JPH105506A - Device for thickening sludge - Google Patents

Device for thickening sludge

Info

Publication number
JPH105506A
JPH105506A JP8188263A JP18826396A JPH105506A JP H105506 A JPH105506 A JP H105506A JP 8188263 A JP8188263 A JP 8188263A JP 18826396 A JP18826396 A JP 18826396A JP H105506 A JPH105506 A JP H105506A
Authority
JP
Japan
Prior art keywords
sludge
added
water
thickened sludge
thickening
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
Application number
JP8188263A
Other languages
Japanese (ja)
Inventor
Seijiro Kagawa
征二郎 香川
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 Co Ltd
Original Assignee
Ishigaki 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 Co Ltd filed Critical Ishigaki Co Ltd
Priority to JP8188263A priority Critical patent/JPH105506A/en
Publication of JPH105506A publication Critical patent/JPH105506A/en
Pending legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Abstract

PROBLEM TO BE SOLVED: To make it possible to settle and thicken sludge added with a flocculating agent by vertically partitioning a thickening vessel with a water permeable resistance plate of meshes, etc., supplying the stock soln. added with the flocculating agent in a lower chamber and providing the upper chamber with a take-out port for separating water. SOLUTION: The thickening vessel 1 is vertically segmented with the resistance plate 2 having water permeability of the coarse meshes, etc., to the extent of allowing the capturing of flocculated floes. The upper chamber 1a of the thickening vessel 1 is provided with an overflow pipe 3 for the separating water. The lower chamber 1b is provided with a thickened sludge withdrawing pipe 4 and is provided with a supply pipe 5 for the raw water added and intimately mixed with a solidifying agent. The thickened sludge added and intimately mixed with the flocculating agent in an intimate mixing vessel 7 flows down in the supply pipe 5 and is then made into a compacted massive state. This sludge is supplied to the thickening vessel 1. The thickening vessel 1 is filled with the thickened sludge. The floating thereof is prohibited by the resistance place 2 and only the moisture accumulates in the upper chamber 1a and is taken out of the overflow pipe 3. A filter layer is formed by the thickened sludge accumulated downward in the lower chamber 1b, by which the highly thickened sludge is formed by removing the moisture.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】この発明は、高分子凝集剤を
用いた汚泥の濃縮装置の改良に関し、従来、沈降濃縮で
は濃縮困難とされていた凝集剤を添加した汚泥を高濃度
に濃縮できる装置を提供せんとするものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement in an apparatus for concentrating sludge using a polymer flocculant. Is to be provided.

【0002】[0002]

【従来の技術】従来、ポリマー等の凝集剤を添加して凝
集した汚泥を濃縮するには、沈降濃縮は困難で一般には
高圧空気等によって凝集フロックを浮上させている。ま
た、起泡剤および空気を加えて浮上させる方法も知られ
ている。特公昭63−33435はその例である。
2. Description of the Related Art Conventionally, in order to concentrate flocculated sludge by adding a flocculant such as a polymer, it is difficult to settle and concentrate the sludge. Generally, flocculated floc is floated by high-pressure air or the like. In addition, a method of floating by adding a foaming agent and air is also known. Japanese Examined Patent Publication No. 33435/1988 is an example.

【0003】[0003]

【発明が解決しようとする課題】然しながら、ポリマー
等の凝集剤を添加して凝集させた下水汚泥は圧密状態が
悪く沈降濃縮では、高濃度に濃縮することは困難であ
る。このため、浮上濃縮法でも常圧浮上濃縮法でも高圧
空気や起泡剤を用いてフロックを浮上させているがこれ
らの方法では、凝集剤の外に、コンプレッサー等の機器
や起泡剤等の添加剤が必要である。
However, sewage sludge aggregated by adding a flocculant such as a polymer has a poor consolidation state, and it is difficult to concentrate to a high concentration by sedimentation and concentration. For this reason, in both the flotation concentration method and the normal pressure flotation concentration method, the floc is levitated using high-pressure air or a foaming agent, but in these methods, in addition to the flocculant, equipment such as a compressor or a foaming agent is used. Additives are required.

【0004】[0004]

【課題を解決するための手段】この発明は上述のような
課題を解決し得るものであって、この発明は、凝集剤を
添加して凝集した汚泥を若干の抵抗下において押し出す
とフロックが塊状となって沈降する点に着目してなされ
たものである。
SUMMARY OF THE INVENTION The present invention can solve the above-mentioned problems. In the present invention, when a flocculant is added and the flocculated sludge is extruded under a slight resistance, the floc is formed into a block. It was made by paying attention to the point of sinking.

