JP2009183834A - Waste water treatment apparatus - Google Patents

Waste water treatment apparatus Download PDF

Info

Publication number
JP2009183834A
JP2009183834A JP2008025283A JP2008025283A JP2009183834A JP 2009183834 A JP2009183834 A JP 2009183834A JP 2008025283 A JP2008025283 A JP 2008025283A JP 2008025283 A JP2008025283 A JP 2008025283A JP 2009183834 A JP2009183834 A JP 2009183834A
Authority
JP
Japan
Prior art keywords
waste water
aeration tank
wastewater
drainage
circulation pump
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
JP2008025283A
Other languages
Japanese (ja)
Other versions
JP4951727B2 (en
Inventor
Isao Akiyama
勲 秋山
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.)
ECO SYSTEM KK
Tsukishima Foods Industry Co Ltd
Original Assignee
ECO SYSTEM KK
Tsukishima Foods Industry Co Ltd
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 ECO SYSTEM KK, Tsukishima Foods Industry Co Ltd filed Critical ECO SYSTEM KK
Priority to JP2008025283A priority Critical patent/JP4951727B2/en
Publication of JP2009183834A publication Critical patent/JP2009183834A/en
Application granted granted Critical
Publication of JP4951727B2 publication Critical patent/JP4951727B2/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

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

  • Activated Sludge Processes (AREA)
  • Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
  • Physical Water Treatments (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To attain improvement in treatment efficiency by an aeration tank as well as improvement in floating-up separation efficiency of fats and oils without using a chemical. <P>SOLUTION: The waste water treatment apparatus includes: a grist lap 3 where fats and oils in the primary waste water exhausted from a factory, a cookroom or the like are stuck to bubbles, so as to be floated up; and an aeration tank 5 where the secondary waste water from the grist lap 3 is treated with bacteria, wherein the waste water in the grist lap 3 is pumped up by a circulation pump 7, and is fed to a pressure regulation device 41 together with the air taken from the inside of the atmosphere. The waste water together with the air fed by the circulation pump 7 is collided against a waste water collision part 63 under pressure conditions in the pressure regulation device 41, so as to form numberless small bubbles, and, regarding the small bubbles and the waste water including a large quantity of oxygen, from an outflow port 45, either is discharged to the grist lap 3, and the other is discharged to the aeration tank 5, respectively. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は油脂分を多く含む排水に適する排水処理装置に関する。   The present invention relates to a wastewater treatment apparatus suitable for wastewater containing a large amount of oil and fat.

従来、工場や厨房等からでる油脂分を多く含む排水にあっては、独特の悪臭を発生したり、下水を詰まらせたり、害虫の温床となり易い等の問題をかかえるところから、排水処理にあたってグリストラップによって油脂分を処理することが義務づけられている。   Conventionally, wastewater containing a large amount of oils and fats from factories and kitchens has problems such as generating a unique odor, clogging sewage, and becoming a hotbed of pests. It is obliged to treat fats and oils by the strap.

グリストラップは、排水中から油脂分を分離させる手段となっており、この分離手段はグリストラップ中に、例えば薬剤を投入することで排水中の気泡に油脂分を付着させ浮上分離させるようになっている。   The grease trap is a means for separating oil and fat from the wastewater, and this separation means attaches the oil and fat to the bubbles in the wastewater and floats and separates them, for example, by introducing a chemical into the greasetrap. ing.

油脂分の浮上分離は、気泡との関係に大きく左右される。特に気泡の径が大きいと油脂分との付着効率が悪く、小さくなるほど付着効率が向上することが実験でも裏付けられている。   The floating separation of fat and oil greatly depends on the relationship with bubbles. In particular, experiments have confirmed that the adhesion efficiency with oils and fats is poor when the bubble diameter is large, and the adhesion efficiency improves as the bubble diameter decreases.

気泡は一般にはポンプによって排水中へ空気を送り込むことで作られるようになるが、気泡の径は大きく薬剤を用いても分離効率が悪くなっているのが現状となっている。しかも、コストがかかる等の問題をかかえる。   Bubbles are generally created by sending air into the waste water by a pump, but the current situation is that the bubble diameter is large and the separation efficiency is poor even when a chemical is used. In addition, there are problems such as high costs.

