JPH0214118B2 - - Google Patents
Info
- Publication number
- JPH0214118B2 JPH0214118B2 JP62011459A JP1145987A JPH0214118B2 JP H0214118 B2 JPH0214118 B2 JP H0214118B2 JP 62011459 A JP62011459 A JP 62011459A JP 1145987 A JP1145987 A JP 1145987A JP H0214118 B2 JPH0214118 B2 JP H0214118B2
- Authority
- JP
- Japan
- Prior art keywords
- section
- bed
- immersion
- water
- sedimentation
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 37
- 238000007654 immersion Methods 0.000 claims description 25
- 238000004062 sedimentation Methods 0.000 claims description 15
- 239000002351 wastewater Substances 0.000 claims description 8
- 230000005484 gravity Effects 0.000 claims description 4
- 238000004891 communication Methods 0.000 claims description 2
- 238000005273 aeration Methods 0.000 description 8
- 239000010802 sludge Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000002452 interceptive effect Effects 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 235000019362 perlite Nutrition 0.000 description 1
- 239000010451 perlite Substances 0.000 description 1
- -1 polypropylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002023 wood 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
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、省エネルギー、省スペースを可能と
する新規な有機性廃水の生物処理装置に関するも
のである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a novel biological treatment device for organic wastewater that enables energy saving and space saving.
従来、生物学的に処理する廃水の生物学的処理
装置として散水床法のように固体の表面に生物
膜を付着させて、そこに原水を流して原水中の
BOD成分などを除去することが知られている。
Conventionally, as a biological treatment device for biologically treating wastewater, a biological film is attached to a solid surface like the sprinkler bed method, and raw water is poured onto it to treat the water in the raw water.
It is known to remove BOD components.
この活性汚泥法等による汚水の生物学学的処理
設備においては、曝気槽の後に別個に沈殿池を必
要とし、しかも曝気後の活性汚泥フロツク群の沈
降速度が小さいため、沈殿池の設置面積は莫大な
ものにならざるを得なかつた。 Biological treatment equipment for sewage using the activated sludge method requires a separate settling tank after the aeration tank, and since the sedimentation rate of the activated sludge flocs after aeration is low, the installation area of the settling tank is small. It had to be huge.
ところが従来では、沈殿池の水面上部の広大な
空間は有効に利用されずに放置されている。ま
た、沈殿池の水面下の分離ゾーンも単に清澄水の
貯留部にしか利用されていない。一方、溶解性
BOD成分を含む有機性廃水は、単に沈殿処理あ
るいは凝集沈殿処理を行つても低BODの処理水
は得られないので、何らかの生物処理を用いた前
処理を行つたのち沈殿処理する必要があつて問題
であつた。
However, in the past, the vast space above the water surface of the sedimentation basin was left unused. Furthermore, the separation zone below the water surface of the settling basin is also used solely as a storage area for clear water. On the other hand, solubility
For organic wastewater containing BOD components, low BOD treated water cannot be obtained by simply performing sedimentation treatment or coagulation sedimentation treatment, so it is necessary to perform pretreatment using some kind of biological treatment before sedimentation treatment. It was a problem.
本発明は、このような従来無駄に放置されてい
た沈殿池上部などの空間を有効に生物処理工程に
利用することによつて、合理的な有機性廃水の生
物処理、沈殿処理を行うことを可能にした装置を
提供することを目的としたものである。 The present invention aims to perform rational biological treatment and sedimentation treatment of organic wastewater by effectively utilizing the space such as the upper part of the sedimentation tank, which was previously wasted, for the biological treatment process. The purpose is to provide a device that makes it possible.
本発明は、槽体内に上部から下部に向かつて順
に水床部3と、浸漬床部6と沈殿部10とを連
通形成せしめ、前記散水床部3の上方に原水散
水部4を配備すると共に、前記浸漬床部6を比
重1.0以下の水に浮上する粒状固体を材として
構成し、該浸漬の床内又は下方に散気装置7を
配設し、さらに前記沈殿部10に処理水流出部1
6を前記浸漬床部6の周囲に形成せしめたこと
を特徴とする廃水の生物学的処理装置である。
In the present invention, a water bed section 3, an immersion bed section 6, and a sedimentation section 10 are formed in communication with each other in order from the top to the bottom in the tank body, and a raw water sprinkling section 4 is disposed above the water sprinkling bed section 3. , the immersion bed section 6 is constructed of a granular solid that floats on water with a specific gravity of 1.0 or less, an aeration device 7 is provided in or below the immersion bed, and a treated water outflow section is provided in the settling section 10. 1
6 is formed around the immersion bed section 6.
