JPH0425043B2 - - Google Patents

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Publication number
JPH0425043B2
JPH0425043B2 JP59248073A JP24807384A JPH0425043B2 JP H0425043 B2 JPH0425043 B2 JP H0425043B2 JP 59248073 A JP59248073 A JP 59248073A JP 24807384 A JP24807384 A JP 24807384A JP H0425043 B2 JPH0425043 B2 JP H0425043B2
Authority
JP
Japan
Prior art keywords
filter
filtration
water
plate
activated carbon
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 - Lifetime
Application number
JP59248073A
Other languages
Japanese (ja)
Other versions
JPS61129014A (en
Inventor
Taeko Suzuki
Sakae Karasawa
Taro Kawamura
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.)
YOKOHAMA TOWN
Original Assignee
YOKOHAMA TOWN
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by YOKOHAMA TOWN filed Critical YOKOHAMA TOWN
Priority to JP59248073A priority Critical patent/JPS61129014A/en
Publication of JPS61129014A publication Critical patent/JPS61129014A/en
Publication of JPH0425043B2 publication Critical patent/JPH0425043B2/ja
Granted legal-status Critical Current

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  • Treatment Of Water By Ion Exchange (AREA)
  • Filtration Of Liquid (AREA)
  • Water Treatment By Sorption (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、汚濁状態の原水をろ過して、清浄
な水を得るためのろ過器に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a filter for filtering contaminated raw water to obtain clean water.

〔従来の技術〕[Conventional technology]

従来のこの種のろ過器としては、例えば、実公
昭58−33772号公報に開示されているものがある。
A conventional filter of this type is disclosed in, for example, Japanese Utility Model Publication No. 58-33772.

このろ過器は、底部に網を張設し、内部に浄化
材を充填した複数個の浄水筒を、上下に重ねて多
重浄水筒をつくり、この多重浄水筒の上に、底部
に網を張設した給水筒をのせた構造のもので、給
水筒から供給した被ろ過水の自然流下による通水
によつて浄化水を得ようとするものである。
This filter consists of multiple water purification tubes with a net on the bottom and a purification material filled inside, which are stacked one above the other to create a multiple water purification tube, and a net is placed on the bottom of the multiple water purification tubes. It is constructed with a built-in water supply cylinder and is intended to obtain purified water through the natural flow of filtered water supplied from the water supply cylinder.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかし、従来のろ過器には、次のような問題点
があつた。
However, conventional filters have the following problems.

(1) 被ろ過水中に含まれるゴミなどの不溶性異物
は、給水筒の底部の網によつて除去されること
になるが、網だけでは不溶性異物が通過してし
まう。このため、浄水筒の浄化材の中に、通過
した不溶性異物が流入ないし混入し、浄化材の
性能が急激に劣化する。
(1) Insoluble foreign substances such as dust contained in the water to be filtered are removed by the net at the bottom of the water bottle, but if the net is only used, the insoluble foreign substances will pass through. For this reason, the insoluble foreign matter that has passed through the water filter enters or mixes into the purifying material of the water purifying cylinder, and the performance of the purifying material rapidly deteriorates.

(2) 被ろ過水は、自然流下によつて浄化材の間を
通過していくが、浄化材は粒状であるので、浄
化材層の中に流下の路ができ、浄化材層におけ
る被ろ過水の流路に偏りが生ずる。このため、
被ろ過水の流路周辺の浄化材のみしか被ろ過水
の浄化に寄与しないことになり、浄化材が有効
に活用されず、浄化効率が低下する。
(2) The water to be filtered passes between the purification materials by gravity, but since the purification materials are granular, there is a path for the water to flow down within the purification material layer, and the water to be filtered in the purification material layer passes through the purification materials. Unevenness occurs in the water flow path. For this reason,
Only the purification material around the flow path of the water to be filtered contributes to the purification of the water to be filtered, and the purification material is not effectively utilized, resulting in a decrease in purification efficiency.

