JPS644477Y2 - - Google Patents
Info
- Publication number
- JPS644477Y2 JPS644477Y2 JP1984068743U JP6874384U JPS644477Y2 JP S644477 Y2 JPS644477 Y2 JP S644477Y2 JP 1984068743 U JP1984068743 U JP 1984068743U JP 6874384 U JP6874384 U JP 6874384U JP S644477 Y2 JPS644477 Y2 JP S644477Y2
- Authority
- JP
- Japan
- Prior art keywords
- water
- raw water
- closed
- opened
- passages
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 89
- 230000003647 oxidation Effects 0.000 claims description 17
- 238000007254 oxidation reaction Methods 0.000 claims description 17
- 238000005192 partition Methods 0.000 claims description 9
- 239000000945 filler Substances 0.000 claims description 8
- 239000010802 sludge Substances 0.000 description 8
- 238000004140 cleaning Methods 0.000 description 6
- 230000003197 catalytic effect Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 239000010840 domestic wastewater Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 description 2
- 230000008439 repair process Effects 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
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)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は、接触酸化槽に関し、詳しくは、都市
下水、生活排水、食品工場等の排水処理、或は、
川河、湖沼を浄化する場合や、上下水道用原水の
浄水処理に使用する接触酸化槽に関するものであ
る。[Detailed description of the invention] [Industrial application field] The present invention relates to a contact oxidation tank, and more specifically, it is used for treating urban sewage, domestic wastewater, wastewater from food factories, etc.
This relates to contact oxidation tanks used for purifying rivers, lakes, and marshes, and for treating raw water for water supply and sewage.
微生物の活動を利用して浄水処理する接触酸化
槽としては、複数枚の仕切板によつて槽内にジグ
ザグ状の通水路を形成し、該通水路内に充填した
充填材間に原水を通過させるもの等、従来から
種々の構造のものが提供されている。しかしなが
ら、従来品は、原水の流量が著しく増大した場合
は、浄水処理能力を超える原水を未処理の状態で
放流しなければならず、原水中の有機性汚濁成分
(以下BODという)の濃度が高い場合には、充分
な浄水処理を行うことができなかつた。また、従
来品は、槽内の掃除や修理を行う場合にその使用
を中止しなければならないという欠点があつた。
A contact oxidation tank that uses microbial activity to purify water uses multiple partition plates to form a zigzag water passage in the tank, and raw water passes between the fillers filled in the water passage. Conventionally, various structures have been provided, such as those that allow However, with conventional products, when the flow rate of raw water increases significantly, raw water that exceeds the water treatment capacity must be discharged untreated, and the concentration of organic pollutants (hereinafter referred to as BOD) in the raw water increases. When it was high, sufficient water purification treatment could not be performed. Furthermore, the conventional product had the disadvantage that its use had to be discontinued when cleaning or repairing the inside of the tank.
本考案は、上述のような従来の欠点を解消した
もので、原水と生物膜との接触酸化効率が良好で
あることは勿論、槽内に複数の通水路を形成する
各仕切板の少なくとも一端縁部に開閉可能な通水
口を設け、各通水路の一側に流入口を、また、そ
れらの他側には流出口をそれぞれ開閉可能に設置
することによつて、原水の流量やBOD濃度に順
応でき、しかも、接触酸化を続行しながら槽内の
掃除や修理等を行えるようにした接触酸化槽を提
供するものである。
The present invention solves the above-mentioned conventional drawbacks, and not only improves the contact oxidation efficiency between raw water and biofilm, but also improves the efficiency of oxidation through contact between raw water and biofilm. By installing a water inlet that can be opened and closed on the edge, and installing an inlet on one side of each water channel and an outlet that can be opened and closed on the other side, it is possible to control the flow rate and BOD concentration of raw water. To provide a catalytic oxidation tank which can be adapted to the above conditions and which allows cleaning and repair of the inside of the tank while continuing catalytic oxidation.
次に、本考案の一実施例を添附の図面において
説明する。
Next, an embodiment of the present invention will be described with reference to the accompanying drawings.
第1図は概略平面図、第2図は第1図−線
断面図、第3図は一部分の拡大斜視図である。 FIG. 1 is a schematic plan view, FIG. 2 is a sectional view taken along the line of FIG. 1, and FIG. 3 is a partially enlarged perspective view.
