JP2001300215A - Running filter cloth type waste liquid treatment apparatus - Google Patents
Running filter cloth type waste liquid treatment apparatusInfo
- Publication number
- JP2001300215A JP2001300215A JP2000125438A JP2000125438A JP2001300215A JP 2001300215 A JP2001300215 A JP 2001300215A JP 2000125438 A JP2000125438 A JP 2000125438A JP 2000125438 A JP2000125438 A JP 2000125438A JP 2001300215 A JP2001300215 A JP 2001300215A
- Authority
- JP
- Japan
- Prior art keywords
- filter cloth
- waste liquid
- sludge
- treatment apparatus
- opening
- 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
Landscapes
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、エンドレス走行ろ
布によって下水処理場等で発生する汚泥を連続的にろ過
濃縮させる廃液処理装置(以下走行ろ布型廃液処理装置
という)に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste liquid treatment apparatus for continuously filtering and condensing sludge generated in a sewage treatment plant or the like by an endless traveling filter cloth (hereinafter referred to as a traveling filter cloth type waste liquid treatment apparatus).
【0002】[0002]
【従来の技術】一般に下水処理場等における廃液処理
は、図7に示すように、最初沈殿池1に下水を流入さ
せ、そこで重力沈降処理によって固液分離される。澄水
は反応タンク2に供給され、そこで活性汚泥処理され
る。活性汚泥処理された澄水は最終沈殿池3で再度重力
沈降処理によって固液分離される。その澄水は滅菌槽4
に供給され、そこで滅菌処理される。そして、滅菌処理
された処理水は、河川、湖沼あるいは海域に放流され
る。一方、最初沈殿池1による沈降汚泥及び最終沈殿池
3による余剰汚泥は、通常混合されて汚泥濃縮槽5に供
給される。汚泥濃縮槽5に供給される混合汚泥の固形物
濃度は、通常1%前後である。混合汚泥は汚泥濃縮槽5
で重力沈降処理され、2%〜3%程度の固形物濃度の濃
縮汚泥が得られる。濃縮汚泥は汚泥貯留槽6に貯留され
る。汚泥貯留槽6に貯留された濃縮汚泥は、脱水機7で
脱水されて、脱水ケーキが得られる。2. Description of the Related Art Generally, in wastewater treatment in a sewage treatment plant or the like, as shown in FIG. The clear water is supplied to the reaction tank 2 where it is treated with activated sludge. The activated sludge-treated clear water is again solid-liquid separated in the final settling basin 3 by gravity settling. The clear water is in sterilization tank 4
Where it is sterilized. Then, the sterilized treated water is discharged to rivers, lakes, or sea areas. On the other hand, the settling sludge from the first settling tank 1 and the excess sludge from the final settling tank 3 are usually mixed and supplied to the sludge thickening tank 5. The solid matter concentration of the mixed sludge supplied to the sludge thickening tank 5 is usually about 1%. Mixed sludge is sludge thickening tank 5
To obtain concentrated sludge having a solid concentration of about 2% to 3%. The concentrated sludge is stored in the sludge storage tank 6. The concentrated sludge stored in the sludge storage tank 6 is dewatered by the dehydrator 7 to obtain a dewatered cake.
【0003】上述した重力沈降による廃液処理法は、電
力消費量が少ないことから、処理費用が安価で済むとい
う利点を有している。しかし、重力沈降による廃液処理
装置は、その設置面積が大きく、しかも、装置の処理能
力が汚泥の性状及び水温に大きく左右される。特に、近
年、廃液中の有機分の増加、あるいは、廃液の集約処理
化に伴う長距離輸送中の廃液の腐敗等によって、汚泥の
沈降性が悪化している。その結果、廃液の集約処理を行
っている廃液処理場の汚泥濃縮槽では、重力沈降処理に
よってコンスタントに固形物濃度で2%以上の濃縮汚泥
を確保することが困難になっている。所定濃度の濃縮汚
泥が得られない場合、後段の脱水処理設備において、脱
水機の安全運転が困難となるばかりか、過剰の脱水処理
設備が必要となる。The above-described waste liquid treatment method by gravity sedimentation has the advantage that the treatment cost can be reduced because the power consumption is small. However, the waste liquid treatment apparatus by gravity sedimentation has a large installation area, and the treatment capacity of the apparatus greatly depends on the properties of sludge and the water temperature. In particular, in recent years, the sedimentability of sludge has been degraded due to an increase in organic components in the waste liquid or decay of the waste liquid during long-distance transportation due to the intensive treatment of waste liquid. As a result, in the sludge concentration tank of the waste liquid treatment plant where the waste liquid is concentrated, it is difficult to constantly secure concentrated sludge having a solid concentration of 2% or more by gravity sedimentation treatment. When the concentrated sludge of a predetermined concentration cannot be obtained, not only the safe operation of the dehydrator is difficult in the subsequent dewatering treatment equipment, but also excessive dewatering treatment equipment is required.
