JPS6147640B2 - - Google Patents

Info

Publication number
JPS6147640B2
JPS6147640B2 JP53047805A JP4780578A JPS6147640B2 JP S6147640 B2 JPS6147640 B2 JP S6147640B2 JP 53047805 A JP53047805 A JP 53047805A JP 4780578 A JP4780578 A JP 4780578A JP S6147640 B2 JPS6147640 B2 JP S6147640B2
Authority
JP
Japan
Prior art keywords
cleaning
sludge
cloth
sponge
water
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.)
Expired
Application number
JP53047805A
Other languages
Japanese (ja)
Other versions
JPS54140267A (en
Inventor
Juichi Hanami
Yutaka Ikuma
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.)
Kurita Water Industries Ltd
Original Assignee
Kurita Water Industries 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 Kurita Water Industries Ltd filed Critical Kurita Water Industries Ltd
Priority to JP4780578A priority Critical patent/JPS54140267A/en
Publication of JPS54140267A publication Critical patent/JPS54140267A/en
Publication of JPS6147640B2 publication Critical patent/JPS6147640B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 この発明は有機質汚泥を過または脱水する媒
体を化学洗浄して再生する過、脱水媒体の洗浄
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for cleaning a filtration or dehydration medium in which a medium for filtration or dehydration of organic sludge is chemically washed and regenerated.

水処理汚泥、ヘドロなどの難脱水性の有機質汚
泥の脱水には、布などの過媒体による過脱
水や、スポンジなどの脱水媒体による脱水、ある
いは両者併用による脱水などが行なわれている。
布による過脱水は布ベルトを無端走行さ
せ、布上に給泥して重力過により脱水した
り、加圧して脱水することが行なわれている。ス
ポンジによる脱水はスポンジロールあるいはスポ
ンジベルト上に給泥し、スポンジの毛管現象によ
り汚泥中の水分を吸い込ませて脱水し、スポンジ
表面から脱水汚泥を掻取るとともに圧搾によりス
ポンジに吸い込まれた水分を除去し、再び給泥、
脱水するようにされている。両者併用による脱水
は布による重力脱水後、布の裏側にスポンジ
を接触させて毛管現象により脱水し、さらに必要
に応じて圧搾を加えて汚泥中の水分を搾り出すよ
うにしている。
For dehydration of organic sludge that is difficult to dewater, such as water treatment sludge and sludge, methods include excessive dehydration using a permeable medium such as cloth, dehydration using a dehydrating medium such as a sponge, or dehydration using a combination of both.
Excessive dehydration using cloth is carried out by running a cloth belt endlessly, supplying mud onto the cloth and dehydrating it by gravity, or dehydrating it by applying pressure. For dewatering using a sponge, sludge is supplied onto a sponge roll or a sponge belt, and the water in the sludge is sucked in and dehydrated by the capillary action of the sponge.The dehydrated sludge is scraped off the surface of the sponge, and the water sucked into the sponge is removed by squeezing. Then, the mud was supplied again.
It is made to dehydrate. Dehydration using both methods involves gravity dehydration using a cloth, followed by dehydration by capillary action by bringing a sponge into contact with the back side of the cloth, and then squeezing the sludge as necessary to squeeze out the water in the sludge.

このような脱水操作中、過または脱水媒体は
脱水汚泥掻取後圧力水または圧力空気噴射により
洗浄しているが、このような常時洗浄でも完全に
洗浄することができず、徐々に汚れが蓄積して目
詰りを起こし、過、脱水能力が低下する。従来
このような能力低下した過、脱水媒体の洗浄再
生法として、媒体を装置外に取出してフラツシン
グ等により洗浄していたが、労力が多い割には洗
浄効果は低く、またシユウ酸等による化学洗浄法
も行なわれたが、洗浄効果は低くかつた。
During such dewatering operations, the dehydrated medium is cleaned by pressure water or pressurized air injection after scraping the dehydrated sludge, but even such constant cleaning cannot completely clean it, and dirt gradually accumulates. This will cause clogging and reduce dehydration capacity. Conventionally, as a cleaning and regenerating method for dehydrating media with reduced capacity, the media was taken out of the equipment and cleaned by flushing, etc., but the cleaning effect was low despite the amount of labor involved, and chemical cleaning using oxalic acid, etc. A cleaning method was also used, but the cleaning effect was low.