次に、本発明の実施例を図面を参照して説明す
れば、槽体1内には、上部から下方に向かつて散
水床部3、浸漬床部6及び沈殿部10がこの
順に連通状態に形成されている。そしてこの浸漬
床部3の上方には原水散水部4が、また、浸漬
床部6の下方には散気装置7がそれぞれ配備さ
れている。前記沈殿部10には越流部16を介し
て越流ロンダー14を前記浸漬床部6の周囲に
区画形成して処理水流出部としてある。
Next, an embodiment of the present invention will be described with reference to the drawings. In the tank body 1, a watering bed section 3, an immersion bed section 6, and a settling section 10 are connected in this order from the top to the bottom. It is formed. A raw water sprinkler section 4 is provided above the immersed floor 3, and an aeration device 7 is provided below the immersed floor 6. In the settling section 10, an overflow launder 14 is sectioned around the immersion bed section 6 via an overflow section 16 to serve as a treated water outflow section.
この場合前記散水床部3からの流出水は沈殿
部10に流入せずに、そのまま槽体1の越流水面
2の下部に設けられた浸漬床部6に下向流で流
入してゆく。しかるのち、浸漬床部6の下部か
ら流出した生物処理水は槽体1内の沈殿部10に
て沈殿分離され、越流部16を経由して越流ロン
ダー14から処理水14′として系外に流出する
ように構成されている。 In this case, the water flowing out from the sprinkler bed 3 does not flow into the settling part 10, but directly flows downward into the immersion bed 6 provided below the overflow water surface 2 of the tank body 1. After that, the biologically treated water flowing out from the lower part of the immersion bed section 6 is separated by precipitation in the settling section 10 in the tank body 1, and is sent out of the system as treated water 14' from the overflow launder 14 via the overflow section 16. It is configured so that it flows out.
図中8はスクレーバ、9は駆動軸、11は排泥
管である。 In the figure, 8 is a scraper, 9 is a drive shaft, and 11 is a mud removal pipe.
しかして、有機性廃水4′は槽体1の上部に設
けられた散水部3へ散水部44から散水され、
散水床内の材表面をフイルム状に流下して行
く間に廃水4′中のBODの60%程度が除去され、
散水床部3の下端から流出し浸漬床部6を経
て沈殿部10に流入する。沈殿部10においては
前記浸漬床部6に流入した水は散気装置7から
供給される空気泡によつて酸素が供給されつつ散
水床部3にて除去されなかつた残留BODを高
度に除去される。また前記沈殿部10にて沈降性
のSS(散水床から剥離した生物膜など)が沈殿
し、スラツジとして堆積し排泥管11より排除す
る。 Thus, the organic wastewater 4' is sprayed from the water sprinkling part 44 to the water sprinkling part 3 provided at the upper part of the tank body 1,
Approximately 60% of the BOD in the wastewater 4' is removed as it flows down the material surface in the sprinkler bed in a film-like manner.
It flows out from the lower end of the sprinkler bed section 3 and flows into the settling section 10 via the immersion bed section 6. In the sedimentation section 10, the water that has flowed into the immersion bed section 6 is supplied with oxygen by air bubbles supplied from the aeration device 7, and residual BOD that was not removed at the sprinkler bed section 3 is highly removed. Ru. Further, in the sedimentation section 10, sedimentary SS (such as biofilm peeled off from the watering bed) is precipitated and deposited as sludge, which is removed from the sludge pipe 11.
かくして得られた処理水14′は浸漬床部6
の越流部16を経て上部から越流ロンダー14を
経由して系外に流出してゆく。 The treated water 14' obtained in this way is transferred to the immersion bed section 6.
It flows out of the system from the upper part through the overflow part 16 and the overflow launder 14.
