JPS6157080B2 - - Google Patents

Info

Publication number
JPS6157080B2
JPS6157080B2 JP6861579A JP6861579A JPS6157080B2 JP S6157080 B2 JPS6157080 B2 JP S6157080B2 JP 6861579 A JP6861579 A JP 6861579A JP 6861579 A JP6861579 A JP 6861579A JP S6157080 B2 JPS6157080 B2 JP S6157080B2
Authority
JP
Japan
Prior art keywords
sludge
freeze
water
thaw
equipment
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
JP6861579A
Other languages
Japanese (ja)
Other versions
JPS55157397A (en
Inventor
Koichi Horiuchi
Yoshitaka Kaai
Hisao Tanaka
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.)
Mitsubishi Electric Corp
Original Assignee
Mitsubishi Electric Corp
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 Mitsubishi Electric Corp filed Critical Mitsubishi Electric Corp
Priority to JP6861579A priority Critical patent/JPS55157397A/en
Publication of JPS55157397A publication Critical patent/JPS55157397A/en
Publication of JPS6157080B2 publication Critical patent/JPS6157080B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 この発明は、凍結融解式スラツジ処理装置のう
ち、特に無薬注スラツジ処理装置に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a freeze-thaw sludge treatment apparatus, and particularly to a chemical-free sludge treatment apparatus.

第1図は従来のこの種スラツジ処理装置を示す
もので、1は水処理装置(図示せず)から排出さ
れた有機性スラツジと、薬注装置5から注入され
たたとえば塩化第2鉄等の凝集剤を混合させる混
合器、2は上記凝集剤の注入によつて上澄液と90
%以上の水分を有するスラツジとに分離する前濃
縮装置、3はこの前濃縮装置2から供給されたス
ラツジを凍結后、これを融解して脱水性の良好な
固形分と水分とに分離するための凍結融解装置、
4はこの凍結融解装置3によつて改質されたスラ
ツジを脱水して、脱水ケーキと過液とに分離す
る遠水分離式、または真空引き式の脱水装置で、
この脱水装置4において生成された脱水ケーキ
は、焼却されるか、または埋立、あるいはコンポ
ステイング等に使用されることはいうまでもな
い。
FIG. 1 shows a conventional sludge treatment device of this type, in which organic sludge 1 is discharged from a water treatment device (not shown) and organic sludge, such as ferric chloride, is injected from a chemical injection device 5. Mixer 2 mixes the flocculant with the supernatant liquid by injecting the flocculant.
A pre-concentration device 3 separates the sludge from the sludge having a moisture content of 2.0% or more, and 3 freezes the sludge supplied from the pre-concentration device 2, then thaws it to separate it into solids and water with good dewaterability. freeze-thaw equipment,
4 is a centrifugal separation-type or vacuum-type dehydration device that dehydrates the sludge modified by the freeze-thaw device 3 and separates it into a dehydrated cake and a filtrate;
It goes without saying that the dehydrated cake produced in this dehydrator 4 is incinerated, landfilled, or used for composting or the like.

従来の凍結融解式スラツジ処理装置は上述した
ように、水処理装置から排出された有機性スラツ
ジに対し、これを固形分と水分とに分離し易くす
るために、どうしても塩化第2鉄等の凝集剤、す
なわち薬品を注入しなければ満足な脱水操作がで
きず、したがつて、スラツジ処理過程によつて生
成された脱水ケーキ、および過液中には必然的
に前記凝集剤中の不純物による重金属汚染が問題
となつている。
As mentioned above, conventional freeze-thaw sludge treatment equipment inevitably uses agglomeration of ferric chloride, etc. to make it easier to separate the organic sludge discharged from the water treatment equipment into solids and water. A satisfactory dewatering operation cannot be achieved without injecting a chemical agent, and therefore, the dehydrated cake produced during the sludge treatment process and the effluent inevitably contain heavy metals due to impurities in the flocculant. Pollution is a problem.