本考案の接触酸化槽は、第1図及び第2図に示
す如く、複数枚の仕切板21,22,23,24
によつて槽1に複数の通水路31,32,33,
34,35を形成してある。第1図においては、
4枚の仕切板21,22,23,24によつて5
つの通水路31,32,33,34,35を形成
したものを例示してあるが、これに限定されな
い。これらの各通水路31,32,33,34,
35内に充填材2を充填してあつて、原水は充填
材2の間を通り移行するようになつている。上記
各仕切板21,22,23,24の少なくとも一
端縁部に開閉可能な通水口41,42,43,4
4を設けてある。通水口41,42,43,44
は、第3図に示す如く、閉塞板3の着脱によつて
開閉可能になつており、この通水口41,42,
43,44を一端縁部に設けた仕切板21,2
2,23,24を交互に配したものを例示してあ
り、通水口41,42,43,44が閉口状態の
ときは、原水が各通水路31,32,33,3
4,35に沿つて充填材2の間を直線状に移行
し、通水口41,42,43,44を開口する
と、原水は充填材2の間を通り通水路31,3
2,33,34,35に沿つてジグザグ状に移行
するようになつている。これら各通水路31,3
2,33,34,35の一側に開閉可能な流入口
51,52,53,54,55を設置してある。
開閉可能な流入口51,52,53,54,55
としては、バルブ61,62,63,64,65
付きの流入管を例示してあり、該バルブの開閉に
より原水を各通水路31,32,33,34,3
5に流入したり、その流入を中止したりすること
ができるようになつている。また、これら各通水
路31,32,33,34,35の他側には開閉
可能な流出口71,,72,73,74,75を
設置してある。開閉可能な流出口71,72,7
3,74,75としては、バルブ81,82,8
3,84,85を設けた放流管を例示してあつ
て、該バルブを開閉することにより、処理水や汚
泥を流出したり、それらの流出を中止することが
できるようになつている。 As shown in FIGS. 1 and 2, the contact oxidation tank of the present invention has a plurality of partition plates 21, 22, 23, 24.
A plurality of water passages 31, 32, 33,
34 and 35 are formed. In Figure 1,
5 by four partition plates 21, 22, 23, 24
Although one in which three water passages 31, 32, 33, 34, and 35 are formed is illustrated, the present invention is not limited to this. Each of these water passages 31, 32, 33, 34,
35 is filled with filler 2, so that raw water passes through between the fillers 2 and migrates. Water ports 41, 42, 43, 4 that can be opened and closed at least on one end edge of each of the partition plates 21, 22, 23, 24
4 is provided. Water outlet 41, 42, 43, 44
can be opened and closed by attaching and detaching the closing plate 3, as shown in FIG.
Partition plates 21 and 2 with 43 and 44 provided on one end edge
2, 23, 24 are arranged alternately, and when the water passages 41, 42, 43, 44 are closed, raw water flows through each water passage 31, 32, 33, 3.
4, 35, and when the water passages 41, 42, 43, 44 are opened, the raw water passes between the filling materials 2 and flows into the water passages 31, 3.
2, 33, 34, and 35 in a zigzag pattern. Each of these water passages 31, 3
Inlets 51, 52, 53, 54, 55 which can be opened and closed are installed on one side of each of the inlets 2, 33, 34, 35.
Openable and closable inlets 51, 52, 53, 54, 55
As for valves 61, 62, 63, 64, 65
An example of an inflow pipe with a valve is shown, and raw water is transferred to each water passage 31, 32, 33, 34, 3 by opening and closing the valve.
5, or stop the inflow. Further, on the other side of each of these water passages 31, 32, 33, 34, 35, openable and closable outflow ports 71, 72, 73, 74, 75 are installed. Outlet ports 71, 72, 7 that can be opened and closed
3, 74, 75 are valves 81, 82, 8
A discharge pipe provided with valves 3, 84, and 85 is shown as an example, and by opening and closing the valves, treated water and sludge can be discharged or their discharge can be stopped.
なお、図中符号4は架台を示し、充填材2は該
架台4上に載置してある。また、符号5は槽1の
流出口側に設けた排泥路を示し、このように排泥
路5を設けてあると、そこに汚泥が留り易く、そ
れの排出を容易に行えるので好ましい。 Note that the reference numeral 4 in the figure indicates a pedestal, and the filler 2 is placed on the pedestal 4. Further, reference numeral 5 indicates a sludge drainage path provided on the outlet side of the tank 1, and if the sludge drainage path 5 is provided in this way, sludge will easily stay there and it can be easily discharged, which is preferable. .