そこで、本発明にあっては薬剤を使用することなく油脂分の浮上分離効率の向上と併せて曝気槽による処理効率の向上が図れる排水処理装置を提供することを目的とする。   Therefore, an object of the present invention is to provide a wastewater treatment apparatus capable of improving the treatment efficiency of an aeration tank in combination with the improvement of the floating separation efficiency of oil and fat without using chemicals.

前記目的を達成するために、本発明にあっては、工場、厨房等から排水される一次排水中の油脂分を気泡に付着させて浮上させるグリストラップと、そのグリストラップからの二次排水をバクテリアによって処理する曝気槽と、前記グリストラップから排水を汲上げ、汲上げた排水と大気中から取入れた空気と一緒に圧力調整装置内へ送り込む循環ポンプとを備え、前記圧力調整装置は、前記循環ポンプによって排水が送り込まれる流入口と、付勢ばねのばね圧で前記流入口の弁座と接触し合う弁体と、前記循環ポンプによって流入口から送り込まれる空気と一緒の排水を衝突させる排水衝突部と、その排水衝突部に衝突させた排水を前記グリストラップ及び曝気槽内へそれぞれ吐出する流出口とを有していることを特徴とする。   In order to achieve the above object, in the present invention, a grease trap that floats by attaching oil and fat in the primary wastewater drained from a factory, kitchen, etc. to the bubbles, and secondary drainage from the grease strap. An aeration tank to be treated with bacteria, and a circulation pump for pumping waste water from the grease trap and feeding the pumped waste water and air taken in from the atmosphere into the pressure regulator, Drainage that collides with the inlet with which the wastewater is sent by the circulation pump, the valve body that contacts the valve seat of the inlet with the spring pressure of the urging spring, and the wastewater with the air that is sent from the inlet by the circulation pump It has a collision part and the outflow port which discharges the waste_water | drain collided with the drainage collision part into the said grease trap and an aeration tank, respectively.

本発明によれば、循環ポンプによって送り込まれる空気と一緒の排水は圧力調整装置の流入口において設定された圧力に高められ大きい運動エネルギーが与えられた状態で排水衝突部と勢いよく衝突し合うことで無数の小さい気泡を作ることができる。   According to the present invention, the drainage together with the air fed by the circulation pump is increased to the pressure set at the inlet of the pressure regulator, and collides with the drainage collision part vigorously in a state where a large kinetic energy is given. Innumerable small bubbles can be made.

無数の小さい気泡を含む排水の一方は、流出口からグリストラップへ、他方は曝気槽へそれぞれ吐出させることができる。   One of the wastewater containing countless small bubbles can be discharged from the outlet to the grease trap and the other to the aeration tank.

この結果、グリストラップにあっては薬剤を用いなくても無数の小さい気泡によって油脂分との付着率がよくなり、油脂分の分離浮上を大幅に向上させることができる。   As a result, in the grease trap, the adhesion ratio with the oil and fat is improved by countless small bubbles without using a chemical, and the separation and floating of the oil and fat can be greatly improved.

一方、曝気槽にあっては酸素を多く含む排水が送り込まれることでバクテリアによる分解が促進され分解処理の向上を図ることができる。   On the other hand, in the aeration tank, wastewater containing a large amount of oxygen is sent in, so that degradation by bacteria is promoted and degradation can be improved.

バクテリアによる分解処理の向上は、実験データで裏付けされたもので、理論的には解明されていないが、1つには小さな気泡となって多量に送り込まれる酸素によってバクテリアがより活性化されるためではないかと考えられることと、また、排水が排水衝突部と衝突する時に排水中の汚水成分も勢いよく衝突することでバクテリアによってとり込まれ分解処理がしやすい状態まで粉砕されるためではないかと考えられている。   The improvement of the degradation process by bacteria is supported by experimental data and is not theoretically elucidated, but one is that bacteria are more activated by oxygen that is sent in large quantities as small bubbles. It is thought that this may be because the wastewater component in the wastewater collides with the drainage collision part, so that it is crushed to a state where it is taken up by bacteria and easily decomposed. It is considered.

以下、図1乃至図6の図面を参照しながら本発明の実施形態について具体的に説明する。   Hereinafter, embodiments of the present invention will be specifically described with reference to FIGS. 1 to 6.

図1は本発明にかかる排水処理装置を示した全体の概要説明図を示している。   FIG. 1 is an overall explanatory view showing a waste water treatment apparatus according to the present invention.

