にするとよ
い。 When depositing metallic silver on the surface of activated carbon fibers, if the deposition is too thick, the water permeability will be impaired and the dechlorination effect will be reduced, and if it is too thin, the sterilization ability and its sustainability will be reduced. The thickness is preferably in the range of 0.05 to 5 μm, more preferably in the range of 0.5 to 1 μm.
たとえば直径10〜20μmの活性炭素繊維を1m2
あたり約200gの目付をした容量100cm2のフエルト
状の活性炭素繊維の表面に、厚さ約0.5μの金属銀
を蒸着し、当該活性炭素繊維を外筒内に充填し、
0.7ppmの残留塩素を含む水道水を200/Hの流
速で通水し、24時間通水を中断して、その後通水
を再開した場合、10秒後の処理水は一般細菌数47
個/ml、1分後の処理水は10個/mlとなり、いづ
れも水道法の水質基準である100個/ml以下の衛
生的な処理水を得ることができる。また銀の溶出
量も0.01ppm以下と小さく、アメリカ公衆衛局の
飲料基準である0.05mg/以下の値とすることが
できる。 For example, 1 m 2 of activated carbon fiber with a diameter of 10 to 20 μm
Metallic silver with a thickness of about 0.5μ is vapor-deposited on the surface of a felt-like activated carbon fiber with a capacity of 100cm 2 and a basis weight of about 200g, and the activated carbon fiber is filled into an outer cylinder.
If tap water containing 0.7 ppm residual chlorine is passed through at a flow rate of 200/h, the water flow is interrupted for 24 hours, and then the water flow is restarted, the treated water after 10 seconds has a general bacterial count of 47.
The number of treated water after 1 minute is 10 particles/ml, which is the water quality standard of the Water Supply Law of 100 particles/ml or less, making it possible to obtain sanitary treated water. The amount of silver eluted is also small, at less than 0.01 ppm, and can be kept below the U.S. Public Health Service beverage standard of 0.05 mg/or less.
以上説明したように本考案の浄水器は脱塩素
水、シヤワー水などを外筒または内筒を回転滑動
させるという簡単な操作で任意に得られるので、
種々の用途に用いることができ、さらにその表面
に金属銀を蒸着した活性炭素繊維を用いることに
より、常に衛生的な脱塩素水を得ることができ
る。 As explained above, the water purifier of the present invention can freely obtain dechlorinated water, shower water, etc. by simply rotating and sliding the outer cylinder or inner cylinder.
It can be used for a variety of purposes, and by using activated carbon fibers whose surfaces are coated with metal silver, it is possible to always obtain sanitary dechlorinated water.
また本考案の浄水器は水道水蛇口に直結できる
ような小型なので、壁あるいは洗し台などに浄水
器を設置する必要もなく、かつビニールホースな
どで連結する必要もない。 Furthermore, since the water purifier of the present invention is small enough to be directly connected to a tap water faucet, there is no need to install the water purifier on a wall or sink, and there is no need to connect it with a vinyl hose.
第1図ないし第6図は、いづれも本考案の実施
態様を示す図面であつて、第1図は浄水器の切欠
断面図、第2図は内筒の説明図、第3図は外筒の
内壁部の説明図、第4図は脱塩素水を得る場合の
流路図、第5図はシヤワー水を得る場合の流路
図、第6図は通常の流下水を得る場合の流路図を
示す。
1……通水孔、2……充填ケース、3……活性
炭素繊維、4……外筒、5……シヤワー穴、6…
…シヤワー板、7……内筒、8,13,14,1
5……流路切替口、12……滑動面、9,10,
11……切欠流路切替口、16……シール材、1
7……泡沫板、18……水の流出口、19……差
し込み口。
Figures 1 to 6 are drawings showing embodiments of the present invention, in which Figure 1 is a cutaway sectional view of the water purifier, Figure 2 is an explanatory diagram of the inner cylinder, and Figure 3 is the outer cylinder. Fig. 4 is a flow path diagram for obtaining dechlorinated water, Fig. 5 is a flow path diagram for obtaining shower water, and Fig. 6 is a flow path diagram for obtaining normal sewage water. Show the diagram. 1...Water hole, 2...Filling case, 3...Activated carbon fiber, 4...Outer cylinder, 5...Shower hole, 6...
... Shower plate, 7 ... Inner cylinder, 8, 13, 14, 1
5...Flow path switching port, 12...Sliding surface, 9, 10,
11...Notch flow path switching port, 16...Sealing material, 1
7... Foam plate, 18... Water outlet, 19... Inlet.
