JPH10309573A - Purification method of sewage and device therefore - Google Patents

Purification method of sewage and device therefore

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Publication number
JPH10309573A
JPH10309573A JP13572697A JP13572697A JPH10309573A JP H10309573 A JPH10309573 A JP H10309573A JP 13572697 A JP13572697 A JP 13572697A JP 13572697 A JP13572697 A JP 13572697A JP H10309573 A JPH10309573 A JP H10309573A
Authority
JP
Japan
Prior art keywords
sewage
filter
separation filter
organic matter
pipe
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
JP13572697A
Other languages
Japanese (ja)
Other versions
JP3238095B2 (en
Inventor
Yoshihiro Iwata
吉弘 岩田
Yoshitoshi Maeda
芳聰 前田
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Individual
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Individual
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Priority to JP13572697A priority Critical patent/JP3238095B2/en
Publication of JPH10309573A publication Critical patent/JPH10309573A/en
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Publication of JP3238095B2 publication Critical patent/JP3238095B2/en
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Abstract

PROBLEM TO BE SOLVED: To provide a purification method of sewage and its device enabling even very dirty sewage to satisfactorily change to industrial waste water and drinking water, etc., by classifying the filters to special filters and performing a special pre-treatment. SOLUTION: A pre-treatment device is constituted of being successively in series connected a sewage receive tank 1, plural stages of electrostatic voltage conductive pipes 13-16, an electrolysis cell 2 and plural stages of electrostatic voltage conductive pipes 30-33. The impurities re removed, dissolved oxygen is increased and water pressure is increased. Succeeding to the pre-treatment device, a residue treating filter 3, an organic matter separation filter 4, a molecular separation filter 5 and an advanced organic matter separation filter 6 are successively in series connected.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、河川の汚水や工場
廃水やヘドロ状のものなどの汚水をフィルタ―によって
処理して浄化水を得る方法及びその装置に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for obtaining purified water by treating wastewater from rivers, industrial wastewater, or sludge-like wastewater with a filter.

【0002】[0002]

【従来の技術】従来から、汚水をフィルタ―によって処
理して飲料水等の浄化水を得ることは普通に行われてい
た。
2. Description of the Related Art Conventionally, sewage has been generally treated by a filter to obtain purified water such as drinking water.

【0003】[0003]

【発明が解決しようとする課題】ところで、前記従来例
の場合、汚水の程度が軽い場合にはフィルタ―のみによ
ってもある程度の飲料水等の浄化水を得ることができた
が、工場廃水やヘドロ状のものなど汚水の程度がひどい
とフィルタ―のみでは所望の浄化水を得ることができな
い虞がある。
By the way, in the case of the above-mentioned conventional example, when the degree of sewage is light, a certain amount of purified water such as drinking water can be obtained only by a filter. If the degree of sewage such as that of a filter is severe, there is a risk that desired purified water cannot be obtained only with a filter.

【0004】本発明は、このような問題点に鑑みてなさ
れたものであり、その目的とするところは、フイルタ―
を特殊なものに区分けし且つ特別の前処理を行うことに
よって、汚れのひどい汚水でも充分に工場排水や飲料水
等になし得る汚水の浄化方法及びその装置を提供しよう
とするものである。
[0004] The present invention has been made in view of such problems, and a purpose thereof is to provide a filter.
The present invention aims to provide a method and an apparatus for purifying sewage which can be sufficiently converted into industrial wastewater, drinking water, and the like even if the sewage is extremely dirty, by classifying the sewage into a special one and performing a special pretreatment.

【0005】[0005]

【課題を解決するための手段】上記目的を達成するため
に、本発明における汚水の浄化方法は、前処理として不
純物の除去と溶存酸素の増加と水圧の増加を施した後、
残留物処理フィルタ―と有機物分離フィルタ―と分子分
離フィルタ―と高度有機物分離フィルタ―を順次流下さ
せるようにしたことを特徴とするものである。
In order to achieve the above object, a method for purifying sewage according to the present invention comprises the steps of removing impurities, increasing dissolved oxygen and increasing water pressure as pretreatments.
A residue treatment filter, an organic matter separation filter, a molecular separation filter, and an advanced organic matter separation filter are sequentially flowed down.

【0006】更に、前記前処理として、汚水受槽内での
攪伴により汚水相互間の汚物のからみ合を解いて汚水に
流動性を付与し、電気分解槽への供給管の途中の複数箇
所で静電圧導電による溶存酸素の増加を図り、電気分解
槽内での通電と加圧空気の供給及び攪伴により汚水相互
間の汚物の微細なからみ合を解いて汚水の流動性を更に
増加させると共に不純物の除去及び汚水の圧力増強を図
り、更にフィルタ―への供給管の途中の複数箇所で静電
圧導電による溶存酸素の増加を図るようにしたことを特
徴とするものでもある。
[0006] Further, as the pretreatment, the entanglement of the sewage between the sewage is released by stirring in the sewage receiving tank to impart fluidity to the sewage, and the sewage is supplied to a plurality of points in the middle of the supply pipe to the electrolysis tank. To increase the amount of dissolved oxygen due to electrostatic potential conduction, and to further increase the fluidity of the wastewater by breaking the fine entanglement of the waste between the wastewater by supplying electricity and supplying compressed air in the electrolysis tank and stirring. In addition, the present invention is characterized in that impurities are removed and sewage pressure is increased, and furthermore, dissolved oxygen is increased by electrostatic voltage conduction at a plurality of points in the supply pipe to the filter.

