JP2000308899A - Waste water purification device - Google Patents
Waste water purification deviceInfo
- Publication number
- JP2000308899A JP2000308899A JP11120014A JP12001499A JP2000308899A JP 2000308899 A JP2000308899 A JP 2000308899A JP 11120014 A JP11120014 A JP 11120014A JP 12001499 A JP12001499 A JP 12001499A JP 2000308899 A JP2000308899 A JP 2000308899A
- Authority
- JP
- Japan
- Prior art keywords
- wastewater
- treatment tank
- decomposition treatment
- interceptor
- waste water
- 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
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、阻集器内の油脂含
有廃水を微生物で分解浄化する廃水浄化装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a wastewater purifying apparatus for decomposing and purifying oil / fat-containing wastewater in an interceptor with microorganisms.
【0002】[0002]
【従来の技術】この種の廃水浄化装置としては、阻集器
内に油脂分離微生物を着生させる微生物担体及びばっき
用空気の供給具を備えたもの(特開平4−179745
号公報)、ストレーナを備えた廃水受入室と、微生物着
床部材及びばっき用空気の供給具を有する油脂分解室と
を備えた定置式のもの(特開平8−229583号公
報)等があり、いずれも定置式で廃水箇所毎に設置して
おく必要がある構造となっている。2. Description of the Related Art This type of wastewater purifying apparatus is provided with a microbial carrier for accumulating microorganisms for separating fats and oils and an air supply device in a collector (Japanese Patent Laid-Open No. 4-179745).
Japanese Patent Application Laid-Open No. Hei 8-229583), and a stationary type equipped with a wastewater receiving chamber equipped with a strainer, and an oil / fat decomposition chamber having a microorganism-implantation member and a supply device for air for blasting. , All of which are stationary and must be installed at each wastewater point.
【0003】[0003]
【発明が解決しようとする課題】前記従来技術は定置式
であるために、定置場所を必要とし、コストが高くな
り、汎用利用ができなくなっている。これは、従来技術
で使用されている微生物の処理能力に原因するものであ
り、従来の微生物は、高濃度の油脂を含む廃水、あるい
は油脂そのものを迅速に処理することが困難であり、そ
のため、阻集器内で又は定置油脂分離室で長時間をかけ
て分解処理する必要があった。Since the above-mentioned prior art is of a stationary type, it requires a stationary place, the cost is high, and general use is impossible. This is due to the processing ability of the microorganisms used in the prior art, and it is difficult for the conventional microorganisms to quickly treat wastewater containing a high concentration of fats and oils, or fats and oils themselves, It was necessary to take a long time to decompose in the interceptor or in the stationary oil / fat separation chamber.
【0004】しかしながら、その後、特許第27870
15号に開示されているように、ブルクホルデリア(B
urkholderia)属に属し、かつ高温で、好気
的に樹脂を資化するブルクホルデリア・セパシア(Bu
rkholderia cepadia)が研究開発さ
れ、高濃度の油脂でも迅速に処理ができるようになって
いる。本発明は、このような従来技術に鑑み、定置場所
を必要とせず、安価でかつ汎用利用ができる廃水浄化装
置を提供することを目的とする。[0004] However, after that, Patent No. 27870
No. 15, as disclosed in Burgholderia (B
burkholderia cepacia (Bu) belonging to the genus urkholderia and aerobically assimilating the resin at high temperatures
Rkholderia cepadia) has been researched and developed so that even high-concentration fats and oils can be treated quickly. An object of the present invention is to provide an inexpensive and general-purpose wastewater purifying apparatus that does not require a fixed place in view of such conventional technology.
【0005】本発明は、機体を設置位置変更可能にし、
この機体に分解処理槽を支持し、かつ廃水吸引機構、微
生物供給機構、ばっき機構、加熱機構及び処理水戻し機
構等を設けて、1箇所だけでなく、別位置にある阻集器
の油脂含有廃水も1台の装置で分解浄化することができ
るようにした廃水浄化装置を提供することを目的とす
る。The present invention makes it possible to change the installation position of an airframe,
This machine supports a decomposition treatment tank, and is equipped with a wastewater suction mechanism, a microorganism supply mechanism, a plating mechanism, a heating mechanism, a treated water return mechanism, and the like. It is an object of the present invention to provide a wastewater purifying apparatus capable of decomposing and purifying wastewater with one device.
