JPH03101900A - Method for dehydrating sewage sludge - Google Patents
Method for dehydrating sewage sludgeInfo
- Publication number
- JPH03101900A JPH03101900A JP1237841A JP23784189A JPH03101900A JP H03101900 A JPH03101900 A JP H03101900A JP 1237841 A JP1237841 A JP 1237841A JP 23784189 A JP23784189 A JP 23784189A JP H03101900 A JPH03101900 A JP H03101900A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- press
- cake
- added
- screw press
- 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
- 239000010801 sewage sludge Substances 0.000 title claims abstract description 10
- 238000000034 method Methods 0.000 title claims description 11
- 239000010802 sludge Substances 0.000 claims abstract description 29
- 235000007164 Oryza sativa Nutrition 0.000 claims description 13
- 239000010903 husk Substances 0.000 claims description 13
- 235000009566 rice Nutrition 0.000 claims description 13
- 240000007594 Oryza sativa Species 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract 1
- 241000209094 Oryza Species 0.000 description 12
- 239000002184 metal Substances 0.000 description 5
- 229920000642 polymer Polymers 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 2
- 239000002562 thickening agent Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 239000005909 Kieselgur Substances 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000000920 calcium hydroxide Substances 0.000 description 1
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 1
- 235000011116 calcium hydroxide Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 210000003608 fece Anatomy 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は下水汚泥の脱水方法の改良に関し、脱水性が
よく、然も、脱水後のケーキの処分が容易な方法を提案
するものである。[Detailed Description of the Invention] [Industrial Application Field] This invention relates to an improvement in a method for dewatering sewage sludge, and proposes a method that has good dewatering properties and allows easy disposal of the cake after dewatering. .
従来、この種下水汚泥の脱水方法として、下水汚泥を濃
縮したのち、この濃縮汚泥に高分子凝集剤を添加してフ
ロックをさらに或長させてこれをベルトプレス、遠心脱
水機で脱水する方法や濃縮汚泥に石炭粉末や珪藻土等の
枦過助材を添加してフィルタプレスやベルトプレスで脱
水することが知られている。特公昭59−24879号
は高分子凝集剤を添加する例であり、特公昭39−70
44号、特公昭56−24600号は、汚泥に消石灰や
炭素粉末を添加する例である。Conventionally, methods for dewatering this type of sewage sludge include methods of concentrating the sewage sludge, adding a polymer flocculant to the thickened sludge to further lengthen the flocs, and dewatering the flocs using a belt press or centrifugal dehydrator. It is known that a filtering aid such as coal powder or diatomaceous earth is added to concentrated sludge and the sludge is dewatered using a filter press or belt press. Japanese Patent Publication No. 59-24879 is an example of adding a polymer flocculant, and Japanese Patent Publication No. 39-70
No. 44 and Japanese Patent Publication No. 56-24600 are examples of adding slaked lime and carbon powder to sludge.
然しなから、従来の高分子凝集剤を添加する方法では、
フロックが比較的弱体であり、これを加圧して炉過脱水
すると、枦布等からケーキを剥離することがむつかしく
、従って、高分子凝集剤を添加した汚泥の脱水は枦布の
再生洗浄の容易なベルトプレスやp材の再生をしない遠
心脱水機で行なわれ、脱水の場合の加圧力低く、これら
の機械で脱水されたケーキは含水率が高い。従って、事
後に焼却するにしても投棄するにしても間殿がある。ま
た、石灰等の助材を添加する方法では、含水率を下げ得
るが添加した助材の量だけ、ケーキが増加し、その処分
に経費を要するのみならず、特に、石灰(消石灰)や珪
藻土を添加するとこれらが燃えないので焼却処分する場
合には間Mがある。However, in the conventional method of adding a polymer flocculant,
The flocs are relatively weak, and if they are pressurized and over-dehydrated in the furnace, it is difficult to separate the cake from the sludge, etc. Therefore, dehydration of sludge added with a polymer flocculant makes it easier to recycle and clean the sludge. The process is carried out using a belt press or a centrifugal dewatering machine that does not regenerate the p-material, and the pressure applied during dewatering is low, and the cake dewatered using these machines has a high moisture content. Therefore, there is a difference between incineration and dumping after the fact. In addition, with the method of adding auxiliary materials such as lime, the moisture content can be lowered, but the cake increases by the amount of the added auxiliary material, and its disposal not only requires expense, but also If these are added, they will not burn, so when disposing of them by incineration, there is a time limit.