【0004】このような問題を解決するための一例とし
て、特開平11−216312号公報に図8に示すよう
な走行ろ布型の廃液処理装置が開示されている。As an example for solving such a problem, Japanese Patent Application Laid-Open No. H11-216312 discloses a traveling filter cloth type waste liquid treatment apparatus as shown in FIG.
【0005】図8は廃液処理装置の概略斜視図である。
走行ろ布型の廃液処理装置は、廃液供給口9及び濃縮廃
液排出口10を有する廃液室8と、ろ液排出口12を有
するろ液室11とを互いに隣接させて構成している。FIG. 8 is a schematic perspective view of a waste liquid processing apparatus.
The traveling filter cloth type waste liquid treatment apparatus is configured such that a waste liquid chamber 8 having a waste liquid supply port 9 and a concentrated waste liquid discharge port 10 and a filtrate chamber 11 having a filtrate discharge port 12 are adjacent to each other.
【0006】廃液室8内の廃液レベルは、ろ液室11内
の廃液レベルより常時、所定高さだけ高くなるようにし
て、ろ過手段15により、廃液室8内の廃液をろ液室1
1に自然流入させ、廃液の供給、排出及びろ液の排出を
調整している。[0006] The waste liquid level in the waste liquid chamber 8 is always higher than the waste liquid level in the filtrate chamber 11 by a predetermined height, and the waste liquid in the waste liquid chamber 8 is filtered by the filtration means 15.
1, the supply and discharge of the waste liquid and the discharge of the filtrate are adjusted.
【0007】ろ液室11には廃液室8内にコ字状に突出
する突出部13を形成して、突出部13の対向する側壁
に、廃液室8に連通する格子状の開口部14が形成され
ている。The filtrate chamber 11 has a projection 13 protruding in a U-shape within the waste liquid chamber 8, and a lattice-shaped opening 14 communicating with the waste liquid chamber 8 is formed on a side wall of the projection 13 opposite to the projection 13. Is formed.
【0008】ろ過手段15は廃液室8に供給された廃液
をろ過するものであり、ポリエステル等からなるろ布1
8が開口部14を被覆しながら、上部ローラ17(駆動
ローラ)と下部ローラ16との間を垂直方向にエンドレ
スに周回走行するように構成されている。The filtering means 15 is for filtering the waste liquid supplied to the waste liquid chamber 8, and includes a filter cloth 1 made of polyester or the like.
8 is configured to run endlessly in a vertical direction between the upper roller 17 (drive roller) and the lower roller 16 while covering the opening 14.
【0009】符号19は、ろ布18を洗浄するための洗
浄手段であり、符号20は汚泥付着量検出手段であり、
符号21は速度制御手段である。Reference numeral 19 denotes cleaning means for cleaning the filter cloth 18, reference numeral 20 denotes sludge adhesion amount detecting means,
Reference numeral 21 denotes speed control means.
【0010】上記した廃液処理装置によれば、混合汚泥
が廃液室8内に流入すると、汚泥分は、連続的に走行し
ているろ布18によりろ過され、開口部14からろ液室
11内に自然に流入する。ろ布18は、開口部14を被
覆しながら走行するので、廃液室8内の混合汚泥が直
接、ろ液室11に流入する恐れはない。これによって、
廃液室8内の汚泥が濃縮される。濃縮された汚泥は、濃
縮廃液排出口10から廃液室8外に排出され、また、ろ
液室11内に流入したろ液は、ろ液排出口12からろ液
室11外に排出され、それぞれ回収される。According to the above-mentioned waste liquid treatment apparatus, when the mixed sludge flows into the waste liquid chamber 8, the sludge is filtered by the continuously running filter cloth 18, and is passed through the opening 14 into the filtrate chamber 11. Flows naturally into Since the filter cloth 18 travels while covering the opening 14, there is no possibility that the mixed sludge in the waste liquid chamber 8 directly flows into the filtrate chamber 11. by this,
The sludge in the waste liquid chamber 8 is concentrated. The concentrated sludge is discharged from the concentrated waste liquid discharge port 10 to the outside of the waste liquid chamber 8, and the filtrate flowing into the filtrate chamber 11 is discharged from the filtrate discharge port 12 to the outside of the filtrate chamber 11. Collected.
