JPH0278491A - Waste water treating apparatus - Google Patents
Waste water treating apparatusInfo
- Publication number
- JPH0278491A JPH0278491A JP63228540A JP22854088A JPH0278491A JP H0278491 A JPH0278491 A JP H0278491A JP 63228540 A JP63228540 A JP 63228540A JP 22854088 A JP22854088 A JP 22854088A JP H0278491 A JPH0278491 A JP H0278491A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- air
- biofilm
- sewage
- pipe
- 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 13
- 239000010865 sewage Substances 0.000 claims abstract description 58
- 238000004065 wastewater treatment Methods 0.000 claims description 36
- 244000005700 microbiome Species 0.000 claims description 18
- 238000000034 method Methods 0.000 claims 1
- 230000001376 precipitating effect Effects 0.000 abstract 1
- 238000004519 manufacturing process Methods 0.000 description 22
- 239000010802 sludge Substances 0.000 description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 238000004062 sedimentation Methods 0.000 description 8
- 238000005273 aeration Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 241000894007 species Species 0.000 description 4
- 241000894006 Bacteria Species 0.000 description 3
- 230000001464 adherent effect Effects 0.000 description 3
- 239000000969 carrier Substances 0.000 description 3
- 238000009423 ventilation Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000032770 biofilm formation Effects 0.000 description 2
- 239000010842 industrial wastewater Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 241000223782 Ciliophora Species 0.000 description 1
- 241000026407 Haya Species 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 241001122767 Theaceae Species 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 239000002699 waste material 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)
Abstract
Description
【発明の詳細な説明】
〔発明の目的〕
（産業上の利用分野）
本発明は下水、産業廃水などを生物学的に処理する廃水
処理装置にかかり、特に廃水処理槽に生物膜を供給する
生物膜供給装置を備えた廃水処理装置に関するものでお
る。[Detailed Description of the Invention] [Objective of the Invention] (Industrial Application Field) The present invention relates to a wastewater treatment device for biologically treating sewage, industrial wastewater, etc., and particularly for supplying biofilm to a wastewater treatment tank. This article relates to a wastewater treatment device equipped with a biofilm supply device.
（従来の技術） 従来の廃水処理装置の一例を第７図に示す。(Conventional technology) An example of a conventional wastewater treatment device is shown in FIG.
第７図において、流入下水１は流入下水管２を介して下
水槽３に流入し、下水槽３は下水供給管４、下水供給ポ
ンプ５および下水供給管６を介して廃水処理、漕７に接
続され、ざらに廃水処理槽７内には生物反応部８、散気
管９、空気管１０．エアリフト管１１．上蓋１２．沈澱
部１３．排水管１４．汚泥引Ｊ友管１５および汚泥引扱
弁１６が構成され、これによって生物反応部８内の廃水
を生物学的に処理している。In FIG. 7, inflow sewage 1 flows into a sewage tank 3 via an inflow sewage pipe 2, and the sewage tank 3 is transferred to a wastewater treatment tank 7 via a sewage supply pipe 4, a sewage supply pump 5, and a sewage supply pipe 6. In the wastewater treatment tank 7, there are a biological reaction section 8, an aeration pipe 9, an air pipe 10. Air lift tube 11. Top lid 12. Sedimentation part 13. Drain pipe 14. A sludge-drawing J-tooth pipe 15 and a sludge-handling valve 16 are configured, and thereby the wastewater in the biological reaction section 8 is treated biologically.
（発明が解決しようとする課題）
しかしながら上記従来の廃水処理装置では■反応部８内
の浮遊汚泥の優占種が担体非付着性の微生物である場合
、反応部８内の担体に微生物が付着ぜず、水処理が安定
しない、■反応部８内の浮遊汚泥の侵占種が繊毛虫類１
８のような不均一な生物膜形成微生物であった場合、第
８図に示すにうに担体１９に付着して不均一な生物膜を
形成し、このため均一な生物膜に比べて流動性が悪化し
、水処理が安定しない、■反応部８内の生物膜が剥離し
た場合、剥離生物膜が流出して処理水の水質を悪化させ
、反応部８内で生物膜を再生させる工程が必要となる、
などの問題がある。(Problems to be Solved by the Invention) However, in the conventional wastewater treatment equipment described above, ■ If the dominant species of suspended sludge in the reaction section 8 is microorganisms that do not adhere to the carrier, the microorganisms adhere to the carrier in the reaction section 8. The water treatment is not stable. ■ The invasive species in the suspended sludge in the reaction section 8 is ciliates 1.
