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JPH01151923A - Apparatus for water intaking from polluted water - Google Patents

Apparatus for water intaking from polluted water

Info

Publication number
JPH01151923A
JPH01151923A JP62312974A JP31297487A JPH01151923A JP H01151923 A JPH01151923 A JP H01151923A JP 62312974 A JP62312974 A JP 62312974A JP 31297487 A JP31297487 A JP 31297487A JP H01151923 A JPH01151923 A JP H01151923A
Authority
JP
Japan
Prior art keywords
tank
air
sewage
water
blower
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.)
Pending
Application number
JP62312974A
Other languages
Japanese (ja)
Inventor
Hiroaki Kawakita
川北 弘明
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP62312974A priority Critical patent/JPH01151923A/en
Publication of JPH01151923A publication Critical patent/JPH01151923A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Drying Of Gases (AREA)

Abstract

PURPOSE:To collect water from polluted water, by application of high voltage electromagnetic discharge to highly humid air just passed an aeration bath so as to transform stem into crystalline drops of water and then circulating the resulting low humid dried air to the aeration bath. CONSTITUTION:By operating a ventilator 2, air is fed to polluted water from a bubble outlet 4 in a bath 1, becomes a highly humid air which is led to an electric conductive material-made part 6 through a ventilating pipe 3, and here a high voltage electromagnetic discharge is applied on the air by a high voltage pressuring apparatus 5 so as to transform steam in the air into crystalline drops of water and take out the drops of water from a liquid outlet 8. Meanwhile the resulting dried air is circulated to the bath 1 through the ventilating pipe 3.

Description

【発明の詳細な説明】 この発明は1ばり気槽の1汚水中をばっ気通過した槽内
多湿空気の水分を1高電圧電磁放電を利用して電空気中
の水蒸気を結晶水滴に変化させて水分だけ除水摂取し1
除湿した乾燥空気を槽内ばり気層空気として循環使用す
る1汚水内水分摂取装置に関する1 従来、公共下水道を有しない地区の1雑、汚水の処理は
1便所汚水の浄化処理以外はとんど考慮されていないの
が現状であり1汚水は、生活排水として河川に放流され
1下水道の場合も1ばっ気、沈殿、消毒、河川放流、の
浄化処理形式であり水の二次利用は行われない。したが
って馬乾期は洗濯、浴用2台所雑水、そして水洗便所等
の生活必需水の大量使用による水不足に苦慮している。
[Detailed Description of the Invention] This invention converts water vapor in the air into crystal water droplets by using high-voltage electromagnetic discharge to convert moisture in humid air that has passed through sewage in an aeration tank into crystalline water droplets. Ingest only water and remove water 1
1. Concerning water intake equipment for sewage water, which circulates and uses dehumidified dry air as stratum air inside the tank. Currently, this is not taken into consideration, and 1) Sewage is discharged into rivers as domestic wastewater, and 1) In the case of sewage systems, 1) Purification treatment methods include aeration, sedimentation, disinfection, and discharge into rivers, and secondary use of water is not carried out. do not have. Therefore, during the horse dry season, residents are struggling with water shortages due to the large amount of water used for daily necessities such as laundry, bathing, two kitchens, and flush toilets.

又1これらの雑排水や工場排水の河川放流等による河川
や地下・kの汚染は進む一方であり1赤しお発生の要因
ともなっている。
Furthermore, the pollution of rivers and underground areas due to the discharge of gray water and industrial wastewater into rivers continues to increase, and is also a factor in the occurrence of red perilla.

この発明は九以上のような従来の欠点を除去して1雑、
汚水をばっ気蒸発させた空気の水分・を摂取し)水分を
除去した乾燥空気を汚水のばっ気相に循環送風する事に
より1雑、汚水から空気を媒体として水分を摂取する〜
汚水内水分摂取装置を提供する事を目的とする。
This invention eliminates the conventional drawbacks such as 9 or more, and 1 miscellaneous,
By aerating and evaporating sewage and ingesting moisture from the air, and circulating and blowing the dry air from which moisture has been removed into the aeration phase of the sewage, 1. Ingest moisture from the sewage using air as a medium.
The purpose is to provide a water intake device for wastewater.

