JPS60889A - Water treating apparatus - Google Patents
Water treating apparatusInfo
- Publication number
- JPS60889A JPS60889A JP9448683A JP9448683A JPS60889A JP S60889 A JPS60889 A JP S60889A JP 9448683 A JP9448683 A JP 9448683A JP 9448683 A JP9448683 A JP 9448683A JP S60889 A JPS60889 A JP S60889A
- Authority
- JP
- Japan
- Prior art keywords
- water
- bone
- layer
- ion exchange
- exchange resin
- 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.)
- Granted
Links
Landscapes
- Water Treatment By Sorption (AREA)
- Treatment Of Water By Ion Exchange (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は水処理装置、特に浄化後の水に力ルシュウム等
の適量の硬度成分を溶解して硬水化する水処理装置に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a water treatment device, and more particularly to a water treatment device that hardens water by dissolving an appropriate amount of hardening components such as phlegmon in purified water.
近年、環境悪化に伴ない河川等の水源が汚染され、一般
家庭に配水される水道水の水質は著しく低下している。In recent years, due to environmental deterioration, water sources such as rivers have become contaminated, and the quality of tap water distributed to general households has deteriorated significantly.
一方、上記河川等から採水した原水を殺菌消毒するため
に浄水場で投入される塩素は、水道水に塩素臭や不快な
味をもたらす原因と成っている。この臭気や不快味の原
因となる塩素やあるいは微量な有機物を除去するために
、各家庭の水道蛇口に、活性炭、あるいはイオン交換樹
脂などからなる吸着体層に水道水を通過させて浄化する
浄水器等の水処理装置を連結しているが、上記イオン交
換樹脂は、水の味と関係が深いカルシュラムやマグネシ
ュウム等の硬度成分を殆ど除去し軟水化してしまうから
、再び、適度の硬度を与えるため、浄化水を麦飯石等の
硬度成分を含有する鉱物に接触させて水質向上を図って
いた。On the other hand, chlorine, which is added at water treatment plants to sterilize raw water taken from rivers and the like, causes tap water to have a chlorine odor and an unpleasant taste. In order to remove chlorine and trace amounts of organic substances that cause this odor and unpleasant taste, tap water is purified by passing it through an adsorbent layer made of activated carbon or ion exchange resin at each household faucet. However, the ion exchange resin softens the water by removing most of the hard components such as calcilum and magnesium, which are closely related to the taste of the water. Therefore, efforts have been made to improve water quality by bringing purified water into contact with minerals containing hardness components, such as maifan stone.
しかしながら、上記麦飯石等の鉱物は硬度成分の溶出量
が少なく、水を単に麦飯石と接触させるだけでは硬度成
分が溶解しないから、水を攪拌しながら接触させる等の
試みがなされてきたが、未だ十分な硬度成分の溶解濃度
を検出するに至っていない。However, minerals such as the above-mentioned Maifan stone elute a small amount of hardness components, and simply bringing water into contact with Maihan stone does not dissolve the hardness components.Therefore, attempts have been made to contact the minerals with water while stirring. A sufficient dissolved concentration of hardness components has not yet been detected.
発明者は、灸゛然物質にもカルシ、つJ 、マグネシュ
ウム等の硬度成分が含まれてし;)ことに着眼し、軟化
後の水に対しても溶解性の高い硬度成分を含有する物質
を得るべく鋭意検討の結果、骨を熱処理すると硬度成分
の溶解性が高く成ることを知り、本発明をするに至った
。The inventor focused on the fact that moxibustion substances also contain hard components such as calci, magnesium, and magnesium, and developed a substance containing hard components that are highly soluble in water after softening. As a result of extensive research to obtain this, it was discovered that heat treatment of bone increases the solubility of hardness components, leading to the present invention.
本発明は、攪拌等の強制溶解手段を設けることなく、し
かも適度に硬化された水を得るために、天然物質より硬
度成分を溶出させることを課題とする。An object of the present invention is to elute hardness components from natural substances in order to obtain appropriately hardened water without using forced dissolution means such as stirring.
上記課題を解決するための本発明の技術手段は、イオン
交換樹脂や活性炭等の吸着体層の下流側に無機化された
果粒状の焼骨によって形成される焼骨層を設け、該焼骨
層によって硬度成分を溶出するようにしたたことである
。The technical means of the present invention for solving the above problems is to provide a charred bone layer formed by mineralized granular charred bone on the downstream side of an adsorbent layer of ion exchange resin, activated carbon, etc. The hardness component is eluted depending on the layer.