【0011】ろ過の進行に伴って、ろ布18には汚泥ケ
ーキが付着し、蓄積するが、この汚泥ケーキは、洗浄手
段19によって、逐次除去される。従って、ろ布18の
ろ過効率が低下することなく、ろ過手段15は、常時、
安定運転される。As the filtration proceeds, the sludge cake adheres to and accumulates on the filter cloth 18. The sludge cake is sequentially removed by the washing means 19. Therefore, the filtering means 15 is always operated without reducing the filtration efficiency of the filter cloth 18.
Stable operation.
【0012】[0012]
【発明が解決する課題】しかしながら、前述した走行ろ
布型の廃液処理装置は以下の問題がある。廃液処理装置
に用いるろ過手段15は、ポリエステル等からなるろ布
18がろ液室に形成された開口部14を被覆しながら、
上部ローラ17と下部ローラ16との間を垂直方向にエ
ンドレスに周回走行し、その間に廃液をろ過して濃縮汚
泥を形成させる。However, the traveling filter cloth type waste liquid treatment apparatus described above has the following problems. Filtration means 15 used in the waste liquid treatment apparatus, while a filter cloth 18 made of polyester or the like covers the opening 14 formed in the filtrate chamber,
It travels endlessly in a vertical direction between the upper roller 17 and the lower roller 16, during which waste liquid is filtered to form concentrated sludge.
【0013】廃液汚泥を連続的にろ過濃縮している間、
エンドレスのろ布18は、連続的に上部ローラ17、下
部ローラ16、開口部14による一定軌道を周回走行し
て、それらと直接接触しているので、次第に摩耗され
る。この場合開口部14との接触が特に摩耗に影響す
る。[0013] During continuous filtration and concentration of the waste liquid sludge,
The endless filter cloth 18 continuously runs around a fixed orbit by the upper roller 17, the lower roller 16, and the opening 14, and is in direct contact with them, so that it is gradually worn. In this case, contact with the opening 14 particularly affects wear.
【0014】ろ布の摩耗を防止する一つの手段として、
摩耗係数の小さい、破断強度の大きい材質のものを選定
することが考えられるが、ろ布が要求される、目詰まり
が少なく、安定した固形物濃度の濃縮汚泥を得ることが
でき、且つ、ろ過効率が高い等の条件を同時に満足させ
る材質のろ布を選定するためには限度がある。それを得
るためには、ろ布が必要以上に高価になる等の問題があ
る。As one means for preventing abrasion of the filter cloth,
It is conceivable to select a material having a low wear coefficient and a high breaking strength. However, a filter cloth is required. There is a limit in selecting a filter cloth of a material that simultaneously satisfies conditions such as high efficiency. To obtain it, there is a problem that the filter cloth becomes unnecessarily expensive.
【0015】本発明は、上記のような問題点の解決を図
ったものであり、廃液室と開口部を有するろ液室を隣接
させて設け、一定の軌道上を周回走行するエンドレスの
ろ布によって汚泥を連続的にろ過濃縮させる廃液処理装
置を対象として、ろ布本来の機能を充分に確保し、ろ布
の摩耗を低減し、寿命を延長できる走行ろ布型廃液処理
装置を提供することを目的とする。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and has an endless filter cloth which is provided adjacent to a waste liquid chamber and a filtrate chamber having an opening, and travels around a fixed track. To provide a traveling filter cloth type waste liquid treatment apparatus that can sufficiently secure the original function of the filter cloth, reduce the wear of the filter cloth, and prolong the service life, for a waste liquid treatment apparatus that continuously filters and concentrates sludge by filtration. With the goal.