【0006】[0006]
【課題を解決するための手段】本発明における課題解決
のための第1の具体的手段は、設置位置変更可能な機体
2に支持された分解処理槽3と、阻集器4内の廃水を廃
水搬送部材5を介して吸引して分解処理槽3に送る廃水
吸引機構6と、分解処理槽3内に好気性の油脂分解微生
物を供給する微生物供給機構7と、分解処理槽3内の微
生物に空気を供給するばっき機構8と、分解処理槽3内
を加熱する加熱機構9と、分解処理槽3から処理後の廃
水を処理水搬送部材10を介して阻集器4に戻す処理水
戻し機構11とを有することである。The first concrete means for solving the problems in the present invention is to dispose wastewater in a decomposition treatment tank 3 supported on a body 2 whose installation position can be changed and wastewater in an interceptor 4 as wastewater. A wastewater suction mechanism 6 for sucking and sending the wastewater to the decomposition treatment tank 3 via the transport member 5, a microorganism supply mechanism 7 for supplying aerobic oil-decomposing microorganisms into the decomposition treatment tank 3, and a microorganism in the decomposition treatment tank 3. An air supply mechanism 8 for supplying air, a heating mechanism 9 for heating the inside of the decomposition treatment tank 3, and a treated water return mechanism for returning treated wastewater from the decomposition treatment tank 3 to the interceptor 4 via the treatment water transport member 10. 11 is provided.
【0007】これによって、定置場所を必要とせず、1
箇所だけでなく、別位置にある阻集器4の油脂含有廃水
も1台の装置で分解浄化することができる。本発明にお
ける課題解決のための第2の具体的手段は、第1の具体
的手段に加えて、前記機体2の下部に車輪13を設けて
移動可能にし、前記廃水吸引機構6の廃水搬送部材5及
び処理水戻し機構11の処理水搬送部材10を分解処理
槽3に連結して阻集器4まで延長可能にしていることで
ある。これによって、機体2を押し動かして、廃水処理
する阻集器4の設置位置まで移動できる。[0007] Thus, no fixed place is required, and
Not only the location but also the oil-containing wastewater of the interceptor 4 at another position can be decomposed and purified by one device. A second concrete means for solving the problem in the present invention is a wastewater conveying member of the wastewater suction mechanism 6 in which a wheel 13 is provided at a lower portion of the body 2 so as to be movable in addition to the first concrete means. 5 and the treated water transport member 10 of the treated water return mechanism 11 are connected to the decomposition treatment tank 3 and can be extended to the interceptor 4. Thus, the body 2 can be pushed and moved to the installation position of the interceptor 4 for wastewater treatment.
【0008】本発明における課題解決のための第3の具
体的手段は、第1又は2の具体的手段に加えて、前記廃
水吸引機構6は廃水搬送部材5を連結した分解処理槽3
の上部空間を負圧にする真空ポンプ14を有し、この真
空ポンプ14の吐出空気を阻集器4の排水管15又はば
っき機構8の少なくとも一方に送風する空気循環手段1
6を有することである。これによって、真空ポンプ14
を廃水吸引機構6の廃水吸引だけでなく、阻集器4の排
水管15の清掃、ばっき機構8の空気供給等に利用でき
る。A third specific means for solving the problem in the present invention is that, in addition to the first or second specific means, the wastewater suction mechanism 6 is provided with a decomposition treatment tank 3 to which a wastewater transport member 5 is connected.
A vacuum pump 14 for reducing the pressure in the upper space of the air pump to a negative pressure, and air circulating means 1 for blowing air discharged from the vacuum pump 14 to at least one of the drainage pipe 15 of the interceptor 4 and the bleeding mechanism 8.
6. Thereby, the vacuum pump 14
Can be used not only for suction of waste water by the waste water suction mechanism 6 but also for cleaning of the drain pipe 15 of the interceptor 4 and supply of air to the stripping mechanism 8.
【0009】本発明における課題解決のための第4の具
体的手段は、移動可能な機体2に支持されていて阻集器
4の貯水容量より容量大の分解処理槽3と、機体2に支
持されていて脱水後の廃水を分解処理槽3に送る脱水機
構17と、阻集器4内の廃水を廃水搬送部材5を介して
吸引して脱水機構17に送る廃水吸引機構6と、阻集器
4貯水容量相当分の油脂を分解するだけの量の好気性の
微生物を分解処理槽3内に定量供給する微生物供給機構
7と、分解処理槽3内の微生物に空気を供給するばっき
機構8と、分解処理槽3内の廃水を加熱する加熱機構9
と、分解処理槽3から処理後の廃水を処理水搬送部材1
0を介して阻集器4に戻す処理水戻し機構11とを有す
ることである。Fourth concrete means for solving the problem in the present invention is a decomposition treatment tank 3 supported by the movable body 2 and having a capacity larger than the water storage capacity of the interceptor 4, and supported by the body 2. A dewatering mechanism 17 for feeding the dewatered wastewater to the decomposition treatment tank 3, a wastewater suction mechanism 6 for sucking wastewater in the interceptor 4 via the wastewater transport member 5 and sending the wastewater to the dewatering mechanism 17, and a water storage for the interceptor 4. A microorganism supply mechanism 7 for supplying a quantity of aerobic microorganisms in a quantity sufficient to decompose an amount of fat or oil into the decomposition treatment tank 3, a feeding mechanism 8 for supplying air to the microorganisms in the decomposition treatment tank 3, Heating mechanism 9 for heating wastewater in decomposition tank 3
And waste water after treatment from the decomposition treatment tank 3
0 and a treated water return mechanism 11 for returning to the interceptor 4 via the zero.
