JPH04313400A - Sludge treating equipment - Google Patents
Sludge treating equipmentInfo
- Publication number
- JPH04313400A JPH04313400A JP3078031A JP7803191A JPH04313400A JP H04313400 A JPH04313400 A JP H04313400A JP 3078031 A JP3078031 A JP 3078031A JP 7803191 A JP7803191 A JP 7803191A JP H04313400 A JPH04313400 A JP H04313400A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- membrane module
- treated
- concentrator
- drawn
- 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
- 239000010802 sludge Substances 0.000 title claims abstract description 31
- 239000012528 membrane Substances 0.000 claims abstract description 19
- 230000000813 microbial effect Effects 0.000 claims description 11
- 238000005273 aeration Methods 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 6
- 239000000126 substance Substances 0.000 abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 5
- XLYOFNOQVPJJNP-DYCDLGHISA-N deuterium hydrogen oxide Chemical compound [2H]O XLYOFNOQVPJJNP-DYCDLGHISA-N 0.000 abstract 1
- 244000005700 microbiome Species 0.000 description 4
- 230000008719 thickening Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000006228 supernatant Substances 0.000 description 1
- 210000003437 trachea Anatomy 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
- Separation Using Semi-Permeable Membranes (AREA)
- Activated Sludge Processes (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は汚泥処理設備に関するも
のである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to sludge treatment equipment.
【0002】0002
【従来の技術】従来、汚泥を処理する設備としては、図
2に示すようなものがある。すなわち、曝気槽21と、
微生物処理槽22と、濃縮槽23とから構成されており
、曝気管21から微生物処理槽22に入れられた汚泥は
上澄液Aが放流される。そして、微生物処理された汚泥
は、一部が返送汚泥Bとして曝気槽23に供給され、他
の汚泥は濃縮槽23に送られる。濃縮槽23において濃
縮された汚泥の固形分はその重力により沈み、その後脱
水される。なお、濃縮槽23のかわりに遠心濃縮器24
を用いて、薬品Cが添加された汚泥を遠心力により濃縮
し、脱水する場合もある。2. Description of the Related Art Conventionally, there is a type of equipment for treating sludge as shown in FIG. That is, the aeration tank 21,
It is composed of a microbial treatment tank 22 and a concentration tank 23, and supernatant liquid A is discharged from the sludge put into the microbial treatment tank 22 from the aeration pipe 21. A part of the microbially treated sludge is supplied to the aeration tank 23 as return sludge B, and the other sludge is sent to the thickening tank 23. The solid content of the sludge concentrated in the thickening tank 23 sinks due to its gravity, and is then dehydrated. Note that the centrifugal concentrator 24 is used instead of the concentration tank 23.
In some cases, sludge to which chemical C has been added is concentrated and dehydrated using centrifugal force.
【0003】0003
【発明が解決しようとする課題】しかしながら、上記従
来の構成によると、汚泥の濃縮のために薬品Cを汚泥に
添加しなければならないため、この薬品Cの添加分だけ
処理すべき被処理物(汚泥)の量が増加するという課題
があった。[Problems to be Solved by the Invention] However, according to the above-mentioned conventional configuration, since the chemical C must be added to the sludge in order to thicken the sludge, the amount of material to be treated ( The problem was that the amount of sludge was increasing.
【0004】本発明は上記課題を解決するもので、薬品
の添加による被処理物の増加を招くことのない汚泥処理
設備を提供することを目的とするものである。[0004] The present invention solves the above-mentioned problems, and aims to provide sludge treatment equipment that does not cause an increase in the amount of material to be treated due to the addition of chemicals.
【0005】[0005]
【課題を解決するための手段】上記課題を解決するため
に本発明は、微生物処理装置とこの微生物処理装置から
排出される汚泥を濃縮する濃縮装置とを有し、上記微生
物処理装置および濃縮装置を、それぞれの槽本体と、こ
の槽本体内に、それぞれ配置された外圧型ろ過膜モジュ
ールと、この外圧型ろ過膜モジュールの下部に配置され
た散気管とから構成したものである。[Means for Solving the Problems] In order to solve the above-mentioned problems, the present invention includes a microbial treatment device and a concentrating device for concentrating sludge discharged from the microbial treatment device. Each tank body is composed of an external pressure type filtration membrane module disposed within each tank body, and an aeration pipe disposed at the lower part of the external pressure type filtration membrane module.