本発明の上記技術適手段によれば、イオン検相Fや活性
炭等の吸着体層を通過して軟1 ノ(は、焼骨の層を通
過する際、該焼゛・、J・・−)度成分を自然に溶出さ
せるから、従来のように攪拌等の強制溶解手段を必要と
せず、硬化された水が得られる。According to the above-mentioned technical means of the present invention, when passing through an adsorbent layer such as ion phase detector F and activated carbon and passing through a layer of burnt bones, ) Since the hardening components are naturally eluted, hardened water can be obtained without the need for forced dissolution means such as stirring as in the past.
更に詳しく言えば、本発明の水処理装置内に流入した水
は、イオン交換樹脂、ゼオライト等の軟化剤と、活性炭
、 ll111瑚等の瀉剤から成る吸着体層を通過する
ことによって軟化されると共に濾過され、臭気や不快な
味を呈する物質が除去されるが、本来的に水道水内に含
まれているカルシュラムやナトリュウム等の、水の味に
関係が深い硬度成分は、上記イオン交換樹脂等の軟化剤
によって殆ど除去される(硬度のあまり低い水は湯ざま
しの水のように、気が抜けた感じがしておいしくない)
。そこで、焼骨の層を通し、再び適量の硬度成分を溶か
すのであるが、この焼骨の層について更に詳述する。More specifically, water flowing into the water treatment apparatus of the present invention is softened by passing through an adsorbent layer consisting of a softening agent such as an ion exchange resin and zeolite, and a diaphragm such as activated carbon and 1111 carbon. Through filtration, substances that give off odors and unpleasant tastes are removed, but the hardness components that are closely related to the taste of water, such as calcilum and sodium, which are originally contained in tap water, are removed by the above-mentioned ion exchange resins, etc. Most of the hardness is removed by the softener (water with very low hardness tastes like boiling water and is not tasty).
. Therefore, an appropriate amount of the hardness component is dissolved again through the burnt bone layer.This burnt bone layer will be explained in more detail.
上記の焼骨は、具体的には魚又は牛等の生骨(2)の群
を、第1図に示、すように炉(1)内において、電極(
3) 、 (3)間に挟み、両極間に高電圧を加えて約
900度の高温にし、この状態で約1時間燃焼して無機
化し、その後約2mm乃至8mm程度の大きさのものに
粉砕して果粒状にしたものである。Specifically, the above-mentioned burnt bones are prepared by placing a group of raw bones (2) of fish or cow etc. in a furnace (1) as shown in FIG.
3) , (3) Place it in between and apply a high voltage between the two poles to a high temperature of about 900 degrees, burn it in this state for about an hour to make it inorganic, and then crush it into pieces with a size of about 2 mm to 8 mm. It is made into fruit granules.
上記焼骨を使用した本発明の一実施例としての水処理装
置は、第2図に示すような構造で、本体ケース(4)と
、こp本体ケース(4)内に装着自在に装填されるカー
トリ・ンジ式のフィルター(5)より構成され、」二記
焼骨t±フィルター(5)内に充填されてl/する。A water treatment device as an embodiment of the present invention using the above-mentioned burnt bones has a structure as shown in FIG. It consists of a cartridge-type filter (5), and is filled into the filter (5) with two burnt bones.
フィルター(5)は、有底筒状の容器(51)の上端開
口部を複数の流入孔(52) 、 (52)を有する蓋
(53)で被差し、この蓋(53)から容器(51)の
底壁に亘ってパイプ(6)が貫設しである。The filter (5) covers the upper end opening of a bottomed cylindrical container (51) with a lid (53) having a plurality of inflow holes (52), (52), and connects the lid (53) to the container (51). ) A pipe (6) extends through the bottom wall of the pipe (6).
又、容器(51)内の上記、(イブ(6)の外(111
1)こt1上流側から発泡性樹脂(30) 、イオン交
換樹n旨(31) 、活性炭(32)と順次充填され、
その下流に果粒状の焼骨(33)が充填されてあり、更
にその下に発泡性樹脂(34)が敷いである。又、パイ
プ(6)の下端部近傍には該パイプ内に水を取入れるた
めの透孔(131) 、 (Ell)が穿設しである。In addition, the above inside the container (51), (outside (111) of Eve (6)
1) From the upstream side of t1, foaming resin (30), ion exchange resin (31), and activated carbon (32) are sequentially filled,
Downstream thereof, charred bone (33) in the form of fruit particles is filled, and further below that, foamable resin (34) is spread. Further, near the lower end of the pipe (6), through holes (131) and (Ell) are bored for introducing water into the pipe.
