JPS60183021A - Filteration of sludge - Google Patents

Filteration of sludge

Info

Publication number
JPS60183021A
JPS60183021A JP59039031A JP3903184A JPS60183021A JP S60183021 A JPS60183021 A JP S60183021A JP 59039031 A JP59039031 A JP 59039031A JP 3903184 A JP3903184 A JP 3903184A JP S60183021 A JPS60183021 A JP S60183021A
Authority
JP
Japan
Prior art keywords
coke powder
filter
coal coke
adsorbed
impurities
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
Application number
JP59039031A
Other languages
Japanese (ja)
Other versions
JPH0212125B2 (en
Inventor
Yoshihiko Takagi
高木 良彦
Kazuo Miyake
一男 三宅
Masao Inoue
正夫 井上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ishigaki Mechanical Industry Co Ltd
Original Assignee
Ishigaki Mechanical Industry Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Ishigaki Mechanical Industry Co Ltd filed Critical Ishigaki Mechanical Industry Co Ltd
Priority to JP59039031A priority Critical patent/JPS60183021A/en
Publication of JPS60183021A publication Critical patent/JPS60183021A/en
Publication of JPH0212125B2 publication Critical patent/JPH0212125B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To enable the application of a precoat filter machine to sludge, by facilitating the adsorption of flocs by forming the same by adding a high-molecular flocculant to a coal coke powder slurry and forming a leakage free coating layer. CONSTITUTION:3-10ppm of a high-molecular flocculant is added to a slurry of a coal coke powder with a particle size of 400mum or less to form floc and a cylindrical filter barrel is rotated in the floc formed slurry and the above mentioned coal coke powder is adsorbed by and laminated to the surface of the filter barrel to form a filter layer. Subsequently, the filter cylinder having the filter layer formed thereto is rotated in sewage to adsorb impurities by the surface of the filter layer and the adsorbed impurities are peeled off along with the laminated coal powder to regenerate the filtering surface and impurities are again adsorbed by the regenerated filtering surface. The concn. of the coating liquid is set to 20-30%.

Description

【発明の詳細な説明】 この発明は、汚泥等の濾過方法の改良に関し、特K、こ
の発明では、P材の表面に濾過助剤を予めコーティング
して濾過層を形成し、この濾過層の表面に付着した液中
の夾雑物をコーティング層と一緒に掻取シ、濾過面を更
゛新し乍ら連続的K濾過を行う形式のいわゆるグリコ−
1・濾過機における濾過方法の改良に関するものでるる
DETAILED DESCRIPTION OF THE INVENTION This invention relates to an improvement in a method for filtering sludge, etc., and in particular, in this invention, the surface of a P material is coated with a filter aid in advance to form a filtration layer, and this filtration layer is This is a so-called glycofilter that performs continuous K filtration while scraping off impurities in the liquid attached to the surface together with the coating layer and renewing the filtration surface.
1. Related to improvements in the filtration method in filters.

従来のプリコート濾過機の濾過助剤として珪藻土が一般
によく知られており、また、パーライト、石炭の微粉末
等多種多様のものが用いられている。然しなから、珪藻
土は不燃性物質を多量に含んでおシ、汚泥のように濾過
分離したケーキを焼却処分をするものに対しては、焼却
しK〈い上に減量効果が少なく、また、他の石炭等の微
粉末を用いる場合には、焼却処分するには有利であるが
、プリコート層の形成がむすがしぐ、下水汚泥のような
大量発生するものに対しては実用化されていない。
Diatomaceous earth is generally well known as a filter aid for conventional precoat filters, and a wide variety of other filter aids such as perlite and fine coal powder are also used. However, diatomaceous earth contains a large amount of non-combustible substances, and when it comes to incineration of filtered cakes such as sludge, it is difficult to incinerate and has little weight reduction effect. When using fine powder such as other coals, it is advantageous for incineration, but it is difficult to put into practical use for things that are generated in large quantities, such as sewage sludge, because the formation of a precoat layer is likely to occur. do not have.