【0010】これによって、定置場所を必要とせず、1
箇所だけでなく、別位置にある阻集器4の油脂含有廃水
も1台の装置で、かつ1回のバッチ処理で分解浄化する
ことができる。This eliminates the need for a fixed place,
Not only the location but also the oil-containing wastewater of the interceptor 4 at another position can be decomposed and purified by one apparatus and one batch process.
【0011】[0011]
【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。図1に示す第1実施形態におい
て、廃水浄化装置1Aは車輪13を有していて移動可能
な機体2上に、分解処理槽3と、廃水吸引機構6と、微
生物供給機構7と、ばっき機構8と、処理水戻し機構1
1とを設けて構成されている。前記分解処理槽3は、金
属又はプラスチックの容器で、単板で形成する、単板の
外面に断熱材を設ける、又は空気層あるいは断熱材を挟
んで二重槽に形成するかしており、その上部の開口が蓋
21によって開閉自在に閉鎖されている。分解処理槽3
の貯水容量は、阻集器4の容量よりも大きくても小さく
てもよい。Embodiments of the present invention will be described below with reference to the drawings. In the first embodiment shown in FIG. 1, a wastewater purifying apparatus 1A includes a decomposition treatment tank 3, a wastewater suction mechanism 6, a microorganism supply mechanism 7, Mechanism 8 and treated water return mechanism 1
1 is provided. The decomposition treatment tank 3 is a metal or plastic container, formed of a single plate, provided with a heat insulating material on the outer surface of the single plate, or formed in a double tank with an air layer or a heat insulating material interposed therebetween, The upper opening is closed by a lid 21 so as to be openable and closable. Decomposition tank 3
May be larger or smaller than the capacity of the interceptor 4.
【0012】この分解処理槽3の上部外面には、分解処
理槽3内を負圧にする真空ポンプ14が設けられてお
り、この真空ポンプ14の吸引口14aが分解処理槽3
に挿入され、または、分解処理槽3の上部に阻集器4内
の廃水を吸い上げ可能な廃水搬送部材5が連結されてい
る。前記廃水搬送部材5及び真空ポンプ14は廃水吸引
機構6を構成しており、廃水搬送部材5は金属パイプで
も形成できるが、ホースで形成して、機体2上に巻き取
り機構を設けておいて、巻き取り機構から引き出しなが
らその先端を阻集器4に挿入するようにしておくことが
好ましい。A vacuum pump 14 is provided on the outer surface of the upper part of the decomposition processing tank 3 to make the inside of the decomposition processing tank 3 a negative pressure.
Or a wastewater transport member 5 capable of sucking wastewater in the interceptor 4 is connected to the upper part of the decomposition treatment tank 3. The wastewater conveying member 5 and the vacuum pump 14 constitute a wastewater suction mechanism 6, and the wastewater conveying member 5 can be formed by a metal pipe, but is formed by a hose, and a winding mechanism is provided on the body 2 in advance. It is preferable to insert the distal end into the interceptor 4 while pulling out from the winding mechanism.
【0013】真空ポンプ14は、分解処理槽3内の上部
空間の空気を吸引して負圧にし、その負圧で廃水搬送部
材5を介して阻集器4内の廃水を吸引するものであり、
吐出パイプ14bから吐出される空気は空気循環手段1
6に用いられる。前記吐出パイプ14bには流量優先弁
22が設けられており、この流量優先弁22には、ばっ
き機構8の空気供給管23と排気管24とが接続されて
おり、空気供給管23が優先側で、必要量の空気が分解
処理槽3内に供給可能になっており、残余の空気はパイ
プ又はホースで形成された排気管24で排水管15に供
給される。The vacuum pump 14 sucks the air in the upper space in the decomposition treatment tank 3 to create a negative pressure, and sucks the wastewater in the interceptor 4 through the wastewater conveying member 5 with the negative pressure.
The air discharged from the discharge pipe 14b is
6 is used. The discharge pipe 14b is provided with a flow rate priority valve 22. The flow rate priority valve 22 is connected to an air supply pipe 23 and an exhaust pipe 24 of the blow mechanism 8, and the air supply pipe 23 has a priority. On the side, a required amount of air can be supplied into the decomposition tank 3, and the remaining air is supplied to the drain pipe 15 by an exhaust pipe 24 formed of a pipe or a hose.