第1図・第2図・第3図に示す第1実施態様の実施例は
1槽(1)に導入口11から汚水を槽(1)内へ導入口
11の水位以上導入した場合に槽(1)内空気は槽(1
)の外へ流出しない。槽(1)低部には気泡出口(4)
を有して槽(1)外の送風機(2)と通気路(3)によ
って連結している。この送風機(2)の吸気口の部分と
槽(1)の上層部分とが通気路(31,(35によって
連結され、この通気路(3)、 (3)の途中には直流
電源14に通じる高電圧加圧機器(5) Cハニ次側両
電極に通じる電導材の部分(6)を配して電導材の部分
(6)の低部には1水滴を受ける液体摂取部分(7)を
有して液体摂取口(8)とつながっている。送風機(2
)と電導材の部分(6)の間の通気路(3)の部分には
外気と通じる通気口(9)。
In the example of the first embodiment shown in FIGS. 1, 2, and 3, when wastewater is introduced into the tank (1) from the inlet 11 into the tank (1) at a level higher than the water level of the inlet 11, (1) The internal air is in the tank (1
) will not leak out. Tank (1) Air bubble outlet (4) at the bottom
The tank (1) is connected to a blower (2) outside the tank (1) by an air passage (3). The air inlet part of this blower (2) and the upper part of the tank (1) are connected by ventilation passages (31, (35), and a part of the ventilation passages (3), (3) leads to a DC power supply 14. High-voltage pressurizing equipment (5) A conductive material part (6) that communicates with both electrodes on the honeycombing side is arranged, and a liquid intake part (7) that receives one water drop is arranged at the bottom of the conductive material part (6). The blower (2) is connected to the liquid intake port (8).
) and the conductive material portion (6), there is a ventilation hole (9) communicating with the outside air in the portion of the ventilation path (3).