この発明は、上述のようなグリコート濾過様における難
点を解消し、プリコー)濾過機を下水汚泥のように大量
に発生するものに対しても、適用可能にしたものであっ
て、その要旨とするところは、粒径が400μ以下の石
炭コークス粉末の溶解液に高分子凝集剤を3〜lo%添
加して70ッりを形成させ、その70ツクを形成した溶
液中で円WIJ型の濾過用を回転させて、その濾過j詞
の表面に上記石炭コークス粉末を吸着積層させて一過層
を形成し、次いで、一過層を形成した濾過用を汚水中で
回転させて、そのn】過層表面に汚水中の夾雑物を吸着
し、この吸着した夾雑物を積層した炭素粉末とともに剥
離して一過面を再生し、再び、夾雑物を吸着するように
したものでるる。
This invention solves the above-mentioned difficulties in Glycoat filtration and makes it possible to apply the Precoat filtration machine to things that are generated in large quantities, such as sewage sludge. However, 3 to 10% of a polymer flocculant is added to a solution of coal coke powder with a particle size of 400μ or less to form a 70ml solution. The above-mentioned coal coke powder is adsorbed and layered on the surface of the filtration material by rotating it to form a temporary layer, and then the filtration material with the first layer formed thereon is rotated in waste water to remove the filtration material. The surface of the layer adsorbs contaminants in waste water, and the adsorbed contaminants are peeled off together with the laminated carbon powder to regenerate the transient surface and adsorb the contaminants again.

すなわち、この発明の最大の特徴をするところは、従来
、コーティングが困難であった石炭コークス粉末の浴M
液中に高分子凝集剤を添加してフロックを形成すること
Kよシ吸着を容易にするとともに、コーティング4Aの
洩出のないコーティング層を形成した点にある。この発
明に用いる石炭コークス粉末の粒度は、次に示す粒度分
布のものを用い、コーティングするに際しては、コーテ
イング液の濃度を20〜3096とし、高分子凝集剤を
3〜IOP添加してフロックを形成したのち、これを回
転ドラノ、の周面に吸着コーティングした使用石炭コー
クス粉末の粒度分布゛(湿式篩分法)(累積%) 0.84 m−2,OIII : 0.02WT* 0
.020.42 〜0.84 : 0.04 0.06
0.25 〜0.42 : 0.14 0.200.1
49 〜0.25 : 6.20 6.400.074
 〜0.149 : 23.20 29.600.04
4 〜0.074 : 12.40 42.00004
4以下 : ss、oo 100.00以下、実施例に
基づいてこの発明を説明する。
In other words, the greatest feature of this invention is that it can be coated in a coal coke powder bath M, which was difficult to coat in the past.
Adding a polymer flocculant to the liquid to form flocs facilitates K-adsorption and forms a coating layer that does not leak the coating 4A. The particle size of the coal coke powder used in this invention has the following particle size distribution. When coating, the concentration of the coating liquid is 20 to 3096, and 3 to IOP of a polymer flocculant is added to form flocs. After that, this was adsorbed and coated on the circumferential surface of a rotating drano to obtain the particle size distribution of the coal coke powder used (wet sieving method) (cumulative %) 0.84 m-2, OIII: 0.02WT* 0
.. 020.42 ~0.84: 0.04 0.06
0.25 ~ 0.42: 0.14 0.200.1
49 ~ 0.25: 6.20 6.400.074
~0.149: 23.20 29.600.04
4 ~ 0.074: 12.40 42.00004
4 or less: ss, oo 100.00 or less This invention will be explained based on Examples.

実施例 l 前述のような粒度分布の石、炭コークス粉末の30%溶
液に、高分子凝集剤(アニオン系)4Fを加え、フロッ
クを形成したのち、該溶液中に回転濾過胴を浸漬(吸着
角度180°)し、これを回転し、その周面に石炭コー
クス粉末を吸着させたところ、5分後に厚み20鰭、3
0分後に50朋、60分後K 6511g、100分後
に80寵のコーティング層を得ることができた。
Example 1 A polymer flocculant (anionic) 4F was added to a 30% solution of stone and charcoal coke powder with the particle size distribution as described above to form flocs, and then a rotating filter cylinder was immersed (adsorbed) in the solution. When this was rotated and coal coke powder was adsorbed on its circumferential surface, after 5 minutes it became 20 fins thick and 3 fins thick.
A coating layer of 50 g was obtained after 0 minutes, 6511 g after 60 minutes, and 80 g after 100 minutes.

この石炭コークス粉末で形成された炉材層を有する回転
θj過胴で清水および水道水を濾過したところ、そのt
t’液の清溶度は8F′T:あった。
When fresh water and tap water were filtered with a rotating θj cylinder having a furnace material layer made of this coal coke powder, the t
The solubility of the t' solution was 8F'T.

実施例 2 実施例1と同じ粒度分nJの石炭コークス粉末の30第
浴浩に高分子凝集剤(アニオン系)5Fを加え、フロッ
クを形成したのら、該溶液中に回転ρ過1阿を浸漬(吸
着角j産180’)し、その周囲に石炭コークス粉末を
吸着させたところ、3分後に201111.30分後ニ
55M、60分咬に75sux、90分後に35gmの
コーディング層を得ることができた。
Example 2 A polymer flocculant (anionic type) 5F was added to the 30th bath of coal coke powder with the same particle size nJ as in Example 1 to form flocs, and then a rotating ρ filter was applied to the solution for 1 hour. After soaking (adsorption angle J 180') and adsorbing coal coke powder around it, a coating layer of 201111 was obtained after 3 minutes, 55M after 30 minutes, 75sux after 60 minutes, and 35gm after 90 minutes. was completed.

