JPS60190300A - Treatment of screen dregs - Google Patents
Treatment of screen dregsInfo
- Publication number
- JPS60190300A JPS60190300A JP59043747A JP4374784A JPS60190300A JP S60190300 A JPS60190300 A JP S60190300A JP 59043747 A JP59043747 A JP 59043747A JP 4374784 A JP4374784 A JP 4374784A JP S60190300 A JPS60190300 A JP S60190300A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- screen
- treatment
- dehydrator
- dregs
- 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 claims abstract description 48
- 239000010865 sewage Substances 0.000 claims abstract description 17
- 238000000926 separation method Methods 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 239000002002 slurry Substances 0.000 claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 6
- 239000007787 solid Substances 0.000 claims 1
- 239000002351 wastewater Substances 0.000 claims 1
- 238000004065 wastewater treatment Methods 0.000 claims 1
- 238000005273 aeration Methods 0.000 abstract description 5
- 230000018044 dehydration Effects 0.000 abstract description 5
- 238000006297 dehydration reaction Methods 0.000 abstract description 5
- 229920006317 cationic polymer Polymers 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract description 2
- 208000005156 Dehydration Diseases 0.000 abstract 3
- 239000000203 mixture Substances 0.000 abstract 3
- 239000000654 additive Substances 0.000 abstract 1
- 230000000996 additive effect Effects 0.000 abstract 1
- 239000002562 thickening agent Substances 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 description 7
- 238000009434 installation Methods 0.000 description 6
- 239000002699 waste material Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000012423 maintenance Methods 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 239000000835 fiber Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 230000002301 combined effect Effects 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ド水ヤの他の有機性汚水の処理にJdいて発
生するスクリーンかすの合理的な処理方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for rationally treating screen residue generated during the treatment of other organic sewage from a water tank.
有機性汚水は、一般に紙類、毛髪、野菜くず等の夾雑物
を多1出に含んでいるために、あらかじめこれらの夾雑
物がスクリーンによって除去されたのち、活性1’5泥
処理などで処理され−〔いる。スクリーンで除去された
夾雑物(以下「スクリーンかす」という)は、きわめて
不衛生であり、従来埋立もしくは焼却にて処分されてい
るが、スクIJ−ンかすの運搬途中での悪臭の発生、汚
水の漏出などの二次公害を招(ため、スクリーンかすを
攪拌洗浄槽で洗浄したのち脱水するという、スクリーン
かずの専用処理施設を設ける例が多くなっている。Organic sewage generally contains a lot of impurities such as paper, hair, and vegetable scraps, so these impurities are first removed with a screen and then treated with activated 1'5 mud treatment. It is - [there is. The impurities removed by screens (hereinafter referred to as "screen scum") are extremely unsanitary and are conventionally disposed of by landfill or incineration, but during transportation of screen scum, a foul odor is generated and sewage is disposed of. This can lead to secondary pollution such as leakage of water, so in many cases dedicated processing facilities for screen waste are being set up, where the screen waste is washed in an agitating cleaning tank and then dehydrated.
しかしながら7このような方法では、当然の結果として
スクリーンかすの洗浄槽と脱水機を設置するために、多
額の設イrIN費、維持経費を安し、維持・1〒埋要員
も必要となるという欠点があった。However,7 such a method naturally requires a large amount of installation and maintenance costs, as well as maintenance and burial personnel, in order to install a screen scum cleaning tank and dewatering machine. There were drawbacks.
本発明は、従来スクリーンかすの処理に不可欠であった
専用の洗浄槽や脱水機を不要とし、同時に有機性汚水処
理過程で発生するtり泥をも合理的に脱水する方法を提
供することを目的とするものである。The present invention aims to provide a method that eliminates the need for a dedicated cleaning tank and dehydrator, which were conventionally indispensable for treating screen scum, and at the same time rationally dewaters sludge generated during the organic sewage treatment process. This is the purpose.
本発明は、有機性汚水処理において、該汚水中の夾、雑
物をスクリーンで除去して得られたスクリーンかすな水
に縣淵したのち、該懸濁スラリなポンプにて圧送し、こ
の圧送されたii5濁スラスラリ液分離して分離スクリ
ーンかすを得、該分離スクリーンかすを前記有機性汚水
処理にて発生した汚泥に混合したのち脱水設備にて脱水
することを特徴とするものである。In organic sewage treatment, the present invention involves removing impurities and impurities in the sewage with a screen, draining the resulting screen-grained water, and then pumping the suspended slurry with a pump. The method is characterized in that the resulting ii5 turbid slurry liquid is separated to obtain a separation screen sludge, the separation screen sludge is mixed with the sludge generated in the organic sewage treatment, and then dehydrated in a dewatering facility.