In the case of a non-uniform biofilm-forming microorganism as shown in Fig. 8, it adheres to the carrier 19 and forms a non-uniform biofilm, as shown in Fig. 8, and therefore has less fluidity than a uniform biofilm. ■If the biofilm inside the reaction section 8 is detached, the detached biofilm will flow out and deteriorate the quality of the treated water, and a step is required to regenerate the biofilm within the reaction section 8. becomes,
There are other problems.
本発明は、廃水処理槽内の生物反応部に常に均一な生物
膜を供給する生物膜供給装置を備えた廃水処理装置を提
供することを目的としている。An object of the present invention is to provide a wastewater treatment device equipped with a biofilm supply device that always supplies a uniform biofilm to a biological reaction section in a wastewater treatment tank.
（発明の構成）
（課題を解決するための手段）
本発明は、下水槽、下水供給管、下水供給ポンプ、沈澱
部および生物反応部を有する廃水処理槽に、生物膜製造
槽を有する生物膜供給装置を付加したものであり、下水
槽は下水供給管を有する下水供給ポンプを介して生物膜
製造槽に接続され、生物膜製造槽の生物反応部は生物膜
供給ポンプを有する生物膜供給管を介して廃水処理槽に
接続され、生物膜製造槽内に砂、活性炭、アンスラサイ
ト、セラミック等の担体を１〜１０％充填し、生物反応
部内部の通気線速度が１０〜４０ｍ／ｈ、生物反応部容
積負荷が１．０〜１０．０Ｋｙ−ＴＯＣ／屑／日で下水
を連続的に供給し、浮遊汚泥の優占種を付着性微生物に
し、それらの微生物を担体にイ」管固定し、生成した生
物膜を廃水処理槽に供給する。これによって廃水処理槽
内の生物牧柵が一定になり、廃水処理槽の生物処理が安
定化する。(Structure of the Invention) (Means for Solving the Problems) The present invention provides a wastewater treatment tank having a sewage tank, a sewage supply pipe, a sewage supply pump, a settling part, and a biological reaction part, and a biofilm production tank having a biofilm production tank. The sewage tank is connected to a biofilm production tank via a sewage supply pump having a sewage supply pipe, and the biological reaction section of the biofilm production tank is connected to a biofilm supply pipe having a biofilm supply pump. The biofilm production tank is connected to the wastewater treatment tank through the tank, and the biofilm production tank is filled with 1 to 10% of carriers such as sand, activated carbon, anthracite, ceramic, etc., and the linear velocity of ventilation inside the biological reaction section is 10 to 40 m/h. Biological reaction section Continuously supplies sewage with a volumetric load of 1.0 to 10.0 Ky-TOC/waste/day, converts the dominant species of suspended sludge into adherent microorganisms, and fixes these microorganisms on carriers in the "I" tube. Then, the generated biofilm is supplied to the wastewater treatment tank. This makes the biological fence in the wastewater treatment tank constant and stabilizes the biological treatment in the wastewater treatment tank.
（実施例） 本発明の一実施例を第１図に示す。(Example) An embodiment of the present invention is shown in FIG.
第１図において、下水槽３内底部に下水供給管４および
下水供給管２１を配設し、下水供給管２１は下水供給ポ
ンプ２３を有する下水供給管２４を介して生物膜製造槽
２５に接続され、下水供給管４は下水供給ポンプ５を有
する下水供給管６を介して廃水処理槽７に接続される。In FIG. 1, a sewage supply pipe 4 and a sewage supply pipe 21 are arranged at the inner bottom of the sewage tank 3, and the sewage supply pipe 21 is connected to a biofilm production tank 25 via a sewage supply pipe 24 having a sewage supply pump 23. The sewage supply pipe 4 is connected to a wastewater treatment tank 7 via a sewage supply pipe 6 having a sewage supply pump 5.
