JPH03146193A - Waste water processing device - Google Patents

Waste water processing device

Info

Publication number
JPH03146193A
JPH03146193A JP1284200A JP28420089A JPH03146193A JP H03146193 A JPH03146193 A JP H03146193A JP 1284200 A JP1284200 A JP 1284200A JP 28420089 A JP28420089 A JP 28420089A JP H03146193 A JPH03146193 A JP H03146193A
Authority
JP
Japan
Prior art keywords
wastewater
ozone
tank
treatment tank
treatment
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
JP1284200A
Other languages
Japanese (ja)
Other versions
JPH0585236B2 (en
Inventor
Hiroshi Saito
弘 斎藤
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.)
YUNISOIDO KK
Original Assignee
YUNISOIDO KK
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 YUNISOIDO KK filed Critical YUNISOIDO KK
Priority to JP1284200A priority Critical patent/JPH03146193A/en
Publication of JPH03146193A publication Critical patent/JPH03146193A/en
Publication of JPH0585236B2 publication Critical patent/JPH0585236B2/ja
Granted 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

  • Biological Treatment Of Waste Water (AREA)
  • Activated Sludge Processes (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Abstract

PURPOSE:To dispense with a special process to extract an oily portion and decompose the oily portion positively with the dissipation of an obnoxious odor so that no sludge generates by ejecting air containing ozone to waste water in a state where microbes are kept in the waste water. CONSTITUTION:After charging a specified amount of microbes 60 in a processing tank 10, ozonizers 34 to 36 are started and a pump 42 is driven. As a result, air containing ozone is ejected from nozzles 21 to 23 after passing through ducts 31 to 33. The air containing ozone ejected from the nozzles 21 to 23 causes the oxidation reduction potential of the treated water to increase. If a sensor 27 detects that the potential has reached a range where microbes act actively, the voltage of the ozonizers 34 to 36 is adjusted by an adjuster 39 so that a controller 50 does not sterilize microbes. In this way, the ozone generation amount is controlled. The oily portion of waste water is decomposed and obnoxious odor is removed by the various actions of microbes dispersed in water, the oxidation process of ozone and decomposition of the oily portion.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、油分を含有した排水又は家庭の雑排水の処理
装置に関する。更に詳しくはホテル、旅館、食堂、レス
トラン、給食センター等の業務用厨房から排出される食
用油を含有した水の処理に適する装置又は家庭の台所や
トイレから排出される雑排水の処理装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an apparatus for treating oil-containing wastewater or domestic gray water. More specifically, it relates to equipment suitable for treating water containing edible oil discharged from commercial kitchens such as hotels, inns, cafeterias, restaurants, and food service centers, or equipment for treating gray water discharged from home kitchens and toilets. It is.

[従来の技術] 従来、この種の処理装置は、業務用においては浮上油分
分離槽又は油吸着マットを備え、浮上した油分を強制的
に取出すか、或いは油吸着マットに油を吸着させてこの
マットを定期的に交換している。
[Prior Art] Conventionally, this type of treatment equipment for commercial use is equipped with a floating oil separation tank or an oil absorption mat, and either the floating oil is forcibly taken out or the oil is adsorbed on the oil absorption mat. Mats are replaced regularly.

また家庭用の排水処理装置においては、嫌気性濾床槽と
接触曝気槽とを備え、嫌気、性濾床槽に嫌気性バクテリ
アを含む土壌を入れ、この嫌気性濾床槽で排水中の有機
物を濾材表面に生成した嫌気性バクテリアにより分解し
た後、この排水を接触曝気槽で散気管から噴出する空気
で混合攪拌し、かつ接触材表面の生物膜と十分に接触さ
せて酸化し、排水中の栄養基質を除去している。
In addition, household wastewater treatment equipment is equipped with an anaerobic filter bed tank and a contact aeration tank, and the anaerobic filter bed tank is filled with soil containing anaerobic bacteria. is decomposed by anaerobic bacteria generated on the surface of the filter medium, and then this wastewater is mixed and agitated in a contact aeration tank with air ejected from an aeration pipe, and brought into sufficient contact with the biological film on the surface of the contact material to oxidize it, and the wastewater is oxidized. nutrient substrates are removed.

[発明が解決しようとする課題] 上記業務用の処理装置においては、排水自体がらは油分
を除去できるものの、取出し作業は悪臭の環境下で行わ
なければならないため煩わしく、しかも単独で或いはマ
ットに吸着させて取出した油分はそのままの形態では廃
棄できず、焼却又は再処理する必要がある問題点があっ
た。
[Problems to be Solved by the Invention] Although the above-mentioned commercial treatment equipment can remove oil from the wastewater itself, the extraction work must be carried out in a foul-smelling environment, which is cumbersome, and moreover, oil can be removed alone or by adsorption to a mat. There was a problem in that the oil extracted from this process could not be disposed of in its original form and had to be incinerated or reprocessed.

