JPH02187111A - Method for concentrating sludge and device therefor - Google Patents

Method for concentrating sludge and device therefor

Info

Publication number
JPH02187111A
JPH02187111A JP1004620A JP462089A JPH02187111A JP H02187111 A JPH02187111 A JP H02187111A JP 1004620 A JP1004620 A JP 1004620A JP 462089 A JP462089 A JP 462089A JP H02187111 A JPH02187111 A JP H02187111A
Authority
JP
Japan
Prior art keywords
water
filtration layer
solids
solid content
outside
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
JP1004620A
Other languages
Japanese (ja)
Other versions
JPH0512004B2 (en
Inventor
Kazuo Goto
和雄 後藤
Hitoshi Yonekawa
米川 均
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.)
NGK Insulators Ltd
Original Assignee
NGK Insulators 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 NGK Insulators Ltd filed Critical NGK Insulators Ltd
Priority to JP1004620A priority Critical patent/JPH02187111A/en
Publication of JPH02187111A publication Critical patent/JPH02187111A/en
Publication of JPH0512004B2 publication Critical patent/JPH0512004B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Abstract

PURPOSE:To eliminate the need for maintenance work such as cleaning of filter cloth, etc., by storing water temporarily after being sucked by low pressure filtration, then scraping solids off a filter layer to separate them, and thereafter forcing the water thus stored through the filter layer to the outside under low pressure, thereby conducting back washing. CONSTITUTION:When a rotary drum 1 is rotated on the center axis 15 clockwise at a specified speed, at first the volume of a chamber 4-1 dipped in a liquid to be concentrated 11 containing solids in a reservoir 10 expands and sucks water by the action of a cam 9 and spring member 5, following which the solids sucked on a felt 3 are scraped off by a scraper 12 and discharged to the outside through a sludge pan 13, while water in each of the chambers 4-1-4-8 is gradually discharged from the position of the chamber 4-5 by the action of the cam 9 to be discharged to the outside through a water pan 14; thereby, back washing of filter cloth 2 and felt 3 is performed, and then a next concentration operation starts.

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明は固形分を含む液体の濃縮方法に関し、特に上・
下水汚泥等の汚泥濃縮方法およびそれに用いる装置に関
するものである。
Detailed Description of the Invention (Industrial Field of Application) The present invention relates to a method for concentrating a liquid containing solids, and in particular,
The present invention relates to a method for concentrating sludge such as sewage sludge and an apparatus used therefor.

(従来の技術) 従来、固形分を含む液体から水分の含有率を減少させて
濃縮する方法としては、重力濃縮法、加圧浮上法、遠心
分離法等の濃縮法が知られており、そのための各種装置
も知られている。
(Prior art) Concentration methods such as gravity concentration, pressure flotation, and centrifugation are conventionally known as methods for concentrating a liquid containing solids by reducing its water content. Various devices are also known.

また、濾過層を介して固形分を含む液体を真空吸引して
、濾過層上に堆積した固形分を掻き取り分離するととも
に、濾過後の液体を外部へ排出する濃縮装置も知られて
いる。
Further, a concentrating device is also known that vacuum-suctions a liquid containing solids through a filtration layer, scrapes and separates the solids accumulated on the filtration layer, and discharges the filtered liquid to the outside.

(発明が解決しようとする課題) しかしながら、上述した方法のうち、重力濃縮法におい
ては、大幅な濃度上昇を達成することができないととも
に、通常12時間以上の長い滞留時間が必要となり、さ
らに設置面積が大となる問題があった。また、加圧浮上
法および遠心分離法にふいては、電力費(動力費)が大
となり、処理コストが高くなるとともに、特に加圧浮上
法においてはメンテナンスが難しい問題があった。
(Problems to be Solved by the Invention) However, among the above-mentioned methods, the gravity concentration method cannot achieve a significant increase in concentration, requires a long residence time of usually 12 hours or more, and requires a large installation area. There was a big problem. In addition, the pressure flotation method and the centrifugation method require high electric power costs (power costs), which increases processing costs, and the pressure flotation method in particular has the problem of difficult maintenance.