前記浸漬床部6は槽体1上部の越流水面2の
下に位置しているので、曝気処理によつて槽体1
内の水流が乱されSSの沈降を妨害するという悪
影響は少なく、また散気装置7を浸漬床内に設
けることによつて槽体1内の水流の乱れはほぼ完
全に防止できる。 Since the immersion floor section 6 is located below the overflow water surface 2 at the upper part of the tank body 1, the tank body 1 is
The adverse effect of disturbing the water flow inside the tank body 1 and interfering with the settling of the SS is small, and by providing the air diffuser 7 in the immersion bed, the turbulence of the water flow inside the tank body 1 can be almost completely prevented.
さらに、浸漬床部6の材として発砲ポリプ
ロピレン粒子、パーライト、木片など比重が1.0
以下の水に浮く粒状固体を使用するので、散気装
置7から供給される空気泡の上昇運動によつて
材が動揺するので、浸漬床部6の目詰まりが発
生することなく、また、下部支持床が不要とな
り、安定した処理を継続することができる。 Furthermore, the materials for the immersion bed section 6 include foamed polypropylene particles, perlite, and wood chips with a specific gravity of 1.0.
Since the following granular solids that float on water are used, the material is agitated by the upward movement of air bubbles supplied from the air diffuser 7, so the immersion bed 6 is not clogged, and the lower part A supporting bed is no longer required and stable processing can be continued.
浸漬床部6に散気された空気は浸漬床部か
ら排出されるが、そのまま系外に排出せずに散水
床部3に導入することにより前記空気を、散水
床部3を確実に好気的雰囲気に維持するために
有効利用することができる。 The air diffused into the immersed bed section 6 is discharged from the immersed bed section, but by introducing the air into the sprinkler bed section 3 without directly discharging it outside the system, the air can be reliably aerobic. It can be effectively used to maintain a safe atmosphere.
本発明は、浸漬床部6を比重1.0以下の水に
浮上する粒状固体を材として構成し、該浸漬の
床内又は下方に散気装置7を配設し、さらに前
沈殿部10に処理水流出部16を前記浸漬床部
6の周囲に形成せしめたことにより、浸漬床部
中に散気装置から供給される空気泡の上昇運動に
よつて材が動揺するので、浸漬床部の目詰ま
りが発生することなく、また、下部支持床が不要
となり、安定した処理を継続することができると
共に、浸漬床部は沈殿池の上部の全面にわたつ
て配置され、空間の利用効率もよく沈殿槽の上部
などの従来未利用の空間を生物処理部として有効
に利用するこができ、装置全体が極めてコンパク
ト化されると共に、散水床の処理水をさらに浸
漬床部で処理するように構成した結果、浸漬
床部に供給する空気量が少なく、かつ散気水深が
1〜2mと浅いため、ブロワー動力が少なく、散
水床処理の消費動力が原水のポンプアツプ動力
のみであることと併せて、生物処理全体の消費エ
ネルギー、即ち「Kg除去BOD/KWH」が非常に
少なくてすむし、浸漬床部からの排空気を散水
床部に導入するので、散水床部への酸素供給
を従来のように自然通風に依存する必要がなくな
り、確実に散床部の嫌気化を防止することがで
き安定した生物学的処理を継続することができ
る。
In the present invention, the immersion bed section 6 is constructed using granular solids floating on water with a specific gravity of 1.0 or less, an aeration device 7 is provided in or below the immersion bed, and the pre-sedimentation section 10 is provided with treated water. By forming the outflow section 16 around the immersed bed section 6, the material is agitated by the upward movement of air bubbles supplied from the aeration device into the immersed bed section, thereby preventing clogging of the immersion bed section. In addition, stable treatment can be continued without the need for a lower support bed, and the immersion bed is placed over the entire upper part of the sedimentation tank, which improves the efficiency of space use. Conventionally unused space such as the upper part can be effectively used as a biological treatment section, and the entire device is made extremely compact.As a result of the structure in which the treated water from the sprinkler bed is further treated at the immersion bed section, Since the amount of air supplied to the submerged bed is small and the depth of the aeration water is shallow at 1 to 2 m, the blower power is low, and the power consumption for the submerged bed treatment is only for pumping up the raw water. The energy consumption (Kg removal BOD/KWH) is very low, and since the exhaust air from the immersion floor is introduced into the sprinkler bed, the oxygen supply to the sprinkler bed can be done by natural ventilation as in the conventional method. This eliminates the need to rely on anaerobic treatment, reliably prevents the spread bed from becoming anaerobic, and allows stable biological treatment to continue.