本発明はこのような欠点を除去して、能力低下
した過、脱水媒体を効率よく洗浄して再生する
方法を提供することを目的としている。
It is an object of the present invention to eliminate such drawbacks and provide a method for efficiently cleaning and regenerating filtration and dehydration media whose capacity has decreased.

本発明は有機質汚泥を過または脱水する布
またはスポンジからなる過、脱水媒体を化学洗
浄して再生する方法において、過酸化物およびア
ルカリを含む洗浄液を前記媒体に接触させて洗浄
することを特徴とする過、脱水媒体の洗浄方法
である。
The present invention is a method for chemically cleaning and regenerating a filtration/dehydration medium made of a cloth or sponge for filtration or dewatering of organic sludge, characterized in that cleaning is carried out by bringing a cleaning solution containing peroxide and an alkali into contact with the medium. This is a method for cleaning dehydrated media.

過、脱水媒体により脱水処理される汚泥とし
ては、水処理汚泥、ヘドロなどあらゆる有機質汚
泥が含まれるが、本発明は特に下水処理場、し尿
処理場などから排出される活性汚泥、消化汚泥な
どの有機質汚泥の脱水に用いられる媒体の洗浄に
適している。このような有機質汚泥は粘質物を含
み、これが媒体の間隙に付着して目詰の原因とな
るが、本発明の洗浄法は、このような物質による
目詰りをも効率よく洗浄除去することができる。
さらに本発明は有機質汚泥に有機高分子凝集剤を
添加して脱水する媒体の洗浄に適している。この
ような凝集剤は凝集作用により媒体への汚泥の付
着を促進するが本発明の洗浄法はこれによる目詰
りをも効率よく洗浄除去することができる。
The sludge to be dehydrated with a filtration and dehydration medium includes all kinds of organic sludge such as water treatment sludge and sludge, but the present invention is particularly applicable to activated sludge, digested sludge, etc. discharged from sewage treatment plants, human waste treatment plants, etc. Suitable for cleaning media used for dewatering organic sludge. Such organic sludge contains sticky substances that adhere to the interstices of the medium and cause clogging, but the cleaning method of the present invention can efficiently clean and remove clogging caused by such substances. can.
Further, the present invention is suitable for cleaning a medium for dewatering organic sludge by adding an organic polymer flocculant thereto. Such a flocculant promotes the adhesion of sludge to the medium through its flocculating action, and the cleaning method of the present invention can also efficiently clean and remove clogging caused by this.

本発明において洗浄対象となる媒体は布、ス
クリーンなどの過媒体、スポンジ、フエルトな
どの脱水媒体である。これらの媒体を備えた脱水
装置としては、過媒体のみを備えたもの、脱水
媒体のみを備えたもの、両者を備えたもの、およ
びこれらに加圧または圧搾機構を付加したものな
どがあるが、いずれの装置の媒体も本発明による
洗浄の対象となる。
In the present invention, the medium to be cleaned is a permeable medium such as a cloth or screen, or a dehydrating medium such as a sponge or felt. Dehydration devices equipped with these media include those equipped only with a permeable medium, those equipped only with a dehydration medium, those equipped with both, and those equipped with a pressurizing or squeezing mechanism. The media of either device is subject to cleaning according to the present invention.

洗浄液としては過酸化物とアルカリを含む水溶
液を使用するが、アルカリ性の過酸化物を使用す
る場合には別にアルカリを添加しなくてもよい場
合がある。過酸化物としては過酸化水素、過酸化
ナトリウム、過炭酸ナトリウムなどが使用でき、
アルカリとしては水酸化ナトリウム、水酸化カリ
ウムなどのか性アルカリが使用できる。過酸化水
素と水酸化ナトリウムを使用する場合は過酸化水
素0.5〜3%(好ましくは1〜2%)、水酸化ナト
リウム2〜8%(好ましくは3〜6%)を含む水
溶液として使用する。過酸化水素が0.5%未満で
は汚れの除去効果が小さく、3%を越えると媒体
(特にスポンジ)に悪影響を与え好ましくない。
水酸化ナトリウムは2%未満では汚れの除去効果
は少なく、8%を越えても効果は上昇しない。
An aqueous solution containing a peroxide and an alkali is used as the cleaning liquid, but when an alkaline peroxide is used, it may not be necessary to separately add an alkali. Hydrogen peroxide, sodium peroxide, sodium percarbonate, etc. can be used as peroxides.
As the alkali, caustic alkalis such as sodium hydroxide and potassium hydroxide can be used. When hydrogen peroxide and sodium hydroxide are used, they are used as an aqueous solution containing 0.5 to 3% (preferably 1 to 2%) hydrogen peroxide and 2 to 8% (preferably 3 to 6%) sodium hydroxide. If the hydrogen peroxide content is less than 0.5%, the stain removal effect will be small, and if it exceeds 3%, it will have an adverse effect on the medium (particularly the sponge), which is not preferable.
If the amount of sodium hydroxide is less than 2%, the stain removal effect will be low, and if it exceeds 8%, the effect will not increase.