これらの問題を解決すべく、特開昭62−262800
号公報において、高分子凝集剤を処理すべき固形分を含
む液体に混合し、水分を高分子ゲル塊として除去する装
置が開示されている。しかしながら、この装置では高分
子凝集剤が使いすてであり、再使用できないため、ラン
ニングコストが大となる問題があるとともに、所定の篩
の準備が難しい問題があった。
In order to solve these problems, Japanese Patent Application Laid-Open No. 62-262800
In the publication, an apparatus is disclosed in which a polymer flocculant is mixed with a liquid containing solids to be treated and water is removed as a polymer gel mass. However, in this device, the polymer flocculant is disposable and cannot be reused, so there is a problem in that the running cost is high and it is difficult to prepare a specific sieve.

さらに、上述した真空吸引を利用した濃縮装置では、定
期的に作業を中断して濾過層を洗浄する必要があるとと
もに、真空吸引機構を設けなければならないため、装置
が大型化して高価となるとともに、処理コストも高くな
る問題があった。
Furthermore, in the above-mentioned concentration device that uses vacuum suction, it is necessary to periodically interrupt the operation to clean the filtration layer, and a vacuum suction mechanism must be provided, which makes the device large and expensive. However, there was a problem in that the processing cost also increased.

本発明の目的は上述した課題を解消して、装置費および
電力費が少なく低ランニングコストが達成できるととも
に、メンテナンスが簡単な汚泥濃縮方法およびそれに用
いる濃縮装置を提供しようとするものである。
SUMMARY OF THE INVENTION An object of the present invention is to solve the above-mentioned problems and provide a sludge thickening method and a thickening device used therein, which can achieve low running costs with low equipment costs and electric power costs, and are easy to maintain.

(課題を解決するための手段) 本発明の汚泥濃縮方法は、濃縮すべき固形分を含む液体
を濾過層を介して低圧で吸引し、濾過層上に固形分を付
着させるとともに濾過後の水分を一旦貯留した後、濾過
層上の固形分を掻き取り分離し、次に貯留した水分を濾
過層を介して低圧で押し出して外部へ排出することを特
徴とするものである。
(Means for Solving the Problems) The sludge concentration method of the present invention suctions a liquid containing solids to be concentrated at low pressure through a filtration layer, deposits the solids on the filtration layer, and removes water after filtration. This method is characterized in that after once storing the solid content on the filtration layer, the solid content is scraped off and separated, and then the stored water is extruded at low pressure through the filtration layer and discharged to the outside.

また、本発明の汚泥a線装置は、濃縮すべき固形分を含
む液体を貯留する貯留槽と、表面に濾過層を設けた透水
性の回転ドラムと、回転ドラムの内側に設けられた体積
を可変することにより貯留槽中の液体を吸引・排出でき
る複数の部屋と、濾過層を介して部屋中に吸引後の濾過
層表面近傍に付着した固形分を掻き取るための固形分除
去手段と、固形分除去後濾過層を介して部屋中の水分を
外部へ押し出して排出するための水分除去手段とを具え
ることを特徴とするものである。
In addition, the sludge A-ray device of the present invention includes a storage tank for storing a liquid containing solids to be concentrated, a water-permeable rotating drum with a filtration layer on its surface, and a volume provided inside the rotating drum. a plurality of chambers capable of suctioning and discharging the liquid in the storage tank by changing the number of chambers; a solid content removal means for scraping off solid matter adhering to the vicinity of the surface of the filtration layer after suction into the room through the filtration layer; The apparatus is characterized by comprising a moisture removing means for pushing and discharging moisture in the room to the outside through the filtration layer after solid content has been removed.

