JPH03114585A - Treatment of sludge - Google Patents
Treatment of sludgeInfo
- Publication number
- JPH03114585A JPH03114585A JP1251754A JP25175489A JPH03114585A JP H03114585 A JPH03114585 A JP H03114585A JP 1251754 A JP1251754 A JP 1251754A JP 25175489 A JP25175489 A JP 25175489A JP H03114585 A JPH03114585 A JP H03114585A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- membrane
- treatment
- fine fibers
- screen
- 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 46
- 239000012528 membrane Substances 0.000 claims abstract description 27
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 238000004140 cleaning Methods 0.000 claims abstract description 11
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims description 11
- 239000010800 human waste Substances 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims 1
- 239000000835 fiber Substances 0.000 abstract description 15
- 230000018044 dehydration Effects 0.000 abstract description 5
- 238000006297 dehydration reaction Methods 0.000 abstract description 5
- 230000029142 excretion Effects 0.000 abstract 4
- 208000005156 Dehydration Diseases 0.000 abstract 3
- 239000011259 mixed solution Substances 0.000 abstract 1
- 238000005273 aeration Methods 0.000 description 2
- 239000000356 contaminant Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002203 pretreatment Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- 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
- Activated Sludge Processes (AREA)
- Treatment Of Sludge (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野1
この発明は、一連のし尿処理工程のうち夾雑物の除去及
び脱水を主たる目的とする前処理工程用の処理方法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application 1] The present invention relates to a treatment method for a pretreatment step whose main purpose is removal of impurities and dehydration among a series of human waste treatment steps.
[従来の技術]
従来知られているし尿処理法は、活性汚泥処理後に沈殿
槽や遠心濃縮機等によって処理水と汚泥に分離して、汚
泥の一部を余剰汚泥として引き抜き、残りは曝気槽に返
送して再び活性汚泥処理を行うものが主流であったが、
前記した沈殿槽や遠心濃縮機等による固液分離法に代わ
って限外濾過膜(以下UP膜という)が使用されるよう
になってきた。[Prior Art] Conventionally known human waste treatment methods involve separating treated water and sludge in a settling tank or centrifugal concentrator after activated sludge treatment, extracting a portion of the sludge as surplus sludge, and leaving the rest in an aeration tank. The mainstream was to send the sludge back to the factory and undergo activated sludge treatment again.
Ultrafiltration membranes (hereinafter referred to as UP membranes) have come to be used in place of the solid-liquid separation methods using sedimentation tanks, centrifugal concentrators, etc. described above.
UF腹膜法、確実に濁質のない処理水が得られる長所は
あるが、混合液が通過する断面積が小さいなめ(平膜の
場合3〜5 mmスリット、チューブ膜の場合11.5
φI!lI+)、夾雑物による閉塞が生じるという問題
点がある。The UF peritoneal method has the advantage of reliably obtaining treated water without turbidity, but the cross-sectional area through which the mixed liquid passes is small (3 to 5 mm slit for flat membranes, 11.5 mm for tube membranes).
φI! lI+), there is a problem that blockage occurs due to contaminants.
そのため、し尿の前段処理として薬品を用いて凝集させ
た後スクリーンや遠心分W!機などによって夾雑物を除
去する方法が採られている。Therefore, as a preliminary treatment for human waste, chemicals are used to coagulate it and then screened or centrifuged. A method is used to remove contaminants using a machine or the like.
[この発明が解決しようとする課題]
ところで、このような事前処理を経たし尿を活性汚泥処
理した後UP膜によって分離して得られる余剰汚泥は、
繊維類を含まない粘性の高い性Iffを持っており、脱
水処理が極めて困難である。[Problems to be Solved by the Invention] By the way, surplus sludge obtained by treating human waste that has undergone such pre-treatment with activated sludge and then separating it with a UP membrane is
It does not contain fibers and has a high viscosity if, making it extremely difficult to dehydrate.
