JPS63130196A - Method and apparatus for treating waste water - Google Patents
Method and apparatus for treating waste waterInfo
- Publication number
- JPS63130196A JPS63130196A JP27545486A JP27545486A JPS63130196A JP S63130196 A JPS63130196 A JP S63130196A JP 27545486 A JP27545486 A JP 27545486A JP 27545486 A JP27545486 A JP 27545486A JP S63130196 A JPS63130196 A JP S63130196A
- Authority
- JP
- Japan
- Prior art keywords
- reaction tank
- water
- solid
- pump
- anaerobic reaction
- 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.)
- Pending
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title abstract description 17
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 33
- 238000011282 treatment Methods 0.000 claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 238000000926 separation method Methods 0.000 claims abstract description 9
- 239000007787 solid Substances 0.000 claims abstract description 8
- 238000004065 wastewater treatment Methods 0.000 claims 2
- 238000011144 upstream manufacturing Methods 0.000 claims 1
- 239000010802 sludge Substances 0.000 abstract description 7
- 239000000126 substance Substances 0.000 abstract description 4
- 241001148470 aerobic bacillus Species 0.000 abstract 1
- 239000012528 membrane Substances 0.000 description 8
- 230000001105 regulatory effect Effects 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用公費〕
本発明は、公共下水道、産業廃水等、有機性を有する廃
水の処理方法及びその装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Public funds for industrial use] The present invention relates to a method and apparatus for treating organic wastewater such as public sewerage and industrial wastewater.
(従来の技術〕
従来の有機性廃水の処理として行なわれていた処理方法
としては、第2図に示すように、調整槽αからの原水を
、好気性反応槽すで活性汚泥法により処理した後、半透
膜槽Cでの半透膜法゛によシ処理を行なう方法(例えば
環境施設1985年A20.56〜57頁)、または、
第3図に示すように、調整槽aからの原水を、嫌気性反
応槽dで嫌気性処理法による処理した後、好気反応槽す
で好気処理法にて処理し、ついで沈殿池Cを経て処理水
として排出する方法(例えば下水道協会誌1985年、
16268 、νoL 23.28〜37頁)等が公表
されている。(Conventional technology) As shown in Figure 2, the conventional treatment method for organic wastewater is that the raw water from the adjustment tank α is treated by the activated sludge method in the aerobic reaction tank. After that, a method of performing semipermeable membrane treatment in a semipermeable membrane tank C (for example, Environmental Facility 1985 A20, pp. 56-57), or
As shown in Figure 3, the raw water from the adjustment tank a is treated in the anaerobic reaction tank d using the anaerobic treatment method, and then treated in the aerobic reaction tank using the aerobic treatment method, and then in the settling tank C. method of discharging it as treated water after
16268, νoL 23.28-37), etc. have been published.
特に近年余栄汚泥発生量の少ない嫌気性処理・特に流動
床タイプが注目されている。また嫌気性処理の後に好気
性処理を行ない、廃水中のBOD値を下げる工夫がなさ
れている。また半透膜、主として限外濾過膜は通常の処
理における沈殿池の代替手段として用いられるものであ
り、そのコンパクト性から近年実施例が多い。Particularly in recent years, anaerobic treatment, especially the fluidized bed type, which produces less Yoei sludge, has been attracting attention. Further, an attempt has been made to perform aerobic treatment after anaerobic treatment to lower the BOD value in wastewater. In addition, semipermeable membranes, mainly ultrafiltration membranes, are used as an alternative to settling tanks in ordinary treatments, and have been used in many recent years due to their compactness.
上記のことから、上記両従来例を組合せた方法、すなわ
ち、第4図に示す経路にて廃水を処理する方法が現在と
られている。In light of the above, a method that combines both of the above conventional examples, ie, a method of treating wastewater through the route shown in FIG. 4, is currently being used.
すなわち、調整槽aからの廃水は嫌気性反応槽d、好気
性反応槽すを直列状に通過した後、中間槽Cに入り、こ
こからさらに半透膜からなる固液分離装置fを経て処理
水として排出されるようになっている。That is, the wastewater from the adjustment tank a passes through an anaerobic reaction tank d and an aerobic reaction tank in series, then enters an intermediate tank C, from which it is further processed through a solid-liquid separator f consisting of a semipermeable membrane. It is designed to be discharged as water.
