JPH0585236B2 - - Google Patents

Info

Publication number
JPH0585236B2
JPH0585236B2 JP1284200A JP28420089A JPH0585236B2 JP H0585236 B2 JPH0585236 B2 JP H0585236B2 JP 1284200 A JP1284200 A JP 1284200A JP 28420089 A JP28420089 A JP 28420089A JP H0585236 B2 JPH0585236 B2 JP H0585236B2
Authority
JP
Japan
Prior art keywords
wastewater
tank
treatment
ozone
wastewater 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.)
Expired - Fee Related
Application number
JP1284200A
Other languages
Japanese (ja)
Other versions
JPH03146193A (en
Inventor
Hiroshi Saito
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

Description

【発明の詳細な説明】[Detailed description of the invention]

[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。 [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ツトを備え、浮上し
た油分を強制的に取出すか、或いは油吸着マツト
に油を吸着させてこのマツトを定期的に交換して
いる。 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。 [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、排水自体か
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ツ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つた。 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
ない不具合があつた。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
物汚泥の量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つた。 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、スラツジを生じない排水処理装置を提供す
ることにある。 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。 [課題を解決するための手段] 上記目的を達成するために、第1図に示すよう
に、本発明の排水処理装置は、排水の流入口11
と処理水の流出口12を有する処理槽10と、オ
ゾン発生素子37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38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39とからなるオゾナイザ34〜36と、オ
ゾナイザ34〜36で発生したオゾンを処理槽1
0内の排水中に空気とともに噴出させるオゾン噴
出手段21,22,23,42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60を処理槽10内の排水中で維
持する微生物維持手段26とを備える。 そしてその特徴ある構成は、この微生物維持手
段26が、導電性金網により形成された筒状体4
4と、この筒状体44に収容された多数の多孔質
のセラミツク誘電体45と、この金網に電気的に
接続された電極46と、この電極46に負電位を
印加して前記セラミツク誘電体45を負イオン化
するアイオナイザ47とを備えることにある。 [作用] 微生物維持手段26のアイオナイザ47により
金網に電気的に接続された電極46に負電位を印
加して、筒状体44に入つたセラミツク誘電体4
5を負イオン化すると、正電位に帯電している好
気性バクテリア、黴等の微生物60が排水中で維
持される。この状態で、オゾン噴出手段21〜2
3,42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60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60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。 [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。 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つて、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(容積約1.0
m3)であつて、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
の槽底部を通つて処理室18に流れるようになつ
ている。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。 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が配設される。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。 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。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。28
aは案内筒28の蓋である。 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0.05ppm〜170ppmのオゾン濃
度範囲内で調整することができる。 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はそれぞれスイツチ34a,3
5a,36a及び42aを介して交流電源43に
接続される。 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
ミツク誘電体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
ラミツク誘電体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。 セラミツク誘電体45は外径が2mm〜15mmの粒
状、ペレツト状、又はブロツク状をなす。筒状体
44は底部を有し、その金網の目はこれらのセラ
ミツク誘電体45が飛出さないように設定され
る。セラミツク誘電体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。 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。 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。 酸化還元電位センサ27の検出出力はコントロ
ーラ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。 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。 処理槽10の蓋10aを開け、予め培養された
微生物60を第1図の矢印に示すように処理槽1
0内に所定量入れた後、スイツチ34a〜36a
を入れてオゾナイザ34〜36を起動し、引続い
てスイツチ42aを入れてポンプ42を駆動す
る。オゾンを1〜2容積%程度含んだ空気が管路
31〜33を通つてノズル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4
6に負電位を印加し、筒状体44に入つたセラミ
ツク誘電体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
生物がセラミツク誘電体45に引寄せられて維持
される。アイオナイザ47が不作動になると、微
生物はセラミツク誘電体45から離れて処理室1
6〜18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。 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。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39
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1000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。 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。 3CH3(CH24CH3+1903→21H2O+18CO2 オゾンを適度に噴出して酸化還元電位を300〜
400mV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
ことができる。 排水は処理室16から処理室17及び18に行
くに従つて浄化され、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を通つて流出する。 第1表は時間平均の排水流入量が2.5m3、時間
最大流入量が5.0m3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JIS−K−0102法に
より行つた。