そこで、特殊高圧型プレス脱水機を用いたり、繊維類の
多いし尿に余剰汚泥を混合して凝集処理後、スクリーン
モスクリユープレスや遠心分離機で脱水処理しているの
が現状であるが、含水率の高い非衛生な脱水ケーキか多
量に発生するという問題点が残る。Therefore, the current practice is to use a special high-pressure press dehydrator, or to mix surplus sludge with human waste containing a lot of fibers, and after flocculation treatment, dewatering treatment is performed using a screen mosque press or centrifugal separator. The problem remains that a large amount of unhygienic dehydrated cake is generated at a high rate.
この発明は上記問題点を解決することを課題とするもの
であって、微細繊維を脱水対象とする余剰汚泥のみに混
入させることにより、難脱水性の余剰汚泥の脱水率の向
上を図ることを目的とするものである。This invention aims to solve the above-mentioned problems, and aims to improve the dewatering rate of difficult-to-dewater surplus sludge by mixing fine fibers only into the surplus sludge to be dewatered. This is the purpose.
[課題を解決するための手段]
この発明は、前記課題を解決するための手段を提供しよ
うとするものであって、し尿を生物反応槽で活性汚泥処
理した後の混合液を循環槽を経て限外濾過膜に導き汚泥
と処理水とに分離するようにした活性汚泥法において、
前記限外濾過膜の前段にセルフクリーニング型スクリー
ンを挿入し、該スクリーンによって前記混合液中のし渣
を除去し余剰汚泥と共に引き抜くようにしたことを特徴
とする汚泥処理法を要旨とするものである。[Means for Solving the Problems] The present invention seeks to provide means for solving the above problems, and is to provide a means for solving the problems described above, in which a mixed liquid after treating human waste with activated sludge treatment in a biological reaction tank is passed through a circulation tank. In the activated sludge method, which separates sludge and treated water through an ultrafiltration membrane,
This method is characterized in that a self-cleaning screen is inserted in front of the ultrafiltration membrane, and the screen removes sludge from the mixed liquid and draws it out together with excess sludge. be.
[実施例] 図面に示した実施例により本発明の詳細な説明する。[Example] The invention will be explained in detail by means of embodiments shown in the drawings.
図中1は生物反応槽であって、細目ドラムスクリーンで
し渣が除去されたし尿Aが貯留槽を経て投入され、ここ
で活性汚泥処理が行われる。In the figure, reference numeral 1 denotes a biological reaction tank, into which night soil A from which human sludge has been removed through a fine drum screen is inputted via a storage tank, where activated sludge treatment is performed.
処理された混合液は循環槽2に流入後、ポンプ3によっ
てUF膜4に送られ、処理水5と返送汚泥6に分離され
る。After the treated mixed liquid flows into the circulation tank 2, it is sent to the UF membrane 4 by the pump 3, and is separated into treated water 5 and return sludge 6.
前記UF膜4の前段にはセルフクリーニング型のスクリ
ーン7が挿入されており、循環槽2からポンプ3によっ
て送られる混合液中のし渣を除去してUF膜の閉塞を防
止する。A self-cleaning screen 7 is inserted in front of the UF membrane 4, and removes scum from the mixed liquid sent by the pump 3 from the circulation tank 2 to prevent clogging of the UF membrane.
このセルフクリーニング型スクリーン7は公知任意のも
のを採択できるが、通過原液中のし渣によって生ずる目
詰まりをセンサによって検出し、通過液の逆流により自
動洗浄される形式のものが最適であり、この洗浄排液は
余剰汚泥8と共に引き抜かれ、脱水処理される。This self-cleaning screen 7 can be of any known type, but it is best to use a type that uses a sensor to detect clogging caused by scum in the passing liquid and automatically cleans it by backflow of the passing liquid. The cleaning waste liquid is extracted together with excess sludge 8 and subjected to dewatering treatment.