【0007】更にまた、前記高度有機物分離フィルタ―
からの水に更に溶存酸素を増加させるようにしたことを
特徴とするものでもある。
Further, the above-mentioned advanced organic matter separation filter
Another feature of the present invention is that the dissolved oxygen is further increased in water.

【0008】また、本発明における汚水の浄化装置は、
汚水受槽と複数段の静電圧導電パイプと電気分解槽と複
数段の静電圧導電パイプを順次直列に接続して前処理装
置を構成し、該前処理装置に続いて残留物処理フィルタ
―と有機物分離フィルタ―と分子分離フィルタ―と高度
有機物分離フィルタ―を順次直列に接続したことを特徴
とするものでもある。
The sewage purification apparatus according to the present invention comprises:
A sewage receiving tank, a plurality of stages of electrostatic conductive pipes, an electrolysis tank, and a plurality of stages of electrostatic conductive pipes are connected in series to form a pretreatment device, and the pretreatment device is followed by a residue treatment filter and organic matter. A separation filter, a molecular separation filter, and an advanced organic matter separation filter are sequentially connected in series.

【0009】更に、前記静電圧導電パイプに低電圧,低
電流の低周波を付与し、前記汚水受槽と電気分解槽に攪
伴機を配置し、且つ電気分解槽に加圧空気の供給管を接
続したことを特徴とするものでもある。
Further, a low voltage and a low current of a low frequency are applied to the electrostatic voltage conductive pipe, a stirrer is disposed in the sewage receiving tank and the electrolysis tank, and a supply pipe of pressurized air is provided in the electrolysis tank. It is also characterized by being connected.

【0010】更にまた、前記高度有機物分離フィルタ―
の下流側に複数段の静電圧導電パイプを接続したことを
特徴とするものでもある。
Furthermore, the above-mentioned advanced organic matter separation filter
A plurality of stages of electrostatic voltage conductive pipes are connected to the downstream side.

【0011】[0011]

【発明の実施の形態】添付図面を参照して本発明の実施
例について説明する。図において、1は汚水受槽、2は
電気分解槽、3は残留物処理フィルタ―、4は有機物分
離フィルタ―、5は分子分離フィルタ―、6は高度有機
物分離フィルタ―である。
Embodiments of the present invention will be described with reference to the accompanying drawings. In the figure, 1 is a sewage receiving tank, 2 is an electrolysis tank, 3 is a residue treatment filter, 4 is an organic matter separation filter, 5 is a molecular separation filter, and 6 is an advanced organic matter separation filter.

【0012】前記汚水受槽1は、上部開口部に河川の汚
水や工場廃水やヘドロ状のものなどの汚水を注入する注
入管7を備え、底部に比較的に緩やかに回転する回転翼
を有する攪伴機8とドレイン管9を備え、胴部に複数段
の電磁バルブ10,10…を備えている。
The sewage receiving tank 1 has an injection pipe 7 for injecting sewage such as river sewage, industrial wastewater, or sludge in an upper opening, and a stirring blade having a relatively slowly rotating blade at the bottom. An auxiliary machine 8 and a drain pipe 9 are provided, and a plurality of electromagnetic valves 10, 10,...

【0013】前記電磁バルブ10の何れかに接続される
ポンプ11と前記電気分解槽2との間の供給管12の途
中には、複数箇所に静電圧導電パイプ13,14,1
5,16等が直列に接続されている。該静電圧導電パイ
プは供給される電圧,電流や周波数等に多少に差はある
がいずれも略同一構成のものであり、図2に示すよう
な、例えば合成樹脂管17の外周に導電コイル18が巻
回されそれを保護カバ―19で覆ったものであって、該
導電コイル18に静電圧コントロ―ルボックス20から
所望の低電圧,低電流の低周波が電線21で供給されて
静電圧導電パイプを構成するようになっている。
In the middle of the supply pipe 12 between the pump 11 connected to any one of the electromagnetic valves 10 and the electrolysis tank 2, a plurality of electrostatic voltage conductive pipes 13, 14, 1 are provided.
5, 16, etc. are connected in series. Although the supplied voltage, current, frequency and the like are somewhat different, the electrostatic voltage conductive pipes have substantially the same configuration. For example, as shown in FIG. Is wound and covered with a protective cover 19, and a desired low voltage and low current low frequency are supplied to the conductive coil 18 from a static voltage control box 20 by an electric wire 21 so that the conductive coil 18 is electrically conductive. It constitutes a pipe.

【0014】前記電気分解槽2は、電気分解用コントロ
―ラ22からの低電圧,低電流が供給される電極23,
23を内部に備え、上部には加圧空気の供給管24を備
え、また、底部には比較的に急速に回転する回転翼を有
する攪伴機25とドレイン管26を備え、胴部には複数
段の電磁バルブ27,27…を備えている。
The electrolysis tank 2 has electrodes 23, to which a low voltage and a low current are supplied from an electrolysis controller 22,
23, a pressurized air supply pipe 24 at the top, a stirrer 25 having rotating blades that rotate relatively rapidly at the bottom, and a drain pipe 26, and a body at the bottom. .. Are provided with a plurality of stages of electromagnetic valves 27.