本発明の一実施例な図面を参照しながら説明すれば、下
水1(雨天時放流下水も包含する)は、スクリーン2に
流入し、スクリーンかす6と除渣下水4に分離される。To explain with reference to the drawings which are an embodiment of the present invention, sewage 1 (including sewage discharged in rainy weather) flows into a screen 2 and is separated into screen scum 6 and sewage 4.
除渣下水4は1次いで最初沈殿池5にて沈殿分離され、
分離された初沈汚泥6はシラフナ7に導かれる一方、上
澄水8は曝気槽9にて生物処理されたのち最終沈殿池1
0でさらに沈降分離され、上澄は処理水11となって流
出する。また、最終沈殿池10で沈殿分離された汚泥の
一部は曝気槽9に返送され、残部の余剰汚泥12はシラ
フナ7に導かれ、前記初沈tll泥6と共に濃縮される
。The filtered sewage 4 is then subjected to sedimentation and separation in the first settling tank 5.
Separated initial settling sludge 6 is led to Shirafuna 7, while supernatant water 8 is biologically treated in an aeration tank 9 and then transferred to a final settling tank 1.
The water is further separated by sedimentation at 0, and the supernatant becomes treated water 11 and flows out. Further, a part of the sludge that has been settled and separated in the final settling tank 10 is returned to the aeration tank 9, and the remaining surplus sludge 12 is led to the Shirafuna 7 and concentrated together with the initial settling tll mud 6.
一方、スクリーン2で分離されたスクリーンかす6は、
要すれば細断機16にて細断されたのち、除渣下水4の
一部4′又は清水その他の適当な水を加えて)踵濁スラ
リ14とされ、ポンプ15によって管路16を経て、後
述する汚泥脱水設備21の設置場所又はその近くに設け
らオtだスクリーン、遠心分離、重力分離などの固液分
離工程17へ圧送される。この懸?1・:5スラリ14
のポンプ15によイノ圧送は、本発明に16いてII(
姿なる意べを有するもので、輸送機能のほかに輸送中に
管路16中に、tLIいてスクリーンかず6が洗浄され
るという重要な、11j、合機能?もつ−Cいる。一般
に、スクリーン2の設置」易ンツ「と7r5泥)ル;1
水設置1iii 21の設置f’2場所は離れており、
F水処卯」易/、【どでは数十〜数ゴnlの距離があり
、稲にはa簡に達することがあり、スクリーンかす6は
ポンプ15(/こ」、る圧送中に管路16中で十分Vこ
洗a)されることが確認された。On the other hand, the screen dregs 6 separated by the screen 2 are
If necessary, the slurry is shredded by a shredding machine 16 and then mixed with a portion 4' of the sewage 4 or fresh water or other suitable water) to form a turbid slurry 14, which is then passed through a pipe 16 by a pump 15. The sludge dewatering equipment 21, which will be described later, is installed at or near the installation site, and the sludge is sent under pressure to a solid-liquid separation process 17, such as an extra screen, centrifugation, or gravity separation. This stake? 1.:5 slurry 14
Ino pressure feeding by the pump 15 of the present invention is described in 16 and II (
In addition to its transportation function, it also has the important function of cleaning the screen 6 with tLI in the pipe 16 during transportation. Motsu-C is here. In general, the installation of the screen 2"easy" and 7r5 mud) le; 1
Water installation 1iii 21 installation f'2 location is far away,
There is a distance of several tens to several gonl in the water treatment area, and it may reach a distance for rice, and the screen waste 6 is transferred to the pipe line during pressure feeding by the pump 15. It was confirmed that V-washing a) was carried out sufficiently in 16.
このようにし−C1圧送された%i濁ススラリ14゜固
液分&ji’C工44i 17で同・夜分b1tされ、
液分18は曝気槽9に送られ′C処理される。また洗浄
、分1々1#された分離スクIJ−ンかず19は、シラ
フナ7で濃縮された濃縮汚泥20に混合されたのち、必
要ならばカチオンポリマなどの脱水助剤を添加し、ロー
ル又はペルトゲレスIiQ /に磯、遠心脱水機、真空
脱水機、スクリュープレス脱水機などの汚泥脱水設備2
1にて脱水され、脱水ケーキ22となる。In this way, the %i turbid soot slurry pumped by C1 was mixed with 14° solid-liquid content &ji'C engineering 44i 17 at the same time, and
The liquid portion 18 is sent to the aeration tank 9 and subjected to 'C treatment. In addition, the washed and separated sludge 19 is mixed with the thickened sludge 20 concentrated in the Shirafuna 7, and if necessary, a dewatering aid such as a cationic polymer is added, and then a roll or Sludge dewatering equipment 2 such as Peltogeles IiQ/Niiso, centrifugal dehydrator, vacuum dehydrator, screw press dehydrator, etc.