?の発明は、上述の脱水性を向上させる添加物の選定と
添加した汚泥の脱水手段に工夫を施すことによって前述
のよう■問題点を解消したものであって、その要旨とす
るところは、下水の濃縮汚泥に、粉砕した籾殻を添加混
合し、この混合汚泥をスクリュープレスで加圧脱水する
ようにしたものである。? The invention solves the above-mentioned problems by selecting additives that improve the dewatering properties and devising means for dewatering the added sludge. Crushed rice husks are added to and mixed with the thickened sludge, and this mixed sludge is dehydrated under pressure using a screw press.
この粉砕籾殻が添加された汚泥は、その微細な固形物が
籾殻粉末によって連結され、水と分離されて強固な核と
なる。従って、スクリュープレスで加圧した場合、フロ
ックが逃げることなく、強圧することができて水分のみ
がスクリュープレスのメタルメッシュによって分離され
る。すなわち、スクリュープレスは、円筒状のP過筒内
で、コーン状の送り体で汚泥が徐々に送られながら送り
羽根によって加圧脱水されるもので、密封状の室内で汚
泥を強圧するもので、ベルトプレス等のように汚泥が逃
げることがなく、高脱水されたケーキが得られるもので
ある。In the sludge to which this crushed rice husk is added, the fine solid matter is connected by the rice husk powder and separated from water to form a strong core. Therefore, when pressurizing with a screw press, strong pressure can be applied without causing flocs to escape, and only moisture is separated by the metal mesh of the screw press. In other words, in a screw press, sludge is gradually fed inside a cylindrical P-tube by a cone-shaped feeder and dehydrated under pressure by a feeder blade, and the sludge is strongly pressurized in a sealed chamber. Unlike belt presses, sludge does not escape, and a highly dehydrated cake can be obtained.
また、このスクリュープレスのp過簡に張られたメタル
メッシュは、ベルトプレスやフィルタプレスの炉布に比
較して、ケーキが付着しに<<、付着目詰りした場合で
もメタルメッシュが剛性を有し強度も高いので高圧洗浄
が可能である。さらにこの脱水方法により得られるケー
キは、籾殻を含んでいるので事後の焼却等の処理が容易
なるは勿論のこと、籾殻はシリカ等の無機質や有機質よ
りなるのでフンポストとして畠地等に還元しても安全で
ある。In addition, compared to the furnace cloth of belt presses and filter presses, the thinly stretched metal mesh of this screw press is less susceptible to cake adhesion, and the metal mesh has more rigidity even if it becomes clogged with adhesion. It also has high strength and can be washed under high pressure. Furthermore, since the cake obtained by this dehydration method contains rice husks, it is of course easy to dispose of them afterward, such as incineration, and since the rice husks are composed of inorganic and organic substances such as silica, they can be returned to fields as dung posts. is also safe.
図は、この発明に係る下水汚泥の脱水方法の概略のフロ
ーシ一トを示し、符号1はトロンメル式濃縮機、2は粉
砕した籾殻のホッパ− 3は濃縮汚泥と籾殻の混合槽、
4は移送ポンプ、5は脱水のためスクリュープレス、6
はケーキホッパ−7は脱水ケーキの取出スクリューであ
る。このように配列した装置では、汚泥濃縮機1に供給
された汚泥は、ここで若干の凝集剤が添加されて濃縮さ
れた汚泥がトロンメルaの開口から取出され、混合槽3
に送られる。そして、混合槽3では籾殻ホッパーかも粉
砕した籾殻が添加混合され、この混合汚泥は、移送ボン
ブ4によってスクリュープレス5で脱水され、ケーキホ
ッパ−6に貯留される。このスクリューブレス5での脱
水において、混合汚泥は粉砕した籾殻を含むので、これ
が核となりスクリュープレス5の送り羽根の加圧に対し
て逃げることがなく、その水分のみがスクリュプレス5
の枦過筒5aで分離され、高脱水ケーキを得ることがで
きる。そして、このような運転を継続してメタルメッシ
ュが目詰りしたときには、メタルメッシュが強度を有す
るので高圧の洗浄水等を用いて、目詰りを容易に解消す
ることができる。以上のようにしてケーキホッパーに溜
ったケーキは取出スクリュー7で取出され、焼却●コン
ポスト化等の次の処理に供することができる。The figure shows a general flowchart of the sewage sludge dewatering method according to the present invention, in which reference numeral 1 is a trommel type thickener, 2 is a hopper for crushed rice husks, 3 is a mixing tank for thickened sludge and rice husks,
4 is a transfer pump, 5 is a screw press for dewatering, 6
The cake hopper 7 is a screw for taking out the dehydrated cake. In the apparatus arranged in this way, the sludge supplied to the sludge thickener 1 is mixed with a small amount of flocculant, the concentrated sludge is taken out from the opening of the trommel a, and then transferred to the mixing tank 3.
sent to. Then, in the mixing tank 3, rice husks crushed by a rice husk hopper are added and mixed, and this mixed sludge is dehydrated by a screw press 5 by a transfer bomb 4 and stored in a cake hopper 6. During dewatering in this screw press 5, the mixed sludge contains crushed rice husks, so this becomes a nucleus and does not escape against the pressure of the feed blades of the screw press 5, and only the water is transferred to the screw press 5.