排水処理装置1は、グリストラップ3と曝気槽5と循環ポンプ7とを備えている。   The waste water treatment apparatus 1 includes a grease trap 3, an aeration tank 5, and a circulation pump 7.

グリストラップ3は、工場、あるいは、厨房等から排出される油脂分を多く含む排水中から油脂分を取除くところで、例えば、工場にあっては一時的に貯留される原水槽から処理量に見合った量だけ排水管9によって排水が送り込まれる。グリストラップ3は浮上分離した油脂分を取除く油脂分取除き装置11と、浮上した油脂分を仕切る油脂分仕切壁12によって仕切られた排水取出し仕切室14がそれぞれ設けられ、排水取出し仕切室14は油脂分仕切壁12の下方の連通口を介して槽内と連通している。   The grease strap 3 is a place where oil or fat is removed from wastewater containing a large amount of oil or fat discharged from a factory or kitchen, for example, in a factory, it is commensurate with the amount of treatment from a raw water tank that is temporarily stored. Drainage is sent by the drain pipe 9 by a certain amount. The grease strap 3 is provided with a fat / oil removing device 11 that removes the oil / fat that has been floated and separated, and a drainage extraction compartment 14 that is partitioned by an oil / fat partition wall 12 that partitions the floated fat / oil. Is communicated with the inside of the tank through a communication port below the oil partition wall 12.

油脂分取除き装置11は気泡と付着して浮上分離した泡状の油脂分がオーバーフローによって集まる集合室13に、例えば、回転する掻集め羽根15が設けられ、掻集め羽根15による回転によって掻き集められた泡状の油脂分を排出路17より外へ排出する構造となっている。   For example, a rotating scraping blade 15 is provided in a gathering chamber 13 where the foamed fat and oil components adhering to air bubbles and separated by floating are collected by overflow, and the fat collecting device 11 is scraped and collected by the rotation of the collecting blade 15. The structure is configured to discharge the foamy oil and fat from the discharge path 17.

なお、排水路17によって一箇所に集められた油脂分はバキュームカーで吸収された後、産業廃棄物処理場へ運ばれ処理される。   The fats and oils collected in one place by the drainage channel 17 are absorbed by a vacuum car and then transported to an industrial waste disposal site for processing.

曝気槽5は、前記グリストラップ3の排水取出し仕切室14と配水管16を介して連通し、グリストラップ3によって一次処理された排水中の汚水成分をバクテリアによって分解処理するところで、曝気槽5内へ空気を送り込む空気供給ポンプ19とバクテリアによって分解処理された処理水を外へ排水する排水管20とを有している。   The aeration tank 5 communicates with the drainage discharge compartment 14 of the grease strap 3 via the water distribution pipe 16, and decomposes the sewage components in the waste water primarily treated by the grease strap 3 with bacteria. An air supply pump 19 for feeding air to the water and a drain pipe 20 for draining treated water decomposed by bacteria to the outside.

空気供給ポンプ19は前記した如く曝気槽5内へ空気を送り込む外に、噴射口19aからの噴射圧によって槽内の排水を循環させる作用を有する。   In addition to sending air into the aeration tank 5 as described above, the air supply pump 19 has a function of circulating waste water in the tank by the injection pressure from the injection port 19a.

循環ポンプ7は、図5に示す如く有段階に調整するつまみ24aが設けられたマニアルインバータ24を備え、入口21と出口23を有するケーシング25内には回転羽根27が設けられている。回転羽根27は、回転によって入口21から取入れた排水を出口23から強制的に吐出させる作用を有し、ロータシャフト35に一体に固着している。ロータシャフト35は、電動部を構成するモータフレーム29に固定支持されたステータ31とステータ31に電流が流れることで回転するロータ33に設けられ、ロータ33によって回転動力が与えられる。   As shown in FIG. 5, the circulation pump 7 includes a manual inverter 24 provided with a knob 24 a that is adjusted stepwise, and a rotating blade 27 is provided in a casing 25 having an inlet 21 and an outlet 23. The rotary vane 27 has a function of forcibly discharging the waste water taken in from the inlet 21 by the rotation from the outlet 23, and is fixed integrally to the rotor shaft 35. The rotor shaft 35 is provided on a stator 31 that is fixedly supported by a motor frame 29 that constitutes an electric part, and a rotor 33 that rotates when a current flows through the stator 31, and rotational power is given by the rotor 33.