また家庭用の処理装置においては、嫌気性バクテリアを
含む土壌の地域差や農薬、除草剤等の汚染程度に起因し
て土質が異なり、バクテリアの分解力にバラツキを生じ
、処理装置が有効に機能しない不具合があった。更に嫌
気性濾床槽で発生したメタンガスのため、極めて強烈な
悪臭が漂うばかりか、接触曝気槽の接触材表面で保持で
きる生物汚泥の全には限界があるため、定期的に接触材
を逆洗する等の保守作業を要する欠点があった。
In addition, in household treatment equipment, the soil quality differs due to regional differences in soil containing anaerobic bacteria and the degree of contamination with pesticides, herbicides, etc., which causes variations in the decomposition power of bacteria, making it difficult for the treatment equipment to function effectively. There was a problem that it did not work. Furthermore, the methane gas generated in the anaerobic filter bed tank has an extremely strong odor, and there is a limit to the amount of biological sludge that can be retained on the surface of the contact material in the contact aeration tank, so the contact material must be reversed periodically. There was a drawback that maintenance work such as washing was required.

本発明の第1の目的は、油分を特別に取出す作業を必要
とせず、悪臭を消散して油分を確実に分解し、スラッジ
を生じない排水処理装置を提供することにある。
A first object of the present invention is to provide a wastewater treatment device that does not require special work to extract oil, dissipates bad odors, reliably decomposes oil, and does not generate sludge.

また本発明の第2の目的は、家庭の雑排水を悪臭を発散
させることなく、一定の水質基準まで浄化し得る排水処
理装置を提供することにある。
A second object of the present invention is to provide a wastewater treatment device that can purify domestic gray water to a certain water quality standard without emitting bad odors.

[課題を解決するための手段] 上記目的を達成するために、本発明の排水処理装置は、
排水の流入口と処理水の流出口を有する処理槽と、オゾ
ン発生素子とこの素子に高周波交流高電圧を印加する高
周波高電圧電源と前記電源電圧又は周波数を調整してオ
ゾン発生量を調整する調整器とからなるオゾナイザと、
前記オゾナイザで発生したオゾンを前記処理槽内の排水
中に空気とともに噴出させるオゾン噴出手段と、予め培
養された好気性バクテリア又は黴のいずれか一方又は双
方を含む微生物を前記処理槽内の排水中で維持する微生
物維持手段とを備えたものである。
[Means for Solving the Problems] In order to achieve the above object, the wastewater treatment device of the present invention has the following features:
A treatment tank having an inlet for wastewater and an outlet for treated water, an ozone generating element, a high frequency high voltage power source that applies a high frequency AC high voltage to this element, and adjusting the power supply voltage or frequency to adjust the amount of ozone generated. an ozonizer consisting of a regulator;
ozone ejection means for ejecting ozone generated by the ozonizer into the waste water in the treatment tank together with air; and microorganisms containing pre-cultured aerobic bacteria and/or mold into the waste water in the treatment tank. microbial maintenance means for maintaining the microorganisms.

[作 用] 微生物維持手段により好気性バクテリア、黴等の微生物
を排水中で維持した状態で、オゾン噴出手段によりオゾ
ンを含む空気を排水に噴出すると、オゾンにより微生物
が活性化するとともに、オゾンの消臭作用及び油脂分解
作用と微生物の油脂分解作用を含む各種分解作用により
、排水の悪臭を消散しながら排水中の有機物質を確実に
分解することができる。
[Effect] When microorganisms such as aerobic bacteria and mold are maintained in the wastewater by the microorganism maintenance means, and air containing ozone is ejected into the wastewater by the ozone ejection means, the microorganisms are activated by the ozone, and the ozone is Various decomposition actions including deodorizing action, fat decomposition action, and oil decomposition action of microorganisms make it possible to reliably decompose organic substances in waste water while dissipating the bad odor of waste water.

[実施例] 次に本発明の実施例を図面に基づいて詳しく説明する。[Example] Next, embodiments of the present invention will be described in detail based on the drawings.

第1図は本発明の第1実施例を示す。10は排水処理装
置の処理槽であって、この例では処理装置は給食センタ
ーの厨房からの排水を処理する装置である。処理槽10
は排水の流入口11と処理水の流出口12を有する。処
理槽10の大きさは、幅70cm、長さ210cm、深
さ100cm (容積的1.0m”)であって、2枚の
隔壁13及び14によりほぼ同容積の3つの処理室16
.17及び18に仕切られる。10aは処理槽10の蓋
である。隔壁13及び14は槽底部から所定の高さだけ
離間して設けられ、処理水は処理室16から処理室17
の槽底部を通って処理室18に流れるようになっている
FIG. 1 shows a first embodiment of the invention. Reference numeral 10 denotes a treatment tank of a wastewater treatment device, and in this example, the treatment device is a device for treating wastewater from the kitchen of a feeding center. Processing tank 10
has an inlet 11 for wastewater and an outlet 12 for treated water. The processing tank 10 has a width of 70 cm, a length of 210 cm, and a depth of 100 cm (1.0 m'' in volume), and the two partition walls 13 and 14 form three processing chambers 16 with approximately the same volume.
.. It is divided into 17 and 18. 10a is a lid of the processing tank 10. The partition walls 13 and 14 are provided at a predetermined height apart from the bottom of the tank, and the treated water flows from the treatment chamber 16 to the treatment chamber 17.
The water flows into the processing chamber 18 through the bottom of the tank.