洗浄方法は目詰まりした媒体を洗浄液と接触さ
せて行なうが、接触の方法は特に限定されない。
布の場合は布上に散布して通過させ、これを
繰返し行なうのが好ましい。スポンジの場合はス
ポンジ表面に散布して内部に浸透させた後圧搾に
より搾り出し、これを繰返し行なうのが好まし
い。いずれも装置から媒体を取りはずす必要はな
く、装置を運転したまま、給泥を停止し、しばら
く水洗した後洗浄液を散布し、洗浄液を循環しな
がら洗浄を行なうとよい。
The cleaning method is carried out by bringing the clogged medium into contact with a cleaning liquid, but the method of contact is not particularly limited.
In the case of cloth, it is preferable to sprinkle the agent on the cloth and allow it to pass through, and repeat this process. In the case of a sponge, it is preferable to spray it on the surface of the sponge and let it penetrate into the sponge, and then squeeze it out by squeezing, and repeat this process. In either case, there is no need to remove the medium from the device; it is better to stop the mud supply while the device is in operation, rinse with water for a while, then spray the cleaning liquid, and perform cleaning while circulating the cleaning liquid.

洗浄の際過酸化物は酸化作用をするとともに発
泡により物理的な洗浄作用をも行なう。またアル
カリは有機物を溶解するとともに過酸化物の分解
を促進する。そして本発明では両者の相乗効果に
より、それぞれ単独の場合よりも優れた洗浄効果
を発揮させることができ、従来の洗浄法で効果の
ない有機質汚泥に使用した過、脱水媒体も効率
よく洗浄することができる。
During cleaning, peroxide not only has an oxidizing effect, but also has a physical cleaning effect by foaming. Alkali also dissolves organic substances and promotes the decomposition of peroxides. In the present invention, due to the synergistic effect of the two, it is possible to achieve a cleaning effect that is better than when either one is used alone, and it is possible to efficiently clean filtration and dehydration media used for organic sludge, which is ineffective with conventional cleaning methods. I can do it.

以下本発明を図面の脱水装置の洗浄に実施した
場合について説明する。図面は脱水装置の正面図
である。この脱水装置により汚泥を脱水するに
は、無端走行する2枚の布ベルト1a,1b上
に給泥装置2a,2bから給泥し、布ベルトが
回転式または非回転式の浸出水流下手段3a,3
b上を走行する間に汚泥中の水分を重力で布裏
側に浸出させ、浸出した水を浸出水流下手段を伝
わせてシユート4a,4bに流下させ重力過脱
水を行なう。
Hereinafter, a case will be described in which the present invention is applied to cleaning the dewatering apparatus shown in the drawings. The drawing is a front view of the dehydrator. To dewater sludge using this dewatering device, sludge is supplied from a sludge supply device 2a, 2b onto two endlessly running cloth belts 1a, 1b, and the cloth belt is rotatable or non-rotating leachate flowing means 3a. ,3
While running on the sludge, moisture in the sludge is leached out to the back side of the cloth by gravity, and the leached water is transmitted through the leaching water flow means and flows down to the chutes 4a and 4b, thereby performing gravity over-drying.