循環ポンプ7の入口21には、前記グリストラップ3の排水取出し仕切室14の底に近い位置から排水を取入れるための吸込管37と大気中から空気を取入れる空気取入口39がそれぞれ設けられている。   The inlet 21 of the circulation pump 7 is provided with a suction pipe 37 for taking in drainage from a position near the bottom of the drainage partitioning compartment 14 of the grease strap 3 and an air inlet 39 for taking in air from the atmosphere. ing.

空気取入口39は前記入口21に近い吸込管37からパイプを立上げることで形成され、回転羽根27の回転時に入口21へ向かう吸込圧が働くことでコストをかけることなく大気中から容易に空気の取込みが可能となっている。この場合、空気取入口39は循環ポンプ7の出口23側に設けることも可能である。なお、この実施形態の場合には出口23側に吐出圧が働くためポンプを用いて強制的に送り込む必要がある。   The air intake 39 is formed by raising a pipe from the suction pipe 37 close to the inlet 21, and the suction pressure toward the inlet 21 acts when the rotary blade 27 rotates, so that air can be easily introduced from the atmosphere without cost. Can be taken in. In this case, the air intake 39 can be provided on the outlet 23 side of the circulation pump 7. In the case of this embodiment, since the discharge pressure acts on the outlet 23 side, it is necessary to forcibly feed using a pump.

一方、循環ポンプ7の出口23は図2に示す如く圧力調整装置41の流入口43と接続している。   On the other hand, the outlet 23 of the circulation pump 7 is connected to the inlet 43 of the pressure regulator 41 as shown in FIG.

圧力調整装置41は、本体ケース41a内に流入口43と流出口45と弁体47とを有し、流出口45は流入口43を通る中心軸線Xと直交する方向に設けられている。   The pressure adjusting device 41 includes an inflow port 43, an outflow port 45, and a valve body 47 in the main body case 41 a, and the outflow port 45 is provided in a direction orthogonal to the central axis X passing through the inflow port 43.

流出口45は、途中から分岐される流出管が接続され図1に示す如く分岐されたその内の一方は第1の配管49を介して前記グリストラップ3と、他方は第2の配管51を介して曝気槽5とそれぞれ連通している。第1の配管49は循環ポンプ7の吸込管37を介してグリストラップ3中の排水の一部が循環する循環用となっている。   The outlet 45 is connected to an outlet pipe branched from the middle, and one of the outlets branched as shown in FIG. 1 is connected to the grease strap 3 via the first pipe 49, and the other is connected to the second pipe 51. Via the aeration tank 5. The first pipe 49 is for circulation in which a part of the drainage in the grease trap 3 circulates through the suction pipe 37 of the circulation pump 7.

弁体47は図2、図3に示す如く、付勢ばね53のばね圧によって流入口43の弁座43aと接触している。付勢ばね53のばね圧V1と流入口43の圧力VとはV1=Vの関係となっていて、流入口43の圧力Vは付勢ばね53のばね圧V1によって決定され、流入口43の圧力は循環ポンプ7の出口23に設けられた圧力計55によって制御管理される。   As shown in FIGS. 2 and 3, the valve body 47 is in contact with the valve seat 43 a of the inlet 43 by the spring pressure of the biasing spring 53. The spring pressure V1 of the urging spring 53 and the pressure V of the inflow port 43 have a relationship of V1 = V. The pressure V of the inflow port 43 is determined by the spring pressure V1 of the urging spring 53, and The pressure is controlled and managed by a pressure gauge 55 provided at the outlet 23 of the circulation pump 7.

付勢ばね53は、一方は弁体47の主体筒57に、他方はばね支持体59によってそれぞれ支持され、ばね支持体59は調整ねじ61によって押圧されている。   One of the urging springs 53 is supported by the main cylinder 57 of the valve body 47, and the other is supported by a spring support body 59, and the spring support body 59 is pressed by an adjustment screw 61.

調整ねじ61は圧力調整装置41の本体ケース41aにねじ部61aが螺合し、その先端はばね支持体59と接触している。調整ねじ61の操作部61bは外にあって、その操作部61bを例えば、右に回転させることで前進し付勢ばね53のばね圧を強くすることが可能となる。   The adjusting screw 61 has a threaded portion 61 a screwed into the main body case 41 a of the pressure adjusting device 41, and its tip is in contact with the spring support 59. The operating portion 61b of the adjusting screw 61 is outside, and the operating portion 61b can be moved forward, for example, by rotating it to the right to increase the spring pressure of the biasing spring 53.