上記従来の方法では、効率があまり高くなかった。また
汚泥の発生量が多かった。また上記方法を実施する装置
にあっては、中間槽が必要で装置が大がかりとなると共
に、使用するポンプの数もP1〜psと最低5個は必要
となり、その数が多かった。The efficiency of the above conventional method was not very high. Also, a large amount of sludge was generated. Moreover, in the apparatus for carrying out the above method, an intermediate tank is required, which makes the apparatus large-scale, and the number of pumps used is also large, P1 to ps, which is at least five.
〔問題点を解決するための手段及び作用〕本発明は上記
のことにかんがみなされたもので、調整槽からの廃水を
高い効率で処理できると共に、汚泥の発生量を少なくす
ることができるようにした廃水の処理方法を提供しよう
とするものであシ、廃水を嫌気性反応槽にて嫌気性反応
処理をした後、固液分離装置で固形分と処理水と非処理
水とに分離し、ついで固液分離装置よりの未処理水を好
気性反応槽にて好気性反応処理をしてから再び嫌気性反
応槽にて嫌気性反応処理させるようにしている。[Means and effects for solving the problems] The present invention has been made in consideration of the above-mentioned problems, and has been developed to enable highly efficient treatment of wastewater from a regulating tank and to reduce the amount of sludge generated. The purpose of this project is to provide a method for treating wastewater, which involves subjecting wastewater to anaerobic reaction treatment in an anaerobic reaction tank, and then separating it into solid content, treated water, and untreated water in a solid-liquid separator. Next, the untreated water from the solid-liquid separator is subjected to an aerobic reaction treatment in an aerobic reaction tank, and then subjected to an anaerobic reaction treatment again in an anaerobic reaction tank.
そして上記方法を実施するために、コンパクトに、かつ
使用するポンプの数を少なく、さらに装置内の流量バラ
ンスを容易に調整することができるようにした装置を提
供しようとするもので、その構成は、ポンプを介装した
流入路にて流入側を調整槽に接続した嫌気性反応槽と、
流出側を上記嫌気性反応槽の流入側にポンプを介して接
続した好気性反応槽と、上記嫌気性反応槽の流出側と好
気性反応槽の流入側とを接続する流路内にその上流側か
ら順次介装されたポンプと、固液分離装置と、減圧装置
とから構成されており、固液分離装置よりの未処理水は
好気性反応槽にて好気性反応処理されてから再び嫌気性
反応槽にて嫌気性処理される。装置内の流量バランスは
両反応槽間に介装したポンプと減圧装置の圧力、流量を
調整することにより制御される。In order to carry out the above method, the present invention aims to provide a device that is compact, uses a small number of pumps, and can easily adjust the flow balance within the device, and its configuration is as follows: , an anaerobic reaction tank whose inflow side is connected to a regulating tank through an inflow channel equipped with a pump;
an aerobic reaction tank whose outflow side is connected to the inflow side of the anaerobic reaction tank via a pump; It consists of a pump, a solid-liquid separator, and a pressure reducing device, which are installed sequentially from the side.The untreated water from the solid-liquid separator is subjected to aerobic reaction treatment in an aerobic reaction tank, and then anaerobic again. Anaerobic treatment is performed in a reaction tank. The flow balance within the apparatus is controlled by adjusting the pressure and flow rate of a pump and pressure reducing device interposed between both reaction vessels.
本発明の実施例を第1図に基づいて説明する。 An embodiment of the present invention will be described based on FIG.
調整槽1に流入した原水はポンプ2により流入路3を経
て嫌気性反応槽4に入り、ここで嫌気性微生物によ#)
BOD成分、SS成分、窒素、リン等の有機質等の一部
を処理する。嫌気性反応槽4を出た廃水は流出路5を経
てポンプ6にて加圧されて固液分離装置7に圧送される
。この固液分離装置7はフィルタ、MF膜等からなる第
1分離手段7Gと、比較的小さな粒子を除去する限外濾
過膜等のクロスフロー型の膜よシなる第2分離手段7b
とからなり、ポンプ6にて嫌気性反応槽4よシ圧送され
てきた廃水はまず第1分離手段7aにて固液が分離され
、ここで分離された汚泥等の固形分は図示しない公知の
手段にて装置外へ排出される。The raw water that has flowed into the adjustment tank 1 enters the anaerobic reaction tank 4 via the inlet channel 3 by the pump 2, where it is treated with anaerobic microorganisms.