流入口11には流入管19が接続され、流出口12には
流出管20が接続される。流出口12は未処理の排水が
容易に流出しないように、流入口11より低位置に設け
られる。
An inflow pipe 19 is connected to the inflow port 11, and an outflow pipe 20 is connected to the outflow port 12. The outflow port 12 is provided at a lower position than the inflow port 11 so that untreated wastewater does not easily flow out.

処理槽10の処理室16.17及び18にはオゾンを含
む空気を噴出するノズル21.22及び23か配設され
る。処理室16にはステンレススチール製金網からなる
箱状のスクリーン24が取外し可能に設けられる。流入
管19の先端はスクリーン24に向けられる。このスク
リーン24はアルミニウム製又は他の金属で作られたも
のでもよく、また流入口11に続く処理室16の外部に
設けてもよい。
The processing chambers 16, 17 and 18 of the processing tank 10 are provided with nozzles 21, 22 and 23 that eject air containing ozone. A box-shaped screen 24 made of stainless steel wire mesh is removably provided in the processing chamber 16. The tip of the inflow pipe 19 is directed toward the screen 24 . This screen 24 may be made of aluminum or other metal and may be provided outside the processing chamber 16 adjacent to the inlet 11.

処理室17には微生物維持器26及び処理水の酸化還元
電位を検出する酸化還元電位センサ27が配設される。
A microorganism maintainer 26 and an oxidation-reduction potential sensor 27 for detecting the oxidation-reduction potential of the treated water are disposed in the processing chamber 17.

処理室18には処理槽底部の水を流出口12に導く案内
筒28が設けられる。28aは案内筒28の蓋である。
The processing chamber 18 is provided with a guide cylinder 28 that guides water at the bottom of the processing tank to the outlet 12. 28a is a lid of the guide tube 28.

ノズル21〜23はそれぞれ管路31.32及び33を
介してオゾナイザ34.35及び36に接続される。オ
ゾナイザ34〜36は、それぞれ誘電体上に電極を形成
したオゾン発生素子37と、これらの素子37に高周波
交流電圧を印加するための高周波高電圧電源38と、こ
の電源38の電圧又は周波数を調整してオゾン発生量を
調整する調整器39により構成される。各調整器39は
オゾン発生量を0 、 O5ppm〜170ppmのオ
ゾン濃度範囲内で調整することができる。
Nozzles 21-23 are connected via lines 31.32 and 33 to ozonizers 34.35 and 36, respectively. The ozonizers 34 to 36 each include an ozone generating element 37 having an electrode formed on a dielectric material, a high frequency high voltage power source 38 for applying a high frequency AC voltage to these elements 37, and adjusting the voltage or frequency of this power source 38. It is composed of a regulator 39 that adjusts the amount of ozone generated. Each regulator 39 can adjust the amount of ozone generated within the ozone concentration range of 0.5 ppm to 170 ppm.

オゾナイザ34〜36には管路41を介してポンプ42
が接続される。ポンプ42、管路41、管路31〜33
及びノズル21〜23はオゾン噴出手段を構成する。オ
ゾナイザ34〜36の電源38とポンプ42はそれぞれ
スイッチ34a、35a、36a及び42aを介して交
流電源43に接続される。
A pump 42 is connected to the ozonizers 34 to 36 via a conduit 41.
is connected. Pump 42, pipe line 41, pipe lines 31 to 33
The nozzles 21 to 23 constitute ozone ejection means. The power supply 38 and pump 42 of the ozonizers 34-36 are connected to an AC power supply 43 via switches 34a, 35a, 36a and 42a, respectively.

微生物維持器26は処理槽10に導入された好気性バク
テリア、黴等の微生物を維持するもので、導電性金網に
より形成された筒状体44と、この筒状体44に充填さ
れた多数の多孔質のセラミック誘電体45と、金網に電
気的に接続された電極46と、この電極46に負電位を
印加してセラミック誘電体45を負イオン化するアイオ
ナイザ47とを備える。アイオナイザ47はパルス電圧
を負電位にバイアスさせる回路を有し、処理槽10の外
部に設けられる。
The microorganism maintainer 26 maintains microorganisms such as aerobic bacteria and mold introduced into the processing tank 10, and includes a cylindrical body 44 formed of a conductive wire mesh and a large number of microorganisms filled in the cylindrical body 44. It includes a porous ceramic dielectric 45, an electrode 46 electrically connected to a wire mesh, and an ionizer 47 that applies a negative potential to the electrode 46 to negatively ionize the ceramic dielectric 45. The ionizer 47 has a circuit that biases the pulse voltage to a negative potential, and is provided outside the processing tank 10.

セラミック誘電体45は外径が2mm〜15mmの粒状
、ペレット状、又はブロック状をなす。筒状体44は底
部を有し、その金網の目はこれらのセラミック誘電体4
5が飛出さないように設定される。
The ceramic dielectric 45 has a grain, pellet, or block shape with an outer diameter of 2 mm to 15 mm. The cylindrical body 44 has a bottom, and the mesh of the wire mesh is connected to these ceramic dielectrics 4.
5 is set so that it does not pop out.