以上のような本考案の接触酸化槽は、繊維強化
ポリエステル樹脂や塩化ビニールの如き合成樹脂
等で形成し、都市下水、生活排水、食品工場等の
排水、上水道用原水等を接触酸化法と呼ばれてい
る方法によつて浄水処理するために使用するもの
である。原水を浄水処理するには、次のようにし
て行う。まず、原水の流量やBOD濃度が通常の
場合は、例えば、バルブ61及び83を開き、他
の全てのバルブ62乃至65,81,82,84
及び85を閉口する。一方、通水口41及び42
から閉塞板3を取外して該通水口を開口すると共
に、他の通水口43及び44は閉塞板3で閉口す
る。次いで、原水を流入口51から通水路31内
に流入する。そうすると、原水は通水路31、通
水口41、通水路32、通水口42、通水路33
に沿つてジグザグ状に、かつ、充填材2の間を流
れる。また、BODの濃度が高い原水を処理する
場合は、バルブ61及び85を開き、その他のバ
ルブ62乃至65、81乃至84を閉じると共
に、全ての通水口41乃至44を開口して、原水
を流入口51から通水路31内に流入する。そう
すると、原水は各通水路31,32,33,3
4,35の充填材2の間及び各通水口41,4
2,43,44を通り各通水路に沿つてジグザグ
状に流れる。この場合は、原水と微生物との接触
酸化時間が長くなる。更に、処理すべき原水の流
量が著しく多いときは、全てのバルブを開口する
一方、全ての通水口を閉じ、原水を各通水路3
1,32,33,34及び35に流入するように
する。そうすると、原水は各通水路に分配されそ
れら内の充填材2間を流れる。なお、処理水は開
口している各流出口より放流する。上述のよう
に、原水が充填材2の間を通り通水路に沿つて直
線的、或は、ジグザグ状に流れる際に、原水と微
生物膜との接触酸化が良好に行われる。また、例
えば通水路33を掃除する場合は、バルブ63を
閉じて流入口53からの原水の流入を止め、少な
くとも通水口42及び43を閉口する。一方、通
水路33内の原水が流出後流出口73のバルブ8
3を閉じて該通水路33内の掃除を行う。この掃
除によつて排泥路5に集積した汚泥はこの排泥路
5から外へ排出れる。この間、通水路33には原
水が流入せず、他の通水路31,32,34,3
5には原水が流入してその処理が行われる。ま
た、他の通水路を掃除する場合も、上記と同様に
行えばよい。
The contact oxidation tank of the present invention as described above is made of synthetic resin such as fiber-reinforced polyester resin or vinyl chloride, and can be used to process urban sewage, domestic wastewater, wastewater from food factories, raw water for water supply, etc. using the contact oxidation method. It is used to purify water using the method described in this article. To purify raw water, proceed as follows. First, if the raw water flow rate and BOD concentration are normal, for example, open valves 61 and 83, and close all other valves 62 to 65, 81, 82, 84.
and 85 is closed. On the other hand, water ports 41 and 42
The closing plate 3 is removed from the drain plate 3 to open the water passage, and the other water passages 43 and 44 are closed by the closing plate 3. Next, the raw water flows into the water passage 31 from the inlet 51. Then, the raw water flows through the water passage 31, the water passage 41, the water passage 32, the water passage 42, and the water passage 33.
It flows in a zigzag pattern along the space between the filling materials 2. In addition, when treating raw water with a high concentration of BOD, open the valves 61 and 85, close the other valves 62 to 65 and 81 to 84, and open all the water ports 41 to 44 to allow the raw water to flow. It flows into the water passage 31 from the inlet 51 . Then, the raw water is
Between the filling materials 2 of 4 and 35 and each water inlet 41 and 4
2, 43, and 44, and flows in a zigzag pattern along each water passage. In this case, the contact oxidation time between the raw water and the microorganisms becomes longer. Furthermore, when the flow rate of raw water to be treated is extremely large, all valves are opened, all water inlets are closed, and the raw water is transferred to each water channel 3.
