JPS6061013A - Solid/liquid separating apparatus - Google Patents
Solid/liquid separating apparatusInfo
- Publication number
- JPS6061013A JPS6061013A JP58167540A JP16754083A JPS6061013A JP S6061013 A JPS6061013 A JP S6061013A JP 58167540 A JP58167540 A JP 58167540A JP 16754083 A JP16754083 A JP 16754083A JP S6061013 A JPS6061013 A JP S6061013A
- Authority
- JP
- Japan
- Prior art keywords
- screen
- sludge
- separated
- liquid
- suspension
- 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.)
- Granted
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 28
- 239000007787 solid Substances 0.000 title abstract description 15
- 239000010802 sludge Substances 0.000 claims abstract description 45
- 238000000926 separation method Methods 0.000 claims abstract description 17
- 239000000725 suspension Substances 0.000 claims abstract description 15
- 229920000642 polymer Polymers 0.000 claims description 8
- 238000004062 sedimentation Methods 0.000 claims description 7
- 239000002002 slurry Substances 0.000 abstract description 6
- 239000006228 supernatant Substances 0.000 abstract description 5
- 238000001556 precipitation Methods 0.000 abstract description 4
- 238000004064 recycling Methods 0.000 abstract description 2
- 239000006194 liquid suspension Substances 0.000 abstract 2
- 230000003311 flocculating effect Effects 0.000 abstract 1
- 238000003756 stirring Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 7
- 238000011282 treatment Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000005189 flocculation Methods 0.000 description 3
- 230000016615 flocculation Effects 0.000 description 3
- 238000005345 coagulation Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001546 nitrifying effect Effects 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、懸濁液中の懸濁固形分を高濃度の濃縮汚泥と
して分離する固液分離方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a solid-liquid separation method for separating suspended solids in a suspension into highly concentrated concentrated sludge.
従来、懸、濁液中の懸濁固形分を分離する方法の一つと
して、スクリーンを利用するものが多くなってきている
みこの方法は、高分子凝集剤によって形成された凝集フ
ロックを、傾斜ウェッジワイヤスクリーン、回転スクリ
ーンその他のスクリーンによって分離するという方法で
あって、固液分離時間がきわめて短かいこと、また分離
された汚泥濃度が、従来の凝集沈殿よりも高くなり、爾
後の脱水その他の汚泥処理を有利にするという利点があ
る。Conventionally, screens are increasingly used as a method for separating suspended solids in suspended or turbid liquids.This method uses a screen to separate flocs formed by a polymer flocculant. This method uses wedge wire screens, rotating screens, and other screens for separation, and the solid-liquid separation time is extremely short, and the separated sludge concentration is higher than that of conventional coagulation and sedimentation, making it difficult to perform subsequent dewatering or other processes. It has the advantage of making sludge treatment advantageous.
しかしながら、スクリニンで液中の凝集フロックを完全
に分離することは不可能であり、スクリーンを通過する
分離液中にかなりの量の固形分が残っているという問題
点があった。また、スクリーンで分離された分離液中の
固形分をさらに分離するために沈殿処理を行っても、沈
殿汚泥濃度はスクリーンで分離された汚泥の半分にも達
せず、これら両汚泥を脱水する場合に、スークリーンで
折角高濃度に濃縮された汚泥が低濃度の沈殿汚泥によっ
て希釈されてしまい、脱水その他の汚泥処理を不利にす
るという問題点もあった。However, it is impossible to completely separate flocs in the liquid using screenin, and there is a problem in that a considerable amount of solid content remains in the separated liquid that passes through the screen. In addition, even if sedimentation treatment is performed to further separate the solid content in the separated liquid separated by the screen, the concentration of the settled sludge does not reach even half of the sludge separated by the screen, and when both sludges are dewatered. Another problem was that the sludge that had been concentrated to a high concentration in the Suclean system was diluted by low-concentration settled sludge, making dewatering and other sludge treatments disadvantageous.