そこで、上記問題点を解決するには、被処理ス
ラツジのPHがさがると、凍結再融解処理スラツジ
の脱水性が著しく改善される点に着目して、スラ
ツジを直接脱イオン処理してスラツジのPHを直接
低下させた後、凍結再融解処理する装置が考えら
れる。しかし、この装置ではスラツジによる脱イ
オン装置の目づまりがひんぱんに生じる。これら
の汚染、目づまりは適当な脱イオン装置の洗浄法
を用いることでさけられるが、洗浄の操作が必要
であることにかわりはなく、装置の操作が煩雑に
なると言う問題点がある。
Therefore, in order to solve the above problems, we focused on the fact that the dewatering performance of freeze-re-thawed sludge is significantly improved when the pH of the sludge to be treated decreases, and by directly deionizing the sludge, the PH of the sludge is A device that directly lowers the temperature and then freezes and re-thaws it is considered. However, in this device, the deionization device is frequently clogged with sludge. Although these contaminations and clogging can be avoided by using a suitable cleaning method for the deionization equipment, there is still a problem that cleaning operations are necessary and the equipment operation becomes complicated.

この発明は、かかる点に着目してなされたもの
で、同じ水処理施設から外部に放流される水の一
部を、陽イオンのみ「H+」イオンに変換して作
つた酸性水をスラツジに添加することにより、従
来のように、凝集剤、すなわち塩化第2鉄等の薬
品を使用しなくても、この凝集剤を使用した場合
と同一程度のスラツジの脱水効果をあげることが
できる無薬注スラツジ処理装置を提供しようとす
るものである。
This invention was made by focusing on this point, and uses acidic water made by converting only the cations into "H + " ions from a portion of the water discharged outside from the same water treatment facility to sludge. By adding a drug-free product, it is possible to achieve the same level of sludge dehydration effect as when using a flocculant, without using conventional flocculants, i.e., chemicals such as ferric chloride. The present invention aims to provide a sludge processing device.

すなわち、第2図はこの発明の一実施例を示す
もので、21は下水等の処理すべき汚水が流入す
る水処理装置、22はこの水処理装置21から放
流された放流水の一部を分割する分割器、23は
この分割された放流水から陽イオンのみを交換
し、水素イオンが増加した酸性水に変換する陽イ
オン交換樹脂充填塔、24は上記水処理装置21
から排出されたスラツジと、上記陽イオン交換樹
脂充填塔23から供給された酸性水とを混合させ
る混合器、3はこの混合器24から供給されたス
ラツジを凍結后、これを融解して脱水性の良好な
固形分と水分とに分離するための凍結融解装置、
4はこの凍結融解装置3によつて改質されたスラ
ツジを脱水して脱水ケーキと、過液とに分離す
る遠心分離式、または真空引き式の脱水装置であ
る。なお第2図において、Aは水処理システム、
Bはスラツジ処理システムを示すものである。
That is, FIG. 2 shows an embodiment of the present invention, in which 21 is a water treatment device into which wastewater to be treated such as sewage flows, and 22 is a part of the water discharged from this water treatment device 21. 23 is a cation-exchange resin packed tower that exchanges only cations from the divided discharged water and converts it into acidic water with increased hydrogen ions; 24 is the water treatment device 21;
A mixer 3 mixes the sludge discharged from the cation exchange resin packed tower 23 with the acidic water supplied from the cation exchange resin packed tower 23, and a mixer 3 freezes the sludge supplied from the mixer 24, then thaws it to dewater it. freeze-thaw equipment for good separation of solids and moisture;
Reference numeral 4 denotes a centrifugal or vacuum type dewatering device that dehydrates the sludge modified by the freeze-thaw device 3 and separates it into a dehydrated cake and a filtrate. In Figure 2, A is the water treatment system,
B shows a sludge treatment system.

