JPS61129014A - Filter - Google Patents

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Publication number
JPS61129014A
JPS61129014A JP59248073A JP24807384A JPS61129014A JP S61129014 A JPS61129014 A JP S61129014A JP 59248073 A JP59248073 A JP 59248073A JP 24807384 A JP24807384 A JP 24807384A JP S61129014 A JPS61129014 A JP S61129014A
Authority
JP
Japan
Prior art keywords
filter
filtration
water
plate
raw water
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP59248073A
Other languages
Japanese (ja)
Other versions
JPH0425043B2 (en
Inventor
Taeko Suzuki
鈴木 妙子
Sakae Karasawa
唐沢 栄
Taro Kawamura
河村 太郎
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.)
YOKOHAMASHI
Original Assignee
YOKOHAMASHI
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 YOKOHAMASHI filed Critical YOKOHAMASHI
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)

Abstract

PURPOSE:To efficiently perform filtering, by stepwise performing filtering by combining a raw water receiver, a first filter pat, a second filter part and a filtrate receiver. CONSTITUTION:In a filter, rough filtering is performed by an uppermost raw water receiver A comprising a raw water receiving cylinder 2, which is equipped with a sludge filer bag 1, polyethylene cloth 4 and a filter plate 3, as a first stage to remove an insoluble substance while the filtrate is flowed down to the first filter part B of a second state. This first filter part B is separated into an activated carbon chamber 12 and an ion exchange resin chamber 15 therebelow and, after the org. substance in water was removed by the activated carbon chamber 12, treated water is flowed down to the ion exchange resin chamber 15 to remove an ionized substance. Subsequently, water is sent to a second filter part C, wherein filter paper 21 and a press lid 20 are placed on a filter plate 22 and the filter paper 21 is certainly pressed by a id press cylinder 26, to be filtered by the filter paper 21 and the obtained filtered water is received by a filtrate receiver D(23).

Description

【発明の詳細な説明】 産業上の利用分野 本発明は汚濁状態の原水2p過して、清浄な水を得るた
めのろ過器に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a filter for obtaining clean water by filtering 2 points of contaminated raw water.

従来の技術 従来のろ過器は一体となった単なる筒状体に異種ろ過材
を混合して収納しtものであつ之−発明が解決しようと
する問題点 従来のろ過器は一体となった単なる筒状体に異種のろ過
材ヲ温会して収納したものであり。
Prior Art Conventional filters are a simple integrated cylindrical body containing a mixture of different types of filter media.The problem to be solved by the invention. Different types of filter media are heated and stored in a cylindrical body.

ろ過動率が悪く、良好な結果が得らバす、1之部材の取
換えも困難であつ之。
The filtration rate is poor, good results cannot be obtained, and it is difficult to replace parts.

問題点を解決するための手段 第2図に於てAは原水受器ケ示し、1は水に通すが固形
物は通さない紙エリなる汚泥ろ過袋で原水受筒2内にひ
ろげて置かれる。3は2団径の穴を多数有するろ過板で
あって、その上には周囲全接着した40メソ/ユのポリ
エチレン布4が密接して置かれる。原水受筒2の下端部
は下方に延長させて接合部5とし、第3図Bに示す第1
ろ過部の上端の接合部5′と嵌合(−13個の凸起6と
5′の突起6′により確実に連結される。
Means for solving the problem In Figure 2, A indicates the raw water receiver, and 1 is a sludge filter bag with a paper rim that allows water to pass through but does not allow solid matter to pass through and is spread out inside the raw water receiver 2. . Reference numeral 3 denotes a filter plate having a large number of holes of two diameters, on which a 40 meso/yu polyethylene cloth 4, which is entirely bonded around the periphery, is closely placed. The lower end of the raw water receiver 2 is extended downward to form a joint 5, and the first joint shown in FIG.
It fits into the joint part 5' at the upper end of the filtration part (-13 protrusions 6 and the protrusion 6' of 5' ensure connection).