【0016】[0016]
【課題を解決するための手段】請求項1による発明は、
廃液室と開口部を有するろ液室を隣接させて設け、開口
部を含む一定の軌道上を周回走行するエンドレスのろ布
によって汚泥を連続的にろ過濃縮させる廃液処理装置に
おいて、前記走行ろ布と該ろ布が接触する開口部面との
間に気泡ベルトを形成させる空気吹出し装置を設けたこ
とを特徴とする走行ろ布型廃液処理装置である。According to the first aspect of the present invention,
In the waste liquid treatment apparatus, a waste liquid chamber and a filtrate chamber having an opening are provided adjacent to each other, and the sludge is continuously filtered and concentrated by an endless filter cloth circulating on a fixed orbit including the opening. A traveling filter cloth type waste liquid treatment apparatus, wherein an air blowing device for forming a bubble belt is provided between the filter cloth and an opening surface with which the filter cloth contacts.
【0017】この発明によれば、走行ろ布が接触する開
口部面との間に気泡ベルトを形成させる空気吹出し装置
を設け、気泡ベルトによって、該ろ布本体を開口部に直
接に接触させないようにしたので、走行ろ布の摩耗を防
止し、その寿命を延長できる。According to the present invention, an air blowing device for forming a bubble belt between the opening filter and the opening surface with which the traveling filter cloth comes into contact is provided so that the filter cloth main body is not directly contacted with the opening by the bubble belt. Therefore, wear of the traveling filter cloth can be prevented, and the life thereof can be extended.
【0018】請求項2による発明は、請求項1の発明に
おいて、空気吹出し装置が開口部下端の走行ろ布側に設
けられたことを特徴とする。The invention according to claim 2 is characterized in that, in the invention according to claim 1, the air blowing device is provided on the traveling filter cloth side at the lower end of the opening.
【0019】この発明によれば、空気吹出し装置を開口
部下端の走行ろ布側に設けで、走行ろ布の内側に空気を
吹出して気泡を付着させ、開口部との間に気泡ベルトを
形成させることができるので、走行ろ布の摩耗を防止
し、その寿命を延長できる。According to the present invention, the air blowing device is provided on the traveling filter cloth side at the lower end of the opening, and blows air to the inside of the traveling filter cloth to attach air bubbles to form a bubble belt between the opening and the opening. As a result, wear of the traveling filter cloth can be prevented, and its life can be extended.
【0020】[0020]
【発明の実施の形態】以下に、本発明の実施の形態を図
によって詳述する。図1、図2は本発明による実施の形
態を示す概略斜視図であり、図1は汚泥供給側から視た
走行ろ布型廃液処理装置の概略斜視図であり、図2は汚
泥引抜き側から視た走行ろ布型廃液処理装置の切欠けを
有する概略斜視図である。図3は図1のA−A線矢視に
よる空気吹出し装置の配置の一例を示す切欠け概略斜視
図である。DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the drawings. 1 and 2 are schematic perspective views showing an embodiment according to the present invention, FIG. 1 is a schematic perspective view of a traveling filter cloth type waste liquid treatment apparatus viewed from a sludge supply side, and FIG. It is the schematic perspective view which has a notch of the traveling filter cloth type waste liquid processing apparatus seen from. FIG. 3 is a cutaway schematic perspective view showing an example of the arrangement of the air blowing device as viewed from the direction of arrows AA in FIG.
【0021】また、図4は本発明による気泡ベルトの説
明図である。廃液に下水処理場で発生した原汚泥を用い
た。FIG. 4 is an explanatory view of a bubble belt according to the present invention. Raw sludge generated at the sewage treatment plant was used as the waste liquid.
【0022】図1,図2において、廃液処理装置22
は、廃液供給口24及び濃縮廃液排出口25を有する廃
液室23と、ろ液排出口27を有するろ液室26とを互
いに隣接させて構成している。In FIG. 1 and FIG.
Is configured such that a waste liquid chamber 23 having a waste liquid supply port 24 and a concentrated waste liquid discharge port 25 and a filtrate chamber 26 having a filtrate discharge port 27 are adjacent to each other.
【0023】廃液室23内の廃液レベルは、ろ液室26
内の廃液レベルより常時、所定高さだけ高くなるように
して、ろ過手段28により、廃液室23内の廃液をろ液
室26に自然流入させ、廃液の供給、排出及びろ液の排
出を調整している。The level of the waste liquid in the waste liquid chamber 23
The waste liquid in the waste liquid chamber 23 is allowed to flow naturally into the filtrate chamber 26 by the filtration means 28 so that the waste liquid level is always higher than the waste liquid level therein by the predetermined height, and supply and discharge of the waste liquid and discharge of the filtrate are adjusted. are doing.