セラミック誘電体45としては、酸化アルミニウム、酸
化チタン、チタン酸バリウム、酸化けい素、酸化マグネ
シウム等又はこれらの複合体が挙げられる。
Examples of the ceramic dielectric 45 include aluminum oxide, titanium oxide, barium titanate, silicon oxide, magnesium oxide, and composites thereof.

この処理槽10に導入される微生物60は澱粉分解作用
、糖分分解作用、脂肪酸分解作用、蛋白質分解作用、リ
グニン分解作用、硝酸化作用、硫酸化作用、繊維素分解
作用をそれぞれ行う細菌、放線菌、根粒菌、酵母菌、硝
化菌、糸状菌の群から所定の割合で複数種類選択配合さ
れた4〜80℃の温度範囲内で作用可能な複合バクテリ
アである。微生物60は列挙する上記菌の中から排水の
温度、水質等に応じて複数種類の菌が適宜選定される。
The microorganisms 60 introduced into this treatment tank 10 are bacteria and actinomycetes that perform starch decomposition, sugar decomposition, fatty acid decomposition, protein decomposition, lignin decomposition, nitrification, sulfation, and fibrinolytic actions. It is a composite bacteria that can act within the temperature range of 4 to 80°C, which is selected from the groups of rhizobia, yeast, nitrifying bacteria, and filamentous bacteria in a predetermined ratio. As the microorganisms 60, a plurality of types of microorganisms are appropriately selected from among the above-mentioned microorganisms according to the temperature, water quality, etc. of the wastewater.

本発明では上記複合バクテリアを用いることにより、従
来の嫌気性バクテリアのように採取する土壌の地域差や
農薬、除草剤等の汚染程度に起因した各種分解作用のバ
ラツキがなく、常に処理装置の油分分解能力を初めとす
る上記各種の分解能力を一定に保つ。また好気性のため
メタンガスのような悪臭のガスを発生しない利点を有す
る。
In the present invention, by using the above-mentioned composite bacteria, unlike conventional anaerobic bacteria, there is no variation in various decomposition effects caused by regional differences in the soil collected or the degree of contamination with pesticides, herbicides, etc., and the oil content in the processing equipment is always maintained. The various decomposition capacities mentioned above, including the decomposition capacity, are kept constant. Also, because it is aerobic, it has the advantage of not producing foul-smelling gases such as methane gas.

酸化還元電位センサ27の検出出力はコントロ−ラ50
に接続され、コントローラ50の制御出力はオゾナイザ
34〜36の調整器39、アイオナイザ47に接続され
る。コントローラ50にはアイオナイザ47を一定時間
作動させるためのタイマ48が設けられる。
The detection output of the oxidation-reduction potential sensor 27 is detected by the controller 50.
The control output of the controller 50 is connected to the regulator 39 of the ozonizers 34 to 36 and the ionizer 47. The controller 50 is provided with a timer 48 for operating the ionizer 47 for a certain period of time.

このような構成の排水処理装置の動作について説明する
The operation of the wastewater treatment device having such a configuration will be explained.

処理槽10の蓋10aを開け、予め培養された微生物6
0を第1図の矢印に示すように処理槽10内に所定量大
れた後、スイッチ34a〜36aを入れてオゾナイザ3
4〜36を起動し、引続いてスイッチ42aを入れてポ
ンプ42を駆動する。
Open the lid 10a of the treatment tank 10 and remove the pre-cultured microorganisms 6.
After a predetermined amount of ozonizer 0 has been added to the treatment tank 10 as shown by the arrow in FIG.
4 to 36, and then turn on the switch 42a to drive the pump 42.

オゾンを1〜2容積%程度含んだ空気が管路31〜33
を通ってノズル21〜23から噴出する。同時にコント
ローラ50はアイオナイザ47をタイマ48により一定
時間だけ作動して電極46に負電位を印加し、筒状体4
4に入ったセラミック誘電体45を負イオン化する。こ
れにより正電位に帯電している好気性バクテリアや菌等
の微生物がセラミック誘電体45に引寄せられて維持さ
れる。
Air containing about 1 to 2% by volume of ozone is supplied to pipes 31 to 33.
It passes through and is ejected from nozzles 21-23. At the same time, the controller 50 operates the ionizer 47 for a certain period of time using the timer 48 to apply a negative potential to the electrode 46, and
The ceramic dielectric material 45 contained in step 4 is negatively ionized. As a result, microorganisms such as aerobic bacteria and fungi that are positively charged are attracted to the ceramic dielectric body 45 and maintained.

アイオナイザ47が不作動になると、微生物はセラミッ
ク誘電体45から離れて処理室16〜18の水中に分散
する。図示しないが、流入管19に流量センサを設け、
流入量が増加したときにアイオナイザ47を不作動にす
ることが好ましい。
When the ionizer 47 is deactivated, the microorganisms leave the ceramic dielectric 45 and disperse into the water in the process chambers 16-18. Although not shown, a flow rate sensor is provided in the inflow pipe 19,
Preferably, the ionizer 47 is deactivated when the inflow increases.

流入管19より排水が処理槽10に流入すると、先ずス
クリーン24により粗大塵埃が捕獲される。
When wastewater flows into the treatment tank 10 from the inflow pipe 19, coarse dust is first captured by the screen 24.