The cake is dehydrated in step 1 to become a dehydrated cake 22.
前記処理方法において、スクリーンかす6を細断機16
によって細断したときは、スクリーンかす6の洗浄効果
が著しく高まり、濃縮汚泥20との混合が均質化されや
すくなるから、脱水効果も向上するという複合効果があ
る。In the processing method, the screen residue 6 is shredded by a shredder 16.
When it is shredded, the cleaning effect of the screen sludge 6 is significantly enhanced, and the mixing with the thickened sludge 20 becomes easier to homogenize, which has the combined effect of improving the dewatering effect.
また、前記のように初沈汚泥6と余剰汚泥12を一緒に
処理する巳とな(、余剰汚泥12に対してのみ分離スク
リーンかす19を混合することも合理的である。すなわ
ち、脱水性の悪い余剰汚泥12に対しての分離スクリー
ンかす19の添加率が多くなるから、離脱水性とされて
いる余剰N5 IQの119水を効果的に行うことがで
き、元来濃縮脱水性の良好な初沈汚泥6は別途容易に脱
水できるから、きわめて合理的である。In addition, as described above, it is also reasonable to treat the initial settling sludge 6 and the surplus sludge 12 together (and to mix the separation screen sludge 19 only with the surplus sludge 12. In other words, it is reasonable to Since the addition ratio of the separation screen sludge 19 to the bad surplus sludge 12 increases, it is possible to effectively remove the surplus N5 IQ 119 water, which is considered to be a water-releasable one, and to use a sludge that originally has good concentration and dewatering properties. This is extremely rational since the sludge 6 can be easily dehydrated separately.
さらにまた、/lテ泥に洗浄2分離された分離スクリー
ンかす19を混合することにより1分離スクリーンかす
19中の特に繊維分が汚泥の脱水助剤の働きをし、きわ
めて低含水率の脱水ケーキを得ることができるが、汚泥
脱水設備21としてスクリュープレス脱水機を使用する
と、前記繊維分tこよって汚泥のt1ψりや共回りが防
止され、圧力が十分にかかつてきわめて低含水率の脱水
ケーキ22を得イフことかできる。Furthermore, by mixing the separated screen sludge 19 that has been washed and separated into the /l mud, the fiber content in the 1-separated screen sludge 19 acts as a dehydration aid for the sludge, resulting in a dehydrated cake with an extremely low water content. However, when a screw press dehydrator is used as the sludge dewatering equipment 21, the fiber content t prevents the sludge from t1ψ rotation and co-rotation, and when the pressure is sufficient, a dehydrated cake 22 with an extremely low water content can be obtained. You can do that if you get it.
なお、i′1;j濁スラリ14の固液分離工程17を省
略(2,11−11,q:5スラリ14をシラフナ7へ
導いて初沈汚泥6や余剰llt泥12の7b’2縮と共
に固液外1iif&することもでき、既存施設の有効利
用が可能となり。Note that the solid-liquid separation step 17 of the i'1; At the same time, it is also possible to perform solid-liquid external 1IIF&, making it possible to effectively utilize existing facilities.
また沈降淵縮件のきわめて良好な+) !1!I#スク
リーンかす19によってt45記が圧密を受け、汚泥自
身の謬縮度を向上することができる。Also, the sedimentation abyss condition is extremely good +)! 1! The t45 sludge is compacted by the I# screen sludge 19, and the degree of compaction of the sludge itself can be improved.
以上述べたようVこ本発明によれば、有機性ρl水処1
’Jijにfdけるスクリーンかずと汚泥の両者をきわ
めて合理的に処Jqjすることができ1次のような有益
なる効果を生ずるものである。As described above, according to the present invention, organic ρl water treatment 1
It is possible to treat both the screen waste and the sludge that go into the tank very rationally, and the following beneficial effects are produced.
(リスクリーンかずの混合によりスクリーンかすと汚泥
を同時に処理することができ、汚泥の脱水をきわめて合
Ijij的、効果的に行うことができ、きわめて低含水
率の脱水ケーキを得ることができる。(By mixing the rescreen scraps, the screen scraps and sludge can be treated at the same time, and the sludge can be dehydrated in a very integrated and effective manner, making it possible to obtain a dehydrated cake with an extremely low water content.
(リ 従来のスクリーンかすだけの洗浄、脱水、貯留、
運搬等の諸作業を不要にし、〕jl+、御中の二次公害
を防止ずく)ことができる。(Re) Conventional cleaning, dehydration, and storage of only screen scum,
This eliminates the need for various operations such as transportation, and prevents secondary pollution.