【0015】前記電磁バルブ27の何れかに接続される
ポンプ28と前記残留物処理フィルタ―3との間の供給
管29の途中には、複数箇所に静電圧導電パイプ30,
31,32,33等が直列に接続されている。該静電圧
導電パイプも供給される電圧,電流や周波数等に多少に
差はあるがいずれも同一構成のものであり、図2で前に
説明したような静電圧導電パイプを構成するようになっ
ている。
In the middle of the supply pipe 29 between the pump 28 connected to any of the electromagnetic valves 27 and the residue treatment filter 3, a plurality of electrostatic voltage conductive pipes 30,
31, 32, 33, etc. are connected in series. Although the supplied voltage, current, frequency, and the like are somewhat different, the electrostatic voltage conductive pipes have the same configuration, and thus constitute the electrostatic voltage conductive pipe as described above with reference to FIG. ing.

【0016】以上が汚水の前処理に利用される装置であ
る。そして、以下,本発明に係るフィルタ―装置による
浄化装置及び所望によって飲料水を得るための総仕上げ
用の静電圧導電パイプ装置について主として図3を参照
して詳述する。
The above is an apparatus used for pretreatment of sewage. Hereinafter, a purification device using a filter device according to the present invention and an electro-static conductive pipe device for finishing the entirety to obtain drinking water as desired will be described in detail mainly with reference to FIG.

【0017】前記残留物処理フィルタ―3は、円筒状の
ケ―ス34内の中心部に、外周に多数の小孔35を備え
た排出管36が設置され、該排出管36の回りにオレフ
ィンポリマ―とポリエステルファイバ―とポリエステル
の重合不織布からなるフィルタ―37が巻回されて配置
され、ケ―ス34の上部には前記供給管29の末端が接
続され、ケ―ス34の下部中央の排出管36出口に接続
管38が、また同下部には廃水管39が接続されて、残
留物処理フィルタ―3を構成している。
The residue treatment filter 3 is provided with a discharge pipe 36 having a large number of small holes 35 on the outer periphery in the center of a cylindrical case 34, and an olefin pipe around the discharge pipe 36. A filter 37 made of polymer, polyester fiber, and polyester non-woven fabric is wound and arranged. An upper end of the case 34 is connected to an end of the supply pipe 29. A connection pipe 38 is connected to the outlet of the discharge pipe 36, and a waste water pipe 39 is connected to the lower part of the discharge pipe 36, thereby forming a residue treatment filter 3.

【0018】前記有機物分離フィルタ―4は、円筒状の
ケ―ス40内の上下部に略5ミクロンのセディメントフ
ィルタ―41,42が配置され、両フィルタ―41,4
2間に繊維状又は粒状の活性炭43が充填されており、
ケ―ス40の下部中央に前記接続管38の末端が、また
同下部には廃水管44が接続され、ケ―ス40の上部に
は接続管45が接続されて、有機物分離フィルタ―4を
構成している。
The organic matter separation filter 4 has a sediment filter 41, 42 of approximately 5 microns disposed in the upper and lower portions of a cylindrical case 40.
A fibrous or granular activated carbon 43 is filled between the two.
The end of the connection pipe 38 is connected to the center of the lower part of the case 40, the waste water pipe 44 is connected to the lower part, and the connection pipe 45 is connected to the upper part of the case 40. Make up.

【0019】前記分子分離フィルタ―5は、円筒状のケ
―ス46内の中心部に、外周に多数の小孔47を備えた
排出管48が設置され、該排出管48の回りに例えば孔
径が0.0001ミクロンのポリアミド重合膜とポリス
ルホンの膜からなるフィルタ―49が巻回されて配置さ
れ、ケ―ス46の上部には前記接続管45の末端が接続
され、ケ―ス46の下部中央の排出管48出口に接続管
50が、また同下部には廃水管51が接続されて、分子
分離フィルタ―5を構成している。
The molecular separation filter 5 is provided with a discharge pipe 48 having a large number of small holes 47 on the outer periphery at a central portion in a cylindrical case 46. A filter 49 made of a polyamide polymer film and a polysulfone film having a thickness of 0.0001 micron is wound and arranged. An end of the connection pipe 45 is connected to an upper part of the case 46, and a lower part of the case 46 is A connection pipe 50 is connected to the outlet of the central discharge pipe 48, and a wastewater pipe 51 is connected to the lower part thereof, thereby constituting a molecular separation filter 5.

【0020】前記高度有機物分離フィルタ―6は、円筒
状のケ―ス52内の上下部に略5ミクロンのセディメン
トフィルタ―53,54が配置され、両フィルタ―5
3,54間に高密度の繊維状又は粒状の活性炭55が充
填されており、ケ―ス52の下部中央に前記接続管50
の末端が、また同下部には廃水管56が接続され、ケ―
ス52の上部には接続管57が接続されて、高度有機物
分離フィルタ―6を構成している。
In the advanced organic matter separation filter 6, sediment filters 53 and 54 of approximately 5 microns are arranged in the upper and lower portions of a cylindrical case 52.
A high-density fibrous or granular activated carbon 55 is filled between the casings 3 and 54.
The wastewater pipe 56 is connected to the end of the
A connection pipe 57 is connected to the upper part of the filter 52 to constitute a high organic matter separation filter-6.