【0014】排気管24には制御弁31が設けられてい
て、制御弁31を開放することにより、空気循環手段1
6の空気を取り出して、排水管15の内部の清掃に用い
られると共に、分解処理槽3から発生する悪臭を排水管
15へ排出できるようになっている。ばっき機構8の空
気供給管23は、分解処理槽3の内底部に屈曲して張り
巡らされており、また、多数の枝管を接続して網状に張
り巡らされており、分解処理槽3内に供給される好気性
の微生物に空気を満遍なく供給する。この供給される空
気は微細気泡にすることが好ましい。The exhaust pipe 24 is provided with a control valve 31. By opening the control valve 31, the air circulation means 1 is opened.
The air of No. 6 is taken out and used for cleaning the inside of the drainage pipe 15, and the offensive odor generated from the decomposition treatment tank 3 can be discharged to the drainage pipe 15. The air supply pipe 23 of the displacing mechanism 8 is bent and stretched around the inner bottom of the decomposition treatment tank 3, and is stretched in a net shape by connecting a number of branch pipes. The air is supplied evenly to the aerobic microorganisms supplied inside. It is preferable that the supplied air be fine bubbles.
【0015】微生物に供給後の空気は、微量の微生物を
含んだ状態で再び真空ポンプ14によって吸引され、ば
っきに使用されるか又は排気管24を介して排水管15
に供給される。この排水管15に供給される空気は微量
の微生物を含有することになり、排水管15内でも多少
の油脂分解が行われる。微生物供給機構7は分解処理槽
3の上部外面に装着されたタンク28内に、液化された
好気性の油脂分解微生物を貯留しており、前記タンク2
8は上部から微生物を補給可能であり、下部には供給管
25が接続され、この供給管25は制御弁26及びエジ
ェクタ手段27を介して空気供給管23に接続されてい
る。The air after being supplied to the microorganisms is sucked again by the vacuum pump 14 in a state containing a trace amount of microorganisms, and is used immediately or the drainage pipe 15 through the exhaust pipe 24.
Supplied to The air supplied to the drainpipe 15 contains a trace amount of microorganisms, and some fats and oils are decomposed even in the drainpipe 15. The microorganism supply mechanism 7 stores liquefied aerobic oil-decomposing microorganisms in a tank 28 mounted on the upper outer surface of the decomposition treatment tank 3.
Numeral 8 is capable of supplying microorganisms from the upper part, and a supply pipe 25 is connected to the lower part. The supply pipe 25 is connected to an air supply pipe 23 via a control valve 26 and an ejector means 27.
【0016】前記微生物供給機構7は、制御弁26を開
放することにより空気供給管23を介して分解処理槽3
内に微生物を供給可能であり、また、空気供給管23内
に循環空気が流れているときには、制御弁26を絞って
エジェクタ手段27で吸い出しながら噴霧状にして供給
することができる。前記微生物は、例えば特許第787
015号に開示されているような、ブルクホルデリア
(Burkholderia)属に属し、かつ高温で、
好気的に樹脂を資化するブルクホルデリア・セパシア
(Burkholderia cepadia)等の、
高濃度の油脂でも迅速に処理ができるものが使用され
る。When the control valve 26 is opened, the microorganism supply mechanism 7 opens the decomposition treatment tank 3 through the air supply pipe 23.
When the circulating air is flowing in the air supply pipe 23, the microorganism can be supplied in the form of a spray while squeezing the control valve 26 and sucking out the ejector means 27. The microorganism is described, for example, in Japanese Patent No. 787.
No. 015, belonging to the genus Burkholderia and at elevated temperatures,
Such as Burkholderia cepadia, which aerobically assimilate resin,
What can be processed quickly even with high-concentration fats and oils is used.
【0017】加熱機構9は、分解処理槽3内の廃水を加
熱するヒータで構成されており、分解処理槽3内に温度
センサ(図示せず)を挿入しておいて、分解処理槽3内
の廃水温度を微生物が効率良く活動する温度に設定す
る。処理水戻し機構11は制御弁30を有してパイプ又
はホース等で形成された処理水搬送部材10で構成さ
れ、処理水搬送部材10は分解処理槽3の底部に接続さ
れており、分解処理後の廃水を阻集器4に戻す。前記廃
水浄化装置1Aでは、阻集器4内の廃水をバッチ処理、
フロー処理のどちらでも行うことができ、分解処理槽3
の容量が阻集器4より大きい場合は、1回のバッチ処理
で全量の廃水を処理することが好ましく、小さい場合は
複数回に分けてバッチ処理を行うか又はフロー処理をす
る。The heating mechanism 9 is constituted by a heater for heating wastewater in the decomposition tank 3, and a temperature sensor (not shown) is inserted into the decomposition tank 3. The temperature of the wastewater is set to a temperature at which the microorganisms can efficiently operate. The treated water return mechanism 11 includes a treated water transport member 10 having a control valve 30 and formed of a pipe or a hose, and the treated water transport member 10 is connected to the bottom of the decomposition treatment tank 3. The wastewater that is later is returned to the interceptor 4. In the wastewater purification device 1A, the wastewater in the interceptor 4 is batch-processed,
It can be performed by either of the flow treatment, and the decomposition treatment tank 3
When the capacity of the wastewater is larger than the interceptor 4, it is preferable to treat the entire amount of wastewater in one batch process, and when it is small, the batch process is performed in a plurality of times or the flow process is performed.