本発明は、これら従来の問題点を解決し、常に安定して
高濃度の濃縮汚泥を得ることができ、汚泥処理をも有利
たらしめる固液分離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 solve these conventional problems and provide a solid-liquid separation method that can always stably obtain highly concentrated concentrated sludge and that also makes sludge treatment advantageous. .
本発明は、懸濁液に少なくとも高分子凝集剤を添加して
凝集フロックを形成せしめたのち、該凝集フロックをス
クリーンによって濃縮分離し、スクリーンを透過した分
離液を沈降分離し、得られた沈殿汚泥を前記懸濁液に混
合することを特徴とするものである。The present invention involves adding at least a polymer flocculant to a suspension to form flocs, then concentrating and separating the flocs using a screen, and separating the separated liquid that has passed through the screen by sedimentation. The method is characterized in that sludge is mixed into the suspension.
本発明の一実施態様を図面を参照しながら説明すれば、
懸濁固形分を含む懸濁液lに少なくとも高分子凝集剤2
を添加するが、液中の色度、リン、CODなどを同時に
除去しようとするときは鉄塩、アルミニウム塩などの無
機凝集剤を併用する。この少なくとも高分子凝集剤2が
添加された懸濁液lを、フロック形成槽3に導き、攪拌
混和して粗大な凝集フロックを形成させて凝集スラリー
4とし、分配槽5を経て約60度に傾斜している傾斜ウ
エッジスイヤスクリーン6を流下させ、濃縮汚泥7とス
クリーン6を透過する分離液8に分離する。このスゲリ
ーン6で分離された濃縮汚泥7は、例えば余剰活性汚泥
の場合は固形物濃度4〜4.5%という高濃度に濃縮さ
れ貯槽9に至る。An embodiment of the present invention will be described with reference to the drawings.
At least 2 polymer flocculants are added to the suspension l containing suspended solids.
However, when trying to remove chromaticity, phosphorus, COD, etc. from the liquid at the same time, an inorganic flocculant such as iron salt or aluminum salt is used in combination. This suspension l to which at least the polymer flocculant 2 has been added is led to a flocculation tank 3, stirred and mixed to form coarse flocs to form a flocculation slurry 4, and passed through a distribution tank 5 to a temperature of about 60 degrees. The sludge is allowed to flow down an inclined wedge sewage screen 6 and is separated into a thickened sludge 7 and a separated liquid 8 that passes through the screen 6. The concentrated sludge 7 separated by this Sgeleen 6 is concentrated to a high solids concentration of 4 to 4.5% in the case of surplus activated sludge, for example, and reaches the storage tank 9.
前記スクリーン6を透過した分離液8には、スクリーン
6では完全に分離しきれなかった固形分が混入しており
、そのまま放流することができない。したがって、この
分離液8を沈殿槽lOに導いて固形物濃度1〜1.5%
程度の沈殿汚泥11と上澄液12とに沈殿分離し、上澄
液12を放流することができる。The separated liquid 8 that has passed through the screen 6 contains solids that could not be completely separated by the screen 6, and cannot be discharged as is. Therefore, this separated liquid 8 is led to the precipitation tank 1O to have a solid content of 1 to 1.5%.
It is possible to separate the precipitated sludge 11 into a supernatant liquid 12 and discharge the supernatant liquid 12.
また、沈殿槽lOで分離された沈殿汚泥11をリサイク
ルし、原懸濁液lに混合して再び前記のようにしてスク
リーン6で固液分離する。ここで注意すべきは、沈殿汚
泥11をスクリーン6で分離された濃縮汚泥7の貯槽9
に導入しないことであり、もし貯槽9に導入ずれは、折
角スクリーン6によって高濃度に濃縮された濃縮汚泥7
の濃度が低濃度の沈殿汚泥11によって希釈されるとい
う好ましからざる結果をもたらす。Further, the settled sludge 11 separated in the settling tank 10 is recycled, mixed with the original suspension 1, and solid-liquid separated again in the screen 6 as described above. What should be noted here is that the storage tank 9 contains the concentrated sludge 7 from which the precipitated sludge 11 has been separated by the screen 6.
