JPS59179192A - Waste water treating apparatus - Google Patents
Waste water treating apparatusInfo
- Publication number
- JPS59179192A JPS59179192A JP58054044A JP5404483A JPS59179192A JP S59179192 A JPS59179192 A JP S59179192A JP 58054044 A JP58054044 A JP 58054044A JP 5404483 A JP5404483 A JP 5404483A JP S59179192 A JPS59179192 A JP S59179192A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- aeration
- chamber
- contact plate
- air
- 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
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
- Biological Treatment Of Waste Water (AREA)
Abstract
Description
【発明の詳細な説明】
本#Iは接触ばつ気式と化学式との組み合わせより廃水
全処理浄化する装置に関し、特に固液分離作用と浄化作
用と全促進すると共に、高性能で小型安価に得られる廃
水処理装置を提供するものである。Detailed Description of the Invention This #I relates to a device for total treatment and purification of wastewater using a combination of a contact aeration method and a chemical method, and in particular, it promotes both solid-liquid separation and purification actions, and is highly efficient, compact, and inexpensive. The present invention provides a wastewater treatment device that can
以下本願の実施例を図面について詳述すると、(1)は
鋼板或いはFRP等より作成された処理槽で。The embodiments of the present application will be described in detail below with reference to the drawings. (1) is a processing tank made of steel plate, FRP, or the like.
その底板(1)aは前方に稍傾斜している。(2)は前
記処理槽(1)?左右に仕切ってはつ気槽(3)と沈降
槽(4)とを区分する仕切板で、その上部中央位置に前
記ばつ気槽(3)からのtLを沈降槽(4)に流通させ
る流通部(51が設けられている。(6)は消毒剤(力
を保留した消毒借(8)全内部に有した貯溜槽で、前記
沈降槽(4)の側面に一体的に設けられており、前記沈
降槽(4)と前記消寡槽(8)との間にはそれらの上部
間全前記流通部(5)Lり低い位置で連通する連通部(
9)が、またAjl記消毒槽(8)には消毒槽(8)を
通過したのちの水液全前記貯溜槽(6]に流出する流出
部(1(J)が夫々設けられている。011は後述する
排水ポンプの1を駆動制御して貯溜槽(6)内の水位全
W8整する水位調整装置で7上下水位を夫々検知するl
対の検知素子01!a、 (11Toが備えられている
。(121は例えば不織布など刀≧ら成る厚味が約10
ruLI程度の粗い網目状の漏孔全有するマツ)8の接
触板で、これが前記ばっ気)Iv!!(3)及び沈降槽
(4)内に夫々上部がg、曲より上方に突出し。The bottom plate (1) a is slightly inclined forward. Is (2) the treatment tank (1)? A partition plate that divides left and right to separate an aeration tank (3) and a settling tank (4), and a distribution plate is placed at the center of the upper part of the partition plate to allow tL from the aeration tank (3) to flow into the settling tank (4). A section (51) is provided. (6) is a storage tank having a disinfectant (disinfectant (8) in which power is reserved) entirely inside, and is integrally provided on the side of the sedimentation tank (4). , between the sedimentation tank (4) and the quenching tank (8), there is a communication part (5) that communicates between the upper parts of the sedimentation tank (4) and the quenching tank (8) at a lower position than the entire flow part (5).
9), each of the disinfection tanks (8) is provided with an outflow portion (1 (J)) through which all the aqueous liquid after passing through the disinfection tank (8) flows out into the storage tank (6). 011 is a water level adjustment device that controls the drainage pump 1 (to be described later) to adjust the water level in the storage tank (6), and detects the 7 upper and lower water levels, respectively.
Pair of sensing elements 01! a, (11To is provided. (121 is made of non-woven fabric, etc., with a thickness of about 10
This is the contact plate of pine) 8, which has all the leakage holes as coarse as ruLI, and this is the contact plate mentioned above. ! (3) and sedimentation tank (4), the upper part of which protrudes above the curve.