第3図に於て8は第1ろ過部であって、7は第1ろ過部
でその上部8はろ過板で2簡径の穴多数を有する。その
上°に40メツシユのポリエチレン布9を置く。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、活性炭を充填し、その中に間隔欠おいて2枚のじゃ
ま板11を浮かせ友状態で置く。このじゃま板11は小
径の穴ケ多数有するポリエチレン樹脂の板である。活性
炭室12の底部は約30度の傾斜があり、活性炭室12
エリも狭いイオン交換樹脂室15に連通ずるので第1ろ
過部の内部全体は漏斗状の構造となっている、活性炭室
の底部でイオン交換樹脂室に通ずる部分には、ろ過板1
3とその上に密接して60メツシユのポリエチレン布が
置かれる。このろ過板13は第5図に示すように十字板
とすることが必要でおる。
In FIG. 3, numeral 8 is a first filtration section, 7 is a first filtration section, and the upper part 8 of the first filtration section is a filtration plate having a large number of holes of two small diameters. A 40 mesh polyethylene cloth 9 is placed on top of it. 10 is a pawl extending downward from the filter plate 8. Reference numeral 12 denotes an activated carbon chamber filled with activated carbon, in which two baffle plates 11 are placed at intervals in a floating manner. This baffle plate 11 is a polyethylene resin plate having many small diameter holes. The bottom of the activated carbon chamber 12 has an inclination of approximately 30 degrees, and the activated carbon chamber 12
The area also communicates with the narrow ion exchange resin chamber 15, so the entire interior of the first filtration section has a funnel-shaped structure.At the bottom of the activated carbon chamber that communicates with the ion exchange resin chamber, there is a filter plate 1.
3 and a 60 mesh polyethylene cloth is placed closely over it. This filter plate 13 needs to be a cross plate as shown in FIG.

15はイオン交換樹脂室で、上部には前述の十字板のろ
過板13と60メツシユのポリエチレン布14があり底
部には2ff径の多数の穴を有するろ過板17とその下
に密接して60メツシユのポリエチレン布18があり、
この間にイオン交換樹脂を充填し、その中間位置イオン
交換樹脂中にじゃま板165c浮か(−た状懇で置(。
Reference numeral 15 denotes an ion-exchange resin chamber, on the top of which there is the above-mentioned cross-shaped filter plate 13 and a 60-mesh polyethylene cloth 14, and on the bottom there is a filter plate 17 with a large number of holes of 2 ff diameter, and a 60-mesh filter is placed closely below it. There is mesh polyethylene cloth 18,
During this period, an ion exchange resin is filled, and a baffle plate 165c is placed floating in the ion exchange resin at an intermediate position.

第4図のCは第2ろ過部で、19は第2ろ過部、20i
ろ紙の押さえ蓋で、 2m+径の多数の穴を有する。最
下端ICは2m径の大多数ヲ肩する濾過板22があり、
このろ過板22と押え蓋2′00間にろ紙21を置く、
ろ紙の数は1〜5枚である。第4図のり、23は受器で
ろ過ヶ完了し九水を受ける容器である。これらの原水受
器(第2図A)、第1ろ過部(第3図B)、第2ろ過部
及び受器(第4図C、D )、H第1図に示すように一
体に重ね合せて使用する。なお24は汚泥ろ過部1の上
端に取付けた掛合部で、これで汚泥ろ過部1を原水受筒
2に引掛ける。第3図Bの下端26は蓋押さえ筒で、第
4図Cの押さえ蓋20を押さえるものである、まfci
K4図Cの25は押え蓋20のつまみである。
C in Figure 4 is the second filtration section, 19 is the second filtration section, 20i
It has a filter paper presser lid with numerous holes of 2m+ diameter. The lowest IC has a filter plate 22 that covers the majority of the 2m diameter.
Place the filter paper 21 between this filter plate 22 and the presser cover 2'00,
The number of filter papers is 1 to 5. In Fig. 4, 23 is a container that receives the nine water after filtration is completed in the receiver. These raw water receiver (Fig. 2A), first filtration part (Fig. 3B), second filtration part and receiver (Fig. 4C, D), H are stacked together as shown in Fig. 1. Use together. Note that 24 is a hooking part attached to the upper end of the sludge filtration part 1, which hooks the sludge filtration part 1 onto the raw water receiving tube 2. The lower end 26 of FIG. 3B is a lid holding cylinder, which holds down the holding lid 20 of FIG. 4C.
25 in Figure C of K4 is the knob of the presser cover 20.