重力脱水部を通過した一方の布ベルト1aを
反転させ、表面の汚泥層が他の布ベルト1bの
汚泥層に対向する状態で重ね合わせ、中間に汚泥
層をはさんで圧着し、これをスポンジロール5
a,5b,5cに接触、圧着して送行させ、この
間スポンジロールの吸引力により汚泥中の水分を
吸引脱水する。スポンジロールは洗浄水管6a,
6b,6cから洗浄水を噴射して洗浄し、絞りロ
ール7a,7b,7cにより吸引した水を絞り出
して回転させ、絞り出された水はシユート8a,
8b,8cに集める。
One of the cloth belts 1a that has passed through the gravity dewatering section is reversed, and the sludge layer on the surface is placed on top of the sludge layer of the other cloth belt 1b, and the sludge layer is sandwiched in between and pressed together. roll 5
a, 5b, and 5c, and are conveyed by contacting and press-bonding, and during this time, the water in the sludge is sucked and dehydrated by the suction force of the sponge roll. The sponge roll has a cleaning water pipe 6a,
Washing water is sprayed from 6b and 6c for washing, and the water sucked out by squeezing rolls 7a, 7b and 7c is squeezed out and rotated, and the squeezed water is sent to chute 8a,
Collect at 8b and 8c.

スポンジロールによる吸引脱水部を通過した
布ベルトは圧着状態のまま圧搾ロール9a,9
b,9c,9d,9eにより圧着されて走行し、
中間にはさんだ汚泥中の水分を圧搾脱水する。搾
り出された水分は水分流下手段10a,10b,
10c,10d,10eを伝わせてシユート11
に流下させる。
The fabric belt that has passed through the suction and dewatering section using sponge rolls is transferred to pressing rolls 9a, 9 while remaining in a crimped state.
Runs while being crimped by b, 9c, 9d, and 9e,
The water in the sludge sandwiched in between is compressed and dehydrated. The squeezed out water is transferred to the water flow down means 10a, 10b,
Shoot 11 by transmitting 10c, 10d, and 10e.
flow down to.

圧搾脱水部を通過した布ベルトは駆動ロール
12a,12bによつて圧着状態を解いて分離
し、それぞれスクレーパー13a,13bにより
付着した汚泥を剥離し、洗浄水管14a,14b
から洗浄水を噴射して洗浄水をシユート15a,
15bに流し、緊張ロール16a,16bに通し
た後、重力脱水部へ循環させる。
The cloth belt that has passed through the compression and dehydration section is released from the compressed state by drive rolls 12a and 12b and separated, and the adhered sludge is removed by scrapers 13a and 13b, respectively, and washed water pipes 14a and 14b are removed.
The cleaning water is sprayed from the chute 15a,
15b, passed through tension rolls 16a and 16b, and then circulated to the gravity dewatering section.

この脱水装置ではスポンジロール5a,5b,
5cおよび圧搾ロール9a,9b,,9c,9
d,9eを走行始端から走行末端に至るに従つて
小径にし、走行末端側に設けた駆動ロール12
a,12bで駆動しているため、走行末端に至る
ほどロールに布が強く圧着され脱水効果が大き
くなるようにされている。
In this dewatering device, sponge rolls 5a, 5b,
5c and pressing rolls 9a, 9b, 9c, 9
d, 9e have smaller diameters from the running start end to the running end, and the drive roll 12 is provided at the running end side.
Since the rollers a and 12b are driven, the cloth is more strongly pressed against the rolls toward the end of the run, and the dewatering effect becomes greater.

さて、この脱水装置におけるスポンジロールお
よび布の洗浄は洗浄水管6a,6b,6c,1
4a,14bから洗浄水を噴射して汚泥の脱水工
程中、常時洗浄を行なつているが、前述のように
このような水による洗浄だけでは完全ではなく、
目詰りの生成に応じて本発明の化学洗浄を実施す
る。
Now, the cleaning of the sponge roll and cloth in this dehydration device is carried out by washing water pipes 6a, 6b, 6c, 1
Washing water is injected from 4a and 14b to constantly wash the sludge during the dewatering process, but as mentioned above, washing with water alone is not complete.
The chemical cleaning of the present invention is carried out in response to the formation of clogging.

化学洗浄を行なうには、まず給泥装置2a,2
bからの給泥を停止し、布ベルト1a,1bは
脱水工程時と同様に走行させ、洗浄水管6a,6
b,6c,14a,14bからしばらくの間洗浄
水を噴射して水洗浄を継続する。このときシユー
ト4a,4b,8a,8b,8c,11,15
a,15bから流出する排水は脱水工程時と同様
に排水管17a,17b……17nから集水管1
8に集め弁19を通して系列に排出する。
To perform chemical cleaning, first the mud supply devices 2a, 2
The supply of mud from b is stopped, the cloth belts 1a and 1b are run in the same way as in the dewatering process, and the washing water pipes 6a and 6 are
Water washing is continued by spraying washing water from b, 6c, 14a, and 14b for a while. At this time, shoots 4a, 4b, 8a, 8b, 8c, 11, 15
The waste water flowing out from a, 15b is transferred from the drain pipes 17a, 17b...17n to the collection pipe 1, as in the dewatering process.
8 and is discharged into the series through a collection valve 19.