余剰汚泥8中には、前記スクリーン7の目詰まり洗浄に
より除去されたし渣が混入されているため、該し液中の
微細繊維類が脱水助材の役目を果たし脱水率が向上する
。Since the surplus sludge 8 contains the residue removed by cleaning the screen 7 from clogging, the fine fibers in the liquid serve as a dewatering aid and improve the dewatering rate.
余剰汚泥中の繊維類含有率を表−1に、余剰汚泥の脱水
テスト結果を表−2に示す。The fiber content in the excess sludge is shown in Table 1, and the results of the dewatering test of the excess sludge are shown in Table 2.
[作用]
生物反応槽1に投入されるし尿は、その前段のドラムス
クリーン(図示せず)でし渣が除去されているが、微細
繊維類は該スクリーンのスリ・yト部を通過して処理系
に流入する。この微細繊維類は生物反応槽1における曝
気混合過程において互いに絡み合って核が形成され、こ
の核に活性汚泥が付着して再びし渣として生長し、U
Fl!4の閉塞原因となっていた。[Function] The human waste input into the biological reaction tank 1 has its human waste removed by a drum screen (not shown) in the preceding stage, but fine fibers pass through the slits and holes of the screen. flows into the processing system. These fine fibers intertwine with each other during the aeration mixing process in the biological reaction tank 1 to form a nucleus, and the activated sludge adheres to this nucleus and grows again as sludge.
Fl! This was the cause of 4 blockages.
しかし本発明によれば、この微細繊維類を含むし渣はU
F膜4の前段に挿入されたセルフクリーニング型スクリ
ーン7によって除去されるので、UF膜4の閉塞が防止
される。However, according to the present invention, the residue containing these fine fibers is U
Since it is removed by the self-cleaning screen 7 inserted before the F membrane 4, clogging of the UF membrane 4 is prevented.
一方、前記スクリーン7で除去された微細繊維類を含む
し渣は、余剰汚泥8と共に引き抜かれ脱水処理されるが
、余剰汚泥中に多量の微細繊維類が混入しているため、
脱水性が飛躍的に向上し脱水ケーキ中の含水率を低下さ
せることができる。On the other hand, the residue containing fine fibers removed by the screen 7 is pulled out together with the surplus sludge 8 and subjected to dewatering treatment, but since a large amount of fine fibers are mixed in the surplus sludge,
Dehydration properties are dramatically improved and the water content in the dehydrated cake can be reduced.
また、余剰汚泥8をUF膜4の前段で引き抜くため、U
F膜を通過する処理液量が減少しUF膜の容量を小型化
することができ、同一容量の場合には寿命が長くなる。In addition, in order to pull out excess sludge 8 before the UF membrane 4, the U
The amount of processing liquid that passes through the F membrane is reduced, and the capacity of the UF membrane can be reduced, and the life span is extended for the same capacity.
[効果]
この発明によれば、限外濾過膜の前段にセルフクリーニ
ング型スクリーンを挿入し、該スクリーンによって前記
混合液中のし渣を除去し余剰汚洟と共に引き抜くように
したことにより、微H繊糺を脱水対象とする余剰汚泥の
みに混入させることができるので、この微細繊維類を脱
水助材として利用して難脱水性の余剰汚泥の脱水率の向
上を四ることが可能となり、凝集剤の添加量を減少させ
ると共に脱水ケーキの含水率を低下させることができ、
処理経費を節約することができる。[Effect] According to the present invention, a self-cleaning screen is inserted in the front stage of the ultrafiltration membrane, and the screen removes the scum from the mixed liquid and draws it out together with the excess dirt. Since the fibers can be mixed only into the surplus sludge to be dewatered, it is possible to use these fine fibers as a dewatering aid to improve the dewatering rate of surplus sludge that is difficult to dewater. It is possible to reduce the amount of additive added and the moisture content of the dehydrated cake.
Processing costs can be saved.
