JPH0253118B2 - - Google Patents
Info
- Publication number
- JPH0253118B2 JPH0253118B2 JP56142907A JP14290781A JPH0253118B2 JP H0253118 B2 JPH0253118 B2 JP H0253118B2 JP 56142907 A JP56142907 A JP 56142907A JP 14290781 A JP14290781 A JP 14290781A JP H0253118 B2 JPH0253118 B2 JP H0253118B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- human waste
- denitrification
- tank
- sludge
- 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 - Lifetime
Links
- 239000007788 liquid Substances 0.000 claims description 44
- 238000000034 method Methods 0.000 claims description 34
- 239000010800 human waste Substances 0.000 claims description 29
- 239000010802 sludge Substances 0.000 claims description 29
- 238000005273 aeration Methods 0.000 claims description 19
- 238000000926 separation method Methods 0.000 claims description 2
- 239000004744 fabric Substances 0.000 description 8
- 239000000706 filtrate Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000029087 digestion Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000005192 partition Methods 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 210000002700 urine Anatomy 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000852 hydrogen donor Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
- Treatment Of Biological Wastes In General (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Description
【発明の詳細な説明】
この発明は、浄化槽汚泥およびし尿を同時に処
理するための方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for simultaneously treating septic tank sludge and human waste.
浄化槽汚泥をし尿処理施設で処理する場合、こ
の両者を最初から混合してしまうか、あるいは浄
化槽汚泥を汚泥処理系に流入させることが一般に
行なわれている。しかしこのような処理形態は、
浄化槽汚泥とし尿の両方を効率よく処理するもの
とはいえない。 When treating septic tank sludge in a human waste treatment facility, it is common practice to mix the two from the beginning or to flow the septic tank sludge into a sludge treatment system. However, this type of processing
It cannot be said that it efficiently processes both septic tank sludge and urine.
この発明は、混入された浄化槽汚泥がし尿の処
理の阻害要因とならないばかりでなく、し尿の脱
窒処理の効率をかえつて向上させることができる
処理方法を提供することを目的としている。 An object of the present invention is to provide a treatment method in which mixed septic tank sludge not only does not become an impediment to the treatment of human waste, but also improves the efficiency of denitrification treatment of human waste.
つぎにこの発明方法の工程の一例を図面にした
がつて説明する。第1図に示す工程において、し
尿は、硝化槽1、脱窒槽2およびばつ気槽3を順
次に通過する間に所定の処理を受けたのち沈澱槽
4に送られ、ここで活性汚泥の沈澱分離が行なわ
れ、上澄液が処理水として排出される。また沈澱
汚泥の一部は硝化槽1に返送汚泥として返送さ
れ、残部は余剰汚泥として排出される。このプロ
セスは通常のし尿処理プロセスとして一般的であ
るので、その詳細な説明は省略する。 Next, an example of the steps of the method of this invention will be explained with reference to the drawings. In the process shown in Fig. 1, human waste passes through a nitrification tank 1, a denitrification tank 2, and an aeration tank 3 in order, and after undergoing prescribed treatment, is sent to a settling tank 4, where it is deposited into activated sludge. Separation takes place and the supernatant liquid is discharged as treated water. Further, a part of the settled sludge is returned to the nitrification tank 1 as return sludge, and the remainder is discharged as surplus sludge. Since this process is common as a normal human waste treatment process, a detailed explanation thereof will be omitted.
一方、し尿とともに処理される浄化槽汚泥は、
この発明方法においては、まず遠心濃縮機5に導
入され、ここで固形物の濃縮が行なわれる。そし
て濃縮液は脱窒槽2に送られ、分離液はばつ気槽
3に送られる。 On the other hand, septic tank sludge, which is treated together with human waste,
In the method of this invention, the solids are first introduced into the centrifugal concentrator 5, where the solids are concentrated. The concentrated liquid is then sent to the denitrification tank 2, and the separated liquid is sent to the aeration tank 3.