【0018】前記廃水浄化装置1Aを使用して飲食店等
の阻集を処理する場合、営業終了後に廃水浄化装置1A
を阻集器4の近傍に移動して設置する。そして、廃水搬
送部材5及び処理水搬送部材10を阻集器4に挿入し、
排気管24を廃水管15に挿入する。次に、真空ポンプ
14を駆動して分解処理槽3内を負圧にしながら、廃水
搬送部材5を介して阻集器4内の廃水を分解処理槽3内
に吸引し、その排気を流量優先弁22を介して空気供給
管23に送り、また、制御弁26を開いて空気と共に微
生物を分解処理槽3内に供給し、加熱機構9で廃水を所
要温度まで上昇させる。In the case of using the waste water purifying apparatus 1A to process a blockage of a restaurant or the like, the waste water purifying apparatus 1A is used after the business is over.
Is moved to and installed near the interceptor 4. Then, the wastewater transport member 5 and the treated water transport member 10 are inserted into the interceptor 4,
The exhaust pipe 24 is inserted into the waste water pipe 15. Next, while driving the vacuum pump 14 to make the inside of the decomposition treatment tank 3 a negative pressure, the wastewater in the interceptor 4 is sucked into the decomposition treatment tank 3 via the wastewater conveying member 5, and the exhaust gas is discharged to the flow rate priority valve. The microorganisms are sent to the air supply pipe 23 via the air supply pipe 22, and the control valve 26 is opened to supply the microorganisms together with air into the decomposition treatment tank 3, and the heating mechanism 9 raises the wastewater to a required temperature.
【0019】なお、タンク28は分解処理槽3の比較的
上位置に配置されているので、真空ポンプ14を駆動す
る前に制御弁26を開放して、微生物をバッチ処理に必
要な量の全量、又はバッチ処理もしくはフロー処理に必
要な量の一部を、分解処理槽3内に注入しておいてもよ
い。真空ポンプ14の作動によって、ばっき機構8の空
気供給管23で分解処理槽3内の微生物をばっきしなが
ら、また、必要に応じてエジェクタ手段27を介して微
生物を補給しながら、分解処理槽3内で油脂分離を行わ
せ、また排気管24を使って排水管15内を清掃する。Since the tank 28 is located relatively above the decomposition tank 3, the control valve 26 is opened before the vacuum pump 14 is driven, so that the total amount of microorganisms required for batch processing can be reduced. Alternatively, a part of the amount required for the batch processing or the flow processing may be injected into the decomposition treatment tank 3. By the operation of the vacuum pump 14, the decomposition treatment is performed while the microorganisms in the decomposition treatment tank 3 are removed by the air supply pipe 23 of the removal mechanism 8 and the microorganisms are supplied through the ejector 27 as necessary. The grease is separated in the tank 3 and the drain pipe 15 is cleaned using the exhaust pipe 24.
【0020】バッチ処理終了後、又はフロー処理の途中
から、分解処理槽3内の底部から浄化された水を、制御
弁30を開放して処理水搬送部材10を介して阻集器4
に戻す。図2は第2実施形態を示しており、この廃水浄
化装置1Bは、廃水吸引機構6が廃水搬送部材5の先端
に水中ポンプ32を設けて構成されており、分解処理槽
3は密閉構造でなくともよく、その代わりに、ばっき機
構8及び空気循環手段16用のブロアー33を必要とし
ている。After the completion of the batch processing or during the flow processing, the purified water from the bottom in the decomposition processing tank 3 is opened by the control valve 30 and intercepted by the interceptor 4 through the processing water transport member 10.
Return to FIG. 2 shows a second embodiment. In this wastewater purifying apparatus 1B, a wastewater suction mechanism 6 is provided with a submersible pump 32 at the tip of a wastewater transport member 5, and a decomposition treatment tank 3 has a closed structure. Instead, a blower 33 for the blast mechanism 8 and the air circulation means 16 is required.
【0021】ブロアー33は分解処理槽3の上部から吸
引口14aを介して空気を吸引し、供給管25及び流量
優先弁22を介してばっき機構8の空気供給管23にば
っき用空気を供給し、これによって空気を循環させ、必
要に応じて制御弁31を開放して排気管24で排水管1
5に清掃用空気を供給する。ばっき機構8の空気供給管
23の複数の分岐管23aにはエアーストーン34が設
けられ、加熱機構9も複数のヒータで構成され、微生物
供給機構7は制御弁26を開放することにより、微生物
をタンク28から自重で分解処理槽3内に供給する構造
となっている。The blower 33 sucks air from the upper part of the decomposition tank 3 through the suction port 14a, and supplies the air to the air supply pipe 23 of the blow mechanism 8 through the supply pipe 25 and the flow rate priority valve 22. Supply, thereby circulating the air, opening the control valve 31 as necessary, and draining the drain pipe 1 with the exhaust pipe 24.