生物膜製造槽２５は生物反応部２９と沈澱部３０から成
り、生物反応部２９内に円筒状のエアリフト管３１と散
気管３２を配設し、沈澱部３０には生物反応部２９と沈
澱部３０とを仕切る上蓋３３と、越流板３４を配設して
いる。The biofilm production tank 25 consists of a biological reaction section 29 and a sedimentation section 30. A cylindrical air lift tube 31 and an aeration tube 32 are arranged in the biological reaction section 29, and a biological reaction section 29 and a sedimentation section are arranged in the sedimentation section 30. 30 and an overflow plate 34 are provided.
さらに生物膜製造槽２５は生物膜供給弁３６を有する生
物膜供給管３５を介して廃水処理槽７に接続され、越流
部４０には排水管４１が接続されている。Further, the biofilm production tank 25 is connected to the wastewater treatment tank 7 via a biofilm supply pipe 35 having a biofilm supply valve 36, and a drain pipe 41 is connected to the overflow section 40.
また担体貯留槽４２は担体供給弁４３を有する担体供給
管４４を介して生物膜製造槽２５に接続されている。廃
水処理槽７は生物反応部８と沈澱部１１とから成り、生
物反応部８内に円筒状のエアリフト管１１と散気管９が
配ニジされ、沈澱部１３には上Ｈ１２と越流板５５が配
設され、越流部５６に排水管１４を接続し、沈澱部１３
の下部に汚泥引央弁１６を有する汚泥引汰管１５が接続
されている。Further, the carrier storage tank 42 is connected to the biofilm production tank 25 via a carrier supply pipe 44 having a carrier supply valve 43 . The wastewater treatment tank 7 consists of a biological reaction section 8 and a settling section 11. A cylindrical air lift pipe 11 and an aeration pipe 9 are arranged in the biological reaction section 8, and an upper H12 and an overflow plate 55 are arranged in the settling section 13. is arranged, the drain pipe 14 is connected to the overflow part 56, and the settling part 13 is connected to the overflow part 56.
A sludge withdrawal pipe 15 having a sludge withdrawal valve 16 is connected to the lower part of the sludge withdrawal pipe 15 .
散気管３２は空気管６１、空気弁６２、空気管６３を介
して、また散気管９は空気管１０、空気弁６７、空気管
６８を介して空気源６４に接続されている。The air diffuser pipe 32 is connected to an air source 64 via an air pipe 61, an air valve 62, and an air pipe 63, and the air diffuser pipe 9 is connected to an air source 64 via an air pipe 10, an air valve 67, and an air pipe 68.
第１図の構成において、エアリフト管３１内部の通気線
速度が１０〜４０ｍ／ｈになるように流量調整可能な空
気源６４を調整し、空気源６４がら空気管６３、空気弁
６２、空気管６１、散気管３２を介してニアリフ１〜管
３１内に空気を供給する。In the configuration shown in FIG. 1, the air source 64 whose flow rate is adjustable is adjusted so that the linear velocity of ventilation inside the air lift pipe 31 is 10 to 40 m/h, and the air source 64 is connected to the air pipe 63, air valve 62, and 61, air is supplied into the near rift 1 to the pipe 31 via the aeration pipe 32.
また生物反応部２９の容積負荷が１．０〜１０．０ＫＦ
Ｉ−ＴＯＣ／ ｒｒｉ１日になるように下水供給ポンプ
２３の流量を調整し、下水槽３内の下水を下水供給ポン
プ２３を有する下水供給管２４を介して生物膜製造槽２
５に、ざらに担体４２を担体供給ポンプ４３を有する担
体供給管４４を介して生物膜供給槽２５に供給する。In addition, the volume load of the biological reaction section 29 is 1.0 to 10.0 KF.
The flow rate of the sewage supply pump 23 is adjusted so that the I-TOC/rri is 1 day, and the sewage in the sewage tank 3 is passed through the sewage supply pipe 24 having the sewage supply pump 23 to the biofilm production tank 2.
5, the carrier 42 is roughly supplied to the biofilm supply tank 25 via a carrier supply pipe 44 having a carrier supply pump 43.