[Industrial Field of 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. [Prior Art] Conventionally, for commercial use, this type of treatment equipment 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. The mats are replaced regularly. 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, and the organic matter in the wastewater is removed by the anaerobic filter bed tank. After decomposition by anaerobic bacteria generated on the surface of the filter media, this wastewater is mixed and agitated in a contact aeration tank with air ejected from an aeration pipe.
In addition, the biofilm on the surface of the contact material is brought into sufficient contact with the biofilm to oxidize and remove the nutrient substrate in the wastewater. [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.
Moreover, the oil extracted either alone or by being adsorbed onto pine cannot be disposed of as it is, and there is a problem that it must be incinerated or reprocessed. 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 not only produces an extremely strong odor, but also has 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. 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 produce sludge. 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. [Means for Solving the Problems] In order to achieve the above object, as shown in FIG.
and a treatment tank 10 having an outlet 12 for treated water, an ozone generating element 37, a high frequency high voltage power source 38 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. Ozonizers 34 to 36 consisting of a regulator 39 and ozone generated in the ozonizers 34 to 36 are transferred to the treatment tank 1.
ozone ejection means 21, 22, 23, 42 that ejects ozone into the waste water in the treatment tank 10 together with air; and microorganism maintenance means 26 for maintaining the microorganisms. The characteristic structure is that the microorganism maintaining means 26 is a cylindrical body 4 formed of a conductive wire mesh.
4, a large number of porous ceramic dielectrics 45 accommodated in this cylindrical body 44, an electrode 46 electrically connected to this wire mesh, and a negative potential applied to this electrode 46 to and an ionizer 47 that negatively ionizes the ionizer 45. [Operation] A negative potential is applied to the electrode 46 electrically connected to the wire mesh by the ionizer 47 of the microorganism maintaining means 26, and the ceramic dielectric 4 that has entered the cylindrical body 44 is heated.
When 5 is negatively ionized, positively charged microorganisms 60 such as aerobic bacteria and mold are maintained in the wastewater. In this state, the ozone jetting means 21 to 2
3 and 42, when air containing ozone is ejected into the wastewater, the ozone activates the microorganisms 60, and the ozone's deodorizing and oil-decomposing effects and the various decomposition effects including the oil-degrading action of the microorganisms 60 cause the wastewater to have a bad odor. It is possible to reliably decompose organic substances in wastewater while dissipating water. [Example] Next, an example of the present invention will be described in detail based on the drawings. FIG. 1 shows a first embodiment of the invention. 10 is 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. The treatment 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 (capacity of approximately 1.0 cm).
m 3 ) and is partitioned by two partition walls 13 and 14 into three processing chambers 16, 17 and 18 having approximately the same volume. 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. An inflow pipe 19 is connected to the inflow port 11,
An outflow pipe 20 is connected to the outflow port 12 . The outlet 12 is designed to prevent untreated wastewater from easily flowing out.
It is provided at a lower position than the inlet 11. 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 metals and may be provided outside the processing chamber 16 adjacent to the inlet 11. The processing chamber 17 includes a microorganism maintainer 26 and an oxidation-reduction potential sensor 27 that detects the oxidation-reduction potential of the treated water.
will be placed. 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. 28
a is the lid of the guide tube 28; Nozzles 21-23 are connected to ozonizers 34, 35 and 36 via conduits 31, 32 and 33, respectively. The ozonizers 34 to 36 each have an ozone generating element 37 formed with an electrode on a dielectric material.
, a high frequency high voltage power supply 38 for applying a high frequency AC voltage to these elements 37, and this power supply 38.
It is composed of a regulator 39 that adjusts the voltage or frequency of the ozone to adjust the amount of ozone generated. Each regulator 39
The amount of ozone generated can be adjusted within the ozone concentration range of 0.05ppm to 170ppm. A pump 42 is connected to the ozonizers 34 to 36 via a conduit 41. pump 42, pipe line 41,
The pipes 31 to 33 and the nozzles 21 to 23 constitute ozone ejection means. The power supply 38 and pump 42 of the ozonizers 34 to 36 are connected to switches 34a and 3, respectively.
