JPH04108597A - Adjustment of flow amount in sewage septic tank - Google Patents
Adjustment of flow amount in sewage septic tankInfo
- Publication number
- JPH04108597A JPH04108597A JP22770890A JP22770890A JPH04108597A JP H04108597 A JPH04108597 A JP H04108597A JP 22770890 A JP22770890 A JP 22770890A JP 22770890 A JP22770890 A JP 22770890A JP H04108597 A JPH04108597 A JP H04108597A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- sewage
- water level
- treatment
- amt
- 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
- 239000010865 sewage Substances 0.000 title claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 244000005700 microbiome Species 0.000 claims abstract description 11
- 238000005273 aeration Methods 0.000 claims abstract description 5
- 239000010802 sludge Substances 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims abstract 3
- 238000004062 sedimentation Methods 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 7
- 230000007423 decrease Effects 0.000 claims description 6
- 238000002203 pretreatment Methods 0.000 claims description 6
- 238000000746 purification Methods 0.000 claims description 2
- 239000002244 precipitate Substances 0.000 claims 1
- 238000001556 precipitation Methods 0.000 claims 1
- 230000000249 desinfective effect Effects 0.000 abstract description 3
- 239000000725 suspension Substances 0.000 abstract 1
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この考案は汚水浄化槽に関し、汚水浄化槽の改良に関す
る。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] This invention relates to a sewage septic tank, and relates to an improvement of a sewage septic tank.
従来、小型合併浄化槽として沈殿分離第1.2槽または
嫌気濾床槽箱1.2室と流動床槽、接触ばっ気槽、沈殿
槽及び消毒槽等を備え、汚水をこれら槽に順次移流させ
つつ浄化していく汚水浄化槽が知られている。Conventionally, a small combined septic tank is equipped with a sedimentation separation tank No. 1.2 or an anaerobic filter bed tank box No. 1.2, a fluidized bed tank, a contact aeration tank, a sedimentation tank, a disinfection tank, etc., and sewage is sequentially advected to these tanks. Sewage septic tanks are known that purify wastewater.
通常、この種の汚水浄化槽においては汚水の発生時間帯
が偏るため、ピーク流入時に合わせ各処理槽の水位を予
め低くしておく必要があり、このため沈殿分離種箱1.
2室または嫌気濾床槽箱1.2室より後段処理槽である
流動床槽、接触ばっ気槽等への汚水移流をエアリフトポ
ンプ等によって強制的に行うことが採られることがある
(例えば実公昭58−39836号公報)。Normally, in this type of sewage septic tank, the sewage generation time is uneven, so it is necessary to lower the water level in each treatment tank in advance to coincide with the peak inflow.
2 room or anaerobic filter bed box Publication No. 58-39836).
しかしながら、エアリフトポンプ等により移流を行うと
、エアリフトポンプへの空気道大量が一定であるにも係
わらず前段処理槽の水位に応じて後段処理槽への移流量
がかなり大幅に変動する問題があり、例えば第3図に示
すように、空気送入量一定の場合、満水時で10β/分
のものが減衰と共に急激に減少し最低水位ではIff/
分となり流量調整としての効果が減少する。However, when advection is performed using an air lift pump or the like, there is a problem in that although the amount of air passage to the air lift pump is constant, the amount of advection to the downstream treatment tank varies considerably depending on the water level in the upstream treatment tank. For example, as shown in Figure 3, when the air supply rate is constant, 10β/min at full water level decreases rapidly with attenuation, and at the lowest water level Iff/min.
minute, and the effectiveness as a flow rate adjustment decreases.
従って、汚水の大量発生時間帯にあっては前段処理槽の
水位上昇に応して移流量も多くなり、後段処理槽の急激
な水位上昇の結果未処理水の排出や、後段処理槽に流動
床槽がある場合は流動床のオーバーフローを生し排出水
の水質基準を充分に維持出来無い恐れがある問題があっ
た。Therefore, during times when a large amount of sewage is generated, the amount of transferred water increases as the water level in the first stage treatment tank rises, and as a result of the rapid rise in the water level in the second stage treatment tank, untreated water is discharged and flows into the second stage treatment tank. When there is a bed tank, there is a problem that the fluidized bed overflows and the water quality standards of the discharged water cannot be maintained sufficiently.
この発明は上記問題点に鑑み、前段処理槽の水位に係わ
らず処理汚水の移流量を一定となし得、安定した汚水浄
化を行える汚水浄化槽を従供することを目的としてなさ
れたものである。In view of the above-mentioned problems, the present invention has been made with the object of providing a sewage septic tank that can maintain a constant transfer amount of treated sewage regardless of the water level of the pre-treatment tank and can perform stable sewage purification.