このスクリーン24は定期的に塵埃が取出され清掃され
る。ノズル21〜23から噴出するオゾンを含んだ空気
により、処理水の酸化還元電位が上昇し、微生物が活発
に作用する300〜400mVの範囲に達したことをセ
ンサ27が検出すると、コントローラ50は微生物を殺
菌しないようにオゾナイザ34〜36の電圧を調整器3
9により下げてオゾン発生量を低減させる。処理水の酸
化還元電位が300mVを下回ると、再び調整器39に
よりオゾン発生量を増加させる。酸化還元電位を300
〜400mVの範囲に維持するために、この例では水1
00(Hlで1時間当り100mgのオゾンを発生する
ようにコントローラ50はオゾナイザ34〜36をそれ
ぞれ制御する。
This screen 24 is periodically cleaned to remove dust. When the sensor 27 detects that the ozone-containing air ejected from the nozzles 21 to 23 increases the oxidation-reduction potential of the treated water and reaches the range of 300 to 400 mV at which microorganisms actively act, the controller 50 Adjust the voltage of ozonizers 34 to 36 to prevent sterilization.
9 to reduce the amount of ozone generated. When the oxidation-reduction potential of the treated water falls below 300 mV, the amount of ozone generated is increased again by the regulator 39. Redox potential to 300
In this example, water 1
The controller 50 controls the ozonizers 34 to 36, respectively, to generate 100 mg of ozone per hour at 0.00 (Hl).

水中に分散した微生物の前述した各種作用とオゾンの酸
化作用及び油分分解作用により、排水中の油分が分解し
、かつ悪臭が消える。例えば、排水中にn−ヘキサンが
含まれている場合には、オゾンは次式によりn−ヘキサ
ンを水と二酸化炭素に分解する。
Due to the aforementioned various actions of the microorganisms dispersed in the water and the oxidizing action and oil decomposition action of ozone, the oil in the wastewater is decomposed and the bad odor disappears. For example, when n-hexane is contained in wastewater, ozone decomposes n-hexane into water and carbon dioxide according to the following equation.

3CH3(CH2)4CH3+ 190*→21120
 + 18CO。
3CH3(CH2)4CH3+ 190*→21120
+18CO.

オゾンを適度に噴出して酸化還元電位を300〜400
mVの範囲に制御することにより好気性バクテリアや黴
等の微生物が増殖し、かつアイオナイザ47で制御され
る微生物維持器26で微生物が処理槽10内で維持され
るため、多量の排水が処理槽10を長時間連続して通過
しても、油分の分解能力は低下せず、排水を安定して浄
化し続けることかできる。
A moderate amount of ozone is emitted to raise the redox potential to 300-400.
Microorganisms such as aerobic bacteria and mold grow by controlling the voltage within the mV range, and the microorganisms are maintained in the treatment tank 10 by the microorganism maintainer 26 controlled by the ionizer 47, so a large amount of wastewater is transferred to the treatment tank. 10 continuously for a long time, the ability to decompose oil does not decrease, and the wastewater can be stably purified.

排水は処理室16から処理室17及び18に行くに従っ
て浄化され、油分が分解され悪臭が消えた処理水は処理
槽10の底部から案内筒28に導かれて流出管20を通
って流出する。
The waste water is purified as it goes from the treatment chamber 16 to the treatment chambers 17 and 18, and the treated water, in which the oil content has been decomposed and the odor has disappeared, is guided from the bottom of the treatment tank 10 to the guide cylinder 28 and flows out through the outflow pipe 20.

第1表は時間平均の排水流入量が2.5m”、時間最大
流入量が5.0m”の厨房排水を本実施例装置で処理し
たときの流入管19で採取した処理前の排水及び流出管
20で採取した処理後の排水の各水質データである。水
質測定はJ Is−に−0102法により行った。
Table 1 shows the untreated wastewater and outflow collected from the inflow pipe 19 when kitchen wastewater with an hourly average inflow of 2.5 m" and a maximum hourly inflow of 5.0 m" was treated with the device of this embodiment. This is water quality data of the treated wastewater collected through the pipe 20. Water quality was measured by the JIS-0102 method.

第  1  表 第1表より本実施例装置が排水を良好な水質基準にまで
処理できることが判明した。
Table 1 From Table 1, it was found that the apparatus of this example was able to treat wastewater to a good water quality standard.

なお、上記排水処理装置は厨房排水処理用に限らず、工
業用の大型プラントにも使用することができる。
Note that the above-mentioned wastewater treatment device can be used not only for kitchen wastewater treatment but also for large-scale industrial plants.

また、微生物60は手操作で処理槽10に入れる以外に
、微生物を流動物質に含ませて、コントローラ50によ
り自動的に供給してもよい。
Further, instead of manually introducing the microorganisms 60 into the processing tank 10, the microorganisms may be included in a fluid substance and automatically supplied by the controller 50.