(3) 被ろ過水の浄化は、浄化筒に充填した浄化材
によつてのみ行われる。浄水筒の底部にある網
は、単に浄化材の溢出を阻止するだけで、ろ過
層として機能しない。このため、従来のろ過器
の浄化能力は左程高くない。
(3) Purification of the water to be filtered is carried out only by the purification material filled in the purification cylinder. The net at the bottom of the water purification cylinder merely prevents the purification material from spilling out, and does not function as a filter layer. For this reason, the purification ability of conventional filters is not as high as the one shown above.

(4) 被ろ過水の浄化は、その自然流下によつて行
い、その流下速度は、主に浄化材の種類、性
状、浄化材層の深さ等によつて一義的に決ま
る。このため、被ろ過水の水質(汚れ)に応じ
た流下速度の制御をすることができない。
(4) The water to be filtered is purified by its natural flow, and the rate of flow is primarily determined by the type and properties of the purifying material, the depth of the purifying material layer, etc. For this reason, it is not possible to control the flow rate according to the quality (dirt) of the water to be filtered.

この発明は、このような従来の問題点を解決す
るためになされたもので、 (1) 浄化材の性能が急激に劣化せず、 (2) 浄化材を有効に活用することができ、 (3) 浄化能力が高く、 (4) 被ろ過水の流下速度を、その水質(汚れ)に
応じて可変制御することができる、 ろ過器を提供することを目的とする。
This invention was made to solve these conventional problems; (1) the performance of the purifying material does not deteriorate rapidly; (2) the purifying material can be used effectively; The purpose of the present invention is to provide a filter that (3) has a high purification ability and (4) can variably control the flow rate of water to be filtered depending on the quality (pollution) of the water.

〔課題を解決するための手段〕[Means to solve the problem]

この発明が提供するろ過器は、第1ろ過筒、第
2ろ過筒、第3ろ過筒およびろ過水受器を、上か
らこの順序で同軸的に重ね合せてなるろ過器であ
つて、前記第1ろ過筒は、下部開口部に設けたろ
過板と、ろ過板の上に密接配置したろ過布と、上
部開口部から入れた汚泥ろ過袋とを備え、前記第
2ろ過筒は、上部と下部がそれぞれ上部ろ過板と
中間部ろ過板とで仕切られた活性炭室と、上部と
下部がそれぞれ中間部ろ過板と下部ろ過板とで仕
切られたイオン交換樹脂室と、前記上部ろ過板、
中間部ろ過板および下部ろ過板に密接配置したろ
過布と、前記活性炭室に充填した活性炭と、前記
イオン交換樹脂室に充填したイオン交換樹脂と、
活性炭とイオン交換樹脂の中に一定の間隔をおい
て上下方向に並列配置した、複数の穴を有するじ
やま板とを備え、前記第3ろ過筒は、下部開口部
に設けたろ過板と、ろ過板の上に載置した少なく
とも1枚のろ紙と、ろ紙の上にのせる多数の穴を
有する押え蓋とを備えているものである。
The filter provided by the present invention is a filter in which a first filter tube, a second filter tube, a third filter tube, and a filtered water receiver are coaxially stacked in this order from above, and The first filter tube includes a filter plate provided in the lower opening, a filter cloth closely placed on the filter plate, and a sludge filtration bag inserted from the upper opening, and the second filter tube has an upper and lower part. an activated carbon chamber separated by an upper filter plate and a middle filter plate, an ion exchange resin chamber whose upper and lower parts are partitioned by an intermediate filter plate and a lower filter plate, respectively; and the upper filter plate.
A filter cloth closely arranged on the middle filter plate and the lower filter plate, activated carbon filled in the activated carbon chamber, and ion exchange resin filled in the ion exchange resin chamber,
The third filtration tube includes a filter plate having a plurality of holes arranged vertically in parallel at regular intervals in activated carbon and an ion exchange resin, and the third filtration tube includes a filter plate provided at a lower opening; It is equipped with at least one sheet of filter paper placed on a filter plate and a presser lid having a large number of holes placed on top of the filter paper.