〔課題を解決するに至った技術〕
即ち、この発明の汚水浄化槽は、汚水を静置することに
より沈殿分離または嫌気性微生物により処理を行う槽と
、好気性微生物により処理を行う流動床槽又は接触ばっ
気処理槽と、最終的↓こ浮遊汚泥を沈殿させる沈殿槽と
排出液を消毒する消毒槽とを備え、前記沈殿分離または
嫌気性微生物により処理を行う槽より後段処理槽へエア
リフトポンプにより一次処理水を強制移流させて流量調
整をしつつ汚水の浄化処理を行っていく汚水浄化槽にお
いて、前記エアリフトポンプが制御装置により間歇運転
制御され、かつ該間歇運転の間隔が、前段処理槽の水位
が上限水位では粗、水位が低くなるに従い間隔を密とし
水位の上下に係わらず移流量を常時一定としてなること
を特徴とするものである。[Technology that has led to solving the problem] That is, the sewage septic tank of the present invention has two types: a tank in which wastewater is left to stand for sedimentation separation or treatment using anaerobic microorganisms, and a fluidized bed tank or a tank in which treatment is performed using aerobic microorganisms. It is equipped with a contact aeration treatment tank, a settling tank for settling the final suspended sludge, and a disinfection tank for disinfecting the discharged liquid, and is transported from the tank where the sedimentation separation or treatment using anaerobic microorganisms is performed to the downstream treatment tank by an air lift pump. In a sewage septic tank that purifies sewage while adjusting the flow rate by forced advection of primary treated water, the air lift pump is controlled to operate intermittently by a control device, and the interval of the intermittent operation is determined by the water level in the pre-treatment tank. The spacing is coarse at the upper limit water level, and as the water level gets lower, the spacing becomes closer, so that the amount of advection is always constant regardless of whether the water level is up or down.
次にこの発明の詳細な説明する。 Next, this invention will be explained in detail.
第1図はこの考案の実施例の断面図、第2図は実施例の
運転状態を示すグラフである。FIG. 1 is a sectional view of an embodiment of this invention, and FIG. 2 is a graph showing the operating state of the embodiment.
この発明の汚水浄化槽1は、汚水を静置することにより
沈殿分離または嫌気性微生物により処理を行う槽IAと
、好気性微生物により処理を行う流動床槽IB又は接触
ばっ気処理槽ICと、最終的に浮遊汚泥を沈殿させる沈
殿槽IDと排出液を消毒する消毒槽1Eとを備え、沈殿
分離または嫌気性微生物により処理を行う槽IAより後
段処理槽IBまたはICへエアリフトポンプ2により一
次処理水Wを強制移流させて流量調整をしつつ汚水の浄
化処理を行っていく汚水浄化槽1において、エアリフト
ポンプ2が制御装W3により間歇運転制御され、かつ該
間歇運転の間隔が、第2図に示すように前段処理槽IA
の水位が上限水位HWLでは粗、水位が低くなるに従い
間隔を密とし水位の上下に係わらず移流量を常時一定と
なるように構成されている。The sewage septic tank 1 of the present invention includes a tank IA that performs sedimentation separation or treatment using anaerobic microorganisms by leaving sewage still, a fluidized bed tank IB or contact aeration treatment tank IC that performs treatment using aerobic microorganisms, and a final treatment tank IC. It is equipped with a sedimentation tank ID to precipitate suspended sludge and a disinfection tank 1E to disinfect the discharged liquid, and the primary treated water is transferred from tank IA, which performs sediment separation or treatment using anaerobic microorganisms, to a subsequent treatment tank IB or IC by an air lift pump 2. In the sewage septic tank 1 that purifies sewage while adjusting the flow rate by forced advection of W, the air lift pump 2 is controlled to operate intermittently by a control device W3, and the intervals of the intermittent operation are shown in FIG. Pre-treatment tank IA
The water level is coarse at the upper limit water level HWL, and as the water level becomes lower, the intervals are made closer, so that the amount of advection is always constant regardless of whether the water level is up or down.
なお、図中2人はエアリフトポンプ2を駆動するニアブ
ロアを示す。Note that two people in the figure represent near blowers that drive the air lift pump 2.
上記制御装置3での制御モードは第2図に示すように前
段処理槽の最高水位HWLでは瞬間的な駆動で待機時間
Sが長く、水位の低下に伴って駆動時間tが増加し、最
低水位LWLに達すれば運転が停止されリセット状態と
なり、再び最高氷位HWLで上記作動が再開されるよう
にされる。As shown in Fig. 2, the control mode of the control device 3 is such that at the highest water level HWL of the pre-treatment tank, the standby time S is long due to instantaneous driving, and as the water level decreases, the driving time t increases, and at the lowest water level When reaching LWL, the operation is stopped and a reset state is entered, and the above-mentioned operation is restarted again at the highest ice level HWL.