脱窒槽2内では、硝化槽1内でBOD除去と硝
酸化を受けた液体に対する脱窒処理が嫌気性条件
のもとで行なわれており、ここに遠心濃縮機5か
ら浄化槽汚泥の濃縮液が添加されると、硝化槽1
から送られた液体中の溶存酸素は速やかに消費さ
れる。またこの濃縮液は脱窒反応を進行させる必
要な炭素源となる。この2つの理由のために、脱
窒槽2内で行なわれる脱窒反応の速度は著るしく
上昇する。さらに遠心濃縮機5で分離された分離
液はばつ気槽3に送られ、脱窒槽2から脱窒液と
ともに、残留BODを除去するためのばつ気処理
を受ける。 In the denitrification tank 2, the denitrification process for the liquid that has undergone BOD removal and nitrification in the nitrification tank 1 is carried out under anaerobic conditions, and the concentrated liquid of septic tank sludge is supplied from the centrifugal concentrator 5. When added, nitrification tank 1
Dissolved oxygen in the liquid sent from the tank is quickly consumed. This concentrated liquid also serves as a necessary carbon source for the denitrification reaction to proceed. Due to these two reasons, the rate of the denitrification reaction carried out in the denitrification tank 2 increases significantly. Further, the separated liquid separated by the centrifugal concentrator 5 is sent to the aeration tank 3, and is subjected to aeration treatment together with the denitrification liquid from the denitrification tank 2 to remove residual BOD.
なお硝化槽1に供給する前に、し尿を嫌気性消
化槽内であらかじめ消化処理し、その消化脱離液
をそのまま、あるいは若干希釈してから硝化槽1
に供給してもよい。 Before supplying the human waste to the nitrification tank 1, the human waste is digested in an anaerobic digestion tank, and the digested and desorbed liquid is sent as is or after being slightly diluted.
may be supplied to
遠心濃縮機5はベカンター形のものでもよいが
好適なものの具体的な構造の一例を第2図に示
す。第2図において符号11で示すハウジング内
には、垂直な回転軸12に支持されたバスケツト
13が収容され、このバスケツト13の内面に沿
つて濾布14が配置されている。このバスケツト
13および濾布14は、外部からプーリ15を介
して回転軸12に供給された動力によつて高速回
転する。そして処理すべき液体は、供給パイプ1
6を経て濾布14の中心部に供給される。回転バ
スケツト13および濾布14は上下を逆にした円
鍾台形をなし、そして高速回転しているので、汚
水中の液分は濾布14およびバスケツト13の小
孔を遠心力の作用で通過して濾液室17内に放射
方向に放出され、固形分は濾布14上を回転中心
から離れる方向(第2図の上方)に遠心力の作用
で移動したのち、濾液室17から隔壁18で分離
された濃縮液室19内に放出される。これによつ
て汚水中のSSの分離が効率よく行なわれ、SSを
多量に含む濃縮液と濾液とがそれぞれパイプ20
及び21を経て個別に取出される。 Although the centrifugal concentrator 5 may be of a becanter type, an example of a preferred specific structure is shown in FIG. A basket 13 supported by a vertical rotating shaft 12 is accommodated within the housing designated by the reference numeral 11 in FIG. 2, and a filter cloth 14 is disposed along the inner surface of the basket 13. The basket 13 and the filter cloth 14 are rotated at high speed by power supplied from the outside to the rotating shaft 12 via the pulley 15. The liquid to be treated is supplied to the supply pipe 1
6 and is supplied to the center of the filter cloth 14. The rotating basket 13 and the filter cloth 14 have an upside-down trapezoidal shape and are rotating at high speed, so the liquid in the wastewater passes through the small holes of the filter cloth 14 and the basket 13 due to the action of centrifugal force. The solids are released into the filtrate chamber 17 in the radial direction, and after moving on the filter cloth 14 in the direction away from the center of rotation (upward in FIG. 2) due to the action of centrifugal force, the solids are separated from the filtrate chamber 17 by the partition wall 18. The concentrated liquid is discharged into the concentrated liquid chamber 19. As a result, SS in the wastewater is efficiently separated, and the concentrated liquid and filtrate containing a large amount of SS are separated from pipe 20.
and 21, and are taken out individually.