If the introduction into the storage tank 9 is delayed, the concentrated sludge 7 that has been concentrated to a high concentration by the screen 6
This has the undesirable result that the concentration of sludge is diluted by the low concentration of settled sludge 11.
このようにして、高濃度のスクリーン分離濃縮汚泥7の
みを、例えば脱水工程13に供給することになり、汚泥
脱水工程の処理能力は向上され、生ずる脱水ろ液の量は
減少する。In this way, only the highly concentrated screen-separated thickened sludge 7 is supplied to, for example, the dewatering step 13, so that the throughput of the sludge dewatering step is improved and the amount of dewatered filtrate produced is reduced.
以上述べたように、本発明は懸濁液中に粗大な凝集フロ
ックを形成し、この凝集フロックをスクリーンによって
高濃度の濃縮汚泥として分離し、スクリーンを透過した
分離液を沈殿分離してその沈殿汚泥を原懸濁液にリサイ
クルするものであるから、次のような効果を得ることが
できるものである。As described above, the present invention forms coarse flocs in a suspension, separates the flocs as highly concentrated concentrated sludge using a screen, and separates the separated liquid that has passed through the screen by precipitation. Since sludge is recycled into a raw suspension, the following effects can be obtained.
■ スクリーン分離と沈殿分離の2段直列分離法により
、スクリーンにおける固形分回収率が悪化した場合でも
、安定して清澄な処理液を得ることができる。(2) The two-stage series separation method of screen separation and precipitation separation makes it possible to stably obtain a clear treated liquid even if the solid content recovery rate in the screen deteriorates.
■ 沈殿汚泥を原懸濁液にリサイクルし、脱水工程など
に供給する汚泥を高濃度のスクリーン濃縮汚泥のみにし
たから、脱水工程などの処理能力が向上する。■ Since settled sludge is recycled to the raw suspension and the sludge supplied to the dewatering process is only high-concentration screen thickened sludge, the processing capacity of the dewatering process is improved.
■ 沈殿汚泥を原懸濁液にリサイクルすることによって
、沈殿汚泥自体が凝集助剤としての効果を発揮する。■ By recycling the settled sludge into the original suspension, the settled sludge itself becomes effective as a coagulation aid.
次に本発明の実施例を示す。Next, examples of the present invention will be shown.
し尿を無希釈で生物学的硝化脱窒素処理した生物処理水
にpec15を1500ダ/l添加したのちCa(OH
)2 でpH4〜5に中和し、さらにノニオン系高分子
凝集剤を10m9/l添加し、混合して凝集スラリとし
、これを60°傾斜ウエツジワイヤスクリーン(目開き
0.5mm)上に流下させたところ、分離時間1〜3秒
で固形物濃度4〜4.8%の濃度汚泥を得たが、スクリ
ーンを透過した分離水の固形分は500〜1000m9
/lと多かった。この分離水を沈殿槽において沈降分離
速度20mm/minで固液分離したところ、固形物濃
度1〜1.5%の沈殿汚泥を得た。After adding 1500 da/l of pec15 to the biologically treated water obtained by biologically nitrifying and denitrifying human waste without diluting it, Ca(OH
) 2 to pH 4 to 5, then add 10 m9/l of a nonionic polymer flocculant, mix to form a flocculation slurry, and place this on a 60° inclined wedge wire screen (openings 0.5 mm). When the sludge was allowed to flow down, a solid sludge with a solid concentration of 4 to 4.8% was obtained in a separation time of 1 to 3 seconds, but the solid content of the separated water that passed through the screen was 500 to 1000 m9.
There were as many as /l. This separated water was subjected to solid-liquid separation in a sedimentation tank at a sedimentation rate of 20 mm/min to obtain precipitated sludge with a solid concentration of 1 to 1.5%.
この沈殿汚泥を上記の生物処理水にリサイクルして再び
上記のスクリーン分離番行ったζころ、スクリーン分離
効果の悪化は認められず、逆にノニオン系高分子凝集剤
の添加量を7m9/lに減少させることができた。This precipitated sludge was recycled into the above-mentioned biologically treated water and subjected to the above-mentioned screen separation again. No deterioration of the screen separation effect was observed, and on the contrary, the amount of nonionic polymer flocculant added was reduced to 7 m9/l. was able to reduce it.