【0024】ろ液室26には廃液室23内にコ字状に突
出する突出部26aを形成して、突出部26aの対向す
る側壁に、廃液室23に連通する格子状の開口部29が
形成されている。The filtrate chamber 26 has a projection 26a projecting in a U-shape in the waste liquid chamber 23, and a lattice-shaped opening 29 communicating with the waste liquid chamber 23 is formed on the opposite side wall of the projection 26a. Is formed.
【0025】ろ過手段28は廃液室23に供給された廃
液をろ過するものであり、ポリエステル等からなる走行
ろ布30が開口部29を被覆しながら、駆動装置37
と接続している上部ローラ31(駆動ローラ)と下部ロ
ーラ32との間を垂直方向にエンドレスに周回走行する
ように構成されている。The filtering means 28 is for filtering the waste liquid supplied to the waste liquid chamber 23. The driving filter 37 covers the opening 29 with the traveling filter cloth 30 made of polyester or the like.
It is configured to run endlessly in a vertical direction between an upper roller 31 (drive roller) and a lower roller 32 connected to the motor.
【0026】一定軌道上にはろ布緊張装置35、蛇行修
正装置36が設けられ、円滑な周回走行ができるように
している。A filter cloth tensioning device 35 and a meandering correction device 36 are provided on a fixed track so as to enable smooth round running.
【0027】符号33は、走行ろ布30を洗浄するため
の洗浄手段である。この他、図示しない汚泥付着量検出
手段、速度制御装置等が接続される。符号38は防臭カ
バーである。Reference numeral 33 denotes cleaning means for cleaning the traveling filter cloth 30. In addition, a sludge adhering amount detecting means (not shown), a speed control device, and the like are connected. Reference numeral 38 denotes a deodorizing cover.
【0028】本発明では、上記した廃液処理装置22を
構成する走行ろ布30が接触する開口部29面との間に
気泡による気泡ベルトを形成させる空気吹出し装置34
を設けたことを特徴とする。In the present invention, an air blowing device 34 for forming a bubble belt by bubbles between the running filter cloth 30 and the surface of the opening 29 which makes up the waste liquid treatment device 22 described above.
Is provided.
【0029】空気吹出し装置34はノズル34bを有す
る空気吹出管34aとコンプレッサー42で構成されて
いる。図1〜図3の実施の形態では開口部29の下端の
走行ろ布側に空気吹出し装置34の空気吹出管34aを
配置したが、これに限定されるものではなく、空気吹出
しにより開口部に接触する走行ろ布との接触面に気泡ベ
ルトを形成できる配置であればよい。また、開口部は格
子状に限定されるものではなく、廃液を走行ろ布により
ろ過できる形状のものであればよい。The air blowing device 34 comprises an air blowing pipe 34a having a nozzle 34b and a compressor 42. In the embodiment of FIGS. 1 to 3, the air blowing pipe 34 a of the air blowing device 34 is disposed on the traveling filter cloth side at the lower end of the opening 29, but the present invention is not limited to this. Any arrangement can be used as long as the bubble belt can be formed on the contact surface with the traveling filter cloth in contact. Further, the opening is not limited to the lattice shape, and may be any shape as long as the waste liquid can be filtered by the traveling filter cloth.
【0030】気泡ベルト43は、図4に示すように、強
制的に気泡を形成させて、開口部29と接触する走行ろ
布30の裏側に気泡を付着させて、走行ろ布30に一定
軌道上で開口部29と直接に接触させないようにし、走
行ろ布30に代わって、走行ろ布30の摩耗を防止する
ものである。As shown in FIG. 4, the bubble belt 43 forcibly forms bubbles, attaches the bubbles to the back side of the traveling filter cloth 30 in contact with the opening 29, and moves the traveling filter cloth 30 over a fixed orbit. This prevents the running filter cloth 30 from being worn in place of the running filter cloth 30 by preventing direct contact with the opening 29.