図面は本発明の実施例を示す縦断面図である。
1……槽体、2……越流水面、3……散水床
部、4……散水部、4′……廃水、6……浸漬
床部、7……散気装置、10……沈殿部、11…
…排泥管、14……越流ロンダー、14′……処
理水、16……越流部。
The drawings are longitudinal sectional views showing embodiments of the present invention. 1... Tank body, 2... Overflow water surface, 3... Sprinkling bed section, 4... Sprinkling section, 4'... Waste water, 6... Immersed bed section, 7... Air diffuser, 10... Sedimentation Part, 11...
... Sludge removal pipe, 14 ... Overflow launder, 14' ... Treated water, 16 ... Overflow section.
Claims (1)
部3と、浸漬床部6と沈殿部10とを連通形成
せしめ、前記散水床部3の上方に原水散水部4
を配備すると共に、前記浸漬床部6を比重1.0
以下の水に浮上する粒状固体を材として構成
し、該浸漬の床内又は下方に散気装置7を配設
し、さらに前記沈殿部10に処理水流出部16を
前記浸漬床部6の周囲に形成せしめたことを特
徴とする廃水の生物学的処理装置。1 A water sprinkling bed section 3, an immersion bed section 6, and a sedimentation section 10 are formed in communication with each other from top to bottom in the tank body, and a raw water sprinkling section 4 is provided above the water sprinkling bed section 3.
At the same time, the immersion bed section 6 has a specific gravity of 1.0.
A diffuser 7 is arranged in or below the immersion bed, and a treated water outlet 16 is provided in the sedimentation section 10 around the immersion bed 6. A biological treatment device for wastewater, characterized in that it is formed by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62011459A JPS62176597A (en) | 1987-01-22 | 1987-01-22 | Apparatus for biological treatment of waste water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62011459A JPS62176597A (en) | 1987-01-22 | 1987-01-22 | Apparatus for biological treatment of waste water |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP55169300A Division JPS5791790A (en) | 1980-12-01 | 1980-12-01 | Apparatus for biologically treating waste water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62176597A JPS62176597A (en) | 1987-08-03 |
JPH0214118B2 true JPH0214118B2 (en) | 1990-04-06 |
Family
ID=11778679
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62011459A Granted JPS62176597A (en) | 1987-01-22 | 1987-01-22 | Apparatus for biological treatment of waste water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62176597A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2554563B2 (en) * | 1991-07-10 | 1996-11-13 | 株式会社荏原製作所 | Method and apparatus for biological treatment of organic wastewater |
WO1996025366A1 (en) * | 1995-02-14 | 1996-08-22 | Andrew David Worthington | Water delivery apparatus |
JP4536396B2 (en) * | 2004-02-25 | 2010-09-01 | 株式会社御池鐵工所 | Water bottom and / or water sludge treatment facility |
ITPD20050278A1 (en) * | 2005-09-26 | 2007-03-27 | Lino Manfrotto & Co Spa | MONOPOD SUPPORT PARTICULARLY FOR VIDEO SHOOTING |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49134158A (en) * | 1973-04-26 | 1974-12-24 | ||
JPS5554089A (en) * | 1978-10-17 | 1980-04-21 | Nissin Electric Co Ltd | Upward flow type biological oxidation treatment apparatus |
-
1987
- 1987-01-22 JP JP62011459A patent/JPS62176597A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49134158A (en) * | 1973-04-26 | 1974-12-24 | ||
JPS5554089A (en) * | 1978-10-17 | 1980-04-21 | Nissin Electric Co Ltd | Upward flow type biological oxidation treatment apparatus |
Also Published As
Publication number | Publication date |
---|---|
JPS62176597A (en) | 1987-08-03 |
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