〔作用〕 (1) 汚泥ろ過袋によつて被ろ過水に含まれるゴミ
などの不溶性異物をろ過するので、不溶性異物
が浄化材に混入、付着することによる浄化材の
性能の劣化を防止することができる。
[Function] (1) Since the sludge filtration bag filters out insoluble foreign matter such as garbage contained in the water to be filtered, it prevents deterioration of the performance of the purification material due to insoluble foreign matter getting mixed into or adhering to the purification material. I can do it.

(2) 浄化材である活性炭とイオン交換樹脂の中に
複数の穴を有するじやま板を介在させるので、
浄化材の中を流下する被ろ過水がじやま板によ
つて迷流し、すべての浄化材と一様に接触す
る。このため、すべての浄化材を有効に活用す
ることができ、浄化効率が向上する。
(2) Since a bamboo board with multiple holes is interposed between the purifying materials activated carbon and ion exchange resin,
The water to be filtered flowing down through the purification material is diverted by the cutting board and comes into uniform contact with all the purification materials. Therefore, all of the purification materials can be used effectively, and purification efficiency is improved.

(3) 活性炭とイオン交換樹脂だけでなく、汚泥ろ
過袋、ろ過板、ろ過布およびろ紙によつて被ろ
過水をろ過するので、その浄化能力を高くする
ことができる。
(3) Since the water to be filtered is filtered not only by activated carbon and ion exchange resin but also by a sludge filter bag, filter plate, filter cloth, and filter paper, its purification ability can be increased.

(4) 第3ろ過筒のろ過板の上に少なくとも1枚の
ろ紙を載置する構成になつているので、ろ紙の
枚数を可変することによつて、被ろ過水の流下
速度を制御し、その水質に最適(汚れの度合に
最適)の流下速度を選択することができる。
(4) Since at least one filter paper is placed on the filter plate of the third filter cylinder, by varying the number of filter papers, the flow rate of the water to be filtered can be controlled, It is possible to select the flow rate that is optimal for the water quality (optimal for the degree of contamination).

〔実施例〕〔Example〕

以下、この発明の実施例を第1図〜第5図によ
つて説明する。第1図は実施例のろ過器の全体構
成を示す縦断面図であり、第2図〜第5図は第1
図のろ過器を分解したときの、各部分の細部構成
を示したものである。
Embodiments of the present invention will be described below with reference to FIGS. 1 to 5. FIG. 1 is a vertical sectional view showing the overall configuration of the filter of the embodiment, and FIGS.
This figure shows the detailed structure of each part when the filter shown in the figure is disassembled.

第2図において、2は第1ろ過筒で、3はその
下部開口部に設けたろ過板である。1は、水は通
すが固形物は通さない紙よりなる汚泥ろ過袋で、
第1ろ過筒2の中に口をひろげて挿入されてい
る。このとき、汚泥ろ過袋1の開口部端縁に設け
た掛止部24が第1ろ過筒2の上部口縁に掛止さ
れる。上記ろ過板3は2mm径の穴を多数有する板
で、その上には周囲を接着した40メツシユのポリ
エチレン布(この発明にいうろ過布)4が密接状
態で置かれている。第1ろ過筒2は、下方に突設
した接合部5を、第3図に示す第2ろ過筒7の上
端部に突設した接合部5bに嵌合し、それぞれに
120度間隔で設けた3個の突起6aと突起6bを
相互に係合することにより、第2ろ過筒7に確実
に連結される。
In FIG. 2, 2 is a first filter cylinder, and 3 is a filter plate provided at its lower opening. 1 is a sludge filter bag made of paper that allows water to pass through but does not allow solid matter to pass through.
It is inserted into the first filter cylinder 2 with its mouth opened. At this time, the hook part 24 provided at the edge of the opening of the sludge filter bag 1 is hooked to the upper edge of the first filter tube 2. The filter plate 3 is a plate having a large number of holes with a diameter of 2 mm, and a 40-mesh polyethylene cloth (filter cloth according to the present invention) 4, whose periphery is bonded, is tightly placed on the filter plate 3. The first filtration tube 2 has a downwardly protruding joint 5 that fits into a joint 5b that protrudes from the upper end of the second filtration tube 7 shown in FIG.
The three protrusions 6a and 6b provided at 120 degree intervals are reliably connected to the second filter cylinder 7 by engaging with each other.