この条件で馴養すると、生物反応部２９内の浮遊汚泥の
微生物優占種がズーグレア、糸状細菌、かびなどの付着
性微生物になる。これらの微生物は付着性が良好でおる
と同時に凝集性沈降性が悪く、いわゆるバルキング原因
微生物と称されており、これらの微生物を担体４２に付
着固定させる。When acclimatized under these conditions, the dominant microbial species in the suspended sludge in the biological reaction section 29 become adherent microorganisms such as zooglaia, filamentous bacteria, and mold. These microorganisms have good adhesion but at the same time poor flocculating and settling properties, and are called so-called bulking-causing microorganisms, and these microorganisms are attached and fixed to the carrier 42.
この条件においては第２図に示すように担体４２にズー
グレア７０と糸状性微生物７１が付着した生物膜、第３
図に示すように担体４２にズーグレア７０のみが付着し
た生物膜、あるいは第４図に示すように担体４２に糸状
性微生物のみが付着した生物膜が形成される。Under these conditions, as shown in FIG.
As shown in the figure, a biofilm is formed in which only zooglaia 70 is attached to the carrier 42, or a biofilm in which only filamentous microorganisms are attached to the carrier 42 as shown in FIG. 4 is formed.
これらの生物膜の厚さは、５０〜２００Ｊ１１ｎとなり
、生物膜形成を顕微鏡でモニタし、形成された生物膜を
生物膜供給弁３６を有する生物膜供給管３５を介して廃
水＋２！！理装置２８に供給する。The thickness of these biofilms is 50 to 200J11n, and the biofilm formation is monitored with a microscope, and the formed biofilm is passed through the biofilm supply pipe 35 having the biofilm supply valve 36 to waste water +2! ! is supplied to the processing device 28.
生物反応部８内の生物膜容量が生物反応部８容積の１〜
１０％になるように生物膜の供給を調整し、これを越え
たときは生物膜供給弁３６を閉じて供給を停止する。The biofilm capacity in the biological reaction section 8 is 1 to 1 of the volume of the biological reaction section 8.
The biofilm supply is adjusted to 10%, and when it exceeds this, the biofilm supply valve 36 is closed to stop the supply.
生物膜を供給した分だけ生物膜″！Ａ造槽２５内の担体
但が減るので、担体４２を生物膜製造槽２５内に供給し
て補給する。Since the amount of carrier in the biofilm production tank 25 decreases by the amount of biofilm supplied, the carrier 42 is supplied into the biofilm production tank 25 to replenish it.
生物膜製造槽２５の上部沈澱部３０の上澄液は、越流板
３４を越えて排水管４１を通して放流される。The supernatant liquid in the upper settling section 30 of the biofilm production tank 25 is discharged through the drain pipe 41 over the overflow plate 34.
下水槽２０内の下水は下水供給ポンプ５を有する下水供
給管６を介して廃水処理槽７に供給され、廃水処理槽７
内の生物反応部８の容積負荷が０．１〜３．ＯＮｇ−丁
ＤＣ／屑／日になるように馴養される。The sewage in the sewage tank 20 is supplied to the wastewater treatment tank 7 via a sewage supply pipe 6 having a sewage supply pump 5.
The volume load of the biological reaction section 8 within the range is 0.1 to 3. It is acclimated to ONg-Ding DC/Kusu/Day.
生物反応部８内で増殖した浮遊汚泥および剥離した生物
膜が余剰汚泥として沈澱部１３内に蓄積すると、汚泥引
扱管１５および汚泥引扱弁１６を介して汚泥が川辺かれ
る。When the floating sludge that has grown in the biological reaction section 8 and the biofilm that has peeled off accumulates in the sedimentation section 13 as surplus sludge, the sludge is discharged to the riverside via the sludge handling pipe 15 and the sludge handling valve 16.
廃水処理槽７の上部沈澱部１３の上澄液は、越流板５５
を通過した後、処理水として排水管１４を通って放流さ
れる。The supernatant liquid in the upper sedimentation section 13 of the wastewater treatment tank 7 is transferred to the overflow plate 55.
After passing through, the water is discharged through the drain pipe 14 as treated water.