【0021】前記接続管57には、複数箇所に静電圧導
電パイプ58,59等が直列に接続されている。該静電
圧導電パイプも供給される電圧,電流や周波数等に多少
に差はあるがいずれも同一構成のものであり、図2で前
に説明したような静電圧導電パイプを構成するようにな
っている。
The connection pipe 57 is connected at plural places with static voltage conductive pipes 58, 59 and the like in series. Although the supplied voltage, current, frequency, and the like are somewhat different, the electrostatic voltage conductive pipes have the same configuration, and thus constitute the electrostatic voltage conductive pipe as described above with reference to FIG. ing.

【0022】以上のような構成において、注入管7から
汚水受槽1の上部開口部に河川の汚水や工場廃水やヘド
ロ状のものなどの汚水が注入されると、この汚水が汚水
受槽1内に所望の水位まで蓄えられ、その間,汚水受槽
1底部の攪伴機8の回転翼が比較的に緩やかに回転して
いるので、汚水が攪伴され汚水相互間の汚物のからみ合
が解かれて汚水に流動性が付与され、からみ合っていた
汚物は分離されて沈澱し、適宜ドレイン管9を開放する
ことにより排出される。
In the above configuration, when sewage such as river sewage, factory effluent, or sludge is injected from the injection pipe 7 into the upper opening of the sewage tank 1, the sewage enters the sewage tank 1. The water is stored up to a desired water level. During this time, the rotating blades of the impeller 8 at the bottom of the sewage receiving tank 1 are rotating relatively slowly, so that the sewage is stirred and the entanglement of the sewage between the sewage is released. Fluidity is imparted to the sewage, and the entangled sewage is separated and settled, and is discharged by opening the drain pipe 9 as appropriate.

【0023】注入管7からの汚水の注入は継続して行わ
れ、汚水受槽1内の汚水が所望の水位になると、その水
位に適応した電磁バルブ10が開かれ、汚水受槽1内で
汚物が分離され流動性が付与された汚水は、ポンプ11
を介して供給管12に順次送られる。
Injection of sewage from the injection pipe 7 is continuously performed, and when the sewage in the sewage receiving tank 1 reaches a desired water level, an electromagnetic valve 10 adapted to the water level is opened, and sewage in the sewage receiving tank 1 is removed. The separated sewage provided with fluidity is supplied to a pump 11
Are sequentially sent to the supply pipe 12.

【0024】供給管12の途中には静電圧導電パイプ1
3,14,15,16等が直列に接続されており、例え
ば,静電圧導電パイプ13には静電圧コントロ―ルボッ
クス20からDL―1の回路で周波数が50HZで電圧
1V,電流1.8mAの低周波,低電圧,低電流が、導
電パイプ14にはDL―2の回路で周波数が100HZ
で電圧1V,電流1.8mAの低周波,低電圧,低電流
が、導電パイプ15にはDL―3の回路で周波数が15
0HZで電圧1V,電流3.6mAの低周波,低電圧,
低電流が、導電パイプ16にはDL―4の回路で周波数
が200HZで電圧1V,電流3.6mAの低周波,低
電圧,低電流がそれぞれ付与されて、パイプ中を流れる
汚水における溶存酸素を増加させる。なお、前記周波
数,電圧,電流は送られる汚水の汚れの程度により汚れ
がひどい程、またブロック内では上流側より下流側で、
その値を高くする傾向があり、周波数は30HZから2
50HZ,電圧は0.5Vから5V,電流は0.8mA
から5mAの範囲内で経験によって選択されるものであ
る。
In the middle of the supply pipe 12, the electrostatic voltage conductive pipe 1
3, 14, 15, 16 and the like are connected in series. For example, the static voltage conductive pipe 13 is a circuit of DL-1 from the static voltage control box 20 and has a frequency of 50 Hz, a voltage of 1 V and a current of 1.8 mA. Low frequency, low voltage and low current are applied to the conductive pipe 14, and the frequency is 100Hz in the DL-2 circuit.
And a low frequency, low voltage and low current of voltage 1 V and current 1.8 mA, and the conductive pipe 15 has a frequency of 15 by a DL-3 circuit.
Low frequency, low voltage of 1 V and current of 3.6 mA at 0 Hz,
A low current, a low frequency, a low voltage, and a low current of 1 V and a current of 3.6 mA at a frequency of 200 Hz and a current of 3.6 mA, respectively, are applied to the conductive pipe 16 in a DL-4 circuit, thereby dissolving dissolved oxygen in sewage flowing through the pipe. increase. The frequency, voltage, and current are more severe depending on the degree of contamination of the wastewater to be sent.
The value tends to be higher, and the frequency is increased from 30 Hz to 2
50Hz, voltage 0.5V to 5V, current 0.8mA
Empirically selected within the range of 5 to 5 mA.