Some of the BOD components, SS components, and organic substances such as nitrogen and phosphorus are treated. The wastewater that has exited the anaerobic reaction tank 4 is pressurized by a pump 6 through an outflow path 5 and is then pumped to a solid-liquid separator 7 . This solid-liquid separator 7 includes a first separation means 7G made of a filter, MF membrane, etc., and a second separation means 7B made of a cross-flow type membrane such as an ultrafiltration membrane for removing relatively small particles.
The wastewater pumped from the anaerobic reaction tank 4 by the pump 6 is first separated into solid and liquid by the first separation means 7a, and the solid content such as sludge separated here is separated by a known method (not shown). It is discharged out of the device by means.
第1分離手段7Gを通過した廃水は第2分離手段7bに
てさらに濾過され、この濾過水は処理水となって処理水
路8よシ外部へ排出される。The wastewater that has passed through the first separation means 7G is further filtered by the second separation means 7b, and this filtered water becomes treated water and is discharged to the outside through the treatment waterway 8.
固液分離装置7にて分離されなかった未処理水は流出路
9に介装した減圧装置IOで圧力が適当なレベルまで低
下されてから好気性反応槽ll内に流入し、ここで好気
性微生物により残った有機質等が除去される。このとき
好気性反応槽11へは吸気路12よりエアが供給されて
いる。The untreated water that has not been separated by the solid-liquid separator 7 has its pressure reduced to an appropriate level by the pressure reducing device IO installed in the outflow path 9, and then flows into the aerobic reaction tank 11, where it is aerobic. Remaining organic substances are removed by microorganisms. At this time, air is supplied to the aerobic reaction tank 11 from the air intake path 12.
好気性反応槽11を通過した廃水は流出路13を通9、
かつポンプ14にて加圧されて上記流入路3と合流して
嫌気性反応槽4内に流入され、原水と共に再び上記処理
がなされ、顆次固液分離装置7よシ処理水として処理水
路8へ排出される。The wastewater that has passed through the aerobic reaction tank 11 passes through the outflow passage 13 9.
The water is pressurized by the pump 14, merges with the inflow channel 3, and flows into the anaerobic reaction tank 4, where it is again subjected to the above treatment together with the raw water, and then passed through the granular solid-liquid separator 7 to the treated water channel 8 as treated water. is discharged to.
上記処理における流量バランスは、調整槽1より流入す
る流入量Q1と固液分離装置7より排出される処理水量
Q2とは同じになるようにする。The flow rate balance in the above treatment is such that the inflow amount Q1 flowing from the adjustment tank 1 and the amount Q2 of treated water discharged from the solid-liquid separator 7 are the same.
このときの流量の調整はポンプ6と減圧装置10の圧力
、流量制御することによってなされる。The flow rate at this time is adjusted by controlling the pressure and flow rate of the pump 6 and pressure reducing device 10.
上記嫌気性反応tlI4と好気性反応槽11は流動床構
成となっている。The anaerobic reaction tlI4 and the aerobic reaction tank 11 have a fluidized bed configuration.
本発明方法によれば、廃水を嫌気性反応槽4にて嫌気性
反応処理をした後、固液分離装置7で固形分と処理水と
未処理水とに分離し、ついで固液分離装置7よりの未処
理水を好気性反応槽11にて好気性反応処理をしてから
再び嫌気性反応槽4にて嫌気性反応させるようにしたか
ら、調整槽1からの廃水を高い効率で処理できると共に
、汚泥の発生量を少なくすることができる。According to the method of the present invention, after wastewater is subjected to anaerobic reaction treatment in the anaerobic reaction tank 4, it is separated into solid content, treated water, and untreated water in the solid-liquid separator 7, and then the solid-liquid separator 7 Since the untreated water is subjected to an aerobic reaction treatment in the aerobic reaction tank 11 and then subjected to an anaerobic reaction again in the anaerobic reaction tank 4, the wastewater from the adjustment tank 1 can be treated with high efficiency. At the same time, the amount of sludge generated can be reduced.