上記第１図の構成を用いると、生物膜供給槽内部の通気
線速度が１０〜４０ｍ／ｈ、容積負荷が１．０〜１０．
０Ｋｙ−丁ＤＣ／Ｉ７ｉ／日になるように馴養すること
によって、生物膜供給槽内の微生物優占種がズーグレア
、糸状細菌、かびなどのバルキング原因微生物になり、
これらの微生物は付着性微生物でおるので微生物との何
着性の悪い担体であってし付着固定でき、膜厚さが５０
〜２００−で均一の生物膜を形成することが可能となり
、この生物膜供給装置で形成した均一の生物膜を廃水処
理槽に供給することによって廃水処理装置ηの水処理を
安定化することが可能となる。When the configuration shown in FIG. 1 is used, the linear ventilation velocity inside the biofilm supply tank is 10 to 40 m/h, and the volume load is 1.0 to 10 m/h.
By acclimating to 0Ky-Dc/I7i/day, the dominant microorganisms in the biofilm supply tank become bulking-causing microorganisms such as zooglaia, filamentous bacteria, and mold.
Since these microorganisms are adherent microorganisms, they can be attached to and fixed on carriers that have poor adhesion with microorganisms, and the film thickness is 50 mm.
It becomes possible to form a uniform biofilm at ~200-, and by supplying the uniform biofilm formed by this biofilm supply device to the wastewater treatment tank, it is possible to stabilize the water treatment in the wastewater treatment device η. It becomes possible.
本発明の他の実施例を第５図および第６図に示す。Another embodiment of the invention is shown in FIGS. 5 and 6.
第５図では、下水槽３内の底部に下水供給管４を挿入し
、下水供給ポンプ５および下水供給管６を介して廃水処
理槽７に連結し、また合成下水槽８０内の底部を合成下
水供給ポンプ８１および合成下水供給管Ｂ２を介して第
１図の実施例と同一構成の生物膜製造槽２５に接続する
。In FIG. 5, a sewage supply pipe 4 is inserted into the bottom of a sewage tank 3, connected to a wastewater treatment tank 7 via a sewage supply pump 5 and a sewage supply pipe 6, and the bottom of a synthetic sewage tank 80 is connected to a wastewater treatment tank 7. It is connected via a sewage supply pump 81 and a synthetic sewage supply pipe B2 to a biofilm production tank 25 having the same configuration as the embodiment shown in FIG.
生物膜製造槽２５は生物反応部２９と沈澱部３０とから
成り、生物反応部２９は生物膜供給弁３６をイアする生
物膜供給管３５を介して廃水処理装置７に接続され、沈
澱部３０は排水管４１を通して放流される。The biofilm production tank 25 consists of a biological reaction section 29 and a sedimentation section 30, and the biological reaction section 29 is connected to the wastewater treatment device 7 via a biofilm supply pipe 35 that connects a biofilm supply valve 36. is discharged through the drain pipe 41.
第５図の構成を用いると、生物膜製造槽２５内に合成下
水が連続的に供給されるので、容積負荷が１、 ＯＫ！
−ＴＯＣ／ ｒｒｉ ／日収下の低負荷であっても、ズ
ーグレア、糸状細菌、かびなどのバルキング原因微生物
が優占種となりやすく、生物膜の形成が容易となる。When the configuration shown in Fig. 5 is used, synthetic sewage is continuously supplied into the biofilm production tank 25, so the volume load is 1. OK!
-TOC/rri/Even at low loads under daily income, bulking-causing microorganisms such as zooglaia, filamentous bacteria, and mold tend to become dominant species, making it easy to form a biofilm.
第６図では、下水槽３内の底部が下水供給管２１、下水
供給ポンプ２３および下水供給管２４を介して生物膜製
造槽２５に、また下水供給管４、下水供給ポンプ５およ
び下水供給管６を介して廃水処理槽７に接続される。In FIG. 6, the bottom of the sewage tank 3 is connected to the biofilm production tank 25 via the sewage supply pipe 21, the sewage supply pump 23 and the sewage supply pipe 24, and the sewage supply pipe 4, the sewage supply pump 5 and the sewage supply pipe. It is connected to a wastewater treatment tank 7 via 6.