【0006】[0006]
【作用】上記構成により、微生物処理装置内において、
微生物分解が行われるとともに外圧型ろ過膜モジュール
によりろ過水が分離されて汚泥がある程度濃縮され、さ
らに濃縮装置内でもその外圧型ろ過膜モジュールにより
ろ過水が分離されて汚泥が一層濃縮される。このように
薬品を混合することなく汚泥を高い濃度まで濃縮するこ
とができる。[Operation] With the above configuration, in the microorganism treatment device,
As microbial decomposition is performed, the filtrate is separated by the external pressure type filtration membrane module, and the sludge is concentrated to some extent.Furthermore, in the concentrator, the filtrate is separated by the external pressure type filtration membrane module, and the sludge is further concentrated. In this way, sludge can be concentrated to a high concentration without mixing chemicals.
【0007】[0007]
【実施例】以下、本発明の一実施例を図1に基づいて説
明する。図1において、1は微生物処理装置で、装置本
体2と、装置本体2内の上部に配置された外圧型第1膜
モジュール3と、この第1膜モジュール3の下部に配置
された第1散気管4とから構成されている。5は微生物
処理装置1に、第1ポンプ6が設けられた供給管7を介
して接続された濃縮装置で、装置本体8と、装置本体8
内の上部に配置された外圧型第2膜モジュール9と、こ
の第2膜モジュール9の下方に配置された第2散気管1
0とから構成されている。また、11,12は各散気管
4,10に空気を供給するための送風機、13は脱水装
置(図示せず)に接続された接続管で、第2ポンプ14
が介装されている。[Embodiment] An embodiment of the present invention will be described below with reference to FIG. In FIG. 1, reference numeral 1 denotes a microbial treatment apparatus, which includes an apparatus main body 2, an external pressure type first membrane module 3 disposed at the upper part of the apparatus main body 2, and a first diffuser disposed at the lower part of the first membrane module 3. It is composed of a trachea 4. 5 is a concentrator connected to the microorganism treatment device 1 via a supply pipe 7 provided with a first pump 6;
An external pressure type second membrane module 9 placed in the upper part of the interior, and a second air diffuser 1 placed below this second membrane module 9.
It is composed of 0. Further, 11 and 12 are blowers for supplying air to each diffuser pipe 4 and 10, 13 is a connecting pipe connected to a dehydrator (not shown), and a second pump 14
is interposed.
【0008】上記構成において、微生物処理装置1内に
投入された原水aは、第1散気管4からの供給空気(酸
素)により微生物処理される。この際、第1膜モジュー
ル3により水分bが強制的に抜き出され、この水分bは
放流される。この第1膜モジュール3による水分の抜き
取りにより少し濃縮された汚泥cが、微生物処理装置1
の底部より第1ポンプ6および供給管7を介して濃縮装
置5に供給される。濃縮装置5に供給された汚泥cは、
第2散気管10からの空気により攪拌され、第2膜モジ
ュール9により水分dが強制的に抜き出される。In the above configuration, the raw water a introduced into the microbial treatment device 1 is treated with microorganisms by the air (oxygen) supplied from the first aeration pipe 4. At this time, the water b is forcibly extracted by the first membrane module 3, and this water b is discharged. The sludge c, which has been slightly concentrated by removing water by the first membrane module 3, is transferred to the microorganism treatment device 1.
is supplied to the concentrator 5 via the first pump 6 and the supply pipe 7 from the bottom. The sludge c supplied to the concentrator 5 is
It is stirred by the air from the second diffuser pipe 10, and the moisture d is forcibly extracted by the second membrane module 9.
【0009】そして、第2膜モジュール9からの水分d
は放流され、濃縮装置5内の汚泥はさらに高濃度に濃縮
される。高濃度に濃縮された汚泥eは、濃縮装置5の底
部より引き出され、第2ポンプ14および接続管13を
介して脱水装置に送られる。[0009] Then, the water d from the second membrane module 9
is discharged, and the sludge in the concentrator 5 is further concentrated to a higher concentration. The highly concentrated sludge e is drawn out from the bottom of the thickening device 5 and sent to the dewatering device via the second pump 14 and the connecting pipe 13.