」二記水処理装置による水処理の実際を述べると、第2
図に示すように、本体ケース(4)の下部に配設した水
入口(41)から取入れられた水は矢印で示すようにフ
ィルター(5)の外周と本体ケース(4)の内周との間
隙内をと昇し、蓋(53)に穿設された流入孔(52)
、 (52)からフィルター(5)内に流れ込み、発
泡性樹脂(30)の下方に侵入してイオン交換樹脂(3
1)の層により軟化され、活性炭(32)の層を通過し
て濾過された後、果粒状の焼骨(33)と接触して硬度
成分を溶出させて、その下の発泡性樹脂(34)を介し
て透孔(6()からノくイブ(6)山に侵入し、最後に
出水管(42)に導かれるのである。” To describe the actual water treatment using water treatment equipment, Part 2
As shown in the figure, the water taken in from the water inlet (41) located at the bottom of the main body case (4) flows between the outer periphery of the filter (5) and the inner periphery of the main body case (4) as shown by the arrow. An inflow hole (52) ascends within the gap and is bored in the lid (53).
, (52) into the filter (5), enters below the foamable resin (30), and enters the ion exchange resin (3).
After being softened by the layer 1) and filtered through the layer of activated carbon (32), it comes into contact with the charred bones (33) to elute the hard components, and the foamed resin (34) below is softened and filtered through the activated carbon (32) layer. It enters the Nokuib (6) mountain through the through hole (6 ()), and is finally led to the water outlet pipe (42).
次に、上記水処理装置内を通過した処理水内における成
分溶解疑の試験結果について、従来のものと比較しなが
ら記載する。Next, the test results of suspected component dissolution in the treated water that passed through the water treatment apparatus will be described in comparison with conventional tests.
試験には、本発明のものの場合、魚の生骨を既述した方
法によって熱処理して得られた位置を約2mm乃至8m
mの果粒状のものに粉砕してこれを200g充填したフ
ィルターを使用し、このフィルターに水温26度の水道
水を毎分2リツトルの割合で30分間通水後、3リツト
ル採水して試料水とした。For the test, in the case of the present invention, the position obtained by heat-treating raw fish bones by the method described above was placed at a distance of about 2 mm to 8 m.
Using a filter filled with 200 g of pulverized granules of 1.5 m, tap water at a temperature of 26 degrees was passed through the filter at a rate of 2 liters per minute for 30 minutes, then 3 liters of water was sampled. It was water.
又、上記200gの位置に代えて3Kgの鉱物性の炭酸
力ルシュウムを充填したものを対比すべき従来のものと
した。In addition, a conventional one for comparison was one in which 3 kg of mineral rhusium carbonate was filled in place of the 200 g.
その結果を以下に示すと、
(1)、カルシュラム含有量
本発明実施例のもの書・Φ4mg/l
従来のもの ・・・・検出されず
(2)、マグネシュウム含有量
本発明実施例のもの舎* a、 2 B/1従来のもの
・・・・検出されず
(3)、リン化合物含有量(リンとして)本発明実施例
のもの・・・O、l 2n+g/l従来のもの ・・・
・検出されず
(4)、カリウム含有量
本発明実施例のもの・・・4 、4+ng/I従来のも
の −Oψ赤検出されず
(5)、すトリウム含有量
本発明実施例のもの・・φ49mg/l従来のもの ・
・・・検出されず
である。The results are shown below: (1) Calsulam content: Example of the present invention - Φ4 mg/l Conventional: Not detected (2) Magnesium content: Example of the present invention * a, 2 B/1 Conventional product... Not detected (3), Phosphorus compound content (as phosphorus) Example of the present invention... O, l 2n+g/l Conventional product...
・Not detected (4), Potassium content in the example of the present invention...4, 4+ng/I Conventional -OψRed Not detected (5), Storium content in the example of the present invention... φ49mg/l conventional type ・
...Not detected.
尚、上記従来のものでも、採水i4に鉱物性炭酸力ルシ
ュウムを水中に30分程度浸し、その後通水する構造の
ものとした場合は硬度成分が検出され、水を撹拌しなが
ら鉱物性炭酸カルシュラムに接触させた場合は接触時間
が30分以内であっても硬度成分は検出される。In addition, even with the above-mentioned conventional method, if a structure is used in which mineral lucium carbonate is immersed in water for about 30 minutes and then water is passed through it, hardness components are detected, and mineral carbonate is extracted while stirring the water. When brought into contact with calcilum, hardness components are detected even if the contact time is within 30 minutes.
上記したように、本発明の水処理装置によれば、活性炭
や、イオン交換樹脂等の吸着体層を通過して献身ヒされ
た水は、無機化された位置の層を通過する際、該位置か
ら上記の割合いで、カルシュウム、マグネシュウム等ノ
硬度成分を自然に溶出させることができるから、従来の
ように攪拌等の強制溶解手段を必要とせず、適度に硬化
された水が得られる。As described above, according to the water treatment device of the present invention, the water that has passed through the adsorbent layer of activated carbon, ion exchange resin, etc., is absorbed when passing through the mineralized layer. Since hard components such as calcium and magnesium can be naturally eluted from the position at the above-mentioned ratio, appropriately hardened water can be obtained without the need for forced dissolution means such as stirring as in the past.
