JP3398924B2 - Wastewater treatment equipment for kitchen waste - Google Patents

Wastewater treatment equipment for kitchen waste

Info

Publication number
JP3398924B2
JP3398924B2 JP04669596A JP4669596A JP3398924B2 JP 3398924 B2 JP3398924 B2 JP 3398924B2 JP 04669596 A JP04669596 A JP 04669596A JP 4669596 A JP4669596 A JP 4669596A JP 3398924 B2 JP3398924 B2 JP 3398924B2
Authority
JP
Japan
Prior art keywords
tank
aerobic
decomposition tank
anaerobic
treated 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.)
Expired - Fee Related
Application number
JP04669596A
Other languages
Japanese (ja)
Other versions
JPH09206787A (en
Inventor
清秀 伊戸川
Original Assignee
クリーンテック株式会社
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 クリーンテック株式会社 filed Critical クリーンテック株式会社
Priority to JP04669596A priority Critical patent/JP3398924B2/en
Publication of JPH09206787A publication Critical patent/JPH09206787A/en
Application granted granted Critical
Publication of JP3398924B2 publication Critical patent/JP3398924B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Processing Of Solid Wastes (AREA)

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は、各種食品材料の調
理ゴミ及び残飯等の厨芥粉砕装置であるディスポーザー
で少量の水を加えながら粉砕した後、ディスポーザーよ
り排出される厨芥含有汚水の装置に関するものである。 【0002】 【従来の技術】従来の厨芥含有汚水の処理装置は、厨芥
含有汚水中の固形物を粉砕する粉砕機と、前記粉砕機で
の粉砕物を含有する厨芥含有汚水を嫌気性微生物固定床
の存在下で嫌気分解する嫌気分解槽と、前記嫌気分解槽
で嫌気分解された処理水を好気性微生物固定床の存在下
で好気処理する好気処理槽と、前記好気処理槽で捕捉あ
るいは生成した懸濁物質や余剰汚泥等を前記嫌気分解槽
へ返送する余剰汚泥等返送手段とを備えたものが存在す
る。 【0003】そして、上記の構成により、ディスポーザ
ーで粉砕された厨芥固形物は嫌気性微生物群により液体
状に可溶化し、更に嫌気処理された処理水を好気処理域
で好気性微生物群により処理し、BOD負荷量を低減さ
せる。好気処理手段でのエアーレーションにより浮上し
た懸濁物質や余剰汚泥等は嫌気分解域に返送して再度処
理を繰り返し、SSの発生のない良好な処理水とし排出
する。 【0004】 【発明が解決しようとする課題】一般に厨芥含有汚水
は、各種食品材料の調理ゴミ及び残飯等の厨芥を粉砕装
置であるディスポーザーで少量の水を加えながら粉砕さ
れ、厨房より排出される。特に、厨芥含有汚水中の微細
固形物は有機物を多量に含むことにより、BOD値、S
S値が非常高く、十分な処理がされずに放流されると、
水質汚染等の公害問題となる。そこで、従来活性汚泥
法、生物膜法等の酸化分解処理法等が行われていたが、
十分な効果が得られず、近年は上記従来のような処理装
置が開発されている。 【0005】しかしながら、前記上記従来の装置では、
好気処理槽で捕捉あるいは発生した懸濁物質や余剰汚泥
等は嫌気分解槽へ直接返送され、再度嫌気分解されて放
流されるのみで、余剰汚泥等の回収作業を省略化するも
のであるから、再度の嫌気分解により余剰汚泥等を全く
皆無に近い状態にしなければならない。 【0006】しかし、余剰汚泥等は好気性処理時の好気
性菌の多量発生によっても自ずと発生し、皆無となるこ
とはあり得ず、嫌気分解槽、好気分解槽内に溜まり嫌気
分解槽及び好気分解槽の両方の掃除を余儀なくされ、両
槽の維持管理は大変である。又、当然ながら放流される
処理水中にも未分解の汚泥も含まれることになる。 【0007】上記点より本発明は、未分解の懸濁汚泥や
余剰汚泥等の沈澱物を濃縮して一箇所に集め、この濃縮
された余剰汚泥等の沈澱物を回収するこにより、嫌気分
解槽、好気分解槽、固液分解槽の掃除等を不要として装
置の維持管理を容易にすると共に、放流される処理水も
清澄で水質汚染等の公害の発生のない厨芥含有汚水の処
理装置を提供しようとするものである。 【0008】 【課題を解決するための手段】上記課題を解決するため
本発明装置は、厨芥を少量の水を加えながら粉砕する粉
砕機と、前記粉砕機での粉砕物を含有する汚水を嫌気性
微生物固定床の存在下で嫌気分解する嫌気分解槽と、前
記嫌気分解槽で嫌気分解された処理水を好気性微生物が
生育・繁殖する流動床の又は固定床の存在下で好気処理
する好気分解槽と、前記好気分解槽の処理水中の懸濁物
質や浮遊物、余剰汚泥等を沈澱させ、上澄水を外部へ放
流する固液分離槽と、前記固液分離槽の沈澱物および処
理水の一部を引き抜き移送する移送手段と、前記移送手
段にて移送された沈澱物および処理水の一部を貯留し、
上澄水を分離して前記好気分解槽に返送することにより
沈澱物の濃縮を図る汚泥濃縮消化槽を備えたことを特徴
とするものである。 【0009】かかる構成により本発明は、厨房より廃棄
された厨芥を少量の水を加えながら粉砕機で粉砕し、こ
の粉砕物を含有する汚水は嫌気分解槽で嫌気性微生物群
により液化分解される。嫌気分解槽で液化分解された処
理水は好気分解槽で流動床又は固定床で生育・繁殖する
好気性微生物群により酸化分解処理され、BOD負荷量
が低減される。次に、固液分離槽で好気分解処理済みの
処理水中の懸濁物質や浮遊物、余剰汚泥等は沈澱され、
上澄水は外部へ放流されるのである。 【0010】そして、固液分離槽で沈澱された懸濁物
質、浮遊物、余剰汚泥等の沈澱物および処理水の一部は
移送手段で汚泥濃縮消化槽で再度濾過され、未分解の余
剰汚泥等は濃縮されて堆積し、その上澄水は再度濾過処
理を受け、分離されて好気分解槽に返送されるため、固
液分離槽内には余剰汚泥等の沈澱物は堆積しないと共
に、返送される好気分解槽には濾過処理された上澄水の
みが導入され、余剰汚泥等の混入はなく、再度好気分解
された後、固液分離槽より上澄水が放流されるので、S
Sの発生のない清澄な排水となる。 【0011】そして、汚泥濃縮消化槽だけには再度の濾
過処理により濃縮された状態の余剰汚泥等の沈澱物が沈
澱しているので、汚泥濃縮消化槽の沈澱物の回収作業の
みを行えばよく、嫌気分解槽、好気分解槽、固液分離槽
の掃除は不要となるのでメンテナンスが容易となる。 【0012】 【発明の実施の形態】以下、本発明の一実施の形態を図
面に基づき説明する。図1は本発明処理装置の一実施の
形態を示す断面図である。而して、図中1は調理場のシ
ンクであり、このシンク1の底部にディスポーザー等の
粉砕機2が設置されている。3は粉砕機2と嫌気分解槽
4間に配設した排水流通管であり、粉砕機2で粉砕され
た粉砕物を含有する厨芥含有汚水はこの汚水流通管3よ
り嫌気分解槽4内に導入される。 【0013】5は嫌気分解槽4内に設けた嫌気性微生物
固定床であり、この嫌気性微生物固定床5には多孔質の
担体としてポリウレタンフォームの担体が多数充填され
て嫌気性微生物を担持し、嫌気性微生物により厨芥含有
汚水は液化分解される。 【0014】6は嫌気分解槽4で液化分解された処理水
が第1室の好気分解槽7内に流出する溢流口であり、嫌
気分解槽4と第1室の好気分解槽7の仕切り壁8の上方
に設けられている。9は第1室の好気分解槽7内に設け
た好気性微生物固定床であり、この好気性微生物固定床
9には多孔質の担体としてポリウレタンフォームの担体
が多数充填されて、好気性微生物を担持している。 【0015】又、第1室の好気分解槽7に隣接して第2
室の好気分解槽10が設置され、内部に前同様の好気性
微生物固定床9が設置されている。第1室の好気分解槽
7と第2室の好気分解槽10との仕切り壁11の下部に
両室に通じる連通口12が設けられている。 【0016】13は第1室の好気分解槽7及び第2室の
好気分解槽10の底部に設けた散気管であり、エアーポ
ンプ14より送り込まれた空気により好気状態に維持さ
れ、嫌気分解槽4で液化分解された処理水は前記好気性
微生物によって酸化分解処理される。 【0017】15は第2室の好気分解槽10で酸化分解
された処理水が隣接の固液分離槽16に流出する移流
口、17は好気分解槽で発生した臭気等のガスを排出す
る排ガス管であり、脱臭装置18を通過したガスが外部
へ排出される。尚、図面では好気分解槽内の好気性微生
物は固定床となっているが、流動床となっていてもよ
い。 【0018】19は固液分離槽16内に設けた濾過層で
あり、酸化分解された処理水中の余剰汚泥等は底部に沈
澱し、処理水は濾過層19により濾過を受け上澄水は固
液分離槽16に設けた放流管20より外部に放流され