【0031】即ち、気泡ベルト43は、気泡を単に上昇
させるのではなく、走行ろ布30の裏側が開口部29と
接触する面即ち格子枠等では気泡ベルトの役割を果た
し、ろ過面では、ろ液と一緒に気泡として、ろ液室26
に入り上昇するものである。従って、走行ろ布30によ
る廃液のろ過に何ら影響を与えない。That is, the bubble belt 43 does not merely raise bubbles, but plays the role of a bubble belt on the surface where the back side of the traveling filter cloth 30 contacts the opening 29, that is, on a lattice frame, etc. Filtration chamber 26 as bubbles with the liquid
And rise. Therefore, it does not affect the filtration of the waste liquid by the traveling filter cloth 30 at all.
【0032】上記した廃液処理装置22によれば、太矢
印に示すように原汚泥が汚泥分配せき47を介して廃液
室23内に流入すると、太矢印に示すように汚泥分は、
連続的に走行している走行ろ布30によりろ過され、開
口部29からろ液室26内に自然に流入する。走行ろ布
30は、開口部29を被覆しながら走行するので、廃液
室23内の原汚泥が直接にろ液室26に流入する恐れは
ない。これによって、廃液室23内の汚泥が濃縮され
る。濃縮された汚泥は、越流せき40を越してシュート
41に入り、濃縮廃液排出口25から廃液室23外に排
出され、また、ろ液室26内に流入したろ液は、ろ液排
出口27からろ液室26外に排出され、それぞれ回収さ
れる。According to the waste liquid treatment apparatus 22 described above, when the raw sludge flows into the waste liquid chamber 23 through the sludge distribution partition 47 as shown by the thick arrow, the sludge content is reduced as shown by the thick arrow.
The water is filtered by the traveling filter cloth 30 running continuously, and naturally flows into the filtrate chamber 26 from the opening 29. Since the traveling filter cloth 30 travels while covering the opening 29, there is no possibility that the raw sludge in the waste liquid chamber 23 directly flows into the filtrate chamber 26. Thereby, the sludge in the waste liquid chamber 23 is concentrated. The concentrated sludge enters the chute 41 via the overflow 40, is discharged from the concentrated waste liquid discharge port 25 to the outside of the waste liquid chamber 23, and the filtrate flowing into the filtrate chamber 26 is discharged to the filtrate discharge port. The liquid is discharged from the filtrate chamber 26 to the outside of the filtrate chamber 26 and is collected.
【0033】また、ろ過の進行に伴って、走行ろ布30
には汚泥ケーキが付着し、蓄積するが、この汚泥ケーキ
は、洗浄手段33によって、逐次除去される。従って、
ろ布30のろ過効率が低下することなく、ろ過手段28
は、常時、安定運転される。符号39はスクレーパを示
す。As the filtration proceeds, the traveling filter cloth 30
The sludge cake adheres to and accumulates on the surface, and this sludge cake is sequentially removed by the washing means 33. Therefore,
The filtering means 28 can be used without reducing the filtration efficiency of the filter cloth 30.
Is always operated stably. Reference numeral 39 indicates a scraper.
【0034】ろ過手段28では走行ろ布30が開口部2
9を被覆しながら、上部ローラ31と下部ローラ32と
の間を垂直方向にエンドレスに周回走行するが、走行ろ
布が接触する開口部面との間に気泡ベルト43を形成し
ているので、開口部29との接触による摩耗が生じな
い。In the filtering means 28, the traveling filter cloth 30 is
While running around the upper roller 31 and the lower roller 32 endlessly in a vertical direction while covering 9, the bubble belt 43 is formed between the upper roller 31 and the lower roller 32 and the opening surface with which the traveling filter cloth comes into contact. Wear due to contact with the opening 29 does not occur.
【0035】従って、本発明による走行ろ布型廃液処理
装置によれば、走行ろ布は廃液のろ過に要求される条件
を主体として選定できるので、安価にろ布材料を入手す
ることができる。Therefore, according to the traveling filter cloth type waste liquid treatment apparatus of the present invention, the traveling filter cloth can be selected mainly based on the conditions required for the filtration of the waste liquid, so that the filter cloth material can be obtained at low cost.