第3図において、7は第2ろ過筒、8はその上
部開口部に設けたろ過板で、2mm径の穴を多数を
有する。その上に、40メツシユのポリエチレン布
9が密接状態で置かれている。10はろ過板8か
ら下方にのびたつめである。12は活性炭室で、
活性炭が充填されている。活性炭12の中には、
上下方向に一定の間隔をおいて2枚のじやま板1
1が挿入されている。このじやま板11は、小径
の穴を多数有するポリエチレン樹脂の板である。
後述するイオン交換樹脂室15に通ずる活性炭室
12の底部は、約30度の逆円錐状の傾斜面になつ
ている。15は、活性炭室12よりも小さいイオ
ン交換樹脂室で、活性炭室12との間はろ過板1
3で仕切られている。ろ過板13の上には密接状
態で60メツシユのポリエチレン布14が置かれて
いる。ろ過板13は、第5図に示すように穴13
aを設けた十字板となつている。イオン交換樹脂
室15の底部には、2mm径の多数の穴を有するろ
過板17が設けられ、その下には密接状態で60メ
ツシユのポリエチレン布18がセツトされてい
る。イオン交換樹脂室15には、陽イオン交換樹
脂が充填されており、その中には、前記じやま板
11と平行にじやま板16が挿入されている。2
6は蓋押え筒で、第4図の押え蓋20を押えるた
めのものである。
In FIG. 3, 7 is a second filter cylinder, 8 is a filter plate provided at the upper opening thereof, and has a large number of holes with a diameter of 2 mm. On top of this, 40 meshes of polyethylene cloth 9 are placed in close contact. 10 is a pawl extending downward from the filter plate 8. 12 is the activated carbon chamber,
Filled with activated carbon. Inside the activated carbon 12,
Two jiyama boards 1 at regular intervals in the vertical direction
1 is inserted. This wall board 11 is a polyethylene resin board having many small diameter holes.
The bottom of the activated carbon chamber 12, which communicates with an ion exchange resin chamber 15 to be described later, has an inverted conical slope of about 30 degrees. 15 is an ion exchange resin chamber smaller than the activated carbon chamber 12, and a filter plate 1 is connected between it and the activated carbon chamber 12.
It is separated by 3. On top of the filter plate 13, 60 meshes of polyethylene cloth 14 are placed in close contact. The filter plate 13 has holes 13 as shown in FIG.
It is shaped like a cross board with a. At the bottom of the ion exchange resin chamber 15, a filter plate 17 having a large number of holes of 2 mm in diameter is provided, and 60 meshes of polyethylene cloth 18 are tightly set under the filter plate 17. The ion exchange resin chamber 15 is filled with a cation exchange resin, and a diagonal plate 16 is inserted in parallel to the diagonal plate 11. 2
Reference numeral 6 denotes a lid holding cylinder, which is used to hold down the holding lid 20 shown in FIG.

第4図において、19は第2ろ過筒である。2
0は後述するろ紙21の押え蓋で、2mm径の多数
の穴を有する。22は第3ろ過筒19の下部開口
部に設けたろ過板で、2mm径の穴を多数有する。
ろ過板22と押え蓋20の間には、ろ紙21が置
かれている。通常、1〜5枚の範囲で所要枚数だ
け置かれる。25は押え蓋20のつまみである。
23はろ過水受器で、ろ過を完了した水を受ける
容器である。
In FIG. 4, 19 is a second filter cylinder. 2
Reference numeral 0 denotes a holding lid for filter paper 21, which will be described later, and has a large number of holes with a diameter of 2 mm. Reference numeral 22 denotes a filter plate provided at the lower opening of the third filter cylinder 19, which has many holes with a diameter of 2 mm.
A filter paper 21 is placed between the filter plate 22 and the holding lid 20. Usually, the required number of cards in the range of 1 to 5 is placed. 25 is a knob of the presser cover 20.
23 is a filtered water receiver, which is a container for receiving filtered water.