(作 用) 上述した構成において、濾過層を介して濃縮すべき固形
分を含む液体を低圧で吸水することにより、固形分とそ
れ以外の液体とを分離でき濃縮が可能となるとともに、
固形分以外の液体を部屋中に貯留し、固形分除去後に濾
過層を介して外部へ排出することによる逆洗を実施して
いるため、濾布洗浄等のメンテナンスをなくすことがで
きる。
(Function) In the above-mentioned configuration, by absorbing the liquid containing the solid content to be concentrated through the filtration layer at low pressure, the solid content and the other liquid can be separated and concentration becomes possible.
Backwashing is performed by storing liquid other than solids in the room and discharging it to the outside through a filtration layer after solids are removed, so maintenance such as filter cloth cleaning can be eliminated.

また、上述した濃縮装置では、部屋の体積を可変するこ
とにより吸水および排水を実施できるため、連続して濃
縮動作ができるとともに、無薬注であっても処理できる
ため高分子凝集剤を使用する場合と比べて低ランニング
コストを達成することができる。
In addition, the above-mentioned concentrator can absorb and drain water by changing the volume of the room, so it can perform continuous concentration operations, and it can also process without chemical injection, so it is possible to use a polymer flocculant. It is possible to achieve lower running costs than in the case of

さらに、各部屋の体積の可変動作をカムを利用して実施
すると、ドラムの回転のみでその動作を制御できるため
好ましい。
Furthermore, it is preferable to use a cam to vary the volume of each room because the operation can be controlled only by rotating the drum.

(実施例) 第1図(a)、 (b) は本発明の濃縮装置の一例の
構成を示す図およびその部分拡大図である。本実施例で
は、透水性のパンチングメタルよりなる回転ドラムl上
に、濾布2を設けさらにその上にフェルト3を設けて濾
過層を構成している。回転ドラム1の内側には、回転ド
ラム1の長手方向に延在するその体積が可変で濃縮すべ
き固形分を含む液体を吸引・排出できる8個の部屋4−
1〜4−8を設けている。各部屋4−1〜4−8はバネ
部材5を介して回転ドラムlの長手方向に延在する鉄板
6−1〜6−8および伸縮自在な弾性部材7−1.7−
2により画成されている。各鉄板6−1〜6−8の部屋
外部には先端にローラを有するカムの従導節8を複数個
設け、従導節8を各部屋4−1〜4−8の伸縮パターン
に従ったカム9にバネ部材5により常に接する状態とし
てカム装置を構成している。また、貯留槽10を設け、
上述した構造の回転ドラム1の一部が貯留[10中の濃
縮すべき固形分を含む液体11中に浸漬するよう設置し
ている。さらに、回転ドラム1の上流側にフェルト3の
表面に吸着した下水汚泥等の固形分を掻き取るためのス
クレーパ12を設けている。また、スクレーパ12によ
り掻き取られた固形分を取り出すための汚泥受は皿13
を設けるとともに、各部屋4−1〜4−8中から濾過層
を介して排出される水分を一旦貯留するための水分光は
皿14を下流側に設けている。
(Example) FIGS. 1(a) and 1(b) are diagrams showing the configuration of an example of the concentrating device of the present invention and a partially enlarged view thereof. In this embodiment, a filter cloth 2 is provided on a rotary drum 1 made of water-permeable punched metal, and a felt 3 is further provided thereon to constitute a filtration layer. Inside the rotating drum 1, there are eight chambers 4- extending in the longitudinal direction of the rotating drum 1, each having a variable volume and capable of sucking and discharging a liquid containing solids to be concentrated.
1 to 4-8 are provided. Each of the chambers 4-1 to 4-8 includes iron plates 6-1 to 6-8 extending in the longitudinal direction of the rotating drum l via a spring member 5, and elastic members 7-1, 7-8 that can be expanded and contracted.
2. A plurality of follower nodes 8 of cams having rollers at the tips are provided outside the chambers of each iron plate 6-1 to 6-8, and the follower nodes 8 follow the expansion and contraction pattern of each chamber 4-1 to 4-8. The cam device is configured such that the cam 9 is always in contact with the spring member 5. In addition, a storage tank 10 is provided,
A part of the rotating drum 1 having the above-described structure is installed so as to be immersed in the liquid 11 containing the solids to be concentrated in the reservoir [10]. Furthermore, a scraper 12 is provided on the upstream side of the rotating drum 1 to scrape off solid matter such as sewage sludge adsorbed on the surface of the felt 3. In addition, a sludge receptacle for taking out the solid content scraped by the scraper 12 is a plate 13.
In addition, a moisture tray 14 is provided on the downstream side for temporarily storing moisture discharged from each of the rooms 4-1 to 4-8 through the filtration layer.