また、スクリーン分離により得られた高濃度の濃縮汚泥
をフィルタプレス脱水機で脱水したが、沖過速度は2.
8〜3.0 kll DS / m @hrという高い
値で、得られた脱水ケーキの含水率は65〜67%であ
った。In addition, the highly concentrated concentrated sludge obtained by screen separation was dehydrated using a filter press dehydrator, but the offshore overspeed was 2.
The moisture content of the obtained dehydrated cake was 65-67% with high values of 8-3.0 kll DS/m@hr.
図面は本発明の一実施態様を示す系統説明図である。
1・・・・・・懸濁液、2・・・・・・高分子凝集剤、
3・・・・・・フロック形成槽、4・・・・・・凝集ス
ラリー、5・・・・・・分配槽、6・・・・・・傾斜ウ
ェッジワイヤスクリーン、7・・・・・・濃縮汚泥、訃
・・・・・分離液、9・・・・・・貯槽、1G・・・・
・・沈殿槽、11・・・・・・沈殿汚泥、12・・・・
・・上澄液、11・・・・・・脱水工程。
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
代理人弁理士 千 1) 稔
代理人弁理士 丸 山 隆 夫The drawing is a system explanatory diagram showing one embodiment of the present invention. 1...Suspension, 2...Polymer flocculant,
3...Floc formation tank, 4...Agglomerated slurry, 5...Distribution tank, 6...Incline wedge wire screen, 7... Thickened sludge, sludge...separated liquid, 9...storage tank, 1G...
...Sedimentation tank, 11...Settled sludge, 12...
...Supernatant liquid, 11...Dehydration step. Patent applicant: Patent attorney representing Ebara Infilco Co., Ltd.
Masayuki Takagi, Patent Attorney 1) Minoru, Patent Attorney Takao Maruyama
Claims (1)
クを形成せしめたのち、該凝集フロックをスクリーンに
よって濃縮分離し、スクリーンを透過した分離液を沈降
分離し、得られた沈殿汚泥を前記懸濁液に混合すること
を特徴とする固液分離方法。After adding at least a polymer flocculant to the suspension to form flocs, the flocs are concentrated and separated using a screen, the separated liquid that has passed through the screen is separated by sedimentation, and the resulting precipitated sludge is transferred to the suspension. A solid-liquid separation method characterized by mixing in a turbid liquid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58167540A JPS6061013A (en) | 1983-09-13 | 1983-09-13 | Solid/liquid separating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58167540A JPS6061013A (en) | 1983-09-13 | 1983-09-13 | Solid/liquid separating apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6061013A true JPS6061013A (en) | 1985-04-08 |
| JPS6345601B2 JPS6345601B2 (en) | 1988-09-09 |
Family
ID=15851592
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58167540A Granted JPS6061013A (en) | 1983-09-13 | 1983-09-13 | Solid/liquid separating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6061013A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102284210A (en) * | 2011-05-31 | 2011-12-21 | 神华集团有限责任公司 | Method for separating and filtering molecular sieve crystallization slurry |
| CN108862700A (en) * | 2018-06-15 | 2018-11-23 | 宁波暄妍日化科技有限公司 | A kind of efficient flocks processing unit of sewage treatment |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5715898A (en) * | 1980-07-01 | 1982-01-27 | Ebara Infilco Co Ltd | Treatment of organic waste liquid |
-
1983
- 1983-09-13 JP JP58167540A patent/JPS6061013A/en active Granted
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5715898A (en) * | 1980-07-01 | 1982-01-27 | Ebara Infilco Co Ltd | Treatment of organic waste liquid |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102284210A (en) * | 2011-05-31 | 2011-12-21 | 神华集团有限责任公司 | Method for separating and filtering molecular sieve crystallization slurry |
| CN108862700A (en) * | 2018-06-15 | 2018-11-23 | 宁波暄妍日化科技有限公司 | A kind of efficient flocks processing unit of sewage treatment |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6345601B2 (en) | 1988-09-09 |
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