上記第1〜第3ろ過筒2,7,19とろ過水受
器23は第1図に示すように、上下方向に同軸的
に重ね合せて使用する。
As shown in FIG. 1, the first to third filter cylinders 2, 7, 19 and the filtered water receiver 23 are used by being coaxially stacked in the vertical direction.

実施例のろ過器は、上記のような構成になつて
いるので、原水は次のように浄化される。
Since the filter of the embodiment has the above-described configuration, raw water is purified as follows.

すなわち、汚濁状態の原水を汚泥ろ過袋1に入
れると、原水の汚濁原因物質中の粗大なものは、
これにより除去される。この汚泥ろ過袋1は、掛
合部24を第1ろ過筒2に引止するようになつて
いるので、目づまりを起こした場合は、直ちに交
換できる。汚泥ろ過袋1を通つて汚泥や不溶性異
物を除かれた水は、第1ろ過筒2の底部のポリエ
チレン布4とろ過板3を通つて粗ろ過される。
In other words, when polluted raw water is put into the sludge filtration bag 1, coarse substances in the raw water contamination-causing substances are
This removes it. This sludge filter bag 1 is designed so that the engaging part 24 is retained on the first filter tube 2, so that if it becomes clogged, it can be replaced immediately. Water from which sludge and insoluble foreign matter have been removed through the sludge filter bag 1 is roughly filtered through the polyethylene cloth 4 and filter plate 3 at the bottom of the first filter tube 2.

粗ろ過された水は、ポリエチレン布9とろ過板
8を通つて、第2ろ過筒7に移る。そして、活性
炭室12を通ると、水中の有機物は活性炭に吸着
除去され、その下のイオン交換樹脂室15へ流下
する。
The coarsely filtered water passes through the polyethylene cloth 9 and the filter plate 8 and moves to the second filter tube 7. When the water passes through the activated carbon chamber 12, the organic matter in the water is adsorbed and removed by the activated carbon, and flows down to the ion exchange resin chamber 15 below.

この活性炭室15には、ろ過板8の下側に活性
炭層中に延びるつめ10があり、活性炭層中には
2枚のじやま板11が入れてあるので、流下する
水は活性炭層中で迷流する。その結果、水と活性
炭の接触面積が大となつて、活性炭の浄化作用が
有効に活用され、ろ過効率が向上する。活性炭室
12の底部は約30度の傾斜面となつているので、
水の流れが促進される。
This activated carbon chamber 15 has a pawl 10 extending into the activated carbon layer below the filter plate 8, and two circumferential plates 11 are inserted into the activated carbon layer, so that the water flowing down is contained in the activated carbon layer. Get lost. As a result, the contact area between water and activated carbon increases, the purifying action of activated carbon is effectively utilized, and filtration efficiency is improved. Since the bottom of the activated carbon chamber 12 has an approximately 30 degree slope,
Water flow is encouraged.

水は、活性炭室12からろ過板13とその上の
ポリエチレン布14を通つて、その下のイオン交
換樹脂室15に流下し、水に含まれるアンモニ
ア、重金属は陽イオン交換樹脂により除去され
る。すでに活性炭室12で有機物が除去されてい
るので、イオン交換樹脂が有機物で汚れることは
なく、水中のイオン化している物質は効果的に除
去される。なお、イオン交換樹脂として陽イオン
交換樹脂に適当な比率で陰イオン交換樹脂を混合
したものを使用すれば、陰イオン物質も除去でき
るので、河川水、雨水をろ過して清浄水を得るこ
ともできる。
Water flows from the activated carbon chamber 12 through the filter plate 13 and the polyethylene cloth 14 above it, and flows down into the ion exchange resin chamber 15 below, where ammonia and heavy metals contained in the water are removed by the cation exchange resin. Since the organic matter has already been removed in the activated carbon chamber 12, the ion exchange resin is not contaminated with organic matter, and the ionized substances in the water are effectively removed. In addition, if you use a mixture of cation exchange resin and anion exchange resin in an appropriate ratio as the ion exchange resin, anion substances can also be removed, so you can obtain clean water by filtering river water and rainwater. can.