【0025】溶存酸素が増加された汚水は供給管12か
ら電気分解槽2に入り、この槽2内で攪伴機25の回転
翼の比較的に急速な回転により汚水が攪伴され汚水相互
間の汚物のからみ合が更に一層解かれて汚水に流動性が
付与されると共に、ここで電気分解用コントロ―ラ22
から例えば電圧100V,電流10Aが電極23に供給
されることにより電気分解が行われて汚水中の汚物が集
められ、且つ加圧空気の供給管24から例えば5気圧の
加圧空気が供給されて汚水は加圧水となる。そして、分
離された汚物は適宜ドレイン管26を開放することによ
り排出される。なお、電極23に付与される電圧,電流
及び加圧空気の加圧は槽2内の汚水の汚れの程度により
汚れがひどい程その値を高くする傾向があり、電圧は5
0Vから300V,電流は5Aから30A、加圧空気は
3気圧から15気圧の範囲内で経験によって選択される
ものである。
The sewage with increased dissolved oxygen enters the electrolysis tank 2 from the supply pipe 12, and the sewage is stirred by the relatively rapid rotation of the rotating blades of the stirring device 25 in the tank 2, and the sewage is intermixed with the sewage. The entanglement of the filth is further unraveled to impart fluidity to the sewage, and the electrolysis controller 22
For example, when a voltage of 100 V and a current of 10 A are supplied to the electrode 23, electrolysis is performed to collect dirt in the sewage, and pressurized air of, for example, 5 atm is supplied from a pressurized air supply pipe 24. Sewage is pressurized water. The separated dirt is discharged by opening the drain pipe 26 as appropriate. The voltage and current applied to the electrode 23 and the pressurization of the pressurized air tend to increase as the dirt gets worse depending on the degree of dirt in the sewage in the tank 2.
0V to 300V, current is 5A to 30A, and pressurized air is empirically selected within the range of 3 to 15 atm.

【0026】電気分解槽2内で汚物が分離され流動性が
付与された加圧汚水は、ポンプ28を介して供給管29
に順次送られる。この供給管29の途中には静電圧導電
パイプ30,31,32,33等が直列に接続されてお
り、例えば,静電圧導電パイプ30には静電圧コントロ
―ルボックス20からDL―5の回路で周波数が100
HZで電圧2V,電流5mAの低周波,低電圧,低電流
が、導電パイプ31にはDL―6の回路で周波数が15
0HZで電圧2V,電流5mAの低周波,低電圧,低電
流が、導電パイプ32にはDL―7の回路で周波数が2
00HZで電圧2V,電流5mAの低周波,低電圧,低
電流が、導電パイプ33にはDL―8の回路で周波数が
250HZで電圧2V,電流5mAの低周波,低電圧,
低電流がそれぞれ付与されて、パイプ中を流れる汚水に
おける溶存酸素を増加させる。なお、前記周波数,電
圧,電流も前記の範囲内で経験によって選択されるもの
である。
The pressurized sewage from which filth is separated in the electrolysis tank 2 and given fluidity is supplied to a supply pipe 29 via a pump 28.
Are sent in sequence. In the middle of the supply pipe 29, static voltage conductive pipes 30, 31, 32, 33 and the like are connected in series. For example, the static voltage conductive pipe 30 is connected to the static voltage control box 20 through the DL-5 circuit. Frequency 100
A low frequency, a low voltage and a low current of 2 V and a current of 5 mA in HZ, and a frequency of 15
At 0 Hz, a low frequency, a low voltage and a low current of 2 V and a current of 5 mA are applied to the conductive pipe 32.
A low frequency, a low voltage and a low current of 2 V and a current of 5 mA at 00 Hz, and a low frequency and a low voltage of a 2 V voltage and a current of 5 mA at a frequency of 250 Hz in a DL-8 circuit in the conductive pipe 33.
Low currents are each applied to increase the dissolved oxygen in the sewage flowing through the pipe. The frequency, voltage, and current are also selected by experience within the above ranges.

【0027】以上のような不純物の除去と溶存酸素の増
加と水圧の増加で流動性を増し前処理を終えた汚水は、
供給管29から残留物処理フィルタ―3のオレフィンポ
リマ―とポリエステルファイバ―とポリエステルの重合
不織布からなるフィルタ―37に送られフィルタ―37
でろ過され、砂,さび,水垢,略5ミクロン以上の微粒
子等が除去されてケ―ス34の下部中央の排出管36出
口から接続管38に送られる。また、前記ろ過による砂
等の残留物は廃水管39から廃液として排出される。
The sewage that has been subjected to the pretreatment by increasing the fluidity by removing the impurities, increasing the dissolved oxygen and increasing the water pressure as described above,
The filter 37 is sent from the supply pipe 29 to the filter 37 composed of an olefin polymer, polyester fiber, and polyester polymerized non-woven fabric of the residue treatment filter 3.
Then, sand, rust, water scale, fine particles having a size of about 5 μm or more are removed, and then sent to the connection pipe 38 from the outlet of the discharge pipe 36 at the lower center of the case 34. The residue such as sand by the filtration is discharged as waste liquid from the waste water pipe 39.

【0028】残留物が処理された汚水は、接続管38か
ら有機物分離フィルタ―4のセディメントフィルタ―4
1に送られ、活性炭43を通過する間に、塩素の除去や
臭気の除去等による水質の改善,有機物の除去が行わ
れ、セディメントフィルタ―42を通り接続管45に送
られる。また、前記除去された有機物等は廃水管44か
ら廃液として排出される。
The sewage treated with the residue is passed through a connection pipe 38 to a sediment filter 4 of an organic matter separation filter 4.
While passing through the activated carbon 43, the water quality is improved by removing chlorine and odor, and organic substances are removed, and then sent to the connection pipe 45 through the sediment filter 42. Further, the removed organic substances and the like are discharged from the wastewater pipe 44 as a waste liquid.