It is connected to an AC power source 43 via 5a, 36a and 42a. The microorganism maintainer 26 maintains microorganisms such as aerobic bacteria and mold introduced into the treatment tank 10, and includes a cylindrical body 44 formed of a conductive wire mesh,
This cylindrical body 44 is filled with a large number of porous ceramic dielectrics 45, an electrode 46 is electrically connected to the wire mesh, and a negative potential is applied to the electrodes 46 to negatively ionize the ceramic dielectrics 45. An ionizer 47 is provided. The ionizer 47 has a circuit that biases the pulse voltage to a negative potential, and is provided outside the processing tank 10. The ceramic dielectric 45 is in the form of granules, pellets, or blocks 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 set so that these ceramic dielectrics 45 do not come out. Examples of the ceramic dielectric 45 include aluminum oxide, titanium oxide, barium titanate, silicon oxide, magnesium oxide, and composites thereof. The microorganisms 60 introduced into this treatment tank 10 include bacteria that perform starch decomposition, sugar decomposition, fatty acid decomposition, proteolysis, lignin decomposition, nitrification, sulfation, and fibrinolytic actions, respectively.
4 to 80℃ with a predetermined ratio of multiple types selected from the group of actinomycetes, rhizobia, yeast, nitrifying bacteria, and filamentous fungi.
It is a complex bacterium that can function within the temperature range of 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. 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. The detection output of the oxidation-reduction potential sensor 27 is connected to the controller 50, and 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. The operation of the wastewater treatment device having such a configuration will be explained. Open the lid 10a of the treatment tank 10 and place the pre-cultured microorganisms 60 into the treatment tank 1 as shown by the arrow in FIG.
After putting a predetermined amount into 0, switch 34a to 36a
is turned on to start the ozonizers 34 to 36, and then the switch 42a is turned on to drive the pump 42. Air containing about 1 to 2% by volume of ozone is ejected from the nozzles 21 to 23 through the pipes 31 to 33. At the same time, the controller 50 uses the ionizer 47
is activated for a certain period of time by the timer 48, and the electrode 4
A negative potential is applied to 6 to negatively ionize the ceramic dielectric 45 that has entered the cylindrical body 44. As a result, microorganisms such as aerobic bacteria and fungi that are positively charged are attracted to the ceramic dielectric body 45 and maintained. When the ionizer 47 becomes inactive, the microorganisms leave the ceramic dielectric 45 and enter the processing chamber 1.
6 to 18 in water. Although not shown, it is preferable to provide a flow rate sensor in the inflow pipe 19 and to disable the ionizer 47 when the inflow rate increases. When wastewater flows into the treatment tank 10 from the inflow pipe 19, coarse dust is first captured by the screen 24. This screen 24 is periodically cleaned to remove dust. The ozone-containing air ejected from the nozzles 21 to 23 increases the oxidation-reduction potential of the treated water and activates microorganisms.
When the sensor 27 detects that the voltage has reached the 400 mV range, the controller 50 adjusts the voltage of the ozonizers 34 to 36 to the regulator 39 so as not to sterilize microorganisms.
This reduces 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. To maintain the redox potential in the range of 300-400mV,
In this example, the controller 50 controls the ozonizers 34 to 36 so that 100 mg of ozone is generated per hour using 1000 g of water. 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. 3CH 3 (CH 2 ) 4 CH 3 +190 3 →21H 2 O + 18CO 2 Emit a moderate amount of ozone to raise the redox potential to 300~
Microorganisms such as aerobic bacteria and mold grow by controlling the voltage within the 400 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 flows into the treatment tank. 10 continuously for a long time, the ability to decompose oil does not decrease, and the wastewater can be stably purified. The wastewater 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 tube 28 and flows out through the outflow pipe 20. do. Table 1 shows the untreated wastewater collected from the inflow pipe 19 and the outflow pipe 20 when kitchen wastewater with an hourly average inflow of 2.5 m 3 and a maximum hourly inflow of 5.0 m 3 was treated with the device of this embodiment. This is the water quality data of the treated wastewater collected in . Water quality measurement was performed according to JIS-K-0102 method.