5 is supplied with cleaning air. An air stone 34 is provided in a plurality of branch pipes 23 a of the air supply pipe 23 of the blast mechanism 8, a heating mechanism 9 is also composed of a plurality of heaters, and the microorganism supply mechanism 7 opens the control valve 26 to Is supplied from the tank 28 into the decomposition treatment tank 3 by its own weight.
【0022】なお、この第2実施形態でも、ブロアー3
3を使って微生物をエジェクタ手段を介してばっき空気
と共に供給することは可能である。図3は第3実施形態
を示しており、この廃水浄化装置1Cは、分解処理槽3
の外側上部に脱水機構17が設けられ、微生物供給機構
7にはタンク28の他に予備タンク37が備えられてい
る。真空ポンプ14は分解処理槽3の外側面に装着され
ており、2本の吸引管38,39が接続されていて、吸
引管38は脱水機構17に、吸引管39はタンク28に
それぞれ接続されており、真空ポンプ14の排気供給は
吐出パイプ14b及び流量優先弁22を介して空気供給
管23に優先的に供給されると共に、排気管24を介し
て排水管15に供給可能となっている。Incidentally, also in the second embodiment, the blower 3
It is possible to use 3 to feed microorganisms together with purged air via ejector means. FIG. 3 shows a third embodiment, in which a wastewater purifying apparatus 1C includes a decomposition treatment tank 3.
A dehydration mechanism 17 is provided on the upper side of the outside, and the microorganism supply mechanism 7 is provided with a spare tank 37 in addition to the tank 28. The vacuum pump 14 is mounted on the outer surface of the decomposition treatment tank 3, and two suction pipes 38 and 39 are connected. The suction pipe 38 is connected to the dehydrating mechanism 17 and the suction pipe 39 is connected to the tank 28. The exhaust supply of the vacuum pump 14 is preferentially supplied to the air supply pipe 23 via the discharge pipe 14 b and the flow rate priority valve 22, and can be supplied to the drain pipe 15 via the exhaust pipe 24. .
【0023】空気供給管23に設けたエジェクタ手段2
7には、予備タンク37内から微生物を取り出す供給管
25aが接続されており、タンク28からの供給とは別
経路で微生物を供給可能になっている。前記脱水機構1
7は遠心脱水式脱水機を有し、容器40内にモータ41
で駆動される脱水かご42が設けられており、容器40
は蓋43により密閉可能になっている。脱水機構17
は、その上部に接続した吸引管38で容器40内を負圧
にすることにより、廃水搬送部材5を介して阻集器4か
ら廃水を吸引して脱水かご42に供給し、脱水かご42
を高速回転させて、残飯、野菜屑等の固形物から水分を
分離させ、その水分を分解処理槽3内に流入させるよう
になっている。前記固形物は蓋43を開放することによ
り取り出される。Ejector means 2 provided in air supply pipe 23
7 is connected to a supply pipe 25a for taking out the microorganisms from the spare tank 37, so that the microorganisms can be supplied in a different path from the supply from the tank. The dehydration mechanism 1
7 has a centrifugal dewatering type dehydrator, and a motor 41
Is provided with a dehydrating basket 42 driven by
Can be hermetically closed by a lid 43. Dehydration mechanism 17
By suctioning waste water from the interceptor 4 via the waste water conveying member 5 and supplying the waste water to the dewatering car 42 by making the inside of the container 40 negative by the suction pipe 38 connected to the upper part thereof,
Is rotated at a high speed to separate moisture from solids such as leftovers and vegetable waste, and the moisture flows into the decomposition treatment tank 3. The solid is taken out by opening the lid 43.
【0024】微生物供給機構7は、タンク28と予備タ
ンク37とを連通管44で連通しており、タンク28は
吸引管39が接続されていて、その内上部を負圧にする
ことにより、連通管44を介して予備タンク37から微
生物を吸引して、一定量貯留可能になっている。前記タ
ンク28の微生物貯留量は、例えば、バッチ処理1回分
に設定しておいて、制御弁26を開放して供給管25か
ら微生物を自重で分解処理槽3内に供給し、微生物量が
不足の場合には、供給管25aからばっき空気と共に追
加供給する。The microorganism supply mechanism 7 communicates the tank 28 with the spare tank 37 through a communication pipe 44. The tank 28 is connected to a suction pipe 39, and the tank 28 is connected to the tank 28 by applying a negative pressure to its upper part. Microorganisms are sucked from the reserve tank 37 via the pipe 44 and can be stored in a certain amount. The amount of stored microorganisms in the tank 28 is set to, for example, one batch treatment, and the control valve 26 is opened to supply the microorganisms from the supply pipe 25 to the decomposition treatment tank 3 by its own weight, and the amount of microorganisms becomes insufficient. In the case of (1), the air is additionally supplied together with the air from the supply pipe 25a.