(9)が有する。この通気口(91,+9)は1個所と
する事も考えられる。そして1高電圧加圧機器(5)の
電源が槽(1)の汚水の量の変化に係合して作動する事
ができる水量感知スイッチ01とつながっている。この
水量感知スイッチαQはフロートスイッチとする事も考
えられる。この電導材の部分(6)は、高電圧加圧機器
(5)によって高電圧(例へばへ千〜二号ボルトの何れ
か)に加圧した場合に)両電極間に火花が飛ばない状態
で両電導材の間隔が明けられている。そして1槽(1)
内に水量感知スイッチ(11の水位以上の水が入った状
態で送風機(2)を動かすと1槽(1)内低部の気泡出
口(4)から気泡状態で汚水に空気の供給を行う事がで
きる。そして槽(2)内の空気は通気路(3)を通り高
電圧加圧機器(5)によって加圧された両電極の電導材
の部分(6)を通過して送風機(2)の吸気口に吸込ま
れて循環され\通気口f91. (91から両電極の電
導材の部分(6)を通過した空気の一部は外気へ放気さ
れて送風機(2)の吸気口に吸い込まれ、この時外気が
一部通気口(9)から吸入される。この装置は1高電圧
を加圧した電導材(6)の間を)加湿された空気が通過
すると為空気中の水 気が高圧電磁放電現象によって一
方の電導材に集まり結晶水滴状となって瞬時に除湿した
空気となるから\例へば毎分50リツトルの送風能力を
持つ送風機の1日の送風量は!II) X 60 X 
24111fi72000リツトルとなる。又)温度2
0度の泡和状態での空気中の水蒸気の看は1リットル当
りの水蒸気の量が0.0172グラムであるから−20
00Xへ0172 = 123Ek 4グラムとなり、
気泡状態で汚水部分を通過した乾燥空気の水蒸気含有率
を泡和状態カー100脱した時に70%と仮定すると1
238X70 * =866グラムとなり〜1日にへ6
〜110トンの蒸りゅう氷状の水を摂取可能である。こ
の量は15人家族の生活量の浄化槽が600リットル/
1a、であるから\浄化槽用としても使用加能であり1
法濯200リツトル、溶用500リツトル、洗面2台所
100!Jソトル、計800リットルであるから雑水用
としても利用可能であり1槽、や送風機、電導材の部分
、気泡出口、送風路、吸気口、高電圧等の大きさを調整
すれば、下水道処理等め大量の汚水を処理する事もでき
る。尚1この高電圧発生機器(5)はに次側に電流が流
れないから機器の熱損失に要する分しか電気を要しない
から、維持費は送風機が主体である。
(9) has. It is also conceivable that the vent hole (91, +9) be provided at one location. The power source of the high-voltage pressurizing device (5) is connected to a water amount sensing switch 01 that can be activated in response to a change in the amount of waste water in the tank (1). It is also possible to use a float switch as the water amount sensing switch αQ. This conductive material part (6) is in a state where no sparks fly between the two electrodes when pressurized to a high voltage (for example, anywhere from 1,000 to 2 volts) by a high voltage pressurizing device (5). There is a gap between both conductive materials. And 1 tank (1)
If you operate the blower (2) when the water level is higher than the water level in the tank (11), air will be supplied to the waste water in the form of bubbles from the air bubble outlet (4) at the bottom of the tank (1). Then, the air in the tank (2) passes through the ventilation path (3), passes through the electrically conductive material parts (6) of both electrodes that are pressurized by the high-voltage pressurizing device (5), and is sent to the blower (2). Some of the air that passes through the conductive material part (6) of both electrodes from the vent f91 is released to the outside air and is sucked into the air inlet of the blower (2). At this time, a portion of the outside air is sucked in through the vent (9).This device removes moisture in the air when the humidified air passes between the conductive materials (6) that are pressurized with a high voltage. is collected on one conductive material by a high-voltage electromagnetic discharge phenomenon, forming crystalline water droplets and instantly becoming dehumidified air. For example, the daily air flow rate of a blower with a blowing capacity of 50 liters per minute is II) X 60 X
24111fi72000 liters. Also) temperature 2
The amount of water vapor in the air in the bubble state at 0 degrees is -20 because the amount of water vapor per liter is 0.0172 grams.
0172 to 00X = 123Ek 4 grams,
Assuming that the water vapor content of the dry air that has passed through the sewage section in a bubble state is 70% when 100 bubbles are removed, the ratio is 1.
238 x 70 * = 866 grams ~ 6 per day
~110 tons of steaming ice water can be ingested. This amount is 600 liters per septic tank, which is the living amount for a family of 15 people.
1a, so it can also be used for septic tanks and 1
200 liters for legal washing, 500 liters for washing, 100 liters for two washrooms! J Sotol has a total capacity of 800 liters, so it can also be used for miscellaneous water, and by adjusting the size of the tank, blower, conductive material, bubble outlet, air passage, air intake, high voltage, etc., it can be used for sewerage. It is also possible to treat large amounts of wastewater. Note that this high voltage generating device (5) does not have current flowing to the downstream side, so it only requires electricity for the heat loss of the device, so the maintenance cost is mainly for the blower.