また上記方法を実施するための装置は、ポンプを介装し
た流入路にて流入側調整槽1に接続した嫌気反応槽4と
、流出側を上記嫌気性反応槽4の流入側にポンプを介し
て接続した好気性反応槽11と、上記嫌気性反応槽4の
流出側と好気性反応槽11の流入側とを接続する流入路
にその上流側から屓次介装されたポンプと、固液分離装
置と、減圧装置とから構成されているから、中間槽が不
要となってコンパクトに構成でき、また装置内に組込む
ポンプも3個と少なくすることができる。また装置内の
流量バランスは両反応槽4,11間に介装したポンプと
減圧装置にて容易に調整することができる。Furthermore, the apparatus for carrying out the above method includes an anaerobic reaction tank 4 connected to the inflow side regulating tank 1 through an inflow path equipped with a pump, and an outflow side connected to the inflow side of the anaerobic reaction tank 4 via a pump. an aerobic reaction tank 11 that is connected to Since it is composed of a separation device and a pressure reducing device, an intermediate tank is not required, and the structure can be made compact, and the number of pumps to be incorporated into the device can be reduced to three. Further, the flow balance within the apparatus can be easily adjusted using a pump and a pressure reducing device interposed between both reaction vessels 4 and 11.
第1図は本発明の実施態櫟を示す説明図、第2図から第
4図は従来例を示す説明図である。
1は調整槽、2,6.14はポンプ、3は流入路、4は
嫌気性反応槽、7は固液分離装置、lOは減圧装置、1
1は好気性反応槽。FIG. 1 is an explanatory diagram showing an embodiment of the present invention, and FIGS. 2 to 4 are explanatory diagrams showing conventional examples. 1 is a regulating tank, 2, 6.14 is a pump, 3 is an inflow path, 4 is an anaerobic reaction tank, 7 is a solid-liquid separation device, 1O is a pressure reducing device, 1
1 is an aerobic reaction tank.
Claims (2)
後、固液分離装置7で固形分と処理水と未処理水とに分
離し、ついで固液分離装置7よりの未処理水を好気性反
応槽11にて好気性反応処理をしてから再び嫌気性反応
槽4にて嫌気性反応処理するようにしたことを特徴とす
る廃水の処理方法。(1) After the wastewater is subjected to anaerobic reaction treatment in the anaerobic reaction tank 4, it is separated into solid content, treated water, and untreated water in the solid-liquid separator 7, and then the untreated water is separated from the solid-liquid separator 7. A wastewater treatment method characterized in that water is subjected to an aerobic reaction treatment in an aerobic reaction tank 11 and then subjected to an anaerobic reaction treatment again in an anaerobic reaction tank 4.
1に接続した嫌気性反応槽4と、流出側を上記嫌気性反
応槽の流入側にポンプ14を介して接続した好気性反応
槽11と、上記嫌気性反応槽4の流出側と好気性反応槽
11の流入側とを接続する流路内にその上流側から順次
介装されたポンプ6と、固液分離装置7と、減圧装置1
0とからなることを特徴とする廃水の処理装置。(2) An anaerobic reaction tank 4 whose inflow side is connected to the adjustment tank 1 through an inflow channel 3 equipped with a pump 2, and a preferred system whose outflow side is connected to the inflow side of the anaerobic reaction tank via a pump 14. A pneumatic reaction tank 11, a pump 6, and a solid-liquid separation device 7, which are sequentially installed in a flow path connecting the outflow side of the anaerobic reaction tank 4 and the inflow side of the aerobic reaction tank 11 from the upstream side thereof. and pressure reducing device 1
A wastewater treatment device comprising: 0.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27545486A JPS63130196A (en) | 1986-11-20 | 1986-11-20 | Method and apparatus for treating waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP27545486A JPS63130196A (en) | 1986-11-20 | 1986-11-20 | Method and apparatus for treating waste water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63130196A true JPS63130196A (en) | 1988-06-02 |
Family
ID=17555750
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP27545486A Pending JPS63130196A (en) | 1986-11-20 | 1986-11-20 | Method and apparatus for treating waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63130196A (en) |
-
1986
- 1986-11-20 JP JP27545486A patent/JPS63130196A/en active Pending
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