生物ＩＩ！！顎造槽２５は生物反応部２９および沈澱部
３０から成り、沈澱部３０は循環水槽供給管９３、循環
水槽供給ポンプ９４および循環水槽供給管９５を介して
循環水槽９６に落とされる。Biology II! ! The jaw-making tank 25 consists of a biological reaction section 29 and a settling section 30, and the settling section 30 is dropped into a circulating tank 96 via a circulating tank supply pipe 93, a circulating tank supply pump 94, and a circulating tank supply pipe 95.
ざらに循環水槽９６の底部に散気管９７を設け、空気管
９８を介して空気源６４に接続し、ざらに循環水槽９６
の最下部を循環水管９９、循環水弁１００、循環水管１
０１を介して生物膜製造槽２５の１ｄ下部に接続する。An aeration pipe 97 is provided at the bottom of the rough circulation water tank 96 and connected to the air source 64 via an air pipe 98.
The lowest part of the circulating water pipe 99, circulating water valve 100, circulating water pipe 1
It is connected to the lower part 1d of the biofilm production tank 25 via 01.
第６図の構成を用いると、生物膜製造槽２５内に直接に
空気を供給Ｕないので、空気と担体の摩擦がなくなり、
生物膜形成抑制が解決され、その結果、生物膜製造ｌＩ
２５内で迅速に生物膜が形成され、廃水処理槽に迅速に
生物膜を供給することが可能となる。When the configuration shown in FIG. 6 is used, air is not directly supplied into the biofilm production tank 25, so there is no friction between the air and the carrier.
Biofilm formation inhibition is solved, resulting in biofilm production lI
A biofilm is rapidly formed within the wastewater treatment tank 25, making it possible to quickly supply the biofilm to the wastewater treatment tank.
以上説明した本発明によれば、下水、産業廃水などの生
物学的処理を行う廃水処理槽に生物膜供給装置を介して
生物膜が供給されるので、安定した廃水処理を行うこと
が可能となる。According to the present invention as described above, biofilm is supplied via the biofilm supply device to a wastewater treatment tank that performs biological treatment of sewage, industrial wastewater, etc., so it is possible to perform stable wastewater treatment. Become.
第１図は本発明による生物膜供給装置を備えた廃水処理
装置の一実施例を示す構成図、第２図、第３図および第
４図は生物膜供給装置ににつで形成される生物膜の外観
を示す図、第５図および第６図はそれぞれ本発明の他の
実施例を示す構成図、第７図は従来の廃水処理装置の一
例を示す構成図、第８図は担体に付着した生物膜の状態
を示ず図で必る。
１・・・流入下水
３・・・下水槽
７・・・廃水処理槽
８．２９・・・生物反応部
１３、３０・・・沈澱部
２５・・・生物膜製造槽
３４、５５・・・越流板
４２・・・担体源
６４・・・空気源
８０・・・合成下水槽
９６・・・循環水槽
代理人 弁理士 猪 股 祥 晃
（ほか１名）
早 １ 剥
手 ３ｍ
第 ４ 父
ギ ５ｒｇＪ
茶 ム 回FIG. 1 is a block diagram showing an embodiment of a wastewater treatment device equipped with a biofilm supply device according to the present invention, and FIGS. 2, 3, and 4 show organisms formed by the biofilm supply device 5 and 6 are block diagrams showing other embodiments of the present invention, FIG. 7 is a block diagram showing an example of a conventional wastewater treatment device, and FIG. 8 is a block diagram showing the appearance of a membrane. The diagram does not show the state of the attached biofilm. 1... Inflow sewage 3... Sewage tank 7... Wastewater treatment tank 8.29... Biological reaction section 13, 30... Sedimentation section 25... Biofilm production tank 34, 55... Overflow plate 42...Carrier source 64...Air source 80...Synthetic sewage tank 96...Circulating water tank Agent Patent attorney Yoshiaki Inomata (and 1 other person) Haya 1 Stripping 3m 4th Sewer 5rgJ tea times
Claims (1)
廃水処理槽を備えた廃水処理装置において、上記下水槽
から廃水の一部が供給されると共に、担体源および空気
源からそれぞれ担体および空気が供給され、生物反応に
よつて微生物が担体に付着した生物膜を生成し、これを
上記廃水処理槽に供給する生物膜供給装置を設けたこと
を特徴とする廃水処理装置。In a wastewater treatment device equipped with a wastewater treatment tank that processes wastewater supplied from a sewage tank using a biological reaction, part of the wastewater is supplied from the sewage tank, and a carrier and air are supplied from a carrier source and an air source, respectively. A wastewater treatment device comprising: a biofilm supplying device that generates a biofilm with microorganisms attached to a carrier through a biological reaction, and supplies the biofilm to the wastewater treatment tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63228540A JPH0278491A (en) | 1988-09-14 | 1988-09-14 | Waste water treating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63228540A JPH0278491A (en) | 1988-09-14 | 1988-09-14 | Waste water treating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0278491A true JPH0278491A (en) | 1990-03-19 |