【0005】すなわち、この発明の要旨とするところ
は、上部に分離水の溢流部を下部に濃縮汚泥の抜取口を
設けた濃縮槽をメッシュ等の通水性を有する抵抗板で上
下に仕切るとともに、その仕切った下室には、凝集剤を
添加した原液の供給口を、上室には、分離水の取出口を
設けたものである。
That is, the gist of the present invention is to separate a concentrating tank provided with an overflow portion of separated water at an upper portion and an outlet for condensed sludge at a lower portion with a resistance plate having a water permeability such as a mesh, and to vertically separate the concentrated tank. The lower chamber is provided with a supply port for a stock solution to which a flocculant is added, and the upper chamber is provided with an outlet for separated water.

【0006】上記凝集剤を添加した原液を濃縮槽に供給
するには、ポンプを用いてもよいが、凝集剤を添加する
ための混和槽を濃縮槽よりも上位に設けて、その水頭差
で供給してもよい。
A pump may be used to supply the concentrate to which the coagulant has been added to the concentrating tank. However, a mixing tank for adding the coagulant is provided at a higher level than the concentrating tank, and the head difference is increased. May be supplied.

【0007】[0007]

【発明の実施の形態】この発明は、凝集剤が添加された
汚泥が圧密状態となったときには、沈降する点に着目し
てなされたもので凝集混和槽から送られる原液中のフロ
ックは、輸送管中の抵抗によって圧密状となり、濃縮槽
に吐出するときには塊状となって濃縮槽中では沈降す
る。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention focuses on the point of sedimentation when sludge to which a flocculant is added becomes condensed, and flocs in a stock solution sent from a flocculation mixing tank are transported. Due to the resistance in the tube, it becomes compacted, and when discharged into the concentration tank, it forms a lump and sediments in the concentration tank.

【0008】したがって、このようにして供給される原
液中のフロックが濃縮槽の下室に充満して、抵抗板によ
る抵抗によって圧密度が増して高濃縮される。そして、
原液中の水分は、抵抗板を通って上澄液として取出され
る。
Accordingly, the floc in the stock solution supplied in this way fills the lower chamber of the concentration tank, and the pressure density is increased by the resistance of the resistance plate, thereby being highly concentrated. And
The water in the stock solution is taken out as a supernatant through a resistance plate.

【0009】すなわち、濃縮槽内では、圧密状となった
フロック層がろ過層となって、水分が分離され、下室に
濃縮汚泥を得ることができるものである。この濃縮汚泥
は、濃縮具合を見計らって、回分式に取出しても、ま
た、連続的に取出してもよいものである。
That is, in the concentration tank, the condensed floc layer becomes a filtration layer, whereby water is separated, and concentrated sludge can be obtained in the lower chamber. The concentrated sludge may be taken out in a batch manner or may be taken out continuously in consideration of the degree of concentration.

【0010】以上の説明でも明らかなように、この発明
に係る装置は、濃縮槽に通水性の抵抗板を設けるのみの
簡単な構成で従来困難とされていた凝集剤による凝集汚
泥を沈降分離可能にしたものであり、特に、圧密にする
ための加圧エネルギーが自然の水頭差で充分でフロック
をこわすことがなく、事後の脱水操作にも好適な濃縮汚
泥を得ることができる。以下、図面に基づいてこの発明
を具体的に説明する。
As is apparent from the above description, the apparatus according to the present invention is capable of settling and separating coagulated sludge by a coagulant, which has been conventionally difficult, with a simple structure in which only a water-permeable resistance plate is provided in a concentration tank. In particular, the pressurizing energy for consolidation is sufficient due to the natural head difference and does not break the floc, so that it is possible to obtain concentrated sludge suitable for the subsequent dewatering operation. Hereinafter, the present invention will be specifically described with reference to the drawings.

【0011】[0011]

【実施例】図1は、この発明に係る濃縮装置を備えた汚
泥の濃縮フローシート図であり、図2は、その要部の拡
大断面図である。図1において、符号1は濃縮槽、2
は、濃縮槽2を上下に区分するように設けた抵抗板で、
通水性を有するメッシュで構成してあり、凝集フロック
を捕捉できる程度の粗いメッシュ(略5mm)で構成し
てある。
1 is a flow sheet diagram of sludge concentration provided with a concentration device according to the present invention, and FIG. 2 is an enlarged sectional view of a main part thereof. In FIG. 1, reference numeral 1 denotes a concentration tank, 2
Is a resistance plate provided so as to divide the concentration tank 2 up and down,
It is composed of a mesh having water permeability, and is composed of a coarse mesh (approximately 5 mm) large enough to capture coagulated flocs.