なお符号22は、多数のノズル23を設けた洗
浄パイプを示し、濾布14等が目詰りしたとき
に、作業を中断して洗浄を行なう際に使用され
る。 Reference numeral 22 designates a cleaning pipe provided with a large number of nozzles 23, which is used to interrupt the operation and perform cleaning when the filter cloth 14 or the like becomes clogged.
第3図および第4図はそれぞれこの発明方法の
他の工程を示している。まず第3図に示した工程
において、し尿はそのまま脱窒槽21に導入さ
れ、ここで循環液中の硝酸と、流入し尿および遠
心濃縮機5からの濃縮液中に含まれているBOD
源を利用して効率よく脱窒処理される。また遠心
濃縮機5からの分離液は、脱窒処理液とともに硝
化槽22に送られ、BOD除去および硝酸化がな
される。そして硝化液の一部は循環液として脱窒
槽21に返送され、残部は沈澱槽4に送られる。 3 and 4 respectively show other steps of the method of the invention. First, in the process shown in FIG. 3, human waste is directly introduced into the denitrification tank 21, where nitric acid in the circulating fluid and BOD contained in the inflowing human waste and the concentrated liquid from the centrifugal concentrator 5 are removed.
Denitrification treatment is carried out efficiently using the source. Further, the separated liquid from the centrifugal concentrator 5 is sent to the nitrification tank 22 together with the denitrification treatment liquid, where BOD is removed and nitrification is performed. A part of the nitrification liquid is returned to the denitrification tank 21 as a circulating liquid, and the remaining part is sent to the precipitation tank 4.
さらに第4図に示した例では、し尿は脱窒槽3
1内でばつ気されながら硝化および脱窒処理され
る。この脱窒槽31には、遠心濃縮機5から送ら
れた浄化槽汚泥の濃縮液も導入されるので、その
内部のMLSSは高レベルとなり、ばつ気を行なつ
ても溶存酸素は0.5mg/以下に保たれる。ばつ
気液は遠心濃縮機32に送られて濃縮され、濃縮
液はばつ気槽31に返送され、分離液は、前記の
遠心濃縮機5からの分離液とともに付着ばつ気槽
33に送られる。この付着ばつ気槽33内では、
適当な濾材に微生物を付着させた生物濾床を用い
てばつ気処理が行なわれ、ばつ気液の一部は脱窒
槽31に循環液として返送され、残部は沈澱槽4
に送られる。また沈澱槽4で分離された沈澱汚泥
の一部は、遠心濃縮機5に送られ、浄化槽汚泥と
ともに濃縮されたのちばつ気槽31に戻される。 Furthermore, in the example shown in Fig. 4, human waste is stored in the denitrification tank 3
Nitrification and denitrification are carried out in a chamber with aeration. Since the concentrated liquid of the septic tank sludge sent from the centrifugal concentrator 5 is also introduced into the denitrification tank 31, the MLSS inside it is at a high level, and even when aeration is performed, dissolved oxygen remains below 0.5mg/. It is maintained. The atomized liquid is sent to the centrifugal concentrator 32 and concentrated, the concentrated liquid is returned to the aeration tank 31, and the separated liquid is sent to the attached aeration tank 33 together with the separated liquid from the centrifugal concentrator 5. Inside this adhesion aeration tank 33,
Aeration treatment is performed using a biological filter bed in which microorganisms are attached to a suitable filter medium, and a part of the atomized liquid is returned to the denitrification tank 31 as a circulating liquid, and the remainder is sent to the sedimentation tank 4.
sent to. Further, a part of the settled sludge separated in the settling tank 4 is sent to the centrifugal concentrator 5, where it is concentrated together with the septic tank sludge, and then returned to the aeration tank 31.