Family
ID=16877994
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63228540A Pending JPH0278491A (en) | 1988-09-14 | 1988-09-14 | Waste water treating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0278491A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1293526C (en) * | 2004-10-19 | 2007-01-03 | 四川新力光源有限公司 | Coloured fluorescent storage instant paster and its making method |
| CN115403217A (en) * | 2022-08-18 | 2022-11-29 | 天津天元新材料科技有限公司 | Water treatment process for treating by adopting fluidized bed biofilm reactor equipment |
-
1988
- 1988-09-14 JP JP63228540A patent/JPH0278491A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1293526C (en) * | 2004-10-19 | 2007-01-03 | 四川新力光源有限公司 | Coloured fluorescent storage instant paster and its making method |
| CN115403217A (en) * | 2022-08-18 | 2022-11-29 | 天津天元新材料科技有限公司 | Water treatment process for treating by adopting fluidized bed biofilm reactor equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5994253B2 (en) | Biological treatment apparatus and method for organic wastewater | |
| CN111675435A (en) | Integrated sewage treatment equipment based on A/O-MBBR (anaerobic-anoxic-aerobic-moving bed biofilm reactor) process and sewage treatment method | |
| KR101075961B1 (en) | Biological and chemical wastewater treatment system variable | |
| CN106315851B (en) | A kind of heterotrophic nitrification aerobic denitrifying bacterium cooperates with denitrification process with ammonia oxidizing bacteria | |
| CN108545890A (en) | A kind of mixed processing technique producing waste water and sanitary sewage | |
| CN111056698A (en) | Wastewater treatment process of multistage biological contact oxidation method | |
| CN206692513U (en) | A kind of dyeing waste water denitrogenation processing system based on MBBR techniques | |
| CN106542636B (en) | A kind of method of quick start whole process autotrophic denitrification | |
| CN105174438B (en) | A kind of method of improved MBR municipal sewage treatments | |
| CN105668946B (en) | A kind of Cattle Wastewater processing system and processing method | |
| CN107265791A (en) | Kitchen garbage slurry fermentation waste water processing unit | |
| CN110540293A (en) | Sewage treatment device and method suitable for large-amplitude fluctuation of water quantity | |
| CN211226837U (en) | Modularization sewage treatment plant | |
| KR101023479B1 (en) | A aerobic deammonification method of SBR type sewage, waste, livestock waste water treatment plant by use of micro sand bio mass, chemical and apparatus therof | |
| CN205990324U (en) | A kind of Bardenpho denitrification dephosphorization apparatus based on MBBR | |
| JPH0278491A (en) | Waste water treating apparatus | |
| KR100491900B1 (en) | Apparatus for sewage and wastewater treatment and method for sewage and wastewater treatment using the same | |
| KR950008382A (en) | Method and apparatus for high concentration organic wastewater treatment using soil microbial group | |
| KR20000045943A (en) | Treating method of wastewater using activated microorganism | |
| Chiemchaisri et al. | Enhancement of oxygen transfer and nitrogen removal in a membrane separation bioreactor for domestic wastewater treatment | |
| CN204918297U (en) | Membrane - bioreactor sewage treatment unit and sewage treatment system thereof | |
| CN208532384U (en) | A kind of multistage multistage integrated sewage processor | |
| CN105523694A (en) | Sewage treatment system based on circular sludge reduction | |
| KR100399702B1 (en) | The method and asparatus of purificating sewage through process of foaming membrane and etc poceses | |
| CN108862842A (en) | A kind of mixed processing method of production and living sewage |