上述した濃縮装置では、第1図において回転ドラム1を
中心軸15に対して時計方向に所定の速度で回転するこ
とにより、カム装置の作用によりまず貯留槽IO中の濃
縮すべき固形分を含む液体11中に浸漬した部屋4−1
の体積が広がり吸水する。その後、フェルト3上に吸着
した固形分は、スクレーパ12により掻き取られて汚泥
受は皿13を介して外部へ排出されるとともに、各部屋
4−1〜4−8中の水分は部屋4−5の位置から徐々に
排水され水分光は皿14を介して外部へ排出され、濾布
2およびフェルト3の逆洗を行なった後、再び次の濃縮
操作に使用される。そのため、第1図に示す装置では、
本発明の汚泥濃縮方法を好適に実施することができる。
In the above-mentioned concentrating device, by rotating the rotating drum 1 clockwise with respect to the central axis 15 at a predetermined speed in FIG. 1, the solid content to be concentrated in the storage tank IO is first contained by the action of the cam device. Room 4-1 immersed in liquid 11
The volume expands and absorbs water. Thereafter, the solid content adsorbed on the felt 3 is scraped off by the scraper 12 and the sludge receiver is discharged to the outside via the tray 13, and the moisture in each of the rooms 4-1 to 4-8 is removed from the room 4-1. Water is gradually drained from the position 5 and the water is discharged to the outside through the dish 14, and after backwashing the filter cloth 2 and the felt 3, it is used again for the next concentration operation. Therefore, in the device shown in Figure 1,
The sludge concentration method of the present invention can be suitably implemented.

また、表面濾過層を形成する濾布2としては、テトロン
やナイロンからなり通気度1〜30cc/cm’・se
c好ましくは4〜10CC/Cm2・SeC程度で耐酸
性、耐アルカリ性の良好なものを用いると好ましく、フ
ェルト3としては多孔質で厚みが1mm以上あるものを
用いると好ましい。濾布およびフェルトの好ましい一例
を第1表、第2表にそれぞれ示す。
The filter cloth 2 forming the surface filtration layer is made of Tetron or nylon and has an air permeability of 1 to 30 cc/cm'·se.
It is preferable to use a material having good acid resistance and alkali resistance, preferably about 4 to 10 CC/Cm2.SeC, and it is preferable to use a felt 3 that is porous and has a thickness of 1 mm or more. Preferred examples of filter cloth and felt are shown in Tables 1 and 2, respectively.

第  1  表 第2表 第2図は本発明の濃縮装置の他の例の構成を示す図であ
る。第2図において、第1図に示す例と同一の部材には
同一の符号を付し、その説明を省略する。第2図に示す
例で第1図に示す例と異なる点は、各部屋4−1〜4−
8の全体を伸縮自在な弾性部材により構成した点と、カ
ム装置を例えば回転ドラム1の両端部に設けた溝カムに
より構成し、従導節8を弾性部材からなる各部屋4−1
〜4−8の底部に設けた回転ドラム1の長手方向に延在
する金具16−1〜16−8と接続した点である。この
ように構成することにより、第1図に示す例と同様、カ
ム装置の作用により各部屋4−1〜4−8の伸縮を行な
うことができる。そのため、第2図に示す装置でも、本
発明の汚泥濃縮方法を好適に実施することができる。
Table 1 Table 2 FIG. 2 is a diagram showing the configuration of another example of the concentrating device of the present invention. In FIG. 2, the same members as in the example shown in FIG. 1 are given the same reference numerals, and their explanations will be omitted. The difference between the example shown in Fig. 2 and the example shown in Fig. 1 is that each room 4-1 to 4-
8 is entirely made of a stretchable elastic member, and the cam device is made of, for example, grooved cams provided at both ends of the rotating drum 1, and the follower section 8 is made of an elastic member in each chamber 4-1.
- 4-8 are connected to the metal fittings 16-1 to 16-8 extending in the longitudinal direction of the rotating drum 1 provided at the bottom. With this configuration, each of the rooms 4-1 to 4-8 can be expanded and contracted by the action of the cam device, similarly to the example shown in FIG. Therefore, even with the apparatus shown in FIG. 2, the sludge concentration method of the present invention can be suitably carried out.