る。 【0019】21は固液分離槽16に沈澱している余剰
汚泥等の沈澱物及び処理水の一部をポンプ22で汚泥濃
縮消化槽23へ移送する汚泥等の移送管である。汚泥濃
縮消化槽23内には多孔質の担体であるポリウレタンフ
ォームの担体等の濾材が充填された濾過層24が設けら
れ、固液分離槽16より移送された沈澱物及び処理水の
一部を貯留し、上澄水は分離し濾過層24を経て分離水
移送管25で前記第1室の好気分解槽7内に返送され、
再度好気処理を受けた後再度濾過され外部に放流され
る。 【0020】 【発明の効果】本発明に依れば、厨芥を粉砕機で粉砕
し、この粉砕物を含む厨芥含有汚水を嫌気分解した後に
好気分解し、固液分離した懸濁物質、浮遊物、余剰汚泥
等の沈澱物及び処理水の一部を汚泥濃縮消化槽へ移送し
再び余剰汚泥等の沈澱物を濾過し、濃縮とした汚泥を貯
留すると共に、分離した上澄水は再度好気処理、及び濾
過され放流されるので、BOD負荷量が低減し、SSの
発生のない清澄な放流水となり、水質汚染もなく公害の
問題も発生しない。又、懸濁物質、浮遊物、余剰汚泥等
の沈澱物は濃縮した状態で汚泥濃縮消化槽だけに堆積す
るため、嫌気分解槽、好気分解槽、固液分離槽の掃除は
全く要せず、汚泥濃縮消化槽での沈澱物の回収作業だけ
で済み、従来に比べ処理装置の維持管理が非常に容易と
なるものである。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a disposer which is a device for crushing various kinds of food materials, such as cooking garbage and garbage, while adding a small amount of water and crushing the garbage. The present invention relates to an apparatus for discharging waste water containing kitchen waste. 2. Description of the Related Art A conventional apparatus for treating garbage-containing sewage is a crusher for crushing solids in garbage-containing sewage, and fixing anaerobic microorganisms to garbage-containing sewage containing the crushed material in the crusher. An anaerobic decomposition tank that anaerobically decomposes in the presence of a bed, an aerobic treatment tank that aerobically treats the treated water anaerobically decomposed in the anaerobic decomposition tank in the presence of a fixed bed of aerobic microorganisms, and the aerobic treatment tank. There is an apparatus provided with a means for returning excess sludge or the like for returning the trapped or generated suspended matter or excess sludge to the anaerobic decomposition tank. [0003] With the above-mentioned structure, the solid garbage crushed by the disposer is solubilized in a liquid state by the anaerobic microorganisms, and the anaerobic treated water is treated by the aerobic microorganisms in the aerobic treatment zone. Then, the BOD load is reduced. Suspended substances and excess sludge that floated by aeration in the aerobic treatment means are returned to the anaerobic decomposition zone, and the treatment is repeated again. Generally, garbage containing garbage is crushed by adding a small amount of water to a garbage such as cooking garbage of various food materials and garbage such as garbage, and discharged from the kitchen. . In particular, fine solids in garbage-containing sewage contain a large amount of organic matter, so that BOD value and S
If the S value is very high and discharged without sufficient treatment,
Pollution problems such as water pollution will occur. Therefore, oxidative decomposition treatment methods such as the activated sludge method and the biofilm method have been conventionally performed.
A sufficient effect cannot be obtained, and in recent years, the above-described conventional processing apparatus has been developed. However, in the above-mentioned conventional apparatus,
Suspended substances and excess sludge trapped or generated in the aerobic treatment tank are returned directly to the anaerobic decomposition tank, and are only anaerobically decomposed again and released, eliminating the work of collecting excess sludge. In this case, the excess sewage and the like must be reduced to almost zero by the anaerobic decomposition again. However, surplus sludge and the like are naturally generated even by a large amount of aerobic bacteria generated during the aerobic treatment, and cannot be completely eliminated. The sludge is accumulated in the anaerobic decomposition tank, the aerobic decomposition tank, and the anaerobic decomposition tank. Both aerobic decomposition tanks have to be cleaned, and maintenance of both tanks is difficult. In addition, naturally, undegraded sludge is also included in the treated water discharged. In view of the above, the present invention provides anaerobic decomposition by concentrating undegraded precipitates such as suspended sludge and excess sludge and collecting them in one place, and recovering the concentrated excess sludge and other precipitates. It is not necessary to clean tanks, aerobic decomposition tanks, and solid-liquid decomposition tanks, so that maintenance and management of the equipment is easy, and the treated water discharged is clear and does not cause pollution such as water