第4図の第2実施態様の場合は、第+4図に記載の送風
機lの吐出風量が可変であり可変風量の操作が槽内の水
量感知スイッチ(14によって行われる部物が異ってい
る。送風機(2)は送風吐出量が二段皆以上の複数吐出
能力を有して1槽(1)内の設置する水量感知スイッチ
(II’、 Kよって作動する。この部分を)例へば送
風機(2八が二通りの吐出風量を常時低吐出風量の状態
として槽内の水量感知スイッチ(11′によって層内汚
水が高水量時に高吐出風量の状態にスイッチが変化する
ように配線して使用すると1汚水の量が多い状態で風量
が多くなるから水分摂取量が増す。尚、この水量感知ス
イッチ(IQoはフロートスイッチとする事も考えられ
る第5図の第3実施態様は、第1実施態様、あるいは第
2実施態様の槽(11が槽(1)の周囲に断熱保温材1
6が施されている。この断熱保温材16の材質を発泡プ
ラスチックス材料として槽+11の外面に吹付施工する
事も考えられる。槽(1)の外面に断熱、保温性を有す
る断熱保温材16を施した場合は全てこの発明の一部で
ある。地中温度は夏20度、)18度位と、はぼ一定で
あるが〜空気の温度が上がると飽和状態での水蒸気含有
量が増加する。又−汚水温度が20度より40度に上が
った方が水中好気菌は活発に消化作用が行われる。した
がってこの第3実施態様の槽を地中に埋設して使用する
と1地中、あるいは外気の温度に槽(1)内の汚水が影
響されないから、%期でも汚水の温度が一定に保たれ入
槽(1)内の高湿度空気も定温となり為定量の水分を摂
取する事ができる。
In the case of the second embodiment shown in Fig. 4, the discharge air volume of the blower l shown in Fig. The blower (2) has a multiple discharge capacity of two or more air discharge volumes, and is activated by the water amount sensing switches (II', K) installed in one tank (1).For example, the blower (2) 28 is used by wiring so that the two types of discharge air volume are always in a low discharge air volume state and the water volume sensing switch (11') in the tank changes the switch to a high discharge air volume state when the amount of sewage in the layer is high. 1. When the amount of sewage is large, the amount of water intake increases because the air volume increases.The third embodiment in FIG. , or the tank of the second embodiment (11 is a heat insulating material 1 around the tank (1)
6 has been applied. It is also conceivable that this heat insulating material 16 is made of foamed plastic material and sprayed onto the outer surface of the tank +11. All cases where a heat insulating material 16 having heat insulation and heat retention properties is provided on the outer surface of the tank (1) are part of this invention. The underground temperature is approximately constant at about 20 degrees Celsius in summer and 18 degrees Celsius in summer, but as the air temperature rises, the water vapor content in the saturated state increases. Also, when the temperature of waste water rises to 40 degrees rather than 20 degrees, aerobic bacteria in the water perform more active digestion. Therefore, when the tank of the third embodiment is used by being buried underground, the sewage in the tank (1) will not be affected by the temperature of the ground or the outside air, so the temperature of the sewage will remain constant even during the % period. The high-humidity air in the tank (1) also has a constant temperature, so a fixed amount of water can be taken in.

第6図の第4実施態様の場合は為第1実施態様、第2実
施態様、第3実施態様の装置の槽(1)内部の底層部分
に液体用発熱体17が配設され−この作動スイッチは槽
(1)内置水内に接する部分に配設された温度感知材!
8によって汚水温度を感知して互変感知スイッチ19に
よって自動入切される。この液体用発熱体17は電熱ヒ
ーターとする事も考えられる。この装置を使用して\槽
内液体汚水温度が20度−40度等の温度に温度感知ス
イッチ19を温度セットして作動すると)槽内汚水が加
温されて好気菌の活動を促し)高温の高湿度空気が得ら
れるから、例へば4へ度の場合の飽和状態での1リット
ル当りの水分の量は()、0512  グラムであるか
ら送風能力5ヘリットル/分の送風機を使用するとへ0
512 X 60 X2.4) X 40 = 294
へ12グチムとなり20度の場合(1238%4  グ
ラム)と比較すると2.3倍以上の3トン近い蒸りゅう
氷状の水を1日で得られる計算になる。
In the case of the fourth embodiment shown in FIG. 6, a heating element 17 for liquid is disposed in the bottom layer inside the tank (1) of the apparatus of the first embodiment, second embodiment, and third embodiment. The switch is a temperature-sensing material placed in the part that touches the water inside the tank (1)!
8 senses the temperature of the waste water, and the tautological sensing switch 19 automatically turns on and off. It is also conceivable that the liquid heating element 17 be an electric heater. When this device is activated by setting the temperature sensor switch 19 to a temperature such as 20 degrees to 40 degrees for liquid waste water in the tank, the waste water in the tank is heated and the activity of aerobic bacteria is promoted. Since high-temperature, high-humidity air can be obtained, for example, the amount of moisture per liter in the saturated state at 4 degrees Celsius is (), 0512 grams, so if a blower with a blowing capacity of 5 heliliters/minute is used, it will be 0.
512 x 60 x 2.4) x 40 = 294
Compared to the case at 20 degrees Celsius (1238% 4 grams), it is calculated that nearly 3 tons of steaming ice-like water can be obtained in one day, which is 2.3 times more.