【0012】上下に区分された濃縮槽1の上室1aに
は、分離水の溢流管3が設けてあり、下室1bには、濃
縮汚泥の引抜管4が設けてある。また、下室1bには、
凝集剤が添加混和された原水の供給管5が開設してあ
る。符号6は、凝集汚泥の掻寄機である。
An overflow pipe 3 for separated water is provided in an upper chamber 1a of the concentration tank 1 which is divided into upper and lower sections, and a withdrawal pipe 4 for concentrated sludge is provided in a lower chamber 1b. In the lower chamber 1b,
A supply pipe 5 for raw water to which a coagulant is added and mixed is provided. Reference numeral 6 is a scraper for coagulated sludge.

【0013】次に、符号7は、凝集剤の混和槽であり、
図示では濃縮槽1よりも高所に設けてそのヘッド差で凝
集剤の添加汚泥を濃縮槽1に供給するようにしている。
符号8は撹拌機、符号9は、高分子凝集剤のタンク、1
0は汚泥槽、11は汚泥供給ポンプ、12は濃縮汚泥の
引抜ポンプである。
Next, reference numeral 7 is a mixing tank for a flocculant,
In the figure, the sludge added with the flocculant is supplied to the thickening tank 1 at a position higher than the thickening tank 1 by the head difference.
Reference numeral 8 denotes a stirrer, reference numeral 9 denotes a tank of a polymer flocculant, 1
Reference numeral 0 denotes a sludge tank, reference numeral 11 denotes a sludge supply pump, and reference numeral 12 denotes a concentrated sludge extraction pump.

【0014】この発明に係る濃縮装置は、上述のように
構成してあり、混和槽7で凝集剤を添加混和された凝集
汚泥は、その水頭差によって供給管5内を流下し、その
供給管5の管内抵抗によって圧密され、塊状となって濃
縮槽1に供給される。この状態を図2に示す。
The concentrating apparatus according to the present invention is configured as described above, and the flocculated sludge to which the flocculant is added and mixed in the mixing tank 7 flows down the supply pipe 5 due to the head difference, and the supply pipe 5 and is supplied to the concentration tank 1 in a lump. This state is shown in FIG.

【0015】このように塊状となった凝集汚泥は、濃縮
槽1内では沈降する。このようにして、下室1bに濃縮
汚泥が充満するが、抵抗板2によって浮上が阻止される
ので、その水分のみが抵抗板を通過して上室1aに溜
り、溢流管3から系外に取出される。
The coagulated sludge thus formed is settled in the concentration tank 1. In this way, the concentrated sludge is filled in the lower chamber 1b, but the floating is prevented by the resistance plate 2, so that only the water passes through the resistance plate and accumulates in the upper chamber 1a, and the water overflows from the overflow pipe 3 to the outside of the system. Is taken out.

【0016】すなわち、下室1b内では、抵抗板2の下
方に溜った濃縮汚泥によってろ過層が形成され、水分の
みが上室1a内に溜るもので、凝集汚泥からさらに水分
を抜き取った状態となり、下室1bに高濃縮汚泥を得る
ことができるものである。
That is, in the lower chamber 1b, a filtration layer is formed by the concentrated sludge accumulated below the resistance plate 2, and only the moisture is accumulated in the upper chamber 1a, and the moisture is further extracted from the coagulated sludge. And highly concentrated sludge can be obtained in the lower chamber 1b.

【0017】このようにして形成された下室1bの濃縮
汚泥は、掻寄機6で掻き寄せた上で、引抜管4から系外
に取り出される。この濃縮汚泥の引き抜き時期は、分離
水の出具合をみて、回分式に引き抜いても、また、連続
的に引き抜いてもよい。何れにしても、この発明に係る
装置では、凝集剤を添加した凝集汚泥をさらに凝集汚泥
をろ材としてろ過することになるので、高濃縮汚泥を得
ることができるものである。
The concentrated sludge thus formed in the lower chamber 1b is scraped by the scraper 6, and then taken out of the system from the drawing pipe 4. The concentrated sludge may be withdrawn in a batchwise manner or in a continuous manner, depending on the condition of the separated water. In any case, in the apparatus according to the present invention, the coagulated sludge to which the coagulant has been added is further filtered using the coagulated sludge as a filter medium, so that highly concentrated sludge can be obtained.