次に薬液タンク20に前述の過酸化物およびア
ルカリを含む洗浄液を調整し、洗浄水管6a,6
b,6c,14a,14bからの洗浄水の噴射を
停止し、ポンプ21を駆動して送液管22a,2
2b……22nを経由して洗浄水管14a,14
bおよび洗浄液管23a,23b,23cから洗
浄液を、布ベルトおよびスポンジロールに均一
に噴射する。この間布ベルトは走行させ、弁1
9を閉じ弁24を開き、洗浄液を循環させる。薬
液タンク20に還流する洗浄液は濁質を含んでい
るため薬液タンク20内に滞留させて濁質を沈降
させ、上澄液のみをポンプ21から送液するよう
にするかあるいはポンプ21の吸液管にストレー
ナ等を設けて濁質が再び送液されることのないよ
うにする。
Next, the cleaning liquid containing the above-mentioned peroxide and alkali is prepared in the chemical tank 20, and the cleaning water pipes 6a, 6
b, 6c, 14a, 14b is stopped, the pump 21 is driven, and the liquid sending pipes 22a, 2
Washing water pipes 14a, 14 via 2b...22n
The cleaning liquid is uniformly sprayed onto the cloth belt and the sponge roll from the cleaning liquid pipes 23a, 23b, and 23c. During this time, the cloth belt is running and the valve 1
9 and open the valve 24 to circulate the cleaning liquid. The cleaning liquid flowing back into the chemical tank 20 contains suspended matter, so either it is left in the chemical tank 20 to settle the suspended matter, and only the supernatant liquid is sent from the pump 21, or the pump 21 sucks the liquid. Install a strainer or the like in the tube to prevent suspended solids from being pumped out again.

洗浄液を布ベルトまたはスポンジロールに噴
射する手段は洗浄水管と兼用してもよく、別に設
けてもよく、また化学洗浄時にだけ取付けるよう
にしてもよい。いずれにしても洗浄液が布また
はスポンジロールの全幅に均一に散布できるよう
にスリツト状または多孔状の散布手段を設けるよ
うにする。
The means for spraying the cleaning liquid onto the cloth belt or sponge roll may also be used as a washing water pipe, may be provided separately, or may be installed only during chemical cleaning. In any case, a slit-like or porous spreading means is provided so that the cleaning liquid can be uniformly spread over the entire width of the cloth or sponge roll.

こうして洗浄液による化学洗浄をしばらく継続
した後、ポンプ21の駆動を停止し、洗浄水管6
a,6b,6c,14a,14bから洗浄水を噴
射して水洗浄を行ない、薬液タンク20の洗浄排
液は酸を注入して中和処理し、洗浄工程を終る。
After chemical cleaning with the cleaning liquid continues for a while, the drive of the pump 21 is stopped and the cleaning water pipe 6
Water cleaning is performed by spraying cleaning water from a, 6b, 6c, 14a, and 14b, and the cleaning liquid in the chemical tank 20 is neutralized by injecting acid to complete the cleaning process.