更に、本発明の上記構成によれば次の利点がある。Furthermore, the above configuration of the present invention has the following advantages.
麦飯石等の鉱物を使用した水処理装置では、硬度成分の
溶解度が低いので、装置内を通過する課程で水と麦飯石
との接触時間を長くする必要があり、必然的に流路が長
くなるから、装置全体が複雑化することがあるが、本発
明の水処理装置の場合、位置が高い再溶解特性を有する
から、水との接触時間が少なくても自然に硬度成分が溶
出することと成り、流路を長くする必要もなく装置が複
雑化する心配がない。In water treatment equipment that uses minerals such as maifan stone, the solubility of hard components is low, so it is necessary to increase the contact time between the water and maifan stone during the process of passing through the equipment, and the flow path is inevitably long. However, in the case of the water treatment equipment of the present invention, the hardness components can be naturally eluted even if the contact time with water is short because the water treatment equipment of the present invention has high redissolution characteristics. Therefore, there is no need to lengthen the flow path and there is no need to worry about complicating the device.
第1図Iよ位置・の製造説HA図、第2図は本発明実施
例の水、処理装置の一部切欠断面図であり、図中、
(31)・φ・活性炭
(32)・・・イオン交換柑脂
(33) 争 争 φ 位置
代理人弁理士板上好博
第2図
第 1 図Fig. 1 is a manufacturing theory HA diagram with positions I and Fig. 2 is a partially cutaway sectional view of the water treatment equipment according to the embodiment of the present invention, and in the figure, (31), φ, activated carbon (32), etc.・Ion-exchanged citrus oil (33) Dispute Dispute φ Position Representative Patent Attorney Yoshihiro Itakami Figure 2 Figure 1
Claims (1)
て濾過し、・その後再び硬度成分を含有する可溶性物質
によって硬化する水処理装置において、上記活性炭やイ
オン交換樹脂等の吸着体層の下流側に、無機化された果
粒状の焼骨によって形成される焼骨層を設け、該焼骨層
によって硬度成分を溶出するようにした水処理装置。In a water treatment device in which water is softened with an ion exchange resin or the like, filtered with activated carbon or the like, and then hardened again with a soluble substance containing a hardness component, on the downstream side of the adsorbent layer of the activated carbon or ion exchange resin, A water treatment device provided with a burnt bone layer formed of mineralized burnt bone in the form of fruit particles, and hard components are eluted by the burnt bone layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9448683A JPS60889A (en) | 1983-05-27 | 1983-05-27 | Water treating apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9448683A JPS60889A (en) | 1983-05-27 | 1983-05-27 | Water treating apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60889A true JPS60889A (en) | 1985-01-05 |
JPS6219237B2 JPS6219237B2 (en) | 1987-04-27 |
Family
ID=14111610
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9448683A Granted JPS60889A (en) | 1983-05-27 | 1983-05-27 | Water treating apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60889A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01168394A (en) * | 1987-12-24 | 1989-07-03 | Tomiya Satou | Filter conditioner to increase hardness of drinking water, goldfish aquarium and water feeder tank |
JPH0427486A (en) * | 1990-05-22 | 1992-01-30 | Tomiya Satou | Method for purifying water and method for decomposing agricultural chemicals |
JP2008149201A (en) * | 2006-12-13 | 2008-07-03 | Mitomo:Kk | Apparatus for generating air-dissolved water |
US7527727B2 (en) * | 2003-10-22 | 2009-05-05 | Plymouth Technology, Inc. | Adsorption system |
-
1983
- 1983-05-27 JP JP9448683A patent/JPS60889A/en active Granted
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01168394A (en) * | 1987-12-24 | 1989-07-03 | Tomiya Satou | Filter conditioner to increase hardness of drinking water, goldfish aquarium and water feeder tank |
JPH0427486A (en) * | 1990-05-22 | 1992-01-30 | Tomiya Satou | Method for purifying water and method for decomposing agricultural chemicals |
US7527727B2 (en) * | 2003-10-22 | 2009-05-05 | Plymouth Technology, Inc. | Adsorption system |
JP2008149201A (en) * | 2006-12-13 | 2008-07-03 | Mitomo:Kk | Apparatus for generating air-dissolved water |
Also Published As
Publication number | Publication date |
---|---|
JPS6219237B2 (en) | 1987-04-27 |
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