作用 汚濁状態の原水を、まず第2図Aに示す原水受器Aの原
水受筒2中に置いた汚泥ろ過部1に入れると、この汚泥
ろ過部1t′s、水を通すが、汚泥や不溶物を通さない
ので、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。この汚泥ろ過部1は上端に掛合部があり、
これに交換できる。汚泥ろ過部を通って汚泥や不溶物勿
除かれ之水は原水受@2の底部の60メツシユのポリエ
チレン布4と2■径の穴を多数有するろ過板3で辿って
粗ろ過される。
When raw water in a state of action pollution is first put into the sludge filtration section 1 placed in the raw water receiver 2 of the raw water receiver A shown in Figure 2A, this sludge filtration section 1t's allows water to pass through, but sludge and Since it does not allow insoluble matter to pass through, coarse substances in raw water pollution-causing substances are removed. This sludge filtration section 1 has a hooking section at the upper end,
You can exchange it for this. The water, from which sludge and insoluble matters have been removed through the sludge filtration section, is coarsely filtered through a 60-mesh polyethylene cloth 4 and a filter plate 3 having a large number of 2-diameter holes at the bottom of the raw water receiver @2.

原水受器A’z通過した水は、40メツシユのポリエチ
レン布9と2+m径の穴多数を有するろ過板8紮辿って
、原水受iAと密着し′fc第1ろ過部(第3図B)の
第1ろ過部7に移る。第1ろ過部の上方部分は活性炭室
12であって、これkmすことVCLり水中の有機物ケ
吸着除去し、その下のイオン交換樹脂室へ流下きせる。
The water that has passed through the raw water receiver A'z follows a 40-mesh polyethylene cloth 9 and a filter plate 8 having a number of holes with a diameter of 2+m, and comes into close contact with the raw water receiver iA'fc first filtration section (Fig. 3B). The process moves to the first filtration section 7. The upper part of the first filtration section is an activated carbon chamber 12, which adsorbs and removes organic matter in the VCL water over a km, and allows it to flow down to the ion exchange resin chamber below.

この活性炭室には、前述のようにろ過板8の下に活性炭
層中に延びるツメ10があり活性炭層中には2枚のじゃ
ま板が入れであるので、流下する水は活性炭層中で遅流
させられ水とる材の接触面積が大となって、ろ過効率を
向上することができる。また底部は約30度の傾斜を1
するので”水の流れを促進する、活性炭室から水は十字
板のろ過板13とその上に密着した60メツ7ユのポリ
エチレン布を通ってその下のイオン交換樹脂室15に流
下し、陽イオン交換樹脂により。
As mentioned above, this activated carbon chamber has a claw 10 extending into the activated carbon layer below the filter plate 8, and two baffle plates are inserted into the activated carbon layer, so that the water flowing down is slowed down in the activated carbon layer. The contact area of the water-collecting material increases, and filtration efficiency can be improved. In addition, the bottom part has a slope of about 30 degrees.
Therefore, the water flows from the activated carbon chamber through the cross-shaped filter plate 13 and the 60 mm/7 mm polyethylene cloth tightly attached to it, and flows into the ion exchange resin chamber 15 below, which promotes water flow. By ion exchange resin.

アンモニア、重金属が除去される。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
物により汚れることがなく。
Ammonia and heavy metals are removed. Already activated carbon chamber 12
Since organic matter is removed, the ion exchange resin will not be contaminated by organic matter.

水中のイオン化(−でいる物質衡効果的に除去できる。Ionization (-) in water can be effectively removed.

ま九陽イオン交換樹脂に適当な比率で陰イオン交換樹@
5C混合すれば、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。このイ
オン交換樹脂室にも、活性炭室と同様に小径の穴2iす
るポリエチレン樹脂の板を、じゃま板としてイオン交換
樹脂中に浮かせであるので、水は遅流となりろ過効率が
向上する。水は第1ろ過部の底部にある2龍径の穴ヲ鳴
するろ過板とその下の60メツシュのポリエチレン布を
経て次の第2ろ退部(第4図C)に移る。
Add anion exchange resin to cation exchange resin in an appropriate ratio
By mixing 5C, anionic substances can also be removed, so river water and rainwater can be filtered to obtain clean water. In this ion-exchange resin chamber, as in the activated carbon chamber, a polyethylene resin plate with small diameter holes 2i is suspended in the ion-exchange resin as a baffle plate, so water flows slowly and the filtration efficiency is improved. The water passes through the filter plate with two diameter holes at the bottom of the first filtration part and the 60 mesh polyethylene cloth below it, and then moves to the next second filtration part (Fig. 4C).