図面の脱水装置を長期間連続運転して、高分子
凝集剤を加えたし尿処理場の余剰活性汚泥の脱水
処理を行ない、布ベルトが濃褐色を呈し、スポ
ンジロールの吸水量が14.5/hrに低下したとこ
ろで、化学洗浄を行なつた場合について以下説明
する。前述のように給泥を停止し、過酸化水素2
%、水酸化ナトリウム5%の洗浄液を布ベルト
およびスポンジロールに噴射し、洗浄液を循環し
て10分間洗浄したところ、布等の汚れは洗浄液
に移行して無色透明であつた洗浄液は褐色にな
り、布は元の色になり、スポンジロールの吸水
性能もほぼ元の34.3/hrに回復した。洗浄の初
期には布ベルトおよびスポンジロール面で盛ん
に発泡を起こし、汚れ物質を強制的に剥離してい
ることが観察された。洗浄廃液は過酸化水素が分
解され、単に有機物を溶解した水酸化ナトリウム
溶液となつたので、これに塩酸を加えて中和し、
活性汚泥処理装置の原水に加えて処理した。
The dewatering equipment shown in the drawing was operated continuously for a long period of time to dehydrate excess activated sludge from a human waste treatment plant with the addition of a polymer flocculant, and the fabric belt turned dark brown and the water absorption rate of the sponge rolls increased to 14.5/hr. A case where chemical cleaning is performed when the temperature has decreased will be described below. Stop the slurry supply as described above, and add hydrogen peroxide 2
When a cleaning solution containing 5% sodium hydroxide and 5% sodium hydroxide was sprayed onto the cloth belt and sponge roll, and the cleaning solution was circulated and washed for 10 minutes, the stains on the cloth were transferred to the cleaning solution, and the cleaning solution, which was clear and colorless, turned brown. , the cloth returned to its original color, and the water absorption performance of the sponge roll was almost restored to its original level of 34.3/hr. In the early stages of cleaning, it was observed that foaming occurred actively on the cloth belt and sponge roll surface, and the soiled substances were forcibly removed. Hydrogen peroxide in the washing waste liquid was decomposed and it simply became a sodium hydroxide solution with organic matter dissolved, so hydrochloric acid was added to neutralize it.
It was added to the raw water of the activated sludge treatment equipment.

洗浄液として2%過酸化水素水を使用して10分
間洗浄した場合は、当初は発泡がみられある程度
の汚れは除去できたが、次第に発泡性がなくな
り、それ以上の洗浄はできなかつた。そして布
も完全に元の色に戻らず、スポンジロールの内部
の汚れは除去できなかつた。5%過酸化水素水を
使用した場合は、布はほぼ洗浄できたが、スポ
ンジロールのスポンジはある程度洗浄できたもの
の、数回の繰返し洗浄によつてスポンジの機械的
性能が劣化し吸水機能も低下して洗浄の目的を達
することができなかつた。また5%および10%水
酸化ナトリウム溶液を使用したところ、洗浄液は
褐色になり布等から汚染物質が移行したことが
認められたが、布はまだ褐色を呈しており、ス
ポンジロールの吸水性能も元に回復しなかつた。
When cleaning for 10 minutes using 2% hydrogen peroxide as the cleaning solution, foaming was observed at first and a certain amount of dirt could be removed, but the foaming properties gradually disappeared and further cleaning was no longer possible. The cloth did not return to its original color completely, and the stains inside the sponge roll could not be removed. When using 5% hydrogen peroxide solution, most of the cloth could be cleaned, but although the sponge of the sponge roll could be cleaned to some extent, the mechanical performance of the sponge deteriorated after repeated washing several times, and the water absorption function also deteriorated. The purpose of cleaning could not be achieved due to the deterioration. When 5% and 10% sodium hydroxide solutions were used, the cleaning solution turned brown and it was observed that contaminants had migrated from the cloth, but the cloth was still brown and the water absorption performance of the sponge roll was poor. It never recovered.

以上本発明を説明したが、本発明によれば、難
脱水性の汚泥を脱水して目詰りを起こした布、
スポンジ等の過、脱水媒体を簡単な操作で効率
よく洗浄して短時間で再生することができる。有
機質汚泥、特に有機高分子凝集剤を添加した有機
質汚泥を脱水し目詰りを生じた媒体のように従来
法では洗浄再生できなかつた媒体をも効率よく洗
浄再生することができる。また洗浄により生成す
る廃液も単に中和するだけで活性汚泥処理法等に
より処理することができ、特別の処理装置を必要
としない。
The present invention has been described above, and according to the present invention, a cloth that has become clogged by dehydrating sludge that is difficult to dewater,
It is possible to efficiently wash filtered and dehydrated media such as sponges with simple operations and regenerate them in a short time. It is possible to efficiently wash and regenerate media that cannot be washed and regenerated using conventional methods, such as media that have become clogged by dewatering organic sludge, especially organic sludge to which an organic polymer flocculant has been added. Moreover, the waste liquid produced by washing can be treated by an activated sludge treatment method or the like by simply neutralizing it, and no special treatment equipment is required.