このイオン交換樹脂室15にも、活性炭室12
と同様に小径の穴を有するポリエチレン樹脂の板
を、じやま板としてイオン交換樹脂中に挿入して
あるので、水はこれによつて迷流となる。その結
果、イオン交換樹脂の浄化作用が有効に活用さ
れ、ろ過効率が向上する。水は第2ろ過筒7の底
部にあるろ過板17とその下のポリエチレン布1
8を経て次の第3ろ過筒19に移る。
This ion exchange resin chamber 15 also has an activated carbon chamber 12.
Similarly, a polyethylene resin plate with small-diameter holes is inserted into the ion exchange resin as a barrier plate, so that the water becomes a stray flow. As a result, the purifying action of the ion exchange resin is effectively utilized, and filtration efficiency is improved. The water is filtered through the filter plate 17 at the bottom of the second filter tube 7 and the polyethylene cloth 1 below it.
8 and then moves to the next third filter cylinder 19.

第3ろ過筒では、ろ過板22の上にろ紙21を
1枚ないし5枚置き、このろ紙の上に押え蓋20
を置き、これを第2ろ過筒7の底部から突出する
蓋押え筒26で確実に押さえる。このように押え
ると、ろ紙21は互に密着するので、水もれが少
なく、ろ紙の間に空気が入らないようになる。押
え蓋20には、つまみ25があるので、着脱容易
である。また、ろ紙21が汚れた場合に、その交
換が容易なので、ろ紙21によるろ過効率を長期
間有効に保持できる。また、ろ紙は1枚から5枚
の範囲で増減すると、水の流下速度が変化するの
で、原水の水質(汚れ)に応じてろ過速度を変え
ることができる。
In the third filter cylinder, one to five pieces of filter paper 21 are placed on the filter plate 22, and a presser lid 20 is placed on top of the filter paper.
and securely press it with the lid presser tube 26 protruding from the bottom of the second filtration tube 7. When pressed in this manner, the filter papers 21 are brought into close contact with each other, which reduces water leakage and prevents air from entering between the filter papers. Since the presser cover 20 has a knob 25, it can be easily attached and detached. Further, when the filter paper 21 becomes dirty, it is easy to replace it, so that the filtration efficiency of the filter paper 21 can be effectively maintained for a long period of time. Furthermore, if the number of filter papers is increased or decreased in the range of 1 to 5, the flow rate of water changes, so the filtration rate can be changed depending on the quality (dirt) of the raw water.

このようにしてろ過された水は最後にろ過水受
器23に入る。このろ過水受器は用途に応じて形
状、大きさを変えることができる。
The water thus filtered finally enters the filtered water receiver 23. The shape and size of this filtered water receiver can be changed depending on the purpose.

上述のように、実施例のろ過器においては、第
1段階で粗ろ過を行つてあらかじめ不溶性異物を
除去するので、不溶性異物の付着による活性炭等
の浄化材の性能の劣化を防止することができる。
As mentioned above, in the filter of the example, in the first stage, rough filtration is performed to remove insoluble foreign matter in advance, so it is possible to prevent deterioration of the performance of the purification material such as activated carbon due to the adhesion of insoluble foreign matter. .

また水は、活性炭室12のつめ10と両方の室
12,15に置いたじやま板11,15により迷
流となるので、浄化材との接触面積が大きくな
り、浄化材の有効活用が可能となる。また活性炭
室12の底部に約30度の傾斜をつけたことにより
流速を増す効果がある。
In addition, the water becomes a stray flow due to the pawl 10 of the activated carbon chamber 12 and the cutting boards 11 and 15 placed in both chambers 12 and 15, so the contact area with the purification material becomes larger and the purification material can be used more effectively. becomes. Furthermore, the bottom of the activated carbon chamber 12 is sloped at approximately 30 degrees, which has the effect of increasing the flow velocity.