第2ろ退部(第4図C)の第2ろ退部はその底部が2+
m径の多数の穴欠有するろ過板22で、その上にろ紙2
1を1枚乃至5枚置き、このろ紙の上に2醜径の穴を多
数有する押さえ蓋2010、第1ろ退部の底部から突出
する蓋押さえ筒26で確実に押さえる。このように押さ
えると、ろ紙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。押さえ蓋20には
、つまみ25があるので着脱容・  易で、ろ紙が汚れ
た場合にろ紙の交換が容易なのでろ紙のろ過動率を長期
間有効に保持できる。
The bottom of the second filtering part (Fig. 4C) is 2+
A filter plate 22 having a large number of holes with a diameter of m, and a filter paper 2 on it.
One to five sheets of filter paper No. 1 are placed on top of the filter paper, and the filter paper is securely pressed with a holding lid 2010 having a large number of holes of two diameters and a lid holding cylinder 26 protruding from the bottom of the first filtration part. When pressed in this way, the filter papers will stick together, reducing water leakage and preventing air from entering between the filter papers. The presser lid 20 has a knob 25, so it can be easily attached and removed, and when the filter paper becomes dirty, it is easy to replace the filter paper, so that the filtration rate of the filter paper can be maintained effectively for a long period of time.

1fcろ紙は1枚から5枚の範囲で増減することにより
原水の水質に応じてろ過速度ヲ変えることができる。こ
のようにしてろ過され之水は最後に第4図Cのろ過水受
器23に入れる。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。
By increasing or decreasing the number of 1fc filter papers in the range of 1 to 5, the filtration speed can be changed depending on the quality of the raw water. The water thus filtered is finally put into the filtered water receiver 23 shown in FIG. 4C. This filtered water receiver has different shapes depending on the application.
You can change the size.

発明の効果 本発明のろ過器に於ては第1段階として最上部の原水受
器Aで粗ろ過を行なって不溶物を除いてから、第2段階
の第1ろ退部へ流下させる。
Effects of the Invention In the filter of the present invention, as a first stage, rough filtration is performed in the uppermost raw water receiver A to remove insoluble matters, and then the raw water is allowed to flow down to the first filtration section of the second stage.

そしてこの第1ろ退部Bは活性炭室とその下のイオン交
換樹脂室とに別れていて活性炭室で水中の有機物を除い
友後、イオン交換樹脂室へ流下させてイオン化した物質
を除く。このような順序で段階的にろ過することにより
効率よくろ過が行なえるのである。活性炭室のツメと両
方の室に置い友じゃま板により水は遅流となりろ材との
接触面積が犬きくなり、ま之活性炭室の底部に約30度
の傾斜上つけたことに上り流込を増す効果かめる。そし
て2舅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の組合せ、十字板のろ過板13と60
メツシユポリエチレン布14の組合せ、艷に2m径の大
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個の組合せケ上部より順次に設ける
ことにより、ろ過速度を安定させることができる。これ
ら衛通過ろ過され之水は最後に第2ろ退部でろ紙によ°
りろ過されるのであるが、このろ紙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、汚れ次場合は速やかに交換できる。そして本発明
のろ過器はろ過を行なうときは、一体にして使用するの
であるが原水受器A。
This first filtration section B is divided into an activated carbon chamber and an ion exchange resin chamber below the activated carbon chamber, in which organic matter in the water is removed, and then ionized substances are removed by flowing down to the ion exchange resin chamber. Filtration can be carried out efficiently by filtering in stages in this order. The claws in the activated carbon chamber and the baffle plates placed in both chambers cause the water to flow slowly and the contact area with the filter material to be narrowed. You can feel the increasing effect. A combination of a filter plate 8 with a large number of holes of 2 diameters and a polyethylene cloth 9 of 40 meshes, and a cross plate filter plate 13 and 60.
The filtration rate can be stabilized by sequentially providing three combinations of mesh polyethylene cloth 14, a combination of a filter plate 17 having a majority of 2 m diameter on the barge, and a 60 mesh polyethylene cloth 18 from the top. can. The water that has been filtered through these sanitary passes is finally passed through filter paper in the second filtration section.
Depending on the quality of the raw water, the filtration speed can be changed by increasing or decreasing the filter paper between one and five sheets, and it can be quickly replaced if it becomes dirty. The filter of the present invention is used as a raw water receiver A when performing filtration.