pollution. It is intended to provide. [0008] In order to solve the above problems, the apparatus of the present invention comprises a crusher for crushing kitchen garbage while adding a small amount of water, and an anaerobic sewage containing crushed material from the crusher. An anaerobic decomposition tank that performs anaerobic decomposition in the presence of a fixed bed of anaerobic microorganisms, and the treated water anaerobically decomposed in the anaerobic decomposition tank is subjected to aerobic treatment in the presence of a fixed bed or a fluidized bed where aerobic microorganisms grow and propagate. An aerobic decomposition tank, a solid-liquid separation tank that precipitates suspended substances and suspended solids, excess sludge, and the like in the treatment water of the aerobic decomposition tank, and discharges supernatant water to the outside; and a sediment in the solid-liquid separation tank. And a transfer means for extracting and transferring a part of the treated water, and storing a part of the precipitate and the treated water transferred by the transfer means,
A sludge concentration digestion tank for separating the supernatant water and returning the supernatant water to the aerobic decomposition tank to concentrate the precipitate is provided. According to the present invention, according to the present invention, kitchen waste discarded from a kitchen is pulverized by a pulverizer while adding a small amount of water, and sewage containing the pulverized material is liquefied and decomposed by anaerobic microorganisms in an anaerobic decomposition tank. . The treated water liquefied and decomposed in the anaerobic decomposition tank is oxidatively decomposed by the aerobic microorganisms that grow and propagate in the fluidized bed or the fixed bed in the aerobic decomposition tank, and the BOD load is reduced. Next, suspended solids and suspended matter in the treated water subjected to aerobic decomposition treatment in the solid-liquid separation tank, excess sludge, etc. are precipitated,
The supernatant water is discharged outside. [0010] The suspended solids and suspended solids precipitated in the solid-liquid separation tank and a part of the treated water such as excess sludge and the treated water are again filtered in the sludge concentration and digestion tank by the transfer means, and undegraded excess sludge is removed. Is concentrated and deposited, and the supernatant water is filtered again, separated and returned to the aerobic decomposition tank, so that no precipitate such as excess sludge is deposited in the solid-liquid separation tank and returned. Only the filtered supernatant water is introduced into the aerobic decomposition tank, and no excess sludge is mixed. After the aerobic decomposition is performed again, the supernatant water is discharged from the solid-liquid separation tank.
It becomes clear drainage without S generation. [0011] Since only the sludge concentration and digestion tank has precipitates such as surplus sludge which has been concentrated by the re-filtration process, only the work of collecting the precipitate in the sludge concentration and digestion tank needs to be performed. Since the anaerobic decomposition tank, the aerobic decomposition tank, and the solid-liquid separation tank do not need to be cleaned, maintenance is facilitated. An embodiment of the present invention will be described below with reference to the drawings. FIG. 1 is a sectional view showing an embodiment of the processing apparatus of the present invention. In the figure, reference numeral 1 denotes a sink of a cooking place, and a pulverizer 2 such as a disposer is installed at the bottom of the sink 1. Reference numeral 3 denotes a drainage flow pipe disposed between the crusher 2 and the anaerobic decomposition tank 4, and garbage containing garbage containing pulverized material crushed by the crusher 2 is introduced into the anaerobic decomposition tank 4 from the sewage flow pipe 3. Is done. Reference numeral 5 denotes an anaerobic microorganism fixed bed provided in the anaerobic decomposition tank 4. The anaerobic microorganism fixed bed 5 is filled with a large number of polyurethane foam carriers as porous carriers to carry anaerobic microorganisms. In addition, kitchen waste water is