また、左に回転させることで後退し付勢ばね53のばね圧を弱めることが可能となり、流入口43からの圧力との関係で、弁体47は弁座43aに対して前進あるいは後退が可能となる。   Further, by rotating to the left, it is possible to move backward and weaken the spring pressure of the biasing spring 53, and the valve body 47 can move forward or backward relative to the valve seat 43a in relation to the pressure from the inlet 43. It becomes.

一方、弁体47と主体筒57の間で、流出口45の上流側には排水衝突部63が設けられている。排水衝突部63は円板状に形成され、弁体47を介して流入口43から吐出される排水が排水衝突部63と衝突した後、流出口45へ向かう流れが確保される構造となっている。   On the other hand, a drainage collision part 63 is provided between the valve body 47 and the main cylinder 57 on the upstream side of the outlet 45. The drainage collision part 63 is formed in a disk shape, and the drainage discharged from the inlet 43 through the valve body 47 collides with the drainage collision part 63, and then the flow toward the outlet 45 is secured. Yes.

この場合、弁体47には図2に示す如く弁体47の外周面に中心軸線Xに沿う複数の通路溝65を設け、弁体47の外周と通路溝65を通過する排水がそれぞれ排水衝突部63と衝突し合う組合せ流れを作る手段とすることが望ましい。   In this case, the valve body 47 is provided with a plurality of passage grooves 65 along the central axis X on the outer peripheral surface of the valve body 47 as shown in FIG. It is desirable to use a means for creating a combined flow that collides with the portion 63.

また、本体ケース41aはねじ部64を緩めることで弁体47及び付勢ばね53等の組付けやメンテナンス管理が容易に行えるようにすることが望ましい。   Further, it is desirable that the main body case 41a can be easily assembled and maintained by the valve body 47 and the urging spring 53 by loosening the screw portion 64.

このように構成された排水処理装置1によれば、循環ポンプ7によって送り込まれる空気と一緒の排水は圧力調整装置41の流入口43において大きい運動エネルギーが与えられた状態で排水衝突部63と勢いよく衝突し合うことで無数の小さい気泡が作られる。   According to the waste water treatment apparatus 1 configured as described above, the waste water together with the air fed by the circulation pump 7 is vigorous with the waste water collision part 63 in a state where a large kinetic energy is given at the inlet 43 of the pressure regulator 41. Countless small bubbles are made by colliding well.

無数の小さい気泡を含む排水の一方は、流出口45からグリストラップ3へ、他方は流出口45から曝気槽5へ向けてそれぞれ吐出される。この時、グリストラップ3にあっては吸込管37→循環ポンプ7→第1の配管49を介して排水の一部は循環する。   One of the wastewater containing innumerable small bubbles is discharged from the outlet 45 to the grease strap 3, and the other is discharged from the outlet 45 to the aeration tank 5, respectively. At this time, in the grease strap 3, a part of the drainage circulates through the suction pipe 37 → the circulation pump 7 → the first pipe 49.

この結果、グリストラップ3にあっては薬剤を用いなくても無数の小さい気泡によって油脂分の付着率がよくなり油脂分の分離浮上が大幅に向上するようになる。   As a result, in the grease strap 3, the adhesion rate of fats and oils is improved by innumerable small bubbles without using chemicals, and separation and floating of the fats and oils are greatly improved.

一方、曝気槽5にあっては酸素を多く含む排水が送り込まれることで活性化されたバクテリアによる分解処理が促進される。   On the other hand, in the aeration tank 5, the decomposition process by the activated bacteria is accelerated | stimulated by the waste_water | drain containing much oxygen being sent.