Claims (1)
部に、最上部に水道水蛇口の差し込み口19を
有し、かつ上方が空洞部、下方が非空洞部であ
る内筒7を、外筒4に対して相対的に回転滑動
自在に貫装するとともに、外筒4の下方周囲部
にシヤワー板6を、また貫装した内筒7の下部
であつて、外筒4の底部滑動面の下方に流出口
18を配し、さらに内筒7上方の空洞部に位置
する側部滑動面に流路切替口8を、また内筒7
下方の非空洞部に位置する側部滑動面に、空洞
部と連通する切欠流路切替口9と、空洞部と連
通することなく下端が開放した切欠流路切替口
11と、空洞部と下端とが貫通する切欠流路切
替口10とを、それぞれ角度をずらして付設
し、さらに外筒4上方の側部滑動面に、内筒7
あるいは外筒4を相対的に回転させることによ
り、前記流路切替口8と合致する流路切替口1
3を、また外筒4下方の側部滑動面に内筒7あ
るいは外筒4を相対的に回転させることによ
り、前記切欠流路切替口9あるいは10とそれ
ぞれ単独で合致する流路切替口14を、また外
筒4の底部滑動面に内筒7あるいは外筒4を相
対的に回転することにより、前記切欠流路切替
口10あるいは11とそれぞれ単独で合致する
流路切替口15を付設することにより、内筒7
あるいは外筒4を相対的に回転滑動させて脱塩
水、水道水のシヤワー水、水道水の通常の流下
水をそれぞれ得られるようになしたことを特徴
とする浄水器。 (2) 金属銀をその表面に蒸着した活性炭素繊維3
を外筒4に内蔵する実用新案登録請求の範囲第
1項記載の浄水器。[Claims for Utility Model Registration] (1) The outer cylinder 4 containing the activated carbon fiber 3 has an insertion port 19 for a tap water faucet at the top, and the upper part is a hollow part and the lower part is a non-contact part. The inner cylinder 7, which is a hollow part, is inserted through the outer cylinder 4 so as to be rotatable and slidable relative to the outer cylinder 4, and the shower plate 6 is installed at the lower peripheral part of the outer cylinder 4, and at the lower part of the inner cylinder 7 which is inserted through the inner cylinder 7. An outflow port 18 is disposed below the bottom sliding surface of the outer cylinder 4, and a flow path switching port 8 is arranged on the side sliding surface located in the cavity above the inner cylinder 7.
On the side sliding surface located in the lower non-cavity part, there is a notched flow path switching port 9 communicating with the cavity, a notched flow path switching port 11 whose lower end is open without communicating with the cavity, and the hollow part and the lower end. and a notch passage switching port 10 through which the inner cylinder 7 and the inner cylinder 7
Alternatively, by relatively rotating the outer cylinder 4, the flow path switching port 1 matches the flow path switching port 8.
3, and by rotating the inner cylinder 7 or the outer cylinder 4 relative to the side sliding surface below the outer cylinder 4, a flow path switching port 14 that individually matches the notched flow path switching port 9 or 10, respectively. In addition, by relatively rotating the inner cylinder 7 or the outer cylinder 4 on the bottom sliding surface of the outer cylinder 4, a flow path switching port 15 is provided which individually matches the notched flow path switching port 10 or 11, respectively. By this, the inner cylinder 7
Alternatively, the water purifier is characterized in that the outer cylinder 4 is rotated and slid relative to each other so that demineralized water, shower water from tap water, and normal flowing tap water can be obtained respectively. (2) Activated carbon fiber 3 with metallic silver deposited on its surface
The water purifier according to claim 1, which is incorporated in the outer cylinder 4.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1981066686U JPS6313831Y2 (en) | 1981-05-11 | 1981-05-11 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1981066686U JPS6313831Y2 (en) | 1981-05-11 | 1981-05-11 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS57181394U JPS57181394U (en) | 1982-11-17 |
JPS6313831Y2 true JPS6313831Y2 (en) | 1988-04-19 |
Family
ID=29862712
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1981066686U Expired JPS6313831Y2 (en) | 1981-05-11 | 1981-05-11 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6313831Y2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01304095A (en) * | 1988-06-01 | 1989-12-07 | Kao Corp | Water purifier |
JP2588600Y2 (en) * | 1991-09-13 | 1999-01-13 | 九州日立マクセル株式会社 | Water purifier |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5135181U (en) * | 1974-09-06 | 1976-03-16 | ||
JPS5239318U (en) * | 1975-09-10 | 1977-03-19 |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5179953U (en) * | 1974-12-20 | 1976-06-24 |
-
1981
- 1981-05-11 JP JP1981066686U patent/JPS6313831Y2/ja not_active Expired
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5135181U (en) * | 1974-09-06 | 1976-03-16 | ||
JPS5239318U (en) * | 1975-09-10 | 1977-03-19 |
Also Published As
Publication number | Publication date |
---|---|
JPS57181394U (en) | 1982-11-17 |
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