なお、本装置における吸引圧力は0.1〜0.3kg/
cm2程度であり、真空脱水機における吸引圧力0.8
〜1、0kg/cm”に比較して極めて小さいものであ
る。
The suction pressure in this device is 0.1 to 0.3 kg/
cm2, and the suction pressure in the vacuum dehydrator is 0.8
~1.0 kg/cm''.

本発明は上述した実施例にのみ限定されるものではなく
、幾多の変形、変更が可能である。例えば、上述した部
屋の分画数は8個に限定されるものではないとともに、
カムの形状および種類も上述した実施例に限定されるも
のでないことは明らかである。
The present invention is not limited only to the embodiments described above, and numerous modifications and changes are possible. For example, the number of compartments in the room mentioned above is not limited to eight, and
It is clear that the shape and type of the cam is also not limited to the embodiments described above.

(発明の効果) 以上の説明から明らかなように、本発明の汚泥濃縮方法
およびそれに用いる装置によれば、濾過層を介して濃縮
すべき固形分を含む液体を低圧で吸水することにより、
簡単かつ低圧で固形分とそれ以外の液体とを分離でき濃
縮が可能となるとともに、固形分以外の液体を部屋中に
貯留し、固形分除去後に濾過層を介して外部へ排出する
ことによる逆洗を実施しているため、濾布の洗浄等のメ
ンテナンスをなくすことができる。そのため、装置費お
よび電力費が少なく低ランニングコストが達成できると
ともに、濾布等のメンテナンスを簡単にすることができ
る。
(Effects of the Invention) As is clear from the above explanation, according to the sludge concentration method of the present invention and the apparatus used therein, by absorbing the liquid containing solids to be concentrated through the filtration layer at low pressure,
It is possible to easily separate solids from other liquids at low pressure and concentrate them, and the liquid other than solids can be stored in a room and discharged outside through a filtration layer after the solids have been removed. Since cleaning is performed, maintenance such as cleaning the filter cloth can be eliminated. Therefore, equipment costs and power costs are low, low running costs can be achieved, and maintenance of filter cloths and the like can be simplified.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図(a)、 (b) はそれぞれ本発明の汚泥濃縮
装置の一例の構成を示す図およびその部分拡大図、第2
図は本発明の汚泥濃縮装置の他の例の構成を示す図であ
る。 ■・・・回転ドラム 3・・・フェルト 5・・・バネ部材 ?−1,7−2・・・弾性部材 9・・・カム 11・・・液体 2・・・濾布 4−1〜4−8・・・部屋 6−1〜6−8・・・鉄板 8・・・従導節 10・・・貯留槽 12・・・スクレーバ 13・・・汚泥受は皿 15・・・中心軸
FIGS. 1(a) and 1(b) are a diagram showing the configuration of an example of the sludge thickening device of the present invention, a partially enlarged view thereof, and FIG.
The figure is a diagram showing the configuration of another example of the sludge thickening device of the present invention. ■...Rotating drum 3...Felt 5...Spring member? -1,7-2...Elastic member 9...Cam 11...Liquid 2...Filter cloth 4-1 to 4-8...Room 6-1 to 6-8...Iron plate 8 ...Subordinate node 10...Storage tank 12...Scraper 13...Sludge receiver is plate 15...Central axis