そして、2mm径の多数の穴を有するろ過板8と
40メツシユのポリエチレン布9の組み合わせ、十
字板のろ過板13と60メツシユポリエチレン布1
4の組合せ、更に2mm径の穴多数を有するろ過板
17と60メツシユのポリエチレン布18の組合せ
の3個の組合せを上部より順次に設けたので、ろ
過速度が安定するとともに、原水の浄化能力が向
上する。
And a filter plate 8 having a large number of holes with a diameter of 2 mm.
Combination of 40 mesh polyethylene cloth 9, cross plate filter plate 13 and 60 mesh polyethylene cloth 1
4 combination, and a combination of a filter plate 17 with a large number of 2 mm diameter holes and a polyethylene cloth 18 of 60 meshes, which are sequentially provided from the top, stabilize the filtration rate and improve the raw water purification ability. improves.

水は最後に第3ろ過筒19のろ紙21によりろ
過されるのであるが、このろ紙21は原水の水質
に応じて1枚から5枚の間で増減してろ過速度を
変えることができるので、水質にあつた浄化が可
能になる。また、汚れた場合は、速やかに交換で
きる。
The water is finally filtered by the filter paper 21 of the third filter tube 19, and the filtration speed can be changed by increasing or decreasing the number of filter papers 21 between 1 and 5 sheets depending on the quality of the raw water. It becomes possible to purify water according to its quality. Also, if it gets dirty, you can quickly replace it.

〔発明の効果〕〔Effect of the invention〕

以上説明したように、この発明は、上記のよう
な構成としたので、次の効果を奏する。
As explained above, since the present invention has the above configuration, it has the following effects.

(1) 浄化材(活性炭、イオン交換樹脂)の急激な
劣化を防止することができる。
(1) Rapid deterioration of purification materials (activated carbon, ion exchange resin) can be prevented.

(2) 浄化材を無駄なく有効に活用することができ
る。
(2) Purification materials can be used effectively without waste.

(3) 被ろ過水の浄化能力を高くすることができ
る。
(3) The ability to purify water to be filtered can be increased.

(4) 被ろ過水の流下速度を、その水質(汚れ)に
応じて可変制御することができる。
(4) The flow rate of the water to be filtered can be variably controlled depending on the quality of the water (dirt).

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

第1図はこの発明の実施例の全体構成を示す縦
断面図、第2図は第1図における第1ろ過筒の縦
断面図、第3図は第1図における第2ろ過筒の縦
断面図、第4図は第1図における第3ろ過筒とろ
過水受器の縦断面図、第5図は第1図における十
字板の平面図である。 1……汚泥ろ過袋、2……第1ろ過筒、3……
ろ過板、4……ポリエチレン布、7……第2ろ過
筒、8……ろ過板、9……ポリエチレン布、11
……じやま板、12……活性炭室、13……ろ過
板、15……イオン交換樹脂室、16……じやま
板、17……ろ過板、18……ポリエチレン布、
19……第3ろ過筒、20……押さえ蓋、21…
…ろ紙、22……ろ過板、23……ろ過水受器。
FIG. 1 is a vertical cross-sectional view showing the overall configuration of an embodiment of the present invention, FIG. 2 is a vertical cross-sectional view of the first filter tube in FIG. 1, and FIG. 3 is a vertical cross-section of the second filter tube in FIG. 1. 4 is a vertical sectional view of the third filter tube and filtered water receiver in FIG. 1, and FIG. 5 is a plan view of the cross plate in FIG. 1. 1... Sludge filter bag, 2... First filter cylinder, 3...
Filter plate, 4... Polyethylene cloth, 7... Second filter tube, 8... Filter plate, 9... Polyethylene cloth, 11
... Diyama board, 12... Activated carbon chamber, 13... Filtration plate, 15... Ion exchange resin chamber, 16... Diyama board, 17... Filter plate, 18... Polyethylene cloth,
19... Third filter cylinder, 20... Pressing lid, 21...
... Filter paper, 22 ... Filter plate, 23 ... Filtered water receiver.