第2図は本発明の第2実施例を示す。この例では処理装
置は家庭の台所やトイレからの雑排水を処理する装置で
ある。第2図において、第1図と同一符号は同一構成部
品をそれぞれ示す。
FIG. 2 shows a second embodiment of the invention. In this example, the treatment device is a device that treats gray water from kitchens and toilets in homes. In FIG. 2, the same reference numerals as in FIG. 1 indicate the same components.

この例では、流出管20は流入管19と同一レベルに設
けられ、隔壁13及び14は槽底部に立設され、それぞ
れ上部に流入管19及び流出管20と同一レベルの開口
を有する。3つの処理室16〜18のノズル21〜23
には共通の管路31を介して単一のオゾナイザ34が接
続される。また処理室18と流出管20との間には消毒
室15が設けられ、この消毒室15には管路31から消
毒用細管31aが延設され、細管31aの先端にはノズ
ル31bが設けられる。16a、17a及び18aは処
理槽10の蓋である。
In this example, the outflow pipe 20 is provided at the same level as the inflow pipe 19, and the partition walls 13 and 14 are erected at the bottom of the tank, and each has an opening at the top thereof at the same level as the inflow pipe 19 and the outflow pipe 20. Nozzles 21 to 23 in three processing chambers 16 to 18
A single ozonizer 34 is connected to the two via a common pipe line 31. Further, a disinfection chamber 15 is provided between the processing chamber 18 and the outflow pipe 20, and a disinfection thin tube 31a is extended from a pipe line 31 to this disinfection chamber 15, and a nozzle 31b is provided at the tip of the thin tube 31a. . 16a, 17a and 18a are lids of the processing tank 10.

この処理槽10の容積は約2 、0m”であって、コン
トローラ50は水1000 文で1時間当り50mgの
オゾンを発生するようにオゾナイザ34を制御する。
The volume of the treatment tank 10 is approximately 2.0 m'', and the controller 50 controls the ozonizer 34 to generate 50 mg of ozone per hour with 1000 g of water.

このような構成の装置では、前記実施例と同様に蓋16
a〜18aを開け、予め培養された好気性バクテリア、
黴等の微生物6、Oを第2図の矢印に示すように処理槽
10内に手操作又は供給装置により所定全入れた後、図
示しないスイッチを入れてオゾナイザ34及びポンプ4
2を駆動する。
In an apparatus having such a configuration, the lid 16 is
Open a to 18a and add pre-cultured aerobic bacteria,
After putting a predetermined amount of microorganisms 6 and O such as mold into the treatment tank 10 manually or by a supply device as shown by the arrows in FIG. 2, a switch (not shown) is turned on and the ozonizer 34 and pump 4
Drive 2.

ノズル21〜23からオゾンを含む空気が噴出するため
、このオゾンの油分分解作用及び消臭作用が生じ、これ
に加えて微生物の油分分解作用を初めとする澱粉分解作
用、糖分分解作用、蛋白質分解作用、リグニン分解作用
、硝酸化作用、硫酸化作用、繊維素分解作用により、処
理槽10内の排水は処理室16から処理室18に流れる
に従い浄化される。消毒室15でオゾンを含む空気によ
り更に消毒される。
Since air containing ozone is ejected from the nozzles 21 to 23, this ozone has an oil decomposition action and a deodorizing action. As the wastewater in the treatment tank 10 flows from the treatment chamber 16 to the treatment chamber 18, it is purified by the lignin decomposition, nitrification, sulfation, and fibrinolysis. Further disinfection is carried out in the disinfection room 15 using air containing ozone.

酸化還元電位センサ27が検出するレドックス電位によ
り、前記実施例と同様にコントローラ50はオゾナイザ
34の調整器39を制御する。
Based on the redox potential detected by the oxidation-reduction potential sensor 27, the controller 50 controls the regulator 39 of the ozonizer 34, as in the previous embodiment.

第2表は一日平均の排水流入量が1.25m”の家庭の
雑排水を本実施例装置で処理したときの処理室16、処
理室17及び流出管20でそれぞれ採取した排水の各水
質データである。水質測定はJIS−に−0102法に
より行った。
Table 2 shows the water quality of the wastewater collected in the treatment chamber 16, treatment chamber 17, and outflow pipe 20 when household gray water with an average daily inflow of 1.25 m'' was treated with the device of this embodiment. Data.Water quality measurement was performed according to JIS-0102 method.

第  2  表 第2表より本実施例装置が家庭用浄化槽として良好な水
質基準にまで処理できることが判明した。
Table 2 From Table 2, it was found that the apparatus of this example can treat water to a good standard for water quality as a domestic septic tank.

なお、第2図に示す排水処理装置は家庭の台所やトイレ
からの雑排水の処理に限らず、第1図の処理装置の後に
続いて設置して、第1図の処理装置で浄化した排水をよ
り一層浄化するようにしてもよい。
The wastewater treatment equipment shown in Figure 2 is not limited to the treatment of gray water from household kitchens and toilets, and can be installed following the treatment equipment shown in Figure 1 to treat wastewater purified by the treatment equipment shown in Figure 1. may be further purified.