Claims (1)

【特許請求の範囲】 1、濃縮すべき固形分を含む液体を濾過層を介して低圧
で吸引し、濾過層上に固形分を付着させるとともに濾過
後の水分を一旦貯留した後、濾過層上の固形分を掻き取
り分離し、次に貯留した水分を濾過層を介して低圧で押
し出して外部へ排出することを特徴とする汚泥濃縮方法
。 2、濃縮すべき固形分を含む液体を貯留する貯留槽と、
表面に濾過層を設けた透水性の回転ドラムと、回転ドラ
ムの内側に設けられた体積を可変することにより貯留槽
中の液体を吸引・排出できる複数の部屋と、濾過層を介
して部屋中に吸水後の濾過層表面近傍に付着した固形分
を掻き取るための固形分除去手段と、固形分除去後濾過
層を介して部屋中の水分を外部へ押し出して排出するた
めの水分除去手段とを具えることを特徴とする濃縮装置
[Claims] 1. A liquid containing solids to be concentrated is sucked at low pressure through a filtration layer, the solids are deposited on the filtration layer, and the water after filtration is temporarily stored, and then A sludge thickening method characterized by scraping and separating the solid content of the sludge, and then extruding the accumulated water at low pressure through a filtration layer and discharging it to the outside. 2. A storage tank for storing a liquid containing solid content to be concentrated;
A water-permeable rotating drum with a filtration layer on its surface, multiple chambers inside the rotating drum that can suck and discharge liquid in the storage tank by varying the volume, and a filtration layer that allows the liquid to be pumped into the room through the filtration layer. a solid content removing means for scraping off solid content adhering to the vicinity of the surface of the filtration layer after water absorption; and a water removal means for pushing and discharging the moisture in the room through the filtration layer to the outside after removing the solid content. A concentrating device characterized by comprising:
JP1004620A 1989-01-13 1989-01-13 Method for concentrating sludge and device therefor Granted JPH02187111A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1004620A JPH02187111A (en) 1989-01-13 1989-01-13 Method for concentrating sludge and device therefor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1004620A JPH02187111A (en) 1989-01-13 1989-01-13 Method for concentrating sludge and device therefor

Publications (2)

Publication Number Publication Date
JPH02187111A true JPH02187111A (en) 1990-07-23
JPH0512004B2 JPH0512004B2 (en) 1993-02-17

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Application Number Title Priority Date Filing Date
JP1004620A Granted JPH02187111A (en) 1989-01-13 1989-01-13 Method for concentrating sludge and device therefor

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JP (1) JPH02187111A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6248684B1 (en) * 1992-11-19 2001-06-19 Englehard Corporation Zeolite-containing oxidation catalyst and method of use
CN110115867A (en) * 2019-05-24 2019-08-13 邓胜万 It is a kind of that principle of absorption system for processing chrome-containing wastewater is generated using water column
CN114620910A (en) * 2022-04-28 2022-06-14 浙江迈图环保科技有限公司 Dyeing alkali decrement sewage treatment process

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6248684B1 (en) * 1992-11-19 2001-06-19 Englehard Corporation Zeolite-containing oxidation catalyst and method of use
CN110115867A (en) * 2019-05-24 2019-08-13 邓胜万 It is a kind of that principle of absorption system for processing chrome-containing wastewater is generated using water column
CN110115867B (en) * 2019-05-24 2021-06-15 邓胜万 System for treating chromium-containing wastewater by adopting water column generation absorption principle
CN114620910A (en) * 2022-04-28 2022-06-14 浙江迈图环保科技有限公司 Dyeing alkali decrement sewage treatment process
CN114620910B (en) * 2022-04-28 2023-06-06 浙江迈图环保科技有限公司 Dyeing alkali deweighting sewage treatment process

Also Published As

Publication number Publication date
JPH0512004B2 (en) 1993-02-17

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