A highly dehydrated cake can be obtained. If the metal mesh becomes clogged by continuing such operation, the clogging can be easily eliminated using high-pressure cleaning water or the like, since the metal mesh has strength. The cake accumulated in the cake hopper as described above is taken out by the take-out screw 7 and can be subjected to subsequent processing such as incineration or composting.
以上の説明で明らかなように、この発明は従来ベルトプ
レスや遠心脱水機を用いて含水率の高いケーキしか得ら
れなかった下水の汚泥を粉砕した籾殻を添加して、これ
をスクリュープレスで脱水することにより高脱水ケーキ
が得られるようにしたものであク、スクリュープレスを
用いるが故に籾殻を添加した汚泥を強圧できる。然も、
連続作業であり稼動効率が高く、従来のフィルタプレス
に比較しても構造が簡単であること、脱水率がこれに比
肩し得る等、難枦過性の下水汚泥の処理上の従来の問題
点を悉く解消したものである。As is clear from the above explanation, this invention adds rice husks obtained by crushing sewage sludge, which conventionally only yielded a cake with high moisture content using a belt press or centrifugal dehydrator, and dehydrated it using a screw press. By doing so, a highly dehydrated cake can be obtained.Because a screw press is used, the sludge to which rice husks have been added can be strongly pressurized. Of course,
Conventional problems in processing difficult-to-permeate sewage sludge, such as continuous operation, high operating efficiency, simple structure compared to conventional filter presses, and comparable dewatering rate. This completely eliminates the problem.
図面は、この発明に係る脱水方法の模式フローシ一トで
ある。The drawing is a schematic flow sheet of the dehydration method according to the present invention.
Claims (1)
この混合汚泥をスクリュープレスで脱水することを特長
とする下水汚泥の脱水方法。(1) Add and mix crushed rice husks to concentrated sewage sludge,
A sewage sludge dewatering method characterized by dewatering this mixed sludge using a screw press.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1237841A JPH03101900A (en) | 1989-09-13 | 1989-09-13 | Method for dehydrating sewage sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1237841A JPH03101900A (en) | 1989-09-13 | 1989-09-13 | Method for dehydrating sewage sludge |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03101900A true JPH03101900A (en) | 1991-04-26 |
Family
ID=17021207
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1237841A Pending JPH03101900A (en) | 1989-09-13 | 1989-09-13 | Method for dehydrating sewage sludge |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03101900A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0850571A3 (en) * | 1996-11-26 | 1998-12-23 | SASIB FOOD S.p.A. | Juice extractor for fruit, in particular for bananas, papayas and tropical fruit in general |
| KR100321061B1 (en) * | 1997-12-16 | 2002-07-18 | 이구택 | How to improve sludge dewatering capacity |
| JP2006000766A (en) * | 2004-06-18 | 2006-01-05 | Ebara Corp | Sludge dehydration method |
| JP2006305518A (en) * | 2005-05-02 | 2006-11-09 | Ebara Engineering Service Co Ltd | Sludge dewatering method and apparatus |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6025595A (en) * | 1983-07-25 | 1985-02-08 | Ebara Infilco Co Ltd | Treatment of organic sludge |
-
1989
- 1989-09-13 JP JP1237841A patent/JPH03101900A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6025595A (en) * | 1983-07-25 | 1985-02-08 | Ebara Infilco Co Ltd | Treatment of organic sludge |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0850571A3 (en) * | 1996-11-26 | 1998-12-23 | SASIB FOOD S.p.A. | Juice extractor for fruit, in particular for bananas, papayas and tropical fruit in general |
| KR100321061B1 (en) * | 1997-12-16 | 2002-07-18 | 이구택 | How to improve sludge dewatering capacity |
| JP2006000766A (en) * | 2004-06-18 | 2006-01-05 | Ebara Corp | Sludge dehydration method |
| JP2006305518A (en) * | 2005-05-02 | 2006-11-09 | Ebara Engineering Service Co Ltd | Sludge dewatering method and apparatus |
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