下部が処理槽(1)の底)jEI(1)aより離れると
共に液の移行方InJで槽内全区画するように消費の間
隔全おいて叡枚乃至数十枚が配設されて論る。(■&は
前記ばつ気槽(3)内の下部に削6已接触板(12+と
直交する方向VC砥び77)つ−側部に片寄って水平状
に設けられた散気管で、これにコンプレツサ■が接続さ
れている。05)はh1工記ばつ気槽(3)内に廃水を
流入する流入管、 (1G+は凝集剤タンク卸から凝集
剤を前記流入管(15)に廃水流入量に比例して供給す
る定流書影ポンプ−(18+はばつ気槽(3)内の沈澱
固形物を定期的に排出するために使用する排出弁209
1は沈降槽(4)内の沈澱固形物を定期的に排出するた
めに使用する排出弁で2上記排出弁(18! + ar
’+と前記貯溜槽(6)の底部に設けた流出管C())
とが夫々排出管(21)を弁して排出ポンプ(221に
接続されている。(23)にばつ気槽(3)の上部に設
けられた空気抜管、(24+は前記接触板(121の押
え具である。A sheet to several dozen sheets are arranged at the entire consumption interval so that the lower part is away from the bottom of the treatment tank (1) (1) a and the tank is divided into all sections according to the liquid transfer method InJ. . (■& is a diffuser pipe installed horizontally at the bottom of the aeration tank (3) with a 6-deep contact plate (VC grinding plate 77 in the direction orthogonal to 12+) and one side. The compressor ■ is connected. 05) is the inflow pipe that flows wastewater into the h1 construction aeration tank (3), (1G+ is the amount of wastewater flowing into the inflow pipe (15) from the flocculant tank wholesaler. A constant flow shadow pump (18 + discharge valve 209 used to periodically discharge the precipitated solids in the aeration tank (3))
1 is a discharge valve used to periodically discharge the settled solids in the sedimentation tank (4); 2 is the discharge valve (18! + ar
'+ and the outflow pipe C () provided at the bottom of the storage tank (6)
are connected to the discharge pump (221) by valves of the discharge pipes (21), respectively. (23) is an air vent pipe provided at the upper part of the aeration tank (3), and (24+ is the contact plate (121)). It is a presser.
し7+”して工場等の有機屏水或カは便所等力)らの汚
水は流入管05)會介してばつり僧(3)内に流入し、
。Then, sewage from organic screens in factories, toilets, etc. flows into the bathhouse (3) through an inflow pipe (05),
.
このときポンプ(16)により流入廃水量に比例して一
定量の例えばポリ塩化アルミ等の凝集剤が自動的に廃水
に例えば約200 p、p、m程度混合される。At this time, a predetermined amount of a coagulant, such as polyaluminum chloride, is automatically mixed into the wastewater by the pump (16) in proportion to the amount of inflowing wastewater, for example, about 200 p, p, m.
前記ばつ気N(3)内KH,大した廃水は散気管031
v為ら噴出する空気の発散に、Il、り空気と混合し
、炉つ散父′#03・がばつ気槽(3)の−側部に片寄
って装備されているので2散気管u3・から噴出する気
泡の上昇にL!ll接触根接触1の前号位置で廃水なフ
二上方に補動し。KH in the above-mentioned air vent N (3), large waste water is transferred to air diffuser pipe 031
The air ejected from the tank (3) is dissipated, mixed with the air, and the two air diffusers (U3) are installed near the side of the aeration tank (3). L for the rise of bubbles gushing out! At the previous position of contact root contact 1, move the waste water upward.