liquefied and decomposed by anaerobic microorganisms. Reference numeral 6 denotes an overflow port through which the treated water liquefied and decomposed in the anaerobic decomposition tank 4 flows out into the aerobic decomposition tank 7 in the first chamber. The anaerobic decomposition tank 4 and the aerobic decomposition tank 7 in the first chamber are provided. Above the partition wall 8. Reference numeral 9 denotes an aerobic microorganism fixed bed provided in the aerobic decomposition tank 7 of the first chamber. The aerobic microorganism fixed bed 9 is filled with a large number of polyurethane foam carriers as porous carriers. Is carried. Further, a second chamber is disposed adjacent to the first aerobic decomposition tank 7.
An aerobic decomposition tank 10 is installed in the room, and the same aerobic microorganism fixed bed 9 as before is installed inside. A communication port 12 communicating with both the first and second aerobic decomposition tanks 7 and 10 is provided below a partition wall 11 between the first and second chambers. Reference numeral 13 denotes an air diffuser provided at the bottom of the aerobic decomposition tank 7 in the first chamber and the aerobic decomposition tank 10 in the second chamber, and is maintained in an aerobic state by air sent from the air pump 14. The treated water liquefied and decomposed in the anaerobic decomposition tank 4 is oxidatively decomposed by the aerobic microorganism. Reference numeral 15 denotes an advection port through which the treated water oxidized and decomposed in the aerobic decomposition tank 10 in the second chamber flows out to an adjacent solid-liquid separation tank 16, and 17 discharges gas such as odor generated in the aerobic decomposition tank. The gas passing through the deodorizing device 18 is discharged to the outside. In the drawings, the aerobic microorganisms in the aerobic decomposition tank are in a fixed bed, but may be in a fluidized bed. Reference numeral 19 denotes a filtration layer provided in the solid-liquid separation tank 16. Excess sludge and the like in the oxidized and decomposed treated water precipitate at the bottom. The treated water is filtered by the filtration layer 19 and the supernatant water is solid-liquid. It is discharged outside through a discharge pipe 20 provided in the separation tank 16. Reference numeral 21 denotes a transfer pipe for sludge or the like for transferring a precipitate such as excess sludge settled in the solid-liquid separation tank 16 and a part of the treated water to a sludge concentration digestion tank 23 by a pump 22. A filtration layer 24 filled with a filter medium such as a polyurethane foam carrier, which is a porous carrier, is provided in the sludge concentration digestion tank 23, and a part of the sediment and treated water transferred from the solid-liquid separation tank 16 is removed. The stored supernatant water is separated and returned to the aerobic decomposition tank 7 of the first chamber via a separation water transfer pipe 25 via a filtration layer 24,
After undergoing aerobic treatment again, it is filtered again and discharged to the outside. According to the present invention, the garbage is crushed by a crusher, and the garbage containing the garbage containing the crushed material is anaerobically decomposed, then aerobically decomposed, and solid-liquid separated suspended substances, suspended Waste, excess sludge, etc. and a part of the treated water are transferred to a sludge concentration and digestion tank, and the excess sludge, etc. are filtered again, and the concentrated sludge is stored. Since it is treated, filtered, and discharged, the BOD load is reduced, clear water without SS is generated, and there is no water pollution and no pollution problem. In addition, since sediments such as suspended solids, suspended solids, and excess sludge accumulate only in the sludge concentration digestion tank in a concentrated state, there is no need to clean the anaerobic decomposition tank, the aerobic decomposition tank, and the solid-liquid separation tank at all. In addition, only the work of collecting the precipitate in the sludge thickening digestion tank is required, and the maintenance and management of the processing apparatus becomes very easy as compared with the related art.