なお第3図および第4図に示した例において
も、第1図の場合と同様に、し尿をあらかじめ嫌
気性消化処理して得た脱離液を処理対象としても
よい。 In the examples shown in FIGS. 3 and 4, as in the case of FIG. 1, the desorbed liquid obtained by previously subjecting human waste to anaerobic digestion may be used as the treatment target.
以上のように、この発明によれば、し尿を嫌気
性条件下で脱窒処理する脱窒工程と、この脱窒工
程からの脱窒液を導入してばつ気処理するばつ気
工程とを備え、し尿と浄化槽汚泥とを同時に処理
するし尿処理プロセスにおいて、上記浄化槽汚泥
を遠心濃縮機で濃縮液と分離液とに分離し、その
濃縮液を上記し尿処理プロセスの脱窒工程に送
り、且つ、上記分離液をばつ気工程に送るプロセ
スとしたので、上記脱窒工程では、流入し尿中の
有機物の脱窒反応に対し上記遠心濃縮機からの浄
化槽汚泥の濃縮液を水素供与体として有効利用で
き、このため、し尿処理と浄化槽汚泥処理とを同
時に且つ非常に効率的に行うことができる。 As described above, the present invention includes a denitrification process in which human waste is denitrified under anaerobic conditions, and an aeration process in which the denitrification liquid from this denitrification process is introduced and aerated. , in a human waste treatment process in which human waste and septic tank sludge are treated simultaneously, the septic tank sludge is separated into a concentrated liquid and a separated liquid by a centrifugal concentrator, and the concentrated liquid is sent to the denitrification step of the human waste treatment process, and Since the separated liquid is sent to the aeration process, the concentrated liquid of the septic tank sludge from the centrifugal concentrator can be effectively used as a hydrogen donor in the denitrification reaction of organic matter in the inflowing human urine in the denitrification process. Therefore, human waste treatment and septic tank sludge treatment can be performed simultaneously and very efficiently.
即ち、し尿処理プロセスの脱窒工程に、遠心濃
縮機から浄化槽汚泥の濃縮液が供給されることに
よつて、上記脱窒工程での汚泥濃度が高くなるの
で、上記遠心濃縮機による浄化槽汚泥の濃縮液を
し尿の脱窒に有効利用でき、その脱窒処理が効率
的に行われ、し尿処理プロセス全体としての処理
効率が従来に比して著しく向上するという効果が
ある。 That is, by supplying concentrated liquid of septic tank sludge from the centrifugal concentrator to the denitrification process of the human waste treatment process, the sludge concentration in the denitrification process increases, so that the concentration of septic tank sludge by the centrifugal concentrator increases. The concentrated liquid can be effectively used for denitrifying human waste, the denitrification treatment is efficiently performed, and the efficiency of the entire human waste treatment process is significantly improved compared to the conventional method.
従つて、この発明では、搬入し尿量と浄化槽汚
泥量との比率から浄化槽汚泥量が多い場合であつ
ても、それらの脱窒を主目的としたし尿処理と浄
化槽汚泥処理とを一つのプロセスで同時に、しか
も非常に効率的に行うことができるという効果が
ある。 Therefore, in this invention, even if the amount of septic tank sludge is large in terms of the ratio between the amount of night soil carried in and the amount of septic tank sludge, human waste treatment and septic tank sludge treatment with the main purpose of denitrification can be performed in one process. At the same time, it has the effect of being very efficient.
第1図はこの発明方法の工程の一例を示すフロ
ーシート、第2図は第1図の工程で用いられた遠
心濃縮機の構造の一例を示す概略的縦断面図、第
3図および第4図はそれぞれ他の工程を示すフロ
ーシートである。
1……硝化槽、2……脱窒槽、3……ばつ気
槽、4……沈澱槽、5……遠心濃縮機、11……
ハウジング、12……回転軸、13……バスケツ
ト、14……濾布、16……供給パイプ、17…
…濾液室、18……隔壁、19……濃縮液室、2
1……脱窒槽、22……硝化槽、31……脱窒
槽、32……遠心濃縮機、33……付着ばつ気
槽。
FIG. 1 is a flow sheet showing an example of the process of the method of the present invention, FIG. 2 is a schematic vertical sectional view showing an example of the structure of a centrifugal concentrator used in the process of FIG. Each figure is a flow sheet showing other steps. 1... Nitrification tank, 2... Denitrification tank, 3... Aeration tank, 4... Sedimentation tank, 5... Centrifugal concentrator, 11...