これに伴い接触板02の後方位置では廃水は下方に疏動
じ、その結果各接触板(121の相互間において第3図
で示すよつに旋回流が生じ、この旋回治に伴って接触板
f12’ jtiの活性汚泥が浮遊すると共に、接触#
(12・に対する過大な生物層の付着により生じる目詰
りが防止され、〃・つ前記凝集剤と廃水との混合が促進
されて凝集作用を増すと共に、接触板Q21及び液中の
微生物に充分な酸素が供給されてその増殖も促進される
。前記接触板<121は粗い網目状の小孔を有して2つ
、これが上部を液面より突出し、下部を処理慴(1)の
底板(島l工り鼎すと共に、仕切板の方向で槽内全区画
するように数枚乃至数十枚がばつ気槽(3)内に配設さ
れているので、廃水は接触板αi4間に分離独立して形
成された液室を順次通って仕切板(2)の方向に流動し
、その過程で浮遊物は接触板02・・全弁して麻過婆れ
・その濾過物は接触板02!内に存在する微生物によっ
て炭酸ガスと水とに分解され、また?M果物は接触板0
2間を旋回しながらllI訂次その大きさと重量金増し
、その一部はばつ坊僧(3)の下部に沈降する。As a result, the waste water flows downward at the rear position of the contact plate 02, and as a result, a swirling flow is generated between each contact plate (121) as shown in FIG. 'jti's activated sludge floats and contact #
(Clogging caused by excessive biological layer adhering to the contact plate Q21 is prevented, and the mixing of the flocculant and wastewater is promoted to increase the flocculation effect, and the contact plate Q21 and microorganisms in the liquid are Oxygen is supplied to promote its growth.The contact plate <121 has two coarse mesh-like small holes, the upper part of which protrudes above the liquid level, and the lower part of which is connected to the bottom plate (island) of the processing chamber (1). At the same time, several to dozens of plates are placed in the aeration tank (3) so as to divide the whole tank in the direction of the partition plate, so that the wastewater is separated and independent between the contact plates αi4. The liquid flows sequentially through the liquid chambers formed in the direction of the partition plate (2), and in the process, the floating substances pass through the contact plate 02... and the filtrate passes through the contact plate 02! The fruit is decomposed into carbon dioxide gas and water by the microorganisms present in the fruit, and the contact plate 0
As it rotates between 2 and 3, it increases in size and weight, and a part of it sinks to the bottom of the monk monk (3).
このようにして流入管(15)力・らばっ気槽(3)内
に流入し7た廃水及び汚水は仕切板(2)の方向に移行
するに従って順次浄化されたのち、仕切gy、+21上
部の流通部(5)から沈降槽(4)内に流入する。沈降
槽(4)内にも前記したと同様に網目状の小孔を有する
接触板02・が配設されておるので2該沈降僧(41内
においても浮遊物のg制作用と固形物の沈降作用とが行
われて固液分離と浄化とが促進される。In this way, the waste water and sewage that flowed into the inflow pipe (15) and into the aeration tank (3) were purified sequentially as they moved toward the partition plate (2), and then moved to the upper part of the partition gy and +21. flows into the sedimentation tank (4) from the flow section (5). In the sedimentation tank (4), there is also a contact plate 02 with mesh-like small holes arranged in the same way as described above. Sedimentation takes place to promote solid-liquid separation and purification.
そしてこのように固液分離がなされ70)っ充分に浄化
された水g、は、連通部(9)より消毒槽(8)内に流
入して消毒作用を受けたのち貯溜槽(6)内に貯溜され
る。前記貯溜槽(6)内においては水位が上昇して上位
の検知素子115に達すると、水位調整装置旧1が作動
して排水ポンプ(221を駆動し、貯溜槽(6)内の水
液が紺出管(2+11 ’に介して外部に放出され或い
は例えは再生水とし7て用いられる。そして貯?li/
P、J (61内の水位が排水ポンプ(221の部側
により低下すると、今度は下位の検仰索子旧rbKL9
水位調整装置aυが作動して前記排水ポンプ@の駆#i
を停止する。The solid-liquid separated water (70), which has been sufficiently purified, flows into the disinfection tank (8) through the communication part (9), receives disinfection action, and then enters the storage tank (6). is stored in When the water level rises in the storage tank (6) and reaches the upper detection element 115, the water level adjustment device old 1 operates to drive the drain pump (221), and the water in the storage tank (6) is drained. The water is discharged to the outside through the water outlet pipe (2+11') or used as reclaimed water, and stored?li/
P, J (When the water level in 61 decreases due to the drainage pump (221), the lower search element old rbKL9
The water level adjustment device aυ operates and the drainage pump @ is driven #i.
stop.