【図面の簡単な説明】 【図1】本発明処理装置の一実施の形態を示す断面図で
ある。 【符号の説明】 1 シンク 2 粉砕機 3 排水流通管 4 嫌気分解槽 5 嫌気性微生物固定床 6 溢流口 7 第1室の好気分解槽 8 仕切り壁 9 好気性微生物固定床 10 第2室の好気分解槽 11 仕切り壁 12 連通口 13 散気管 14 エアーポンプ 15 移流口 16 固液分離槽 17 排ガス管 18 脱臭装置 19 濾過層 20 放流管 21 移送管 22 ポンプ 23 汚泥濃縮消化槽 24 濾過層 25 分離水移送管
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a sectional view showing an embodiment of the processing apparatus of the present invention. [Description of Signs] 1 sink 2 crusher 3 drainage pipe 4 anaerobic decomposition tank 5 anaerobic microorganism fixed bed 6 overflow 7 aerobic decomposition tank in first room 8 partition wall 9 aerobic microorganism fixed bed 10 second room Aerobic decomposition tank 11 partition wall 12 communication port 13 air diffuser 14 air pump 15 transfer port 16 solid-liquid separation tank 17 exhaust gas pipe 18 deodorizer 19 filtration layer 20 discharge pipe 21 transfer pipe 22 pump 23 sludge concentration digestion tank 24 filtration layer 25 Separation water transfer pipe