第7図の第5実施態様は1第1実施態様、第2実施態様
、第3実施態様の装置の送風機(2)と気泡出口(4)
とを連結する通気路(3)の内部の途中の部分に気体加
熱用発熱体20が配設され為この作動スイッチは槽(1
)内部の低層部分の汚水内に接する部分に配設された温
度感知材18によって汚水の温度を感知して温度感知ス
イッチ19によりて自動入切される。この気体加熱用発
熱体20は電熱ヒーターとする事もできる。この装置を
使用して槽(1)内汚水温度が20度〜40.度等の温
度に温度感知スイッチ19をセットして作動すると、送
風機(2)に山って通気路(3)内を通り槽(1)内汚
水に気泡出口(4)から空気が吐出する途中で気体加熱
用発熱体20によって加温されるから1第4実施態様と
全く同じ効果を得る事ができる。
The fifth embodiment of FIG.
A heating element 20 for heating the gas is disposed in the middle of the ventilation path (3) connecting the tank (1).
) The temperature of the waste water is sensed by the temperature sensing material 18 disposed in the lower part of the interior that is in contact with the waste water, and the temperature sensing switch 19 is automatically turned on and off. This gas heating heating element 20 can also be an electric heater. Using this device, the temperature of the sewage in tank (1) is between 20 degrees and 40 degrees. When the temperature sensing switch 19 is set to a temperature such as Since the gas is heated by the heating element 20 for heating the gas, it is possible to obtain exactly the same effect as in the first and fourth embodiments.

以上の装置を設置して使用すると1次のような効果を奏
する。第1実施態様の場合は1地中温度内外の常@(セ
氏20度〜18度)で定風量の条件で乾燥空気を媒体と
して汚水内の水分を結晶水滴の状態で定量摂取する事が
できるから\槽の大きさや送風機の能力、二次側高電圧
の大小、電導材の間隔や面積2通気口の大小や数2通気
路a断面の大きさや気泡出口の大小、水量感知スイッチ
の槽内感知位置、汚水導入口位置と汚水量、液体摂取口
位置2等を決定すれば、汚水中の指定水分だけ除く事が
できる。したがって、除々、に濃縮される汚水を一定時
期に欠み取る事によって機能を維持する事ができるから
、摂取した水質は蒸留水に近く、この1ま下水に放流し
ても1河川や地下水の汚染の心配は皆無である。又1こ
の摂取水を、1便所の洗浄水や洗濯、溶槽用、散水や園
芸用の水等に二次利用する事もできる。第2実施態様の
場合は1送風機の送風能力が二通り以上に変化するから
1M内汚水の大量導入時に水分の摂取能力を上げる事に
より1大量汚水投入に対処する事ができる。第3実施態
様の場合は1槽が槽外に対して断熱保温の性能を有する
事により、末期の寒冷地区の槽内温度を一定に保持でき
るから1摂水能力と汚水槽内の好気菌の活生化を保持で
きる。第4実施態様の場合は一槽内の液体温度を上昇さ
せる事により)汚水槽内の好気菌の活性化と摂取水の増
加を促す事ができる。第5実施態様の場合は1加温空気
を槽内汚水内に送る事によって1第4実施態様と全く同
じ効果を得る事ができる。そして1この装置の高電圧加
圧装置に要する電力の消耗使用量は)高電圧加圧機器の
熱損失に要する電気量であるから1送風機、加温発熱体
)に要する電気料が主でありへ維持費が安い。
When the above device is installed and used, the following effects are produced. In the case of the first embodiment, it is possible to take in a fixed amount of moisture in sewage in the form of crystalline water droplets using dry air as a medium under conditions of a constant air flow at a constant underground temperature (20 degrees Celsius to 18 degrees Celsius). From the size of the tank, the capacity of the blower, the size of the secondary high voltage, the spacing and area of conductive materials, the size and number of vents, the number of ventilation channels, the size of the cross section, the size of the air bubble outlet, and the water level sensing switch inside the tank. By determining the sensing position, the sewage inlet position, the amount of sewage, the liquid intake position 2, etc., it is possible to remove only the specified moisture from the sewage. Therefore, the function can be maintained by removing the gradually concentrated wastewater at a certain period of time, so the quality of the ingested water is close to that of distilled water, and even if it is discharged into the sewage system, only one river or underground water can be used. There is no need to worry about contamination. In addition, this intake water can be used for secondary purposes such as flushing water for toilets, washing, bathing, watering, gardening, etc. In the case of the second embodiment, since the blowing capacity of one blower changes in two or more ways, it is possible to cope with one large amount of sewage input by increasing the water intake capacity when a large amount of 1M sewage is introduced. In the case of the third embodiment, one tank has the ability to insulate and retain heat from the outside of the tank, so it is possible to maintain a constant temperature inside the tank in the final stage of cold regions. Activation can be maintained. In the case of the fourth embodiment, by increasing the temperature of the liquid in one tank, it is possible to activate the aerobic bacteria in the sewage tank and increase the intake of water. In the case of the fifth embodiment, exactly the same effect as the first and fourth embodiments can be obtained by sending heated air into the wastewater in the tank. 1) The amount of electricity required for the high-voltage pressurizing device of this device is the amount of electricity required for heat loss of the high-voltage pressurizing equipment, so 1) The electricity cost required for the blower, heating element) is the main amount. Maintenance costs are low.