以上のように本願によれば・ばっ気慴内に散気管を配設
して外気の供給により微生物に酸素を供給すると共に、
水液に旋回流を付与するように構成したので、微生物が
増殖され、〃1つこれに伴って濾過物の分解が促進され
ると共に接触板に対する1ゐ大ガ生物鳩の何着が防止で
きて濾過作用全高め2また複c′i、板の接触板?配設
したことにより濾過作用と沈降作用とが繰り返ターされ
て固液分離と浄化作用とが効率よく行われ、従って高負
荷のものに有効であると共に、小型安価に得られ、さら
にばつ惣僧内に@果剤全供給する構成としたので、微生
物が充分に生育しない初期段階においてもその凝集作用
により浄化が行われ4)と共に、全体として浄化作用が
IJg進するなどの利点’(r Hする。As described above, according to the present application, a diffuser pipe is provided in the aeration chamber to supply oxygen to microorganisms by supplying outside air, and
Since the structure is configured to give a swirling flow to the aqueous liquid, microorganisms are multiplied, which promotes the decomposition of the filtrate and also prevents the landing of large-sized biological pigeons on the contact plate. Is the filtration effect fully increased 2 and the contact plate of the plate? Due to this arrangement, the filtration action and sedimentation action are repeated, and the solid-liquid separation and purification action are performed efficiently. Therefore, it is effective for high-load applications, and can be obtained in a small and inexpensive manner. Since the structure is such that all of the fruit is supplied to the inside of the cell, purification is carried out by its aggregation effect even in the initial stage when microorganisms do not grow sufficiently4), and the purification effect is accelerated as a whole. Have sex.
図面は本部の実施例を示すもので、第1図は縦断正面図
、第2図は横断平面図、第3図は縦断側面図である。
図中(1)は処坤借、(2jは仕切機、(3)はばつ気
槽、(4)げ沈降槽、(51は流通部、(6)は貯溜槽
2(8)は消毒惜、(9)は連辿部、00)は流出部、
(12Iは接触板、031は散気管−IJ4JItlコ
ylvツサ、Q51 (rl m 入管、(1,61U
定流量形ポンプ、aカは凝集剤タンクである。
特許用仙人 株式会社五光製作所
第1図
〜117
V 1r
第3図
ゑThe drawings show an embodiment of the headquarters, with FIG. 1 being a vertical front view, FIG. 2 being a cross-sectional plan view, and FIG. 3 being a vertical side view. In the figure, (1) is the storage tank, (2j is the partition machine, (3) is the aeration tank, (4) is the sedimentation tank, (51 is the distribution section, (6) is the storage tank 2 (8) is the disinfection tank) , (9) is the continuous tracing part, 00) is the outflow part,
(12I is the contact plate, 031 is the air diffuser - IJ4JItl coylv tube, Q51 (rl m entry pipe, (1,61U
Constant flow type pump, A is a flocculant tank. Patent Sennin Goko Seisakusho Co., Ltd. Figure 1 ~ 117 V 1r Figure 3 E
Claims (3)
の上部が液面より突出し、その下部がばつ気槽底部よジ
離れると共に液の移行方向で槽内全区画するように配設
し、刀)つばつ気槽内の下部に、接触板と直父する方向
に延び力λつ一側部に片寄って散気管を装備したこと全
特徴とする廃水処理装置。(1) A contact plate with mesh-like leak holes is placed in the aeration tank so that its upper part protrudes above the liquid level and its lower part moves away from the bottom of the aeration tank, dividing the entire tank in the direction of liquid transfer. A wastewater treatment device characterized in that a diffuser pipe is installed at the lower part of the air tank, extending in a direction directly opposite to the contact plate, and biased toward one side with a force of λ.