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

図面は実施例に使用した脱水装置の正面図であ
り、1a,1bは布ベルト、2a,2bは給泥
装置、3a,3bは浸出水流下手段、5a,5
b,5cはスポンジロール、9a,9b……9e
は圧搾ロール、20は薬液タンクである。
The drawing is a front view of the dewatering device used in the example, in which 1a and 1b are cloth belts, 2a and 2b are mud supply devices, 3a and 3b are leachate flow means, and 5a and 5
b, 5c are sponge rolls, 9a, 9b...9e
2 is a pressing roll, and 20 is a chemical solution tank.

Claims (1)

【特許請求の範囲】 1 有機質汚泥を過または脱水する布または
スポンジからなる過、脱水媒体を化学洗浄して
再生する方法において、過酸化物およびアルカリ
を含む洗浄液を前記媒体に接触させて洗浄するこ
とを特徴とする過、脱水媒体の洗浄方法。 2 過酸化物は過酸化水素である特許請求の範囲
第1項記載の過、脱水媒体の洗浄方法。 3 アルカリは水酸化ナトリウムである特許請求
の範囲第1項または第2項記載の過、脱水媒体
の洗浄方法。 4 洗浄液は過酸化水素0.5〜3%および水酸化
ナトリウム2〜8%を含む水溶液である特許請求
の範囲第1項記載の過、脱水媒体の洗浄方法。 5 洗浄液を循環する特許請求の範囲第1項ない
し第4項のいずれかに記載の過、脱水媒体の洗
浄方法。
[Claims] 1. A method for chemically cleaning and regenerating a filtration/dehydration medium made of cloth or sponge for filtration or dewatering of organic sludge, in which the medium is brought into contact with a cleaning solution containing peroxide and an alkali for cleaning. A method for cleaning a super-dehydrated medium, characterized by: 2. The method for cleaning a perhydration and dehydration medium according to claim 1, wherein the peroxide is hydrogen peroxide. 3. The method for cleaning a percolation/dehydration medium according to claim 1 or 2, wherein the alkali is sodium hydroxide. 4. The method for cleaning a percolation and dehydration medium according to claim 1, wherein the cleaning liquid is an aqueous solution containing 0.5 to 3% hydrogen peroxide and 2 to 8% sodium hydroxide. 5. A method for cleaning a filtration and dehydration medium according to any one of claims 1 to 4, in which a cleaning liquid is circulated.
JP4780578A 1978-04-24 1978-04-24 Washing of filtration and dehydrating mediums Granted JPS54140267A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4780578A JPS54140267A (en) 1978-04-24 1978-04-24 Washing of filtration and dehydrating mediums

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4780578A JPS54140267A (en) 1978-04-24 1978-04-24 Washing of filtration and dehydrating mediums

Publications (2)

Publication Number Publication Date
JPS54140267A JPS54140267A (en) 1979-10-31
JPS6147640B2 true JPS6147640B2 (en) 1986-10-20

Family

ID=12785575

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4780578A Granted JPS54140267A (en) 1978-04-24 1978-04-24 Washing of filtration and dehydrating mediums

Country Status (1)

Country Link
JP (1) JPS54140267A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01283146A (en) * 1988-05-11 1989-11-14 Sapitsuku:Kk Transfer printing apparatus
JPH01288446A (en) * 1988-05-16 1989-11-20 Nippon Denso Co Ltd Pad print wiper
JPH01291831A (en) * 1988-05-20 1989-11-24 Mitsubishi Electric Corp Positioning device

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5663233A (en) * 1979-10-29 1981-05-29 Mitsubishi Motors Corp Method and device for engine test
JPS5745317A (en) * 1980-09-03 1982-03-15 Tsukishima Kikai Co Ltd Washing method for filter cloth of dehydrator
JPH07155518A (en) * 1993-12-08 1995-06-20 Sanshin Seisakusho:Kk Filtering and refining method of suspension liquid
JPH07155515A (en) * 1993-12-08 1995-06-20 Sanshin Seisakusho:Kk Regenerating method of filter material
JP5164763B2 (en) * 2008-09-22 2013-03-21 株式会社クボタ Belt type concentrator and belt cleaning method for belt type concentrator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01283146A (en) * 1988-05-11 1989-11-14 Sapitsuku:Kk Transfer printing apparatus
JPH01288446A (en) * 1988-05-16 1989-11-20 Nippon Denso Co Ltd Pad print wiper
JPH01291831A (en) * 1988-05-20 1989-11-24 Mitsubishi Electric Corp Positioning device

Also Published As

Publication number Publication date
JPS54140267A (en) 1979-10-31

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