【0018】[0018]

【発明の効果】このように、この発明は、従来沈降濃縮
は不可能とされた凝集剤添加の汚泥の沈降濃縮を可能に
するとともに、特に、濃縮汚泥自体をろ材としてろ過し
て水分を切るもので、高濃縮を可能にしたものである。
然も、従来の浮上濃縮に比較して、コンプレッサー等の
浮上手段を必要とせず、また、凝集フロックを掻きまぜ
ることがないので、事後の脱水処理等に好適な濃縮汚泥
を得ることができるものである。
As described above, the present invention enables the sedimentation and concentration of sludge to which a coagulant has been added, which has been impossible to settle and concentrate in the past. It enables high concentration.
Of course, compared to conventional flotation and concentration, it does not require flotation means such as a compressor, and does not stir flocculated flocs, so that it is possible to obtain concentrated sludge suitable for subsequent dehydration treatment and the like. It is.

【図面の簡単な説明】[Brief description of the drawings]

【図1】この発明に係る濃縮装置を備えた汚泥濃縮のフ
ローシート図である。
FIG. 1 is a flow sheet diagram of sludge concentration provided with a concentration device according to the present invention.

【図2】この発明に係る濃縮装置の拡大縦断面図であ
る。
FIG. 2 is an enlarged vertical sectional view of the concentration device according to the present invention.

【符号の説明】[Explanation of symbols]

1 濃縮槽 2 抵抗板 1a 上室 1b 下室 3 溢流管 4 引抜管 5 供給管 7 混和槽 DESCRIPTION OF SYMBOLS 1 Concentration tank 2 Resistance plate 1a Upper chamber 1b Lower chamber 3 Overflow pipe 4 Extraction pipe 5 Supply pipe 7 Mixing tank

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 上部に分離水の溢流部を、下部に濃縮汚
泥の抜取口4を設けた濃縮槽1をメッシュ等の通水性を
有する抵抗板2で上下に仕切るとともに、その仕切った
下室1bには、凝集剤を添加した原液の供給口5を、上
室1aには分離水の取出口3を設けてなる汚泥の濃縮装
置。
1. An overflow section of separated water at an upper portion and a thickening tank 1 provided with an outlet 4 for concentrated sludge at a lower portion thereof are vertically divided by a resistance plate 2 having water permeability such as a mesh. A sludge concentrator comprising a chamber 1b provided with a supply port 5 for a stock solution to which a flocculant has been added, and an upper chamber 1a provided with an outlet 3 for separated water.
【請求項2】 上記凝集剤を添加した原液の混和槽7が
濃縮槽1よりも上位に設置され、原液をその水頭差で濃
縮槽1に供給することを特長とする請求項1記載の汚泥
の濃縮装置。
2. The sludge according to claim 1, wherein the mixing tank 7 for the stock solution to which the flocculant is added is provided above the thickening tank 1, and the stock solution is supplied to the thickening tank 1 with its head difference. Concentrator.
JP8188263A 1996-06-27 1996-06-27 Device for thickening sludge Pending JPH105506A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8188263A JPH105506A (en) 1996-06-27 1996-06-27 Device for thickening sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8188263A JPH105506A (en) 1996-06-27 1996-06-27 Device for thickening sludge

Publications (1)

Publication Number Publication Date
JPH105506A true JPH105506A (en) 1998-01-13

Family

ID=16220620

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8188263A Pending JPH105506A (en) 1996-06-27 1996-06-27 Device for thickening sludge

Country Status (1)

Country Link
JP (1) JPH105506A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1417016A1 (en) * 2001-08-15 2004-05-12 Texaco Development Corporation Reactor and solids settler for grey water treatment
CN114392588A (en) * 2021-12-17 2022-04-26 金堆城钼业汝阳有限责任公司 Method for improving concentration of concentrated tailings by using inclined plate thickener

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1417016A1 (en) * 2001-08-15 2004-05-12 Texaco Development Corporation Reactor and solids settler for grey water treatment
EP1417016A4 (en) * 2001-08-15 2006-02-22 Texaco Development Corp Reactor and solids settler for grey water treatment
CN114392588A (en) * 2021-12-17 2022-04-26 金堆城钼业汝阳有限责任公司 Method for improving concentration of concentrated tailings by using inclined plate thickener
CN114392588B (en) * 2021-12-17 2024-01-19 金堆城钼业汝阳有限责任公司 Method for improving concentration of tailings by using inclined plate thickener

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