【0029】有機物が処理された汚水は、接続管45か
ら分子分離フィルタ―5のミクロンのポリアミド重合膜
とポリスルホンの膜からなるフィルタ―49に送られフ
ィルタ―49でろ過され、ウイルス,微細な混濁物,コ
ロイド状物質,石灰,放射性物質,ヒ素等の無機塩類が
除去されてケ―ス46の下部中央の排出管48出口から
接続管50に送られる。また、前記ろ過による分離され
た分子は廃水管51から廃液として排出される。
The sewage treated with the organic matter is sent from the connection pipe 45 to a filter 49 made of a micron polyamide polymer membrane and a polysulfone membrane of the molecular separation filter 5 and filtered by the filter 49 to remove viruses and fine turbidity. Materials, colloidal substances, lime, radioactive substances, and inorganic salts such as arsenic are removed and sent to the connecting pipe 50 from the outlet pipe 48 at the lower center of the case 46. The molecules separated by the filtration are discharged from the wastewater pipe 51 as a waste liquid.

【0030】分子分離がなされた汚水は、接続管50か
ら最終の高度有機物分離フィルタ―6のセディメントフ
ィルタ―53に送られ、活性炭55を通過する間に、水
中の微量臭気の除去,最終有機物の除去等ハイレベルの
分離が行われ、セディメントフィルタ―54を通り接続
管57に送られる。また、前記除去された有機物等は廃
水管56から廃液として排出される。
The sewage subjected to molecular separation is sent from the connection pipe 50 to the sediment filter 53 of the final advanced organic matter separation filter 6, and while passing through the activated carbon 55, removal of trace odors in the water and final organic matter Is removed and sent to the connecting pipe 57 through the sediment filter 54. Further, the removed organic substances and the like are discharged from the waste water pipe 56 as a waste liquid.

【0031】以上の過程を経て浄化された水は、工場の
排水或は他の使用水となる。
The water purified through the above-mentioned process becomes the waste water of the factory or other water used.

【0032】そして、前記高度有機物分離フィルタ―6
から接続管57に送られる水を飲料水として使用する場
合には、図1に示すように接続管57の途中に直列に接
続されている静電圧導電パイプ58,59等に前記浄化
された水を通過させるとよい。その場合、例えば,静電
圧導電パイプ58には静電圧コントロ―ルボックス20
からDL―9の回路で周波数が80HZで電圧1V,電
流5mAの低周波,低電圧,低電流が、導電パイプ59
にはDL―10の回路で周波数が100HZで電圧1
V,電流5mAの低周波,低電圧,低電流がそれぞれ付
与されると、パイプ中を流れる水における溶存酸素を増
加される。なお、前記周波数,電圧,電流も前記の範囲
内で経験によって選択されるものである。
And, the advanced organic matter separation filter-6
When the water sent to the connecting pipe 57 is used as drinking water, the purified water is supplied to the electrostatic voltage conductive pipes 58 and 59 connected in series in the connecting pipe 57 as shown in FIG. Should be passed through. In this case, for example, the electrostatic voltage control pipe 20 is attached to the electrostatic voltage conductive pipe 58.
From the DL-9 circuit, a low frequency, low voltage and low current of 1 V voltage and 5 mA current at a frequency of 80 Hz are applied to the conductive pipe 59.
Is a DL-10 circuit with a frequency of 100Hz and a voltage of 1
When a low frequency, a low voltage and a low current of 5 V and a current of 5 mA are applied, the dissolved oxygen in the water flowing through the pipe is increased. The frequency, voltage, and current are also selected by experience within the above ranges.

【0033】以上のように、河川の汚水や工場廃水やヘ
ドロ状のものなどの汚水は、不純物の除去と溶存酸素の
増加と水圧の増加を施す前処理で流動性も増され、残留
物処理フィルタ―と有機物分離フィルタ―と分子分離フ
ィルタ―と高度有機物分離フィルタ―と順次流下されて
不純物が確実に捕捉排除されて浄化された水となる。
As described above, sewage such as river sewage, factory effluent, or sludge-like sewage is increased in fluidity by pretreatment in which impurities are removed, dissolved oxygen is increased, and water pressure is increased. The filter, the organic matter separation filter, the molecular separation filter, and the advanced organic matter separation filter are sequentially flowed down, so that impurities are reliably trapped and eliminated to obtain purified water.

【0034】そして、前記浄化された水は、更に静電圧
導電による溶存酸素の増加を図ることにより飲料水に適
した水となる。
Then, the purified water becomes water suitable for drinking water by further increasing dissolved oxygen by electrostatic voltage conduction.

【0035】[0035]

【発明の効果】本発明は以上のように、前処理として不
純物の除去と溶存酸素の増加と水圧の増加を施した後、
残留物処理フィルタ―と有機物分離フィルタ―と分子分
離フィルタ―と高度有機物分離フィルタ―を順次流下さ
せたので、各フィルタ―に格別の負担をかけることな
く、汚れのひどい汚水でも不純物の確実な捕捉排除がで
きて所望の浄化された水を得ることができる。
As described above, according to the present invention, as a pretreatment, after removing impurities, increasing dissolved oxygen and increasing water pressure,
Since the residue treatment filter, organic matter separation filter, molecular separation filter, and advanced organic matter separation filter flow down sequentially, no extra burden is imposed on each filter, and even in highly contaminated sewage, impurities can be reliably captured. It can be removed to obtain the desired purified water.