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B09B 3/00 C02F 3/30 C02F 11/00 - 11/20 C02F 3/00 C02F 3/02 - 3/10 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) B09B 3/00 C02F 3/30 C02F 11/00-11/20 C02F 3/00 C02F 3/02-3 / Ten

Claims (1)

(57)【特許請求の範囲】 【請求項1】 厨芥を少量の水を加えながら粉砕する粉
砕機と、前記粉砕機での粉砕物を含有する汚水を嫌気性
微生物固定床の存在下で嫌気分解する嫌気分解槽と、前
記嫌気分解槽で嫌気分解された処理水を好気性微生物が
生育・繁殖する流動床の又は固定床の存在下で好気処理
する好気分解槽と、前記好気分解槽の処理水中の懸濁物
質や浮遊物、余剰汚泥等を沈澱させ、上澄水を外部へ放
流する固液分離槽と、前記固液分離槽の沈澱物および処
理水の一部を引き抜き移送する移送手段と、前記移送手
段にて移送された沈澱物および処理水の一部を貯留し、
上澄水を分離して前記好気分解槽に返送することにより
沈澱物の濃縮を図る汚泥濃縮消化槽を備えたことを特徴
とする厨芥含有汚水の処理装置。
(57) [Claims] [Claim 1] A crusher for crushing kitchen garbage while adding a small amount of water, and sewage containing crushed material from the crusher is anaerobically digested in the presence of an anaerobic microorganism fixed bed. An anaerobic decomposition tank for decomposing, an aerobic decomposition tank for aerobically treating the treated water anaerobically decomposed in the anaerobic decomposition tank in the presence of a fluidized bed or a fixed bed in which aerobic microorganisms grow and propagate, A solid-liquid separation tank that precipitates suspended substances and suspended solids, excess sludge, and the like in the treated water of the decomposition tank and discharges the supernatant water to the outside, and pulls out and transfers the precipitate in the solid-liquid separation tank and part of the treated water. Transfer means, and store a part of the precipitate and treated water transferred by the transfer means,
An apparatus for treating garbage-containing sewage, comprising a sludge concentration and digestion tank for separating supernatant liquid and returning it to the aerobic decomposition tank to concentrate precipitates.
JP04669596A 1996-02-07 1996-02-07 Wastewater treatment equipment for kitchen waste Expired - Fee Related JP3398924B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04669596A JP3398924B2 (en) 1996-02-07 1996-02-07 Wastewater treatment equipment for kitchen waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04669596A JP3398924B2 (en) 1996-02-07 1996-02-07 Wastewater treatment equipment for kitchen waste