1, 32, 33, 34 and 35. Then, the raw water is distributed to each water passage and flows between the fillers 2 therein. The treated water will be discharged from each open outlet. As described above, when the raw water passes between the fillers 2 and flows linearly or in a zigzag manner along the water passage, oxidation through contact between the raw water and the microbial membrane is well performed. For example, when cleaning the water passage 33, the valve 63 is closed to stop the flow of raw water from the inlet 53, and at least the water passages 42 and 43 are closed. On the other hand, after the raw water in the water passage 33 flows out, the valve 8 at the outlet 73
3 is closed and the inside of the water passage 33 is cleaned. Through this cleaning, the sludge accumulated in the sludge channel 5 is discharged from the sludge channel 5 to the outside. During this time, raw water does not flow into the water passage 33, and other water passages 31, 32, 34, 3
Raw water flows into 5 and is treated. Also, when cleaning other water passages, the same procedure as above may be used.
以上のように本考案の接触酸化槽よれば、原水
の接触酸化が良好に行われる。また、本考案は、
槽内に複数の通水路を形成する各仕切板の少なく
とも一端縁部に開閉可能な通水口を設け、各通水
路の一側に流入口を、また、それらの他側には流
出口をそれぞれ開閉可能に設置してあつて、原水
を全ての通水路に分配して流入したり、一部分の
通水路に流入したり、更には、全ての通水路に沿
つてジグザグ状に流れるようにすることもできる
ので、原水の流量やBOD濃度に応じて適宜に使
用できる。また、原水の流入の停止と処理水や汚
泥の放出とを各通水路毎に行えるように構成して
あるから、他の槽に原水を流入して接触酸化を続
行しながら掃除や修理等を行うことができるもの
である。
As described above, according to the catalytic oxidation tank of the present invention, catalytic oxidation of raw water is performed satisfactorily. In addition, this invention
Each partition plate forming a plurality of water passages in the tank is provided with a water passage port that can be opened and closed on at least one end edge, and each water passage has an inlet on one side and an outlet on the other side. It is installed so that it can be opened and closed so that the raw water can be distributed to all the waterways, flow into some of the waterways, or flow in a zigzag pattern along all the waterways. It can also be used as appropriate depending on the flow rate and BOD concentration of raw water. In addition, since the structure is configured so that the inflow of raw water can be stopped and the treated water and sludge can be discharged for each water channel, cleaning and repairs can be carried out while raw water flows into other tanks and catalytic oxidation continues. It is something that can be done.
図面は本考案の一実施例を示し、第1図は概略
平面図、第2図は第1図−線断面図、第3図
は一部分の拡大斜視図である。
図中1は槽、2は充填材、21,22,23,
24は仕切板、31,32,33,34,35は
通水路、51,52,53,54,55は流入
口、71,72,73,74,75は流出口を示
す。
The drawings show one embodiment of the present invention, in which FIG. 1 is a schematic plan view, FIG. 2 is a sectional view taken along the line of FIG. 1, and FIG. 3 is a partially enlarged perspective view. In the figure, 1 is a tank, 2 is a filler, 21, 22, 23,
24 is a partition plate, 31, 32, 33, 34, 35 are water passages, 51, 52, 53, 54, 55 are inlets, and 71, 72, 73, 74, 75 are outlets.
Claims (1)
形成し、該通水路内に充填材を充填をした接触酸
化槽において、上記各仕切板の少なくとも一端縁
部に開閉可能な通水口を設け、前記各通水路の一
側に開閉可能な流入口を設置すると共に、該各通
水路の他側には開閉可能な流出口を設置したこと
を特徴とする接触酸化槽。 In a contact oxidation tank in which a plurality of passageways are formed in the tank by a plurality of partition plates, and the passageways are filled with a filler, a water passageway that can be opened and closed at at least one end edge of each of the partition plates. A contact oxidation tank characterized in that an inlet that can be opened and closed is installed on one side of each of the water passages, and an outlet that can be opened and closed on the other side of each of the water passages.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1984068743U JPS60179394U (en) | 1984-05-11 | 1984-05-11 | Contact oxidation tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1984068743U JPS60179394U (en) | 1984-05-11 | 1984-05-11 | Contact oxidation tank |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60179394U JPS60179394U (en) | 1985-11-28 |
JPS644477Y2 true JPS644477Y2 (en) | 1989-02-06 |
Family
ID=30603769
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1984068743U Granted JPS60179394U (en) | 1984-05-11 | 1984-05-11 | Contact oxidation tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60179394U (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002102875A (en) * | 2000-09-29 | 2002-04-09 | Babcock Hitachi Kk | Water cleaning apparatus and method |
-
1984
- 1984-05-11 JP JP1984068743U patent/JPS60179394U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS60179394U (en) | 1985-11-28 |
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