【0036】更に、前記前処理として、汚水受槽内での
攪伴により汚水相互間の汚物のからみ合を解いて汚水に
流動性を付与し、電気分解槽への供給管の途中の複数箇
所で静電圧導電による溶存酸素の増加を図り、電気分解
槽内での通電と加圧空気の供給及び攪伴により汚水相互
間の汚物の微細なからみ合を解いて汚水の流動性を更に
増加させると共に不純物の除去及び汚水の圧力増強を図
り、更のフィルタ―への供給管の途中の複数箇所で静電
圧導電による溶存酸素の増加を図るようにした場合に
は、後続する各フィルタ―の負担をより軽くすることが
できる。
Further, as the pretreatment, the entanglement of the sewage between the sewage is released by stirring in the sewage receiving tank to impart fluidity to the sewage, and the sewage is supplied to a plurality of points in the middle of the supply pipe to the electrolysis tank. To increase the amount of dissolved oxygen due to electrostatic potential conduction, and to further increase the fluidity of the wastewater by breaking the fine entanglement of the waste between the wastewater by supplying electricity and supplying compressed air in the electrolysis tank and stirring. In addition, in order to remove impurities and increase the pressure of sewage, and to increase dissolved oxygen by electrostatic voltage conduction at several points in the supply pipe to further filters, the burden on each subsequent filter Can be made lighter.

【0037】そして、高度有機物分離フィルタ―からの
水に更に溶存酸素を増加させるようにした場合には、酸
素含有量が多い飲料水を得ることができる。
When the dissolved oxygen is further increased in the water from the advanced organic matter separation filter, drinking water having a high oxygen content can be obtained.

【0038】また、汚水受槽と複数段の静電圧導電パイ
プと電気分解槽と複数段の静電圧導電パイプを順次直列
に接続して前処理装置を構成し、該前処理装置に続いて
残留物処理フィルタ―と有機物分離フィルタ―と分子分
離フィルタ―と高度有機物分離フィルタ―を順次直列に
接続したので、各フィルタ―に格別の負担をかけること
なく、汚れのひどい汚水でも不純物の確実な捕捉排除が
でき、所望の浄化された水を得る装置を有効に得ること
ができる。
Also, a sewage receiving tank, a plurality of stages of electrostatic voltage conductive pipes, an electrolysis tank and a plurality of stages of electrostatic voltage conductive pipes are connected in series in order to constitute a pretreatment device. The treatment filter, organic matter separation filter, molecular separation filter, and advanced organic matter separation filter are connected in series, so that no extra burden is placed on each filter, and even impurities that are extremely dirty can be reliably trapped and eliminated. And a device for obtaining desired purified water can be effectively obtained.

【0039】更に、前記静電圧導電パイプに低電圧,低
電流の低周波を付与し、前記汚水受槽と電気分解槽に攪
伴機を配置し、且つ電気分解槽に加圧空気の供給管を接
続した場合には、前処理が充分に行われて後続する各フ
ィルタ―の負担をより軽くする装置となる。
Furthermore, a low voltage and a low current of a low frequency are applied to the electrostatic voltage conductive pipe, a stirrer is disposed in the sewage receiving tank and the electrolysis tank, and a supply pipe of pressurized air is provided in the electrolysis tank. When connected, the pre-processing is sufficiently performed to reduce the load on each subsequent filter.

【0040】更にまた、高度有機物分離フィルタ―の下
流側に複数段の静電圧導電パイプを接続した場合には、
酸素含有量が多い飲料水として適した浄化水を得る装置
を有効に得ることができる。
Furthermore, when a plurality of stages of electrostatic voltage conducting pipes are connected downstream of the advanced organic matter separation filter,
An apparatus for obtaining purified water suitable as drinking water having a high oxygen content can be effectively obtained.

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

【図1】本発明に係る汚水から浄化水を得る方法に使用
する装置の構成図である。
FIG. 1 is a configuration diagram of an apparatus used for a method for obtaining purified water from wastewater according to the present invention.

【図2】図2は本発明に有効に利用できる静電圧導電パ
イプの説明図である。
FIG. 2 is an explanatory view of an electrostatic voltage conductive pipe that can be effectively used in the present invention.

【図3】図3は本発明に有効に利用できるフィルタ―装
置の説明図である。
FIG. 3 is an explanatory diagram of a filter device that can be effectively used in the present invention.