【0025】図3中、符号46、47、48は、制御弁
26、30、31等と同様な開閉用の制御弁であり、こ
れらの制御弁は、手動操作で開閉してもよいが、電気的
に開閉するようにしてもよい。また、脱水機構17は重
力式でもよく、分解処理槽3の内上部に収納するもので
もよい。なお、本発明は前記実施の形態に限定されるも
のではなく、種々変形することができる。例えば、3つ
の実施形態の構成部分を適宜組み合わせたり、真空ポン
プ14、タンク28等を機体2に直接搭載したりしても
よい。また、機体2はフォークリフト等で運搬して設置
位置を変更するようにしてもい。In FIG. 3, reference numerals 46, 47, and 48 denote opening and closing control valves similar to the control valves 26, 30, 31, and the like. These control valves may be opened and closed manually. It may be opened and closed electrically. Further, the dehydrating mechanism 17 may be of a gravity type or may be housed in the upper part of the decomposition tank 3. Note that the present invention is not limited to the above embodiment, and can be variously modified. For example, the components of the three embodiments may be appropriately combined, or the vacuum pump 14, the tank 28, and the like may be directly mounted on the body 2. Further, the body 2 may be transported by a forklift or the like to change the installation position.
【0026】[0026]
【発明の効果】以上詳述した本発明によれば、定置場所
を必要とせず、1箇所だけでなく、別位置にある阻集器
の油脂含有廃水も1台の装置で分解浄化することがで
き、安価でかつ汎用利用ができる。According to the present invention described in detail above, it is possible to decompose and purify wastewater containing oil and fat not only at one place but also at the interceptor at another place without using a fixed place. It is inexpensive and can be used for general purposes.
【図1】本発明の第1の実施の形態を示す断面説明図で
ある。FIG. 1 is an explanatory sectional view showing a first embodiment of the present invention.
【図2】第2の実施の形態を示す断面説明図である。FIG. 2 is an explanatory sectional view showing a second embodiment.
【図3】第3の実施の形態を示す断面説明図である。FIG. 3 is an explanatory cross-sectional view showing a third embodiment.
1 廃水浄化装置 2 機体 3 分解処理槽 4 阻集器 5 廃水搬送部材 6 廃水吸引機構 7 微生物供給機構 8 ばっき機構 9 加熱機構 10 処理水搬送部材 11 処理水戻し機構 13 車輪 14 真空ポンプ 15 排水管 16 空気循環手段 17 脱水機構 DESCRIPTION OF SYMBOLS 1 Wastewater purification apparatus 2 Airframe 3 Decomposition tank 4 Interceptor 5 Wastewater conveyance member 6 Wastewater suction mechanism 7 Microorganism supply mechanism 8 Deposition mechanism 9 Heating mechanism 10 Processed water conveyance member 11 Processed water return mechanism 13 Wheels 14 Vacuum pump 15 Drain pipe 16 Air circulation means 17 Dehydration mechanism
Claims (4)
解処理槽と、阻集器内の廃水を廃水搬送部材を介して吸
引して分解処理槽に送る廃水吸引機構と、分解処理槽内
に好気性の油脂分解微生物を供給する微生物供給機構
と、分解処理槽内の微生物に空気を供給するばっき機構
と、分解処理槽内を加熱する加熱機構と、分解処理槽か
ら処理後の廃水を処理水搬送部材を介して阻集器に戻す
処理水戻し機構とを有することを特徴とする廃水浄化装
置。1. A decomposition treatment tank supported by a body whose installation position can be changed, a wastewater suction mechanism for sucking wastewater in an interceptor through a wastewater conveying member and sending the wastewater to the decomposition treatment tank, A microbial supply mechanism that supplies aerobic fat and oil-decomposing microorganisms, a feeding mechanism that supplies air to the microorganisms in the decomposition treatment tank, a heating mechanism that heats the inside of the decomposition treatment tank, and a wastewater after treatment from the decomposition treatment tank A waste water purifying device having a treated water return mechanism for returning the treated water to the interceptor via the treated water conveying member.