Publications (2)

Publication Number Publication Date
JPH09206787A JPH09206787A (en) 1997-08-12
JP3398924B2 true JP3398924B2 (en) 2003-04-21

Family

ID=12754526

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04669596A Expired - Fee Related JP3398924B2 (en) 1996-02-07 1996-02-07 Wastewater treatment equipment for kitchen waste

Country Status (1)

Country Link
JP (1) JP3398924B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102476127A (en) * 2010-11-29 2012-05-30 上海万帝环境技术有限公司 Food waste and domestic sewage combined treatment system
CN105152465B (en) * 2015-07-23 2017-09-05 李华 A kind of tower integrated treatment unit for sewage disposal
CN110681462B (en) * 2018-04-26 2021-04-27 赣州市束薪再生资源有限公司 Household garbage treatment device and using method thereof
CN109485209A (en) * 2019-01-10 2019-03-19 立德环保设备制造(广州)有限公司 A kind of O2The integration apparatus of AO technique food and drink wastewater treatment

Also Published As

Publication number Publication date
JPH09206787A (en) 1997-08-12

Similar Documents

Publication Publication Date Title
US4487697A (en) Biological waste-water-treatment method
CA2284740A1 (en) A system for purification of domestic household effluent
JPH10235315A (en) Treatment of fluid organic waste
KR100458564B1 (en) a method and apparatus for wastewater treatment
JP3398924B2 (en) Wastewater treatment equipment for kitchen waste
JPH08117731A (en) Garbage treatment apparatus
AU2003221763A1 (en) Aerobic wastewater management system, apparatus, and method
JPH0839100A (en) Simultaneous treatment of kitchen waste water and garbage
JP3208843B2 (en) Method for treating high-concentration organic wastewater and wastewater treatment equipment used for the method
CN112279459A (en) Toilet sewage treatment method
JP2756657B2 (en) Advanced treatment septic tank
JP2001252682A (en) Sewage treatment method for livestock waste water and apparatus therefor
JPH05337493A (en) Treatment of concentrated organic waste water containing solid
JPH08155488A (en) Combined purification tank and treatment method for garbage, etc.
JP4013125B2 (en) Remodeling method of existing single septic tank to garbage disposal equipment
CN214457489U (en) Domestic sewage treatment device
JPH0623337A (en) Treatment of carbage and kitchen waste water
JP2000005739A (en) Garbage treating apparatus and method for operating garbage treating apparatus
JP3125265B2 (en) Sludge treatment function enhancement system for septic tank
JP3877482B2 (en) Garbage disposal equipment
JP3716461B2 (en) Concentration method in the receiving tank for biological filtration backwash wastewater
JP3288560B2 (en) Membrane separation tank and septic tank
JPH0639391A (en) Method for treating waste water
KR960003926B1 (en) Aerobic excrement tank
CN112811724A (en) Efficient nitrogen and phosphorus removal process for sewage

Legal Events

Date Code Title Description
S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

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

Free format text: PAYMENT UNTIL: 20090221

Year of fee payment: 6

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

Free format text: PAYMENT UNTIL: 20100221

Year of fee payment: 7

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

Free format text: PAYMENT UNTIL: 20100221

Year of fee payment: 7

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313114

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

Free format text: PAYMENT UNTIL: 20100221

Year of fee payment: 7

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

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

Free format text: PAYMENT UNTIL: 20100221

Year of fee payment: 7

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

Free format text: PAYMENT UNTIL: 20110221

Year of fee payment: 8

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

Free format text: PAYMENT UNTIL: 20110221

Year of fee payment: 8

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

Free format text: PAYMENT UNTIL: 20120221

Year of fee payment: 9

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

Free format text: PAYMENT UNTIL: 20120221

Year of fee payment: 9

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313113

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

Free format text: PAYMENT UNTIL: 20120221

Year of fee payment: 9

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

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

Free format text: PAYMENT UNTIL: 20130221

Year of fee payment: 10

LAPS Cancellation because of no payment of annual fees