図6はその実験結果を示したもので、SS(汚水):A、BOD(酸素供給量):B、N−HEX(油):Cを調べたものである。各A:B:Cの法定基準値はA:600、B:600、C:30(mg/l)となっている。それに対してAの原水(460mg/l)、Bの原水(940mg/l)、Cの原水(140mg/l)を流したところ、放水値はA:44mg/l、B:15mg/l、C:0mg/lとなり、大幅に改善された成績結果が得られた。   FIG. 6 shows the experimental results, in which SS (sewage): A, BOD (oxygen supply amount): B, and N-HEX (oil): C were examined. The legal reference values for each A: B: C are A: 600, B: 600, and C: 30 (mg / l). On the other hand, when the raw water of A (460 mg / l), the raw water of B (940 mg / l) and the raw water of C (140 mg / l) were passed, the water discharge values were A: 44 mg / l, B: 15 mg / l, C : 0 mg / l, and the results were greatly improved.

これは、理論的には解明されていないが小さい気泡による多量の酸素によってバクテリアが活性化されることと、排水中の汚水成分が衝突時にバクテリアによって分解されやすい状態に粉砕されるためではないかと考えられる。   Although this is not theoretically clarified, it is because bacteria are activated by a large amount of oxygen due to small bubbles and that sewage components in the waste water are crushed into a state that is easily decomposed by bacteria at the time of collision. Conceivable.

本発明にかかる排水処理装置全体の概要説明図。BRIEF DESCRIPTION OF THE DRAWINGS Outline explanatory drawing of the whole waste water treatment equipment concerning the present invention. 圧力調整装置を拡大した概要断面図。An outline sectional view which expanded a pressure regulation device. 圧力調整装置の弁体及び排水衝突部を示した概要斜視図。The schematic perspective view which showed the valve body and drainage collision part of the pressure regulator. 循環ポンプと圧力調整装置の配置関係を示した概要拡大説明図。The outline expansion explanatory view showing the arrangement relation of a circulation pump and a pressure regulation device. 循環ポンプの断面を示した概要説明図。The schematic explanatory drawing which showed the cross section of the circulation pump. SS、BOD、N−HEXの実験結果を示す説明図。Explanatory drawing which shows the experimental result of SS, BOD, and N-HEX.

符号の説明Explanation of symbols

3…グリストラップ
5…曝気槽
7…循環ポンプ
21…入口
23…出口
41…圧力調整装置
43…流入口
45…流出口
47…弁体
53…付勢ばね
63…排水衝突部
DESCRIPTION OF SYMBOLS 3 ... Grease strap 5 ... Aeration tank 7 ... Circulation pump 21 ... Inlet 23 ... Outlet 41 ... Pressure regulator 43 ... Inlet 45 ... Outlet 47 ... Valve body 53 ... Energizing spring 63 ... Drainage collision part

Claims (1)

工場、厨房等から排水される一次排水中の油脂分を気泡に付着させて浮上させるグリストラップと、そのグリストラップからの二次排水をバクテリアによって処理する曝気槽と、前記グリストラップから排水を汲上げ、汲上げた排水と大気中から取入れた空気と一緒に圧力調整装置内へ送り込む循環ポンプとを備え、前記圧力調整装置は、前記循環ポンプによって排水が送り込まれる流入口と、付勢ばねのばね圧で前記流入口の弁座と接触し合う弁体と、前記循環ポンプによって流入口から送り込まれる空気と一緒の排水を衝突させる排水衝突部と、その排水衝突部に衝突させた排水を前記グリストラップ及び曝気槽内へそれぞれ吐出する流出口とを有していることを特徴とする排水処理装置。   A grease trap that floats the oil and fat in the primary wastewater drained from the factory, kitchen, etc. by adhering to the bubbles, an aeration tank that treats the secondary wastewater from the grease strap with bacteria, and pumps wastewater from the grease strap. A circulating pump that feeds the drained water pumped up and pumped into the pressure adjusting device together with air taken in from the atmosphere, and the pressure adjusting device includes an inlet port through which the waste water is fed by the circulating pump, and a biasing spring. The valve body that contacts the valve seat of the inlet by spring pressure, the drainage collision part that collides with the wastewater together with the air fed from the inlet by the circulation pump, and the drainage that collides with the drainage collision part A wastewater treatment apparatus having an grease outlet and an outlet for discharging into the aeration tank.
JP2008025283A 2008-02-05 2008-02-05 Wastewater treatment equipment Expired - Fee Related JP4951727B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2008025283A JP4951727B2 (en) 2008-02-05 2008-02-05 Wastewater treatment equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2008025283A JP4951727B2 (en) 2008-02-05 2008-02-05 Wastewater treatment equipment

Publications (2)