【0036】図5は本発明に用いる空気吹出し装置の配
置の他例を示す切欠け概略斜視図であり、図6は図5に
より形成される気泡ベルトの説明図である。図3,図4
と共通する箇所には同じ符号を付けて、その説明の一部
を省略した。FIG. 5 is a cutaway schematic perspective view showing another example of the arrangement of the air blowing device used in the present invention, and FIG. 6 is an explanatory view of the bubble belt formed according to FIG. Figures 3 and 4
The same reference numerals are given to the parts common to and the description thereof is partially omitted.
【0037】空気吹出し装置44は開口部29の縦桟を
構成する複数のノズル45bを有する空気吹出管45a
と、空気吹出管45aに圧縮空気を配分する本管45c
と、本管45cに圧縮空気を供給するとコンプレッサー
42で構成されている。開口部29の横桟は補強材とし
て用いている。しかし、横桟も必要に応じて空気吹出管
とすることもできる。The air blowing device 44 has an air blowing tube 45a having a plurality of nozzles 45b forming a vertical bar of the opening 29.
And a main pipe 45c for distributing compressed air to the air blowing pipe 45a
When compressed air is supplied to the main pipe 45c, the main pipe 45c is constituted by the compressor 42. The horizontal rail of the opening 29 is used as a reinforcing material. However, the horizontal rail can also be formed as an air blowing pipe if necessary.
【0038】空気吹出管45aは開口部29の汚泥供給
側と濃縮汚泥排出側の縦桟に設けている。一般に、走行
ろ布が縦桟に接触しながら上下方向に走行するので、縦
桟を空気吹出管45aで構成して、空気吹出管45aの
ノズル45bから空気を吹出し、気泡ベルト46を容易
に形成できる。気泡ベルト46は、図6に示すように、
複数の空気吹出管45aから強制的に空気を吹出し、気
泡を形成させて、開口部29の空気吹出管45aと接触
する走行ろ布30の裏側に気泡を付着させて、空気吹出
管45aと直接に接触させないようにし、走行ろ布30
の摩耗を防止する。The air blowing pipes 45a are provided on the vertical rails on the sludge supply side and the concentrated sludge discharge side of the opening 29. In general, since the traveling filter cloth travels in the vertical direction while being in contact with the longitudinal crosspieces, constitutes a vertical bar at the air outlet pipe 45a, blowing air from the nozzle 45 b of the air discharge pipe 45a, the bubbles belt 46 easily Can be formed. The bubble belt 46 is, as shown in FIG.
Air is forcibly blown out from the plurality of air blowing pipes 45a to form air bubbles, and the air bubbles are adhered to the back side of the traveling filter cloth 30 that comes into contact with the air blowing pipes 45a in the openings 29, so that the air directly flows into the air blowing pipes 45a. To avoid contact with the running filter cloth 30.
To prevent abrasion.
【0039】[0039]
【発明の効果】以上のように、本発明は、廃液室と開口
部を有するろ液室を隣接させて設け、一定の軌道上を周
回走行するエンドレスの走行ろ布によって汚泥を連続的
にろ過濃縮させる廃液処理装置を対象として、走行ろ布
が接触する開口部面との間に気泡ベルトを形成させる空
気吹出し装置を設けるという簡単な構造によって、ろ布
本来の機能を充分に確保し、走行ろ布の摩耗を低減し、
寿命を延長できる。As described above, according to the present invention, a waste liquid chamber and a filtrate chamber having an opening are provided adjacent to each other, and the sludge is continuously filtered by an endless traveling filter cloth which runs around a fixed track. For the waste liquid treatment device to be concentrated, the simple function of providing an air blowing device to form an air bubble belt between the opening surface and the running filter cloth is in contact with the filter cloth. Reduce the wear of the filter cloth,
Life can be extended.
【図1】本発明による実施の形態を示す汚泥供給側から
視た概略斜視図である。FIG. 1 is a schematic perspective view showing an embodiment according to the present invention as viewed from a sludge supply side.
【図2】図1の裏側の汚泥引抜き側から視た概略斜視図
である。FIG. 2 is a schematic perspective view seen from the sludge extraction side on the back side of FIG.
【図3】図1のA−A線矢視による空気吹出し装置の配
置の一例を示す切欠け概略斜視図である。FIG. 3 is a cutaway schematic perspective view showing an example of the arrangement of the air blowing device as viewed from the direction of arrows AA in FIG. 1;
【図4】本発明に用いる気泡ベルトの一例を示す説明図
である。FIG. 4 is an explanatory diagram showing an example of a bubble belt used in the present invention.