[発明の効果] 以上述べたように、本発明によれば、オゾンにより微生
物の各種作用を活性化するとともに、オゾンの消臭作用
及び油脂分解作用と、微生物の油脂分解作用を含む各種
の分解作用とを併用し、かつ処理中に流出し易い微生物
の維持手段を設けることにより、業務用の厨房から流出
される排水から油分を特別に取出すことなく、継続して
排水の悪臭を消散しながら排水中の油分を確実に分解す
ることができる。特に本発明によれば排水中に含まれる
有機物を主として二酸化炭素と水に分解するのでスラッ
ジの発生がなく、処理装置の保守点検を簡便に行うこと
ができる。
[Effects of the Invention] As described above, according to the present invention, ozone activates various actions of microorganisms, and also activates ozone's deodorizing action and fat-decomposing action, and various decomposition actions including the oil-decomposing action of microorganisms. By using this function in combination with the above-mentioned action and by providing a means to maintain microorganisms that tend to flow out during treatment, it is possible to continuously dissipate bad odors from wastewater without having to specifically extract oil from wastewater discharged from commercial kitchens. It is possible to reliably decompose oil in wastewater. In particular, according to the present invention, since the organic matter contained in the wastewater is mainly decomposed into carbon dioxide and water, no sludge is generated, and maintenance and inspection of the treatment equipment can be carried out easily.

また家庭の雑排水を悪臭を発散させることなく、一定の
水質基準まで浄化することができる。
In addition, it is possible to purify domestic gray water to a certain water quality standard without emitting bad odors.

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

第1図は本発明第1実施例の排水処理装置の構成図。 第2図は本発明第2実施例の排水処理装置の構成図。 10:処理槽、 11:流入口、 12:流出口、 13.14:隔壁、 16.17,18:処理室、 19:流入管、 20:流出管、 21.22,23:ノズル(オゾン噴出手段)、24ニ
スクリーン、 26:微生物維持器(微生物維持手段)、27二酸化還
元電位センサ、 28二案内筒、 34.35.36+オゾナイザ、 37;オゾン発生素子、 38:高周波高電圧電源、 39:調整器、 42:ポンプ(オゾン噴出手段)、 44:筒状体、 45:セラミック誘電体、 46:電極、 47:アイオナイザ、 60:微生物。
FIG. 1 is a configuration diagram of a wastewater treatment apparatus according to a first embodiment of the present invention. FIG. 2 is a configuration diagram of a wastewater treatment device according to a second embodiment of the present invention. 10: Treatment tank, 11: Inlet, 12: Outlet, 13.14: Partition wall, 16.17, 18: Processing chamber, 19: Inflow pipe, 20: Outflow pipe, 21.22, 23: Nozzle (ozone jet means), 24 Niscreen, 26: Microorganism maintenance device (microorganism maintenance means), 27 Dioxidation reduction potential sensor, 28 Two guide tubes, 34. 35. 36 + Ozonizer, 37; Ozone generation element, 38: High frequency high voltage power supply, 39 : Regulator, 42: Pump (ozone ejection means), 44: Cylindrical body, 45: Ceramic dielectric, 46: Electrode, 47: Ionizer, 60: Microorganism.

Claims (1)