また、UP膜の前段において余剰汚泥を引き抜くように
したため(JF膜の容量を小さくすることができ、同一
容量であればその寿命を長期化することができる。In addition, since excess sludge is extracted at the stage before the UP membrane (the capacity of the JF membrane can be reduced, and the capacity is the same, its life can be extended).
図面はこの発明方法を示す工程図である。 1:生物反応槽 2:循環槽 3:ポンプ 限外濾過膜 処理水 返送汚泥 セルフクリーニング型スクリーン し渣を含む余剰汚泥 The drawings are process diagrams showing the method of this invention. 1: Biological reaction tank 2: Circulation tank 3: Pump ultrafiltration membrane treated water Returned sludge self-cleaning screen Excess sludge including residue
Claims (1)
循環槽を経て限外濾過膜に導き汚泥と処理水とに分離す
るようにした活性汚泥法において、前記限外濾過膜の前
段にセルフクリーニング型スクリーンを挿入し、該スク
リーンによって前記混合液中のし渣を除去して余剰汚泥
と共に引き抜くようにしたことを特徴とする汚泥処理法
。1) In the activated sludge method, in which the mixed liquid after treating human waste with activated sludge in a biological reaction tank is guided to an ultrafiltration membrane through a circulation tank and separated into sludge and treated water, the pre-stage of the ultrafiltration membrane A sludge treatment method characterized in that a self-cleaning screen is inserted into the liquid mixture, and the screen removes sludge from the mixed liquid and draws it out together with excess sludge.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1251754A JPH03114585A (en) | 1989-09-29 | 1989-09-29 | Treatment of sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1251754A JPH03114585A (en) | 1989-09-29 | 1989-09-29 | Treatment of sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03114585A true JPH03114585A (en) | 1991-05-15 |
Family
ID=17227428
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1251754A Pending JPH03114585A (en) | 1989-09-29 | 1989-09-29 | Treatment of sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03114585A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001219197A (en) * | 2000-02-10 | 2001-08-14 | Suido Kiko Kaisha Ltd | Excretion residue removing apparatus |
JP2006037932A (en) * | 2004-07-30 | 2006-02-09 | Valeo Thermal Systems Japan Corp | Compressor with foreign matter removal device |
JP2012000585A (en) * | 2010-06-18 | 2012-01-05 | Kubota Corp | Wastewater treatment facility, wastewater treatment method and method of reconstructing wastewater treatment facility |
JP4856649B2 (en) * | 2004-10-06 | 2012-01-18 | ルーク ファールツォイク・ヒドラウリク ゲゼルシャフト ミット ベシュレンクテル ハフツング ウント コンパニー コマンディートゲゼルシャフト | Air conditioner compressor or air conditioner |
JP2017159204A (en) * | 2016-03-08 | 2017-09-14 | 住友重機械エンバイロメント株式会社 | Water treatment equipment and operation method thereof |
-
1989
- 1989-09-29 JP JP1251754A patent/JPH03114585A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2001219197A (en) * | 2000-02-10 | 2001-08-14 | Suido Kiko Kaisha Ltd | Excretion residue removing apparatus |
JP4611480B2 (en) * | 2000-02-10 | 2011-01-12 | 水道機工株式会社 | Screen removal device |
JP2006037932A (en) * | 2004-07-30 | 2006-02-09 | Valeo Thermal Systems Japan Corp | Compressor with foreign matter removal device |
JP4856649B2 (en) * | 2004-10-06 | 2012-01-18 | ルーク ファールツォイク・ヒドラウリク ゲゼルシャフト ミット ベシュレンクテル ハフツング ウント コンパニー コマンディートゲゼルシャフト | Air conditioner compressor or air conditioner |
JP2012000585A (en) * | 2010-06-18 | 2012-01-05 | Kubota Corp | Wastewater treatment facility, wastewater treatment method and method of reconstructing wastewater treatment facility |
JP2017159204A (en) * | 2016-03-08 | 2017-09-14 | 住友重機械エンバイロメント株式会社 | Water treatment equipment and operation method thereof |
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