【符号の説明】[Explanation of symbols]

1 汚水受槽 2 電気分解槽 3 残留物処理フィルタ― 4 有機物分離フィルタ― 5 分子分離フィルタ― 6 高度有機物分離フィルタ― 8,25 攪伴機 13,14,15,16 静電圧導電パイプ 20 静電圧コントロ―ルボック
ス 24 加圧空気の供給管 30,31,32,33 静電圧導電パイプ 58,59 静電圧導電パイプ
DESCRIPTION OF SYMBOLS 1 Sewage receiving tank 2 Electrolysis tank 3 Residue treatment filter 4 Organic matter separation filter 5 Molecular separation filter 6 Advanced organic matter separation filter 8,25 Stirrer 13,14,15,16 Static electricity conductive pipe 20 Static electricity control -Box 24 Pressurized air supply pipe 30, 31, 32, 33 Static voltage conductive pipe 58, 59 Static voltage conductive pipe

───────────────────────────────────────────────────── フロントページの続き (72)発明者 前田 芳聰 大阪府吹田市藤白台1丁目2番B24―307 号 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Yoshitoshi Maeda 1-2-2 Fujishirodai, Suita-shi, Osaka B2-307

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】汚水を多段の直列に配列したフィルタ―を
通過させて浄化する方法において、前処理として不純物
の除去と溶存酸素の増加と水圧の増加を施した後、残留
物処理フィルタ―と有機物分離フィルタ―と分子分離フ
ィルタ―と高度有機物分離フィルタ―を順次流下させる
ようにしたことを特徴とする汚水の浄化方法。
In a method for purifying sewage by passing through a series of filters arranged in series, after removing impurities, increasing dissolved oxygen and increasing water pressure as a pretreatment, a residual treatment filter is provided. A method for purifying sewage, characterized by sequentially flowing down an organic matter separation filter, a molecular separation filter, and an advanced organic matter separation filter.
【請求項2】前記前処理として、汚水受槽内での攪伴に
より汚水相互間の汚物のからみ合を解いて汚水に流動性
を付与し、電気分解槽への供給管の途中の複数箇所で静
電圧導電による溶存酸素の増加を図り、電気分解槽内で
の通電と加圧空気の供給及び攪伴により汚水相互間の汚
物の微細なからみ合を解いて汚水の流動性を更に増加さ
せると共に不純物の除去及び汚水の圧力増強を図り、更
にフィルタ―への供給管の途中の複数箇所で静電圧導電
による溶存酸素の増加を図るようにしたことを特徴とす
る請求項1記載の汚水から飲料水を得る方法。
2. The pretreatment according to claim 1, wherein the sewage is entangled in the sewage receiving tank to disentangle the sewage and impart fluidity to the sewage. To increase the amount of dissolved oxygen due to electrostatic potential conduction, and to further increase the fluidity of the wastewater by breaking the fine entanglement of the waste between the wastewater by supplying electricity and supplying compressed air in the electrolysis tank and stirring. 2. The wastewater according to claim 1, wherein the impurities are removed and the pressure of the wastewater is increased, and furthermore, the dissolved oxygen is increased by electrostatic voltage conduction at a plurality of points in the supply pipe to the filter. How to get drinking water.
【請求項3】前記高度有機物分離フィルタ―からの水に
更に溶存酸素を増加させるようにしたことを特徴とする
請求項1又は請求項2記載の汚水の浄化方法。
3. The method for purifying sewage according to claim 1, wherein the dissolved oxygen in the water from the advanced organic matter separation filter is further increased.
【請求項4】汚水を多段の直列に配列したフィルタ―を
通過させて浄化する装置において、汚水受槽と複数段の
静電圧導電パイプと電気分解槽と複数段の静電圧導電パ
イプを順次直列に接続して前処理装置を構成し、該前処
理装置に続いて残留物処理フィルタ―と有機物分離フィ
ルタ―と分子分離フィルタ―と高度有機物分離フィルタ
―を順次直列に接続したことを特徴とする汚水の浄化装
置。
4. An apparatus for purifying sewage water by passing through a multistage filter arranged in series, wherein a sewage receiving tank, a plurality of stages of electrostatic voltage conductive pipes, an electrolysis tank, and a plurality of stages of electrostatic voltage conductive pipes are sequentially connected in series. Sewage, wherein a pretreatment device is constituted by connecting the pretreatment device, and a residue treatment filter, an organic matter separation filter, a molecular separation filter, and an advanced organic matter separation filter are sequentially connected in series following the pretreatment device. Purification equipment.
【請求項5】前記静電圧導電パイプに低電圧,低電流の
低周波を付与し、前記汚水受槽と電気分解槽に攪伴機を
配置し、且つ電気分解槽に加圧空気の供給管を接続した
ことを特徴とする請求項4記載の汚水の浄化装置。
5. A low-frequency and low-current low frequency is applied to the electrostatic voltage conductive pipe, a stirrer is disposed in the sewage receiving tank and the electrolysis tank, and a supply pipe for pressurized air is provided in the electrolysis tank. The sewage purification apparatus according to claim 4, wherein the apparatus is connected.
【請求項6】前記高度有機物分離フィルタ―の下流側に
複数段の静電圧導電パイプを更に接続したことを特徴と
する汚水の浄化装置。
6. An apparatus for purifying sewage water, wherein a plurality of stages of electrostatic voltage conductive pipes are further connected downstream of the advanced organic matter separation filter.
JP13572697A 1997-05-12 1997-05-12 Sewage purification method and apparatus Expired - Lifetime JP3238095B2 (en)

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JP3238095B2 JP3238095B2 (en) 2001-12-10

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009301587A (en) * 2009-09-28 2009-12-24 Yoshitoshi Maeda Water vending machine
CN108314226B (en) * 2018-02-02 2021-02-09 哈尔滨工程大学 Electrochemical system for treating ship domestic sewage
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