Housing, 12... Rotating shaft, 13... Basket, 14... Filter cloth, 16... Supply pipe, 17...
...Filtrate chamber, 18...Partition wall, 19...Concentrate chamber, 2
1... denitrification tank, 22... nitrification tank, 31... denitrification tank, 32... centrifugal concentrator, 33... adhesion aeration tank.
Claims (1)
と、この脱窒工程からの脱窒液を導入してばつ気
処理するばつ気工程とを備え、し尿と浄化槽汚泥
を同時に処理するし尿処理プロセスにおいて、上
記浄化槽汚泥を遠心濃縮機で濃縮液と分離液とに
分離し、その濃縮液を上記し尿処理プロセスの脱
窒工程に送り、且つ、上記分離液をばつ気工程に
送ることを特徴とするし尿および浄化槽汚泥の処
理方法。 2 上記し尿処理プロセスのばつ気工程は付着ば
つ気槽内で行われ、この付着ばつ気槽内に、脱窒
液を固液分離処理した処理液が供給される特許請
求の範囲第1項記載のし尿および浄化槽汚泥の処
理方法。[Scope of Claims] 1. A denitrification process that denitrifies human waste under anaerobic conditions, and an aeration process that introduces and aerates the denitrifying liquid from this denitrification process, and removes human waste from a septic tank. In the human waste treatment process in which sludge is treated at the same time, the septic tank sludge is separated into a concentrated liquid and a separated liquid using a centrifugal concentrator, the concentrated liquid is sent to the denitrification step of the human waste treatment process, and the separated liquid is removed. A method for treating human waste and septic tank sludge, characterized by sending it to an air process. 2. According to claim 1, the aeration step of the human waste treatment process is carried out in an aeration tank, and a treatment liquid obtained by solid-liquid separation of denitrification liquid is supplied into the aeration tank. How to treat human waste and septic tank sludge.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14290781A JPS5843296A (en) | 1981-09-10 | 1981-09-10 | Treatment of night soil and sludge from purifying tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14290781A JPS5843296A (en) | 1981-09-10 | 1981-09-10 | Treatment of night soil and sludge from purifying tank |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5843296A JPS5843296A (en) | 1983-03-12 |
JPH0253118B2 true JPH0253118B2 (en) | 1990-11-15 |
Family
ID=15326382
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14290781A Granted JPS5843296A (en) | 1981-09-10 | 1981-09-10 | Treatment of night soil and sludge from purifying tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5843296A (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4774491B2 (en) * | 2006-06-09 | 2011-09-14 | 株式会社西原環境 | Solid-liquid separation system |
JP6154250B2 (en) * | 2013-08-28 | 2017-06-28 | 三菱重工環境・化学エンジニアリング株式会社 | Organic waste treatment method and organic waste treatment facility |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5586594A (en) * | 1978-12-25 | 1980-06-30 | Kubota Ltd | Treating method of water for denitrification |
JPS55104694A (en) * | 1979-01-30 | 1980-08-11 | Nippon Kokan Kk <Nkk> | Treatment of purification tank sludge |
-
1981
- 1981-09-10 JP JP14290781A patent/JPS5843296A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5586594A (en) * | 1978-12-25 | 1980-06-30 | Kubota Ltd | Treating method of water for denitrification |
JPS55104694A (en) * | 1979-01-30 | 1980-08-11 | Nippon Kokan Kk <Nkk> | Treatment of purification tank sludge |
Also Published As
Publication number | Publication date |
---|---|
JPS5843296A (en) | 1983-03-12 |
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