尚1次のような実施例もできる。Incidentally, the following embodiment can also be used.

(1)S槽外の通気路(3)の部分に断熱保温材を施工
する。
(1) Install a heat insulating material on the ventilation path (3) outside the S tank.

(2)1電導材の部分(6)を高位置に配設し、高架水
槽21の槽内と液体摂取口(8)の間を封水の状態で配
する。
(2) The conductive material portion (6) is placed at a high position to provide a water seal between the inside of the elevated water tank 21 and the liquid intake port (8).

そうすると1第1実施例の場合は1通気路(3)の部分
を通過する空気が外気の温度の影響を受けないから1冬
期に良い。第2実施例の場合は)結露水滴の状態で摂取
した水は高架水内に自動的に入るから1雑水用として1
このまま二次利用する事ができる。(第8図に記載。)
Then, in the case of the first embodiment, the air passing through the ventilation path (3) is not affected by the temperature of the outside air, so it is suitable for the winter season. In the case of the second embodiment), the water taken in the form of condensed water automatically enters the elevated water, so 1 for miscellaneous water and 1
You can use it for secondary purposes as is. (Described in Figure 8.)

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

第1図、第2図、第3図はそれぞれこの発明5の第1実
施態様の一部断面配管配線図、一部断面斜視図、配線系
 図。第4図は第2実施態様の一部断面配管配線図。第
5図は第3実施態様の一部断面配管配線図。第6図は)
第4実施態様の一部断面配管配線図。第7図は九第5実
施態様の一部断面配管配線図。第8図は1この発明の第
2実施例の口。(5)は高電圧加圧機器。(6)は電導
材の部分。(7)。13は排水口。14は直流電源。1
4’l’l交流電源。15はマンホール。16は断熱保
温材。17は液体用発熱体。18は温度感知材。i’1
9は温度感知スイッチ(温度センサー)。20は気体加
熱用発熱体。21は高架水槽。
FIGS. 1, 2, and 3 are a partially sectional piping and wiring diagram, a partially sectional perspective view, and a wiring system diagram, respectively, of the first embodiment of the fifth invention. FIG. 4 is a partially sectional piping wiring diagram of the second embodiment. FIG. 5 is a partially cross-sectional piping wiring diagram of the third embodiment. Figure 6)
Partial cross-sectional piping wiring diagram of the fourth embodiment. FIG. 7 is a partially cross-sectional piping and wiring diagram of the ninth embodiment. FIG. 8 shows a mouth of a second embodiment of the present invention. (5) is a high voltage pressurizing device. (6) is the conductive material part. (7). 13 is the drain. 14 is a DC power supply. 1
4'l'l AC power supply. 15 is a manhole. 16 is a heat insulating material. 17 is a heating element for liquid. 18 is a temperature sensing material. i'1
9 is a temperature sensing switch (temperature sensor). 20 is a heating element for heating gas. 21 is an elevated water tank.