■ スクリーンかす専用の洗浄槽、脱水機等の設(+i
fiが不゛堤となり、設備費、維持、経費をカ1j減す
ることができろ。■ Installation of cleaning tank, dehydrator, etc. exclusively for screen residue (+i
FI becomes a barrier, and equipment costs, maintenance, and expenses can be reduced by 1j.
図面は/l(発明の一実施例を示す系統説明図である。
1・・・下水、2・・・スクリーン、6・・・スクリー
ンがす、4,4′・・・除直下水、5・・・最初沈殿池
、6・・・初沈汚泥、7・・・シラフナ、9・・・曝気
槽、10・・・最終沈殿池、11・・・処理水、12・
・・余剰汚泥、16・・・イ(B断機、14・・・懸濁
スラリ、15川ポンプ、16・・・管路、17・・・固
液分し;准工程、19・・・分離スクリーンかす、20
・・・濃縮汚泥、21・・・79泥脱水設備。
22・・・脱水ケーキ。
特許出願人 荏原インフィルコ株式会社代理人 弁理士
高 木 正 行The drawing is /l (system explanatory diagram showing one embodiment of the invention. 1...Sewage, 2...Screen, 6...Screen gas, 4, 4'...Sewage directly removed, 5 ... Initial settling tank, 6... Initial settling sludge, 7... Shirafuna, 9... Aeration tank, 10... Final settling tank, 11... Treated water, 12.
...Excess sludge, 16...A (B cutter, 14...Suspended slurry, 15 River pump, 16...Pipe line, 17...Solid-liquid separation; Associate process, 19... Separation screen residue, 20
...Thickened sludge, 21...79 Sludge dewatering equipment. 22...Dehydrated cake. Patent applicant: Ebara Infilco Co., Ltd. Representative Patent attorney: Masayuki Takagi
Claims (1)
・スクリーンで除去して得られたスクリーンかすを水に
懸濁したのち、該懸濁スラリをポンプに℃圧送し、この
圧送された懸濁スラリを固液針!!+18 して分離ス
クリーンかずを得。 該分離スクリーンかすを前記有機性汚水処理にて発生し
た汚泥に混合したのち脱水設備にて脱水することを特徴
とするスクリーンかすの処理方法。 2 前記スクリーンかすを細断したのち水に懸濁するも
のである特許請求の範囲第1項記載のスクリーンかすの
処理方法。 3、 前記有機性lケ水処理にて発生した汚泥が余剰汚
泥である特、請求の範囲第1項又は第2項記載のスクリ
ーンかすの処理方法。 4 前記脱水設備がスクリュープレス脱水機を使用する
ものである特許請求の範囲第1項、第2項又は第:つ項
記載のスクリーンかすの処理方法。[Claims] J. In organic wastewater treatment, impurities in the wastewater 4
- After suspending the screen residue obtained by removing it with a screen in water, the suspended slurry is pumped to a pump at °C, and this pumped suspended slurry is transferred to a solid liquid needle! ! +18 and get a separation screen scrap. A method for treating screen dregs, which comprises mixing the separated screen dregs with the sludge generated in the organic sewage treatment and then dewatering the sludge in a dewatering facility. 2. The method for treating screen scum according to claim 1, wherein the screen scum is shredded and then suspended in water. 3. The method for treating screen dregs according to claim 1 or 2, wherein the sludge generated in the organic water treatment is surplus sludge. 4. The method for treating screen dregs according to claim 1, 2 or 2, wherein the dewatering equipment uses a screw press dehydrator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59043747A JPS60190300A (en) | 1984-03-09 | 1984-03-09 | Treatment of screen dregs |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59043747A JPS60190300A (en) | 1984-03-09 | 1984-03-09 | Treatment of screen dregs |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS60190300A true JPS60190300A (en) | 1985-09-27 |
Family
ID=12672350
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59043747A Pending JPS60190300A (en) | 1984-03-09 | 1984-03-09 | Treatment of screen dregs |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60190300A (en) |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS529944A (en) * | 1975-07-11 | 1977-01-25 | Dorr Oliver Inc | Method of disposing of refuse filtered from waste water |
JPS5617690A (en) * | 1979-07-24 | 1981-02-19 | Ebara Infilco Co Ltd | Dehydrating method for sludge |
-
1984
- 1984-03-09 JP JP59043747A patent/JPS60190300A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS529944A (en) * | 1975-07-11 | 1977-01-25 | Dorr Oliver Inc | Method of disposing of refuse filtered from waste water |
JPS5617690A (en) * | 1979-07-24 | 1981-02-19 | Ebara Infilco Co Ltd | Dehydrating method for sludge |
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