【図5】本発明に用いる空気吹出し装置の配置の他例を
示す切欠け概略斜視図である。FIG. 5 is a cutaway schematic perspective view showing another example of the arrangement of the air blowing device used in the present invention.
【図6】図5により形成される気泡ベルトの説明図であ
る。FIG. 6 is an explanatory view of a bubble belt formed according to FIG. 5;
【図7】従来の下水処理場における廃液処理方法を示す
流れ図である。FIG. 7 is a flowchart showing a conventional wastewater treatment method in a sewage treatment plant.
【図8】従来の走行ろ布型廃液処理装置の一例を示す概
略斜視図である。FIG. 8 is a schematic perspective view showing an example of a conventional traveling filter cloth type waste liquid treatment apparatus.
22 廃液処理装置 23 廃液室 24 廃液供給口 25 濃縮廃液排出口 26 ろ液室 27 ろ液排出口 28 ろ過手段 29 開口部 30 走行ろ布 31 上部ローラ 32 下部ローラ 33 洗浄手段 34、44 空気吹出し装置 34a、45a 空気吹出管 34b 45b ノズル 35 ろ布緊張装置 36 蛇行修正装置 37 駆動装置 38 防臭カバー 39 スクレーパ 40 越流堰 41 シュート 42 コンプレッサー 43、46 気泡ベルト 45b 本管 47 汚泥分配せき Reference Signs List 22 Waste liquid treatment device 23 Waste liquid chamber 24 Waste liquid supply port 25 Concentrated waste liquid discharge port 26 Filtration chamber 27 Filtrate discharge port 28 Filtration means 29 Opening 30 Running filter cloth 31 Upper roller 32 Lower roller 33 Cleaning means 34, 44 Air blowing device 34a, 45a Air blowing tube 34b 45b nozzle 35 Filter cloth tensioning device 36 Meandering correction device 37 Drive device 38 Odor control cover 39 Scraper 40 Overflow weir 41 Chute 42 Compressor 43, 46 Bubble belt 45b Main pipe 47 Sludge distribution
Claims (2)
せて設け、開口部を含む一定の軌道上を周回走行するエ
ンドレスのろ布によって汚泥を連続的にろ過濃縮させる
廃液処理装置において、前記走行ろ布と該ろ布が接触す
る開口部面との間に気泡ベルトを形成させる空気吹出し
装置を設けたことを特徴とする走行ろ布型廃液処理装
置。1. A waste liquid treatment apparatus for providing a waste liquid chamber and a filtrate chamber having an opening adjacent to each other and continuously filtering and condensing sludge with an endless filter cloth circulating on a fixed orbit including an opening. A traveling filter cloth type waste liquid treatment apparatus, further comprising an air blowing device for forming a bubble belt between the traveling filter cloth and an opening surface with which the filter cloth contacts.
側に設けられたことを特徴とする請求項1記載の走行ろ
布型廃液処理装置。2. The traveling filter cloth type waste liquid treatment apparatus according to claim 1, wherein the air blowing device is provided on the traveling filter cloth side at the lower end of the opening.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000125438A JP3758461B2 (en) | 2000-04-26 | 2000-04-26 | Travel filter type waste liquid treatment equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000125438A JP3758461B2 (en) | 2000-04-26 | 2000-04-26 | Travel filter type waste liquid treatment equipment |
Publications (2)
Publication Number | Publication Date |
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JP2001300215A true JP2001300215A (en) | 2001-10-30 |
JP3758461B2 JP3758461B2 (en) | 2006-03-22 |
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ID=18635395
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Application Number | Title | Priority Date | Filing Date |
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JP2000125438A Expired - Fee Related JP3758461B2 (en) | 2000-04-26 | 2000-04-26 | Travel filter type waste liquid treatment equipment |
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Cited By (1)
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CN117899539A (en) * | 2024-03-20 | 2024-04-19 | 山西兴源盛科技有限公司 | Antifreezing solution filtering device |
-
2000
- 2000-04-26 JP JP2000125438A patent/JP3758461B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN117899539A (en) * | 2024-03-20 | 2024-04-19 | 山西兴源盛科技有限公司 | Antifreezing solution filtering device |
CN117899539B (en) * | 2024-03-20 | 2024-05-24 | 山西兴源盛科技有限公司 | Antifreezing solution filtering device |
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