Publication Number Publication Date
JP2009183834A true JP2009183834A (en) 2009-08-20
JP4951727B2 JP4951727B2 (en) 2012-06-13

Family

ID=41067666

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2008025283A Expired - Fee Related JP4951727B2 (en) 2008-02-05 2008-02-05 Wastewater treatment equipment

Country Status (1)

Country Link
JP (1) JP4951727B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104787827A (en) * 2015-03-24 2015-07-22 徐州工程学院 1,1-dichloroethylene separation system and separation process thereof
CN104944514A (en) * 2015-06-12 2015-09-30 徐州工程学院 Separation device for trichloromethane in underground water and application of separation device

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07290042A (en) * 1994-04-29 1995-11-07 Idec Izumi Corp Waste water treating device
JPH10180065A (en) * 1996-12-26 1998-07-07 Jiinasu:Kk Atomizing method and device therefor
JP2004016885A (en) * 2002-06-14 2004-01-22 Hitachi Industries Co Ltd Method and apparatus for separating oil and water
JP2005199252A (en) * 2004-01-13 2005-07-28 Chuya Ishibashi Method for producing and operating functionalized water flow
JP2006289313A (en) * 2005-04-14 2006-10-26 Matsushita Electric Ind Co Ltd Apparatus and method for treating organic waste water

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07290042A (en) * 1994-04-29 1995-11-07 Idec Izumi Corp Waste water treating device
JPH10180065A (en) * 1996-12-26 1998-07-07 Jiinasu:Kk Atomizing method and device therefor
JP2004016885A (en) * 2002-06-14 2004-01-22 Hitachi Industries Co Ltd Method and apparatus for separating oil and water
JP2005199252A (en) * 2004-01-13 2005-07-28 Chuya Ishibashi Method for producing and operating functionalized water flow
JP2006289313A (en) * 2005-04-14 2006-10-26 Matsushita Electric Ind Co Ltd Apparatus and method for treating organic waste water

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104787827A (en) * 2015-03-24 2015-07-22 徐州工程学院 1,1-dichloroethylene separation system and separation process thereof
CN104944514A (en) * 2015-06-12 2015-09-30 徐州工程学院 Separation device for trichloromethane in underground water and application of separation device

Also Published As

Publication number Publication date
JP4951727B2 (en) 2012-06-13

Similar Documents

Publication Publication Date Title
JP5469594B2 (en) Method and device for purifying liquid effluent
US5484534A (en) Energy conserving method of water treatment
RU2585635C1 (en) Method for disinfection and cleaning of fluids and process line therefor
JP4951727B2 (en) Wastewater treatment equipment
JP5250758B2 (en) Miscellaneous wastewater treatment equipment, miscellaneous wastewater treatment system and miscellaneous wastewater treatment method using a cavitation effect.
JP2006320886A (en) Micron bubble generator
AU2017388564C1 (en) Systems and methods for removing volatile compounds from water-storage tanks
JP2022510098A (en) Electrochemical wastewater treatment system capable of controlling the concentration of selected compounds in the reactor
KR101065720B1 (en) An apparatus for treating food waste from a sink
CN111137960B (en) Air-float separation method and device for solid-liquid separation in waste emulsion
JP6159495B2 (en) Floating separator
RU75186U1 (en) DEVICE FOR DEEP BIOLOGICAL WASTE TREATMENT
JP3961649B2 (en) Deaerator
CN107459104B (en) Oil-water separator
KR20040006690A (en) Apparatus for removing foam in aeration tank
JP6587559B2 (en) Deodorizing device
AU2005200936A1 (en) The treatment of waste water
KR102096827B1 (en) Freshwater lake water quality improvement device
JP2004216286A (en) Method and apparatus for microbial decomposition treatment of sewage oil component in sewage tank of grease trap
KR20150055247A (en) Apparatus and system for treating sewage
CN217808831U (en) A high-efficient air supporting device for sewage treatment
KR200275551Y1 (en) Wastewater disposal plant
JP2005230706A (en) Biological grease trap
RU2701023C1 (en) Oil-containing wastewater treatment plant
RU79547U1 (en) FLOTATION WATER TREATMENT DEVICE

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20110202

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20110824

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20110906

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20111031

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20111122

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A711

Effective date: 20111222

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20111222

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20111222

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20120227

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20150323

Year of fee payment: 3

LAPS Cancellation because of no payment of annual fees