にし、前記廃水吸引機構の廃水搬送部材及び処理水戻し
機構の処理水搬送部材を分解処理槽に連結して阻集器ま
で延長可能にしていることを特徴とする請求項1に記載
の廃水浄化装置。2. The apparatus according to claim 1, wherein a wheel is provided at a lower portion of the body so as to be movable, and a waste water transport member of the waste water suction mechanism and a treated water transport member of the treated water return mechanism are connected to a decomposition treatment tank and can be extended to an interceptor. The wastewater purifying apparatus according to claim 1, wherein:
した分解処理槽の上部空間を負圧にする真空ポンプを有
し、この真空ポンプの吐出空気を阻集器の排水管又はば
っき機構の少なくとも一方に送風する空気循環手段を有
することを特徴とする請求項1又は2に記載の廃水浄化
装置。3. The wastewater suction mechanism has a vacuum pump for reducing the pressure in the upper space of the decomposition treatment tank to which the wastewater transport member is connected, and discharges air from the vacuum pump to a drain pipe of an interceptor or a blower mechanism. The wastewater purification device according to claim 1 or 2, further comprising an air circulation unit that sends air to at least one of the wastewater purification units.
の貯水容量より容量大の分解処理槽と、機体に支持され
ていて脱水後の廃水を分解処理槽に送る脱水機構と、阻
集器内の廃水を廃水搬送部材を介して吸引して脱水機構
に送る廃水吸引機構と、阻集器貯水容量相当分の油脂を
分解するだけの量の好気性の微生物を分解処理槽内に定
量供給する微生物供給機構と、分解処理槽内の微生物に
空気を供給するばっき機構と、分解処理槽内の廃水を加
熱する加熱機構と、分解処理槽から処理後の廃水を処理
水搬送部材を介して阻集器に戻す処理水戻し機構とを有
することを特徴とする廃水浄化装置。4. A decomposing tank supported by a movable body and having a capacity larger than the water storage capacity of the interceptor; a dehydrating mechanism supported by the body to send dewatered wastewater to the decomposing tank; A wastewater suction mechanism that sucks wastewater from the wastewater through a wastewater transport member and sends it to a dehydration mechanism, and supplies a fixed amount of aerobic microorganisms in the decomposition treatment tank in an amount sufficient to decompose oil and fat equivalent to the water storage capacity of the interceptor A microorganism supply mechanism, a mechanism for supplying air to the microorganisms in the decomposition treatment tank, a heating mechanism for heating wastewater in the decomposition treatment tank, and a wastewater treated from the decomposition treatment tank via a treated water transport member. A wastewater purifying apparatus, comprising: a treated water return mechanism for returning to the interceptor.
Priority Applications (1)
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JP12001499A JP4267753B2 (en) | 1999-04-27 | 1999-04-27 | Waste water purification equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12001499A JP4267753B2 (en) | 1999-04-27 | 1999-04-27 | Waste water purification equipment |
Publications (2)
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JP2000308899A true JP2000308899A (en) | 2000-11-07 |
JP4267753B2 JP4267753B2 (en) | 2009-05-27 |
Family
ID=14775776
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JP12001499A Expired - Lifetime JP4267753B2 (en) | 1999-04-27 | 1999-04-27 | Waste water purification equipment |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002331276A (en) * | 2001-05-08 | 2002-11-19 | Shinyo Sangyo Kk | Wet type organic waste fermentative decomposition treatment machine utilizing drainage |
JP2005512770A (en) * | 2001-12-13 | 2005-05-12 | インバイロンメンタル オペレイティング ソリューションズ インコーポレイテッド | Wastewater treatment process and equipment |
US7794592B2 (en) | 2006-06-29 | 2010-09-14 | Ralph Brown | Wastewater disinfection apparatus and methods |
KR101269845B1 (en) | 2010-05-12 | 2013-06-07 | 엄재수 | Wastewater treatment systems using strain |
CN113683206A (en) * | 2021-09-12 | 2021-11-23 | 仇静 | Microbial sewage treatment system and treatment method thereof |
-
1999
- 1999-04-27 JP JP12001499A patent/JP4267753B2/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002331276A (en) * | 2001-05-08 | 2002-11-19 | Shinyo Sangyo Kk | Wet type organic waste fermentative decomposition treatment machine utilizing drainage |
JP2005512770A (en) * | 2001-12-13 | 2005-05-12 | インバイロンメンタル オペレイティング ソリューションズ インコーポレイテッド | Wastewater treatment process and equipment |
US7794592B2 (en) | 2006-06-29 | 2010-09-14 | Ralph Brown | Wastewater disinfection apparatus and methods |
KR101269845B1 (en) | 2010-05-12 | 2013-06-07 | 엄재수 | Wastewater treatment systems using strain |
CN113683206A (en) * | 2021-09-12 | 2021-11-23 | 仇静 | Microbial sewage treatment system and treatment method thereof |
CN113683206B (en) * | 2021-09-12 | 2023-10-20 | 深圳市汪德弗科技有限公司 | Microorganism sewage treatment system and treatment method thereof |
Also Published As
Publication number | Publication date |
---|---|
JP4267753B2 (en) | 2009-05-27 |
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