[作用〕
この発明の汚水浄化槽1において、前段処理槽IAの水
位が最高水位HWLとなり汚水の受容量が少なくなれば
、制御装置3により汚水の後段処理槽への強制移流が開
始される。[Function] In the sewage septic tank 1 of the present invention, when the water level of the front-stage treatment tank IA reaches the highest level HWL and the amount of sewage received decreases, the control device 3 starts forced advection of the sewage to the rear-stage treatment tank.
この時、最高水位時HWL時ではエアリフトポンプ2の
駆動時間は短いが前段処理槽IAの水位が高いため一回
の駆動での移流量は大きい、また水位低下に伴いエアリ
フトポンプ2の駆動時間は長くされていくため、結局単
位時間当たりの移流量は略一定とすることができ、後段
処理槽での急激な水位上昇によるオーバーフローやショ
ートバスが防止される。At this time, at the highest water level (HWL), the driving time of the air lift pump 2 is short, but since the water level in the pre-treatment tank IA is high, the amount of transfer in one drive is large, and as the water level decreases, the driving time of the air lift pump 2 is Since the length is increased, the amount of transfer per unit time can be kept approximately constant, and overflow and short bath caused by a sudden rise in water level in the downstream treatment tank can be prevented.
この発明の汚水浄化槽は以上説明したように、汚水移流
量がエアリフトポンプの間歇運転状態の制御により平均
的には一定流量とされているため、後段沈殿槽での処理
水の水位上昇速度が良く防止され未処理水の排出等が防
止されるのである。As explained above, in the sewage septic tank of the present invention, the amount of sewage transferred is kept constant on average by controlling the intermittent operation of the air lift pump, so the water level of the treated water in the downstream settling tank increases at a high rate. This prevents the discharge of untreated water.
第1図はこの考案の実施例の断面図、 第2図は 実施例の制御状態を示すグラフ、 第3図は従来例 ’7/fD ?2[E] Figure 1 is a sectional view of an embodiment of this invention. Figure 2 is A graph showing the control state of the embodiment, Figure 3 is a conventional example '7/fD ? 2 [E]
Claims (1)
微生物により処理を行う槽と、好気性微生物により処理
を行う流動床槽又は接触ばっ気処理槽と、最終的に浮遊
汚泥を沈殿させる沈殿槽とを備え、前記沈殿分離または
嫌気性微生物により処理を行う槽より後段処理槽へエア
リフトポンプにより一次処理水を強制移流させて流量調
整をしつつ汚水の浄化処理を行っていく汚水浄化槽の流
量調整方法において、前記エアリフトポンプが制御装置
により間歇運転制御され、かつ該間歇運転の間隔が、前
段処理槽の水位が上限水位では粗、水位が低くなるに従
い間隔を密とし水位の上下に係わらず移流量を常時一定
としてなることを特徴とする汚水浄化槽の流量調整方法
。(1) A tank that performs sedimentation separation or treatment using anaerobic microorganisms by leaving sewage still, a fluidized bed tank or contact aeration treatment tank that performs treatment using aerobic microorganisms, and a sedimentation tank that ultimately precipitates suspended sludge. A flow rate of a sewage septic tank, which is equipped with a tank and performs purification treatment of sewage while adjusting the flow rate by forcibly advecting the primary treated water from the tank where the treatment is performed using precipitation separation or anaerobic microorganisms to the downstream treatment tank using an air lift pump. In the adjustment method, the air lift pump is controlled to operate intermittently by a control device, and the interval between the intermittent operations is coarse when the water level of the pre-treatment tank is at the upper limit water level, and becomes closer as the water level decreases, regardless of whether the water level is up or down. A method for adjusting the flow rate of a sewage septic tank, characterized in that the amount of advection is kept constant at all times.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22770890A JPH04108597A (en) | 1990-08-28 | 1990-08-28 | Adjustment of flow amount in sewage septic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22770890A JPH04108597A (en) | 1990-08-28 | 1990-08-28 | Adjustment of flow amount in sewage septic tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04108597A true JPH04108597A (en) | 1992-04-09 |
Family
ID=16865111
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22770890A Pending JPH04108597A (en) | 1990-08-28 | 1990-08-28 | Adjustment of flow amount in sewage septic tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04108597A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07124579A (en) * | 1993-11-01 | 1995-05-16 | Kirin Brewery Co Ltd | Purifier tank with flow rate control device |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5839837U (en) * | 1981-06-25 | 1983-03-16 | 宇部興産株式会社 | Plastic parts for vibration welding |
-
1990
- 1990-08-28 JP JP22770890A patent/JPH04108597A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5839837U (en) * | 1981-06-25 | 1983-03-16 | 宇部興産株式会社 | Plastic parts for vibration welding |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07124579A (en) * | 1993-11-01 | 1995-05-16 | Kirin Brewery Co Ltd | Purifier tank with flow rate control device |
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