【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。 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。 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。 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。 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2
0と同一レベルの開口を有する。3つの処理室1
6〜18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。 この処理槽10の容積は約2.0m3であつて、コ
ントローラ50は水1000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。 このような構成の装置では、前記実施例と同様
に蓋16a〜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60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
により所定量入れた後、図示しないスイツチを入
れてオゾナイザ34及びポンプ42を駆動する。 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。 酸化還元電位センサ27が検出するレドツクス
電位により、前記実施例と同様にコントローラ5
0はオゾナイザ34の調整器39を制御する。 第2表は一日平均の排水流入量が1.25m3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
−K−0102法により行つた。
[Table] Table 1 shows that the apparatus of this example can treat wastewater to a good water quality standard. Note that the above-mentioned wastewater treatment device can be used not only for kitchen wastewater treatment but also for large-scale industrial plants. 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. 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. In this example, the outflow pipe 20 is provided at the same level as the inflow pipe 19, the partition walls 13 and 14 are provided upright at the bottom of the tank, and the inflow pipe 19 and the outflow pipe 2 are provided at the top, respectively.
It has an aperture at the same level as 0. 3 processing chambers 1
A common pipe line 31 is provided for the nozzles 21 to 23 of 6 to 18.
A single ozonizer 34 is connected via. Additionally, a disinfection chamber 15 is located between the processing chamber 18 and the outflow pipe 20.
A disinfection chamber 15 is provided with a disinfection thin tube 31a extending from a conduit 31, 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. The volume of the treatment tank 10 is approximately 2.0 m 3 , and the controller 50 controls the ozonizer 34 to generate 50 mg of ozone per hour using 1000 m of water. In the apparatus having such a configuration, the lids 16a to 18a are opened in the same manner as in the previous embodiment, and microorganisms 60 such as aerobic bacteria and molds that have been cultured in advance are manually introduced into the processing tank 10 as shown by the arrows in FIG. After adding a predetermined amount using the operation or supply device, a switch (not shown) is turned on to drive the ozonizer 34 and the pump 42. 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. Based on the redox potential detected by the oxidation-reduction potential sensor 27, the controller 5
0 controls the regulator 39 of the ozonizer 34. Table 2 shows the water quality data 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 3 was treated with the device of this embodiment. It is. Water quality measurement is JIS
-K-0102 method was used.