【特許請求の範囲】 1)排水の流入口と処理水の流出口を有する処理槽と、 オゾン発生素子とこの素子に高周波交流高電圧を印加す
る高周波高電圧電源と前記電源電圧又は周波数を調整し
てオゾン発生量を調整する調整器とからなるオゾナイザ
と、 このオゾナイザで発生したオゾンを前記処理槽内の排水
中に空気とともに噴出させるオゾン噴出手段と、 予め培養された好気性バクテリア又は黴のいずれか一方
又は双方を含む微生物を前記処理槽内の排水中で維持す
る微生物維持手段と を備えた排水処理装置。 2)処理槽に微生物を供給する微生物供給手段を備えた
請求項1記載の排水処理装置。 3)排水の流入口の近傍に粗大塵埃を捕獲するスクリー
ンが設けられた請求項1記載の排水処理装置。 4)処理槽内に処理水の酸化還元電位を検出するセンサ
が設けられ、オゾナイザの調整器は前記センサの検出信
号により調整される請求項1記載の排水処理装置。 5)1又は2以上の隔壁で処理槽を仕切ることにより前
記処理槽に複数の処理室が形成され、オゾン噴出手段が
各処理室に設けられた請求項1記載の排水処理装置。 6)隔壁が槽底部から所定の高さだけ離間して設けられ
た請求項5記載の排水処理装置。 7)微生物維持手段は、導電性金網により形成された筒
状体と、この筒状体に収容された多数の多孔質のセラミ
ック誘電体と、この金網に電気的に接続された電極と、
この電極に負電位を印加して前記セラミック誘電体を負
イオン化するアイオナイザとを備えた請求項1記載の排
水処理装置。 8)微生物は澱粉分解作用、糖分分解作用、脂肪酸分解
作用、蛋白質分解作用、リグニン分解作用、硝酸化作用
、硫酸化作用、繊維素分解作用をそれぞれ行う細菌、放
線菌、根粒菌、酵母菌、硝化菌、糸状菌の群から所定の
割合で複数種類選択配合された4〜80℃の温度範囲内
で作用可能な複合バクテリアである請求項1記載の排水
処理装置。 9)処理水の流出口が排水の流入口より低位置に設けら
れ、前記流出口に処理槽底部の水を導く案内筒が接続さ
れた請求項1記載の排水処理装置。
[Claims] 1) A treatment tank having an inlet for wastewater and an outlet for treated water, an ozone generating element, a high frequency high voltage power supply that applies a high frequency AC high voltage to this element, and adjusting the power supply voltage or frequency. an ozonizer comprising a regulator that adjusts the amount of ozone generated by the ozonizer, an ozone ejection means that ejects the ozone generated by the ozonizer into the waste water in the treatment tank together with air, and a pre-cultured aerobic bacteria or mold and a microorganism maintaining means for maintaining microorganisms containing one or both of them in the waste water in the treatment tank. 2) The wastewater treatment apparatus according to claim 1, further comprising a microorganism supply means for supplying microorganisms to the treatment tank. 3) The wastewater treatment device according to claim 1, further comprising a screen for capturing coarse dust near the inlet of the wastewater. 4) The wastewater treatment apparatus according to claim 1, wherein a sensor for detecting the oxidation-reduction potential of the treated water is provided in the treatment tank, and the ozonizer regulator is adjusted by a detection signal from the sensor. 5) The wastewater treatment apparatus according to claim 1, wherein a plurality of treatment chambers are formed in the treatment tank by partitioning the treatment tank with one or more partition walls, and an ozone jetting means is provided in each treatment chamber. 6) The wastewater treatment apparatus according to claim 5, wherein the partition wall is provided at a predetermined height apart from the bottom of the tank. 7) The microorganism maintaining means includes a cylindrical body formed of a conductive wire mesh, a large number of porous ceramic dielectrics housed in the cylindrical body, and an electrode electrically connected to the wire mesh.
The wastewater treatment apparatus according to claim 1, further comprising an ionizer that applies a negative potential to the electrode to negatively ionize the ceramic dielectric. 8) Microorganisms include bacteria, actinomycetes, rhizobia, and yeast bacteria that perform starch decomposition, sugar decomposition, fatty acid decomposition, proteolysis, lignin decomposition, nitrification, sulfation, and fibrinolytic actions, respectively. 2. The wastewater treatment device according to claim 1, which is a composite bacterium which is selected from the group of nitrifying bacteria and filamentous fungi in a predetermined ratio and is capable of acting within a temperature range of 4 to 80°C. 9) The wastewater treatment apparatus according to claim 1, wherein the outlet of the treated water is provided at a lower position than the inlet of the wastewater, and a guide tube for guiding water from the bottom of the treatment tank is connected to the outlet.
JP1284200A 1989-10-31 1989-10-31 Waste water processing device Granted JPH03146193A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1284200A JPH03146193A (en) 1989-10-31 1989-10-31 Waste water processing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1284200A JPH03146193A (en) 1989-10-31 1989-10-31 Waste water processing device

Publications (2)

Publication Number Publication Date
JPH03146193A true JPH03146193A (en) 1991-06-21
JPH0585236B2 JPH0585236B2 (en) 1993-12-06

Family

ID=17675461

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1284200A Granted JPH03146193A (en) 1989-10-31 1989-10-31 Waste water processing device

Country Status (1)

Country Link
JP (1) JPH03146193A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000271592A (en) * 1999-03-24 2000-10-03 Ebara Corp Anaerobic treatment method of grease-containing waste water
US6303025B1 (en) * 2000-02-17 2001-10-16 Jon E. Houchens Water purification system with baffled flow
JP2006314911A (en) * 2005-05-12 2006-11-24 Takasago Thermal Eng Co Ltd Sludge treatment method and waste water treatment system for biological treatment tank
JP2007203132A (en) * 2006-01-31 2007-08-16 Shinichi Fukada Continuous operation type garbage-treating apparatus
JP2008036467A (en) * 2006-08-01 2008-02-21 Takasago Thermal Eng Co Ltd Control system for biological treatment tank
JP2009285554A (en) * 2008-05-28 2009-12-10 Delica Chef:Kk Solid food organic waste treating method

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63236596A (en) * 1987-03-25 1988-10-03 Nippon Steel Corp Treatment of waste water with activated sludge

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63236596A (en) * 1987-03-25 1988-10-03 Nippon Steel Corp Treatment of waste water with activated sludge

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2000271592A (en) * 1999-03-24 2000-10-03 Ebara Corp Anaerobic treatment method of grease-containing waste water
US6303025B1 (en) * 2000-02-17 2001-10-16 Jon E. Houchens Water purification system with baffled flow
JP2006314911A (en) * 2005-05-12 2006-11-24 Takasago Thermal Eng Co Ltd Sludge treatment method and waste water treatment system for biological treatment tank
JP2007203132A (en) * 2006-01-31 2007-08-16 Shinichi Fukada Continuous operation type garbage-treating apparatus
JP4643460B2 (en) * 2006-01-31 2011-03-02 晋一 深田 Continuous operation type garbage processing equipment
JP2008036467A (en) * 2006-08-01 2008-02-21 Takasago Thermal Eng Co Ltd Control system for biological treatment tank
JP2009285554A (en) * 2008-05-28 2009-12-10 Delica Chef:Kk Solid food organic waste treating method

Also Published As

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