【0010】0010
【発明の効果】以上のように本発明によれば、薬品を添
加することなく汚泥の濃度を高めることができるので濃
縮後の被処理物の量が増加することはなく、その後の処
理の能率化を図ることができる。Effects of the Invention As described above, according to the present invention, the concentration of sludge can be increased without adding chemicals, so the amount of material to be treated after concentration does not increase, and the efficiency of subsequent treatment can be improved. It is possible to aim for
【図1】本発明の一実施例における汚泥処理設備の概略
構成図である。FIG. 1 is a schematic configuration diagram of sludge treatment equipment in one embodiment of the present invention.
【図2】従来例における汚泥処理設備の概略構成図であ
る。FIG. 2 is a schematic diagram of a conventional sludge treatment facility.
1 微生物処理装置 2 装置本体 3 第1膜モジュール 4 第1散気管 5 濃縮装置 7 供給管 8 装置本体 9 第2膜モジュール 10 第2散気管 1 Microbial treatment equipment 2 Device body 3 First membrane module 4 First diffuser pipe 5 Concentration device 7 Supply pipe 8 Device body 9 Second membrane module 10 Second diffuser pipe
Claims (1)
から排出される汚泥を濃縮する濃縮装置とを有し、上記
微生物処理装置および濃縮装置を、それぞれの槽本体と
、この槽本体内に、それぞれ配置された外圧型ろ過膜モ
ジュールと、この外圧型ろ過膜モジュールの下部に配置
された散気管とから構成したことを特徴とする汚泥処理
設備。Claim 1: A microbial treatment device and a concentration device for concentrating sludge discharged from the microbial treatment device, wherein the microbial treatment device and concentration device are installed in respective tank bodies and in the tank body, respectively. A sludge treatment facility comprising an external pressure type filtration membrane module and an aeration pipe placed below the external pressure type filtration membrane module.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3078031A JPH04313400A (en) | 1991-04-11 | 1991-04-11 | Sludge treating equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3078031A JPH04313400A (en) | 1991-04-11 | 1991-04-11 | Sludge treating equipment |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04313400A true JPH04313400A (en) | 1992-11-05 |
Family
ID=13650445
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3078031A Pending JPH04313400A (en) | 1991-04-11 | 1991-04-11 | Sludge treating equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04313400A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5868934A (en) * | 1996-05-28 | 1999-02-09 | Sharp Kabushiki Kaisha | Method and apparatus for organic wastewater treatment capable of preventing decrease in permeation efficiency of submerged membrane without dilution |
WO2000071222A3 (en) * | 1999-05-20 | 2001-03-22 | Se Jun Park | Drainage sludge dehydration and dry system |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5879586A (en) * | 1981-11-04 | 1983-05-13 | Japan Organo Co Ltd | Method and device for concentrating sludge water |
JPS61274799A (en) * | 1985-05-31 | 1986-12-04 | Agency Of Ind Science & Technol | Apparatus for treating waste water |
JPH0286893A (en) * | 1988-09-22 | 1990-03-27 | Kubota Ltd | Activated sludge treating device |
JPH0321327A (en) * | 1989-06-16 | 1991-01-30 | Kubota Corp | Suspension concentrating equipment |
-
1991
- 1991-04-11 JP JP3078031A patent/JPH04313400A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5879586A (en) * | 1981-11-04 | 1983-05-13 | Japan Organo Co Ltd | Method and device for concentrating sludge water |
JPS61274799A (en) * | 1985-05-31 | 1986-12-04 | Agency Of Ind Science & Technol | Apparatus for treating waste water |
JPH0286893A (en) * | 1988-09-22 | 1990-03-27 | Kubota Ltd | Activated sludge treating device |
JPH0321327A (en) * | 1989-06-16 | 1991-01-30 | Kubota Corp | Suspension concentrating equipment |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5868934A (en) * | 1996-05-28 | 1999-02-09 | Sharp Kabushiki Kaisha | Method and apparatus for organic wastewater treatment capable of preventing decrease in permeation efficiency of submerged membrane without dilution |
WO2000071222A3 (en) * | 1999-05-20 | 2001-03-22 | Se Jun Park | Drainage sludge dehydration and dry system |
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