【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。 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。 [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
るのでスラツジの発生がなく、処理装置の保守点
検を簡便に行うことができる。 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。
[Table] From Table 2, it was found that the device of this example can treat water to a good water quality standard as a domestic septic tank. 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. [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, organic matter contained in wastewater is mainly decomposed into carbon dioxide and water, so no sludge is generated, and maintenance and inspection of the treatment equipment can be carried out easily. 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、2
1,22,23……ノズル(オゾン噴出手段)、
24……スクリーン、26……微生物維持器(微
生物維持手段)、27……酸化還元電位センサ、
28……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
ミツク誘電体、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... Processing tank, 11... Inlet, 12... Outlet, 13, 14... Partition wall, 16, 17, 18...
...Processing chamber, 19...Inflow pipe, 20...Outflow pipe, 2
1, 22, 23... Nozzle (ozone ejection means),
24... Screen, 26... Microorganism maintenance device (microorganism maintenance means), 27... Redox potential sensor,
28... Guide tube, 34, 35, 36... Ozonizer, 37... Ozone generating element, 38... High frequency high voltage power supply, 39... Regulator, 42... Pump (ozone ejection means), 44... Cylinder shaped 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11と処理水の流出口12を有
する処理槽10と、 オゾン発生素子37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38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39とからなるオゾナイザ34,35,
36と、 前記オゾナイザ34〜36で発生したオゾンを
前記処理槽10内の排水中に空気とともに噴出さ
せるオゾン噴出手段21,22,23,42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60を前記処理槽
10内の排水中で維持する微生物維持手段26と を備えた排水処理装置であつて、 前記微生物維持手段26は、導電性金網により
形成された筒状体44と、この筒状体44に収容
された多数の多孔質のセラミツク誘電体45と、
この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前記セラミツク誘電
体45を負イオン化するアイオナイザ47とを備
えたことを特徴とする排水処理装置。 2 処理槽10に微生物60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11の近傍に粗大塵埃を捕獲す
るスクリーン24が設けられた請求項1記載の排
水処理装置。 4 処理槽10内に処理水の酸化還元電位を検出
するセンサ27が設けられ、オゾナイザ34〜3
6の調整器39は前記センサ27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13,14で処理槽10
を仕切ることにより前記処理槽10に複数の処理
室16,17,18が形成され、オゾン噴出手段
21〜23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13,14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請求項1記載の排水処理装
置。 8 処理水の流出口12が排水の流入口11より
低位置に設けられ、前記流出口12に処理槽底部
の水を導く案内筒28が接続された請求項1記載
の排水処理装置。
[Scope of Claims] 1. A treatment tank 10 having an inlet 11 for wastewater and an outlet 12 for treated water, an ozone generating element 37, a high frequency high voltage power supply 38 that applies a high frequency AC high voltage to this element, and the power supply voltage. Or an ozonizer 34, 35, which is composed of a regulator 39 that adjusts the frequency and adjusts the amount of ozone generated.
36, ozone ejection means 21, 22, 23, 42 for ejecting ozone generated in the ozonizers 34 to 36 together with air into the waste water in the treatment tank 10, and either pre-cultured aerobic bacteria or mold. A wastewater treatment device comprising a microorganism maintaining means 26 that maintains microorganisms 60 containing one or both of them in the waste water in the treatment tank 10, the microorganism maintaining means 26 having a cylindrical shape formed of a conductive wire mesh. body 44, a large number of porous ceramic dielectric bodies 45 housed in this cylindrical body 44,
A wastewater treatment device characterized by comprising an electrode 46 electrically connected to the wire mesh, and an ionizer 47 that applies a negative potential to the electrode 46 to negatively ionize the ceramic dielectric 45. 2. The wastewater treatment apparatus according to claim 1, further comprising a microorganism supply means for supplying the microorganisms 60 to the treatment tank 10. 3. The wastewater treatment device according to claim 1, further comprising a screen 24 for capturing coarse dust near the inlet 11 of the wastewater. 4 A sensor 27 is provided in the treatment tank 10 to detect the oxidation-reduction potential of the treated water, and the ozonizers 34 to 3
2. The wastewater treatment apparatus according to claim 1, wherein the regulator 39 of No. 6 is adjusted by the detection signal of the sensor 27. 5 Processing tank 10 with one or more partition walls 13, 14
2. The wastewater treatment apparatus according to claim 1, wherein a plurality of treatment chambers 16, 17, and 18 are formed in the treatment tank 10 by partitioning the treatment chambers, and ozone jetting means 21 to 23 are provided in each treatment chamber. 6. The wastewater treatment apparatus according to claim 5, wherein the partition walls 13 and 14 are provided at a predetermined height apart from the bottom of the tank. 7 Microorganism 60 has starch decomposition action, sugar decomposition action,
Bacteria, actinomycetes, rhizobia, and yeast bacteria that perform fatty acid decomposition, proteolysis, lignin decomposition, nitrification, sulfation, and fibrinolysis, respectively.
2. The wastewater treatment device according to claim 1, which is a composite bacterium that 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. 8. The wastewater treatment apparatus according to claim 1, wherein the treated water outlet 12 is provided at a lower position than the wastewater inlet 11, and a guide tube 28 for guiding water from the bottom of the treatment tank is connected to the outlet 12.
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 JPH03146193A (en) 1991-06-21
JPH0585236B2 true 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)

Families Citing this family (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
JP4907103B2 (en) * 2005-05-12 2012-03-28 高砂熱学工業株式会社 Sludge treatment method for biological treatment tank
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
JP5325461B2 (en) * 2008-05-28 2013-10-23 株式会社デリカシェフ Solid food organic waste treatment 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

Also Published As

Publication number Publication date
JPH03146193A (en) 1991-06-21

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