このコーティング層を用いて、清水および水道水なθう
遇した結果、そのp液の清澄度は略8Pであった。
When this coating layer was used to treat fresh water and tap water, the clarity of the p liquid was approximately 8P.

すなわち、コーティング層の厚み80〜85m、ip液
の清澄度8Fは従来用いられている珪藻土等のプリコー
ト利と保色なく、これらに代えて使用し得ることが確認
された。
That is, it was confirmed that the thickness of the coating layer is 80 to 85 m and the clarity of the IP liquid is 8F, which can be used in place of conventionally used precoat materials such as diatomaceous earth without color retention.

以上の説明で明らかなようK、この発明は、従来、一般
に用いられている珪藻±VC代λ−で、石炭コークス粉
末を用いてプリコート−過層の形成に成功し、大tK発
生する汚泥にプリコートρ過機を適用することを++J
能+tc シたものでるり、石炭コークス粉末が従来の
珪藻土等に比較して格安でるることからしても、産業」
1得られる利益は著大なるものでるる。
As is clear from the above explanation, this invention has succeeded in forming a precoat overlayer using coal coke powder in the conventionally commonly used diatom ± VC range λ-, and has succeeded in forming a precoat overlayer in the sludge generated at large tK. Applying pre-coat ρ filter machine ++J
Noh + TC Shitamono De Ruri, and considering that coal coke powder is cheaper than conventional diatomaceous earth, etc., it is an industry standard.
1.The profits gained will be enormous.

Claims (1)

【特許請求の範囲】[Claims] (1) 粒径が400μ以下の石炭コークス粉末の溶解
液に高分子凝集剤を3〜IOF添加してフロックを形成
させ、そのフロックを形成した浴液中で、円筒型の濾過
層を回転させて、その濾過層の表面K J1記石炭コー
クス粉末を吸着積層させて濾過層を形成し、次いて、濾
過層を形成した濾過層を汚水中で回転させて、その1過
層表面に汚水中の夾雑物を吸着し、この吸着した夾雑物
を積層した石炭コークス粉末とともに剥離して濾過面を
再生し、再び、夾雑物を吸着することを特徴とする汚泥
等の1濾過方法。
(1) 3 to IOF of a polymer flocculant is added to a solution of coal coke powder with a particle size of 400μ or less to form flocs, and a cylindrical filtration layer is rotated in the bath liquid in which the flocs are formed. Then, the surface of the filtration layer is adsorbed and laminated with coal coke powder to form a filtration layer.Then, the filtration layer with the formed filtration layer is rotated in the waste water, and the surface of the first filter layer is coated with the sewage water. A filtration method for sludge, etc., characterized by adsorbing impurities, peeling off the adsorbed impurities together with laminated coal coke powder to regenerate the filtration surface, and adsorbing the impurities again.
JP59039031A 1984-03-01 1984-03-01 Filteration of sludge Granted JPS60183021A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59039031A JPS60183021A (en) 1984-03-01 1984-03-01 Filteration of sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59039031A JPS60183021A (en) 1984-03-01 1984-03-01 Filteration of sludge

Publications (2)

Publication Number Publication Date
JPS60183021A true JPS60183021A (en) 1985-09-18
JPH0212125B2 JPH0212125B2 (en) 1990-03-19

Family

ID=12541735

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59039031A Granted JPS60183021A (en) 1984-03-01 1984-03-01 Filteration of sludge

Country Status (1)

Country Link
JP (1) JPS60183021A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009136821A (en) * 2007-12-10 2009-06-25 Kumeta Seisakusho:Kk Dust collector
JP2015107484A (en) * 2013-12-03 2015-06-11 フナン ユニバーシティ オブ サイエンス アンド テクノロジーHunan University of Science and Technology Sludge dewatering conditioning agent and deep dewatering method thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2553214Y2 (en) * 1990-09-05 1997-11-05 株式会社ユーシン Action structure of operation knob

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009136821A (en) * 2007-12-10 2009-06-25 Kumeta Seisakusho:Kk Dust collector
JP2015107484A (en) * 2013-12-03 2015-06-11 フナン ユニバーシティ オブ サイエンス アンド テクノロジーHunan University of Science and Technology Sludge dewatering conditioning agent and deep dewatering method thereof

Also Published As

Publication number Publication date
JPH0212125B2 (en) 1990-03-19

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