。 その上部が液面Lp突出し、その下部がばつ気槽底部よ
り離れると共に液の移行方向で槽内全区画する工うに配
設し、71”つばつ気槽内の下部に、接触板と直父する
方向に延び〃)つ−側部に片をって散気管會装侑し史に
ばつ気槽における廃水流入部に対し、縦果剤葡供給する
機構を備えたことを特徴とする廃水処理装置t。(2) A contact plate with mesh-like leak holes inside the aeration tank. The upper part protrudes from the liquid level Lp, and the lower part is separated from the bottom of the aeration tank, dividing the entire tank in the direction of liquid transfer. A wastewater treatment system comprising: an aeration pipe extending in the direction of the aeration tank; device t.
と全形成すると共に、仕切板の上部に流通部を設け、前
記谷槽内に2網目状の漏孔會有する接触板?、その上部
が液面よジ突出し、下部が処理槽の底部より離れると共
に液の移行方向で槽内全区画するように配設し、刀)つ
ばつ気槽内の下部に。 接触板と直父する方向に延びかつ一側部に片寄って散気
管を装備したことを特徴とする廃水処理装置。(3) The treatment tank is partitioned by a partition plate to completely form an aeration tank and a sedimentation tank, and a contact plate is provided with a flow section at the top of the partition plate and has two mesh-like leak holes in the valley tank. ? The upper part protrudes beyond the liquid level, and the lower part is separated from the bottom of the processing tank and is arranged so as to partition the entire tank in the direction of liquid transfer. A wastewater treatment device characterized by being equipped with an aeration pipe that extends in a direction facing the contact plate and is offset to one side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58054044A JPS59179192A (en) | 1983-03-31 | 1983-03-31 | Waste water treating apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58054044A JPS59179192A (en) | 1983-03-31 | 1983-03-31 | Waste water treating apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59179192A true JPS59179192A (en) | 1984-10-11 |
Family
ID=12959595
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58054044A Pending JPS59179192A (en) | 1983-03-31 | 1983-03-31 | Waste water treating apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59179192A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62136293A (en) * | 1985-12-09 | 1987-06-19 | Gokou Seisakusho:Kk | Contact oxidation type waste water treatment apparatus |
JPS6344996A (en) * | 1986-04-18 | 1988-02-25 | Katsumi Iida | Device of treating water by surface aeration and immersed filter bed |
JPH03143599A (en) * | 1989-10-26 | 1991-06-19 | Hitachi Plant Eng & Constr Co Ltd | Waste water treating device |
CN107176757A (en) * | 2017-06-20 | 2017-09-19 | 温州正建设有限公司 | A kind of municipal wastewater processing equipment and sewage treatment process |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5259950A (en) * | 1975-08-18 | 1977-05-17 | Nitto Kako Kk | Net suspension system waste water treating method that use mtcrobe |
JPS5612198A (en) * | 1979-07-10 | 1981-02-06 | Matsushita Electric Ind Co Ltd | Forming unit of diaphragm for loudspeaker |
-
1983
- 1983-03-31 JP JP58054044A patent/JPS59179192A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5259950A (en) * | 1975-08-18 | 1977-05-17 | Nitto Kako Kk | Net suspension system waste water treating method that use mtcrobe |
JPS5612198A (en) * | 1979-07-10 | 1981-02-06 | Matsushita Electric Ind Co Ltd | Forming unit of diaphragm for loudspeaker |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62136293A (en) * | 1985-12-09 | 1987-06-19 | Gokou Seisakusho:Kk | Contact oxidation type waste water treatment apparatus |
JPS6344996A (en) * | 1986-04-18 | 1988-02-25 | Katsumi Iida | Device of treating water by surface aeration and immersed filter bed |
JPH03143599A (en) * | 1989-10-26 | 1991-06-19 | Hitachi Plant Eng & Constr Co Ltd | Waste water treating device |
CN107176757A (en) * | 2017-06-20 | 2017-09-19 | 温州正建设有限公司 | A kind of municipal wastewater processing equipment and sewage treatment process |
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