Claims (6)

【特許請求の範囲】[Claims] (1)、槽内空気が槽外へ流出しない槽の、導入口から
槽内へ導入した汚水に、送風機によって気泡状態で空気
の供給を行う事ができるばっ気槽と送風機の吸気口の部
分とを通気路により連結し、通気路の途中に、高電圧を
加圧した二次側両電極の電導材の部分を配設して、電導
材の部分に発生する結晶水滴を摂取する液体摂取部分を
有し、送風機と電導材の間の通気路を含む部分に、外気
と通じる通気口を有して、高電圧加圧部分の電源、ある
いは電導材の操作が、槽内汚水量の変化に係合して作動
するスイッチの、汚水内水分摂取装置。
(1) In a tank where the air inside the tank does not flow out of the tank, the aeration tank and the air intake port of the blower can supply air in the form of bubbles using a blower to the wastewater introduced into the tank from the inlet. are connected by a ventilation path, and in the middle of the ventilation path, a conductive material part of both secondary electrodes that is pressurized with a high voltage is placed, and liquid intake is performed to take in crystal water droplets generated on the conductive material part. The part that includes the ventilation path between the blower and the conductive material has a vent that communicates with the outside air, so that the power source of the high voltage pressurized part or the operation of the conductive material can change the amount of sewage in the tank. A waste water intake device of a switch which is activated by engagement with the sewage water intake device.
(2)、送風機の吐出風量が可変であり、槽内汚水量の
変化に係合して送風機が作動する、特許請求の範囲第1
項に記載の、汚水内水分摂取装置。
(2) The discharge air volume of the blower is variable, and the blower operates in response to changes in the amount of sewage in the tank.
Water intake device in sewage as described in Section 1.
(3)、ばっ気槽に断熱保温材を施した、特許請求の範
囲第1項、あるいは第2項に記載の、汚水内水分摂取装
置。
(3) The waste water intake device according to claim 1 or 2, wherein the aeration tank is provided with a heat insulating material.
(4)、ばっ気槽内に、槽内汚水の温度の変化に係合し
て作動する加温装置を有する、特許請求の範囲第1項、
あるいは第2項、あるいは第3項に記載の、汚水内水分
摂取装置。
(4) Claim 1, which has a heating device in the aeration tank that operates in response to a change in the temperature of the sewage in the tank;
Alternatively, the sewage water intake device according to item 2 or 3.
(5)、加温装置が、槽内の汚水内の部分に配設する液
体用発熱体である、特許請求の範囲第4項に記載の、汚
水内水分摂取装置。
(5) The water intake device in sewage according to claim 4, wherein the heating device is a heating element for liquid disposed in a portion of the tank inside the sewage.
(6)、加温装置が、送風機と汚水内気泡吐出口とを連
結する通気路を含む部分の何れかの部分に配設する気体
加温用発熱体である、特許請求の範囲第4項に記載の、
汚水内水分摂取装置。
(6) Claim 4, wherein the heating device is a heating element for heating gas disposed in any part of a part including an air passage connecting the blower and the air bubble discharge port in the sewage. As stated in
Water intake device in sewage.
JP62312974A 1987-12-09 1987-12-09 Apparatus for water intaking from polluted water Pending JPH01151923A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62312974A JPH01151923A (en) 1987-12-09 1987-12-09 Apparatus for water intaking from polluted water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62312974A JPH01151923A (en) 1987-12-09 1987-12-09 Apparatus for water intaking from polluted water

Publications (1)

Publication Number Publication Date
JPH01151923A true JPH01151923A (en) 1989-06-14

Family

ID=18035720

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62312974A Pending JPH01151923A (en) 1987-12-09 1987-12-09 Apparatus for water intaking from polluted water

Country Status (1)

Country Link
JP (1) JPH01151923A (en)

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