Claims (1)

【特許請求の範囲】[Claims] 1 第1ろ過筒、第2ろ過筒、第3ろ過筒および
ろ過水受器を、上からこの順序で同軸的に重ね合
せてなるろ過器であつて、前記第1ろ過筒は、下
部開口部に設けたろ過板と、ろ過板の上に密接配
置したろ過布と、上部開口部から入れた汚泥ろ過
袋とを備え、前記第2ろ過筒は、上部と下部がそ
れぞれ上部ろ過板と中間部ろ過板とで仕切られた
活性炭室と、上部と下部がそれぞれ中間部ろ過板
と下部ろ過板とで仕切られたイオン交換樹脂室
と、前記上部ろ過板、中間部ろ過板および下部ろ
過板に密接配置したろ過布と、前記活性炭室に充
填した活性炭と、前記イオン交換樹脂室に充填し
たイオン交換樹脂と、活性炭とイオン交換樹脂の
中に一定の間隔をおいて上下方向に並列配置し
た、複数の穴を有するじやま板とを備え、前記第
3ろ過筒は、下部開口部に設けたろ過板と、ろ過
板の上に載置した少なくとも1枚のろ紙と、ろ紙
の上にのせる多数の穴を有する押え蓋とを備えて
いることを特徴とするろ過器。
1 A filter consisting of a first filtration tube, a second filtration tube, a third filtration tube, and a filtered water receiver stacked coaxially in this order from above, wherein the first filtration tube has a lower opening. The second filtration tube is equipped with a filtration plate provided on the filtration plate, a filtration cloth closely placed on the filtration plate, and a sludge filtration bag inserted from the upper opening, and the second filtration tube has an upper part and a lower part that are connected to the upper filtration plate and an intermediate part, respectively. An activated carbon chamber separated by a filter plate, an ion exchange resin chamber whose upper and lower parts are partitioned by an intermediate filter plate and a lower filter plate, respectively, and an activated carbon chamber which is in close contact with the upper filter plate, the intermediate filter plate, and the lower filter plate. The arranged filter cloth, the activated carbon filled in the activated carbon chamber, the ion exchange resin filled in the ion exchange resin chamber, and a plurality of filter cloths arranged vertically in parallel with a certain interval between the activated carbon and the ion exchange resin. The third filter tube includes a filter plate provided at the lower opening, at least one filter paper placed on the filter plate, and a plurality of filter paper placed on the filter paper. 1. A filter comprising: a presser cover having a hole;
JP59248073A 1984-11-26 1984-11-26 Filter Granted JPS61129014A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59248073A JPS61129014A (en) 1984-11-26 1984-11-26 Filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59248073A JPS61129014A (en) 1984-11-26 1984-11-26 Filter

Publications (2)

Publication Number Publication Date
JPS61129014A JPS61129014A (en) 1986-06-17
JPH0425043B2 true JPH0425043B2 (en) 1992-04-28

Family

ID=17172800

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59248073A Granted JPS61129014A (en) 1984-11-26 1984-11-26 Filter

Country Status (1)

Country Link
JP (1) JPS61129014A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2711129B1 (en) * 1993-10-12 1996-02-02 Aerospatiale Washing water treatment and recycling station for a washing machine.
KR100461903B1 (en) * 2002-12-13 2004-12-17 한국수자원공사 Meandering flow powered activated charcoal contactor with paneled barriers

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5833772A (en) * 1981-08-24 1983-02-28 Hitachi Ltd Processor switching system
JPS5833772U (en) * 1981-08-29 1983-03-04 スズキ株式会社 motorcycle intake system

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5833772A (en) * 1981-08-24 1983-02-28 Hitachi Ltd Processor switching system
JPS5833772U (en) * 1981-08-29 1983-03-04 スズキ株式会社 motorcycle intake system

Also Published As

Publication number Publication date
JPS61129014A (en) 1986-06-17

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