第1ろ退部、第2ろ退部、受器は夫々分離できるので、
点検、部材の交換に便利である。このように本発明のろ
過器は従来のろ過器に比し顕著な効果ヶ有する。
The first filtration part, the second filtration part, and the receiver can be separated, so
Convenient for inspection and parts replacement. As described above, the filter of the present invention has remarkable effects compared to conventional filters.

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

第1図は本発明の特徴とする使用状態を示す縦断面図、
′@2図Aは原水受器の縦断面図、第3図Bは第1ろ退
部の縦断面図、第4図Cは第2ろ退部、Dは受器を示す
。第5図は十字板のろ過板ケ示す。 1・・・汚泥ろ退部、2・・・原水受筒、3・・・ろ過
板、4・・・ポリエチレン布、7・・・第1ろ退部、8
・・・ろ過板、9・・・ポリエチレン布、11・・・じ
ゃま板。 12・・・活性炭室、13・・・十字板のろ過板、15
・・・イオン交換樹脂室、16・・・じゃま板、17・
・・ろ過板、18・・・ポリエチレン布、19・・・第
2ろ退部、20・・・押さえ蓋、21・・・ろ紙、22
・・・ろ過板、23・・・受器。
FIG. 1 is a longitudinal cross-sectional view showing a usage state that is a feature of the present invention;
'@2 Figure A is a vertical sectional view of the raw water receiver, Figure 3 B is a vertical sectional view of the first filtration part, Figure 4 C is the second filtration part, and D shows the receiver. Figure 5 shows the cross plate filter plate. DESCRIPTION OF SYMBOLS 1... Sludge filtration part, 2... Raw water receiver, 3... Filter plate, 4... Polyethylene cloth, 7... First filtration part, 8
... Filter plate, 9 ... Polyethylene cloth, 11 ... Baffle board. 12...Activated carbon chamber, 13...Cross plate filter plate, 15
...Ion exchange resin chamber, 16...Baffle board, 17.
...Filtering plate, 18... Polyethylene cloth, 19... Second filtration retraction part, 20... Pressing lid, 21... Filter paper, 22
...filter plate, 23...receiver.

Claims (1)

【特許請求の範囲】[Claims] 汚泥ろ過袋、ポリエチレン布、ろ過板を備えた原水受筒
よりなる原水受器、上部にポリエチレン布とろ過板を有
し底部にろ過板とポリエチレン布を有する第1ろ過筒の
活性炭室にはツメ、ポリエチレン布、十字板のろ過板と
活性炭中に浮かばせたじやま板を有し、その下部イオン
交換樹脂室にはイオン交換樹脂とその中に浮ばせたじや
ま板を有する第1ろ過部、ろ過板を兼ねた押さえ蓋と底
部のろ過板の間にろ紙を入れ第1ろ過筒の底部の蓋押さ
え筒でろ紙を互に密着させた第2ろ過部、その下のろ過
水を受ける受器を一体に組合せたことを特徴とするろ過
器
A raw water receiver consisting of a raw water receiver equipped with a sludge filter bag, a polyethylene cloth, and a filter plate, a polyethylene cloth and a filter plate on the top, and a filter plate and a polyethylene cloth on the bottom.The activated carbon chamber of the first filter tube has a claw. , a filter plate made of polyethylene cloth, a cross plate, and a filter board suspended in activated carbon, and a first filtration chamber with an ion exchange resin and a filter board suspended in the lower ion-exchange resin chamber. part, a second filtration part in which a filter paper is placed between a holding lid that also serves as a filtration plate and a filtration plate at the bottom, and the filter papers are brought into close contact with each other by a lid holding cylinder at the bottom of the first filtration cylinder; a receiver below that for receiving filtered water; A filter characterized by the combination of
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 true JPS61129014A (en) 1986-06-17
JPH0425043B2 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)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0647597A1 (en) * 1993-10-12 1995-04-12 AEROSPATIALE Société Nationale Industrielle Installation for treating and recycling washing water of 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 method
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 method
JPS5833772U (en) * 1981-08-29 1983-03-04 スズキ株式会社 motorcycle intake system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0647597A1 (en) * 1993-10-12 1995-04-12 AEROSPATIALE Société Nationale Industrielle Installation for treating and recycling washing water of a washing machine
FR2711129A1 (en) * 1993-10-12 1995-04-21 Aerospatiale Water treatment and recycling station for washing a washing machine.
KR100461903B1 (en) * 2002-12-13 2004-12-17 한국수자원공사 Meandering flow powered activated charcoal contactor with paneled barriers

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