この発明の凍結融解式スラツジ処理装置は上記
のように構成されているので、水処理装置21に
よつてスラツジと分離された放流水の一部は、分
割器22を経て陽イオン交換樹脂充填塔23に送
り込まれる。この陽イオン交換樹脂充填塔23に
送り込まれた放流水は、その比電気伝導度K(μ
/cm)が5000前後あるため、この陽イオン交換
樹脂充填塔23を通過させることによつてその水
素イオン濃度の絶対量を上げることができ、PH値
を下げた酸性水にすることができるものである。
そして、この陽イオン交換樹脂充填塔23から放
出された酸性水と、水処理装置21から排出され
たスラツジとを混合器24において混合すると、
スラツジ側のPH値が下がつてスラツジ中のタンパ
ク質等が凝集する。これは褐変反応として間接的
に観察されるもので、このときのスラツジのPH値
は、第3図に示すように「PH4」付近が小量の酸
で最大の効果をあげる点であることがわかる。こ
のように、混合されたスラツジは次段の凍結融解
装置3において改質されたのち、脱水装置4にお
いて脱水ケーキとなるわけである。
Since the freeze-thaw sludge treatment apparatus of the present invention is constructed as described above, a part of the discharged water separated from the sludge by the water treatment apparatus 21 is passed through the divider 22 to the cation exchange resin packed column. Sent to 23. The discharged water sent into this cation exchange resin packed tower 23 has a specific electrical conductivity K (μ
/cm) is around 5,000, so by passing it through this cation exchange resin packed tower 23, the absolute amount of hydrogen ion concentration can be increased, making it possible to make acidic water with a lower PH value. It is.
Then, when the acidic water discharged from the cation exchange resin packed tower 23 and the sludge discharged from the water treatment device 21 are mixed in the mixer 24,
The pH value on the sludge side decreases and proteins in the sludge aggregate. This is indirectly observed as a browning reaction, and the pH value of the sludge at this time is around PH4, which is the point where a small amount of acid has the greatest effect, as shown in Figure 3. Recognize. In this way, the mixed sludge is reformed in the next freeze-thaw device 3, and then turned into a dehydrated cake in the dewatering device 4.

なお、上述した一実施例(第2図)において
は、処理すべきスラツジが下水の場合について述
べたが、この下水のほかに、し尿処理スラツジ、
または浄化槽スラツジ等の有機性スラツジ等の処
理にも適用し得ることはもちろん、上記混合器2
4の前段または後段に濃縮装置を挿入してもよ
い。
In the above embodiment (Fig. 2), the sludge to be treated is sewage, but in addition to this sewage, human waste treated sludge,
The above mixer 2 can also be applied to the treatment of organic sludge such as septic tank sludge.
A concentrator may be inserted before or after step 4.

以上述べたように、この発明によれば、水処理
装置と、スラツジ処理装置とを有機的に結合し、
従来のように、スラツジの凝集剤である危険な薬
品を用いなくても、スラツジの脱水効果を充分に
発揮させることができ、薬品を含まず、しかも含
水率の低い脱水ケーキを得ることができる効果を
有するものである。
As described above, according to the present invention, the water treatment device and the sludge treatment device are organically combined,
The sludge dehydration effect can be fully demonstrated without using dangerous chemicals that are coagulants for sludge as in the past, and a dehydrated cake that does not contain chemicals and has a low moisture content can be obtained. It is effective.

また、スラツジに添加する酸性水は、SS(懸
濁)成分がずつと少ない水処理装置からの放流水
を原料として用いるので、陽イオン交換樹脂充填
塔内でのSS成分による目づまりが少なく、実用
上は洗浄操作が不必要であると言う効果を有す
る。
In addition, the acidic water added to the sludge uses discharged water from a water treatment equipment with very little SS (suspended) components as a raw material, so there is less clogging caused by SS components in the cation exchange resin packed column, making it practical for practical use. The above has the advantage that cleaning operations are unnecessary.

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

第1図は従来の凍結融解式スラツジ処理装置を
示す配管図、第2図はこの発明の一実施例を示す
配管図、第3図はスラツジの処理効果特性図であ
る。 図面中、3は凍結融解装置、4は脱水装置、2
1は水処理装置、22は分割器、23は陽イオン
交換樹脂充填塔である。なお、図中同一符号は同
一または相当部分を示す。
FIG. 1 is a piping diagram showing a conventional freeze-thaw sludge processing apparatus, FIG. 2 is a piping diagram showing an embodiment of the present invention, and FIG. 3 is a characteristic diagram of sludge treatment effects. In the drawing, 3 is a freeze-thaw device, 4 is a dehydration device, 2
1 is a water treatment device, 22 is a divider, and 23 is a cation exchange resin packed column. Note that the same reference numerals in the figures indicate the same or corresponding parts.

Claims (1)

【特許請求の範囲】[Claims] 1 後段に脱水装置を有する凍結融解処理装置の
前段に、水処理装置によりスラツジと分離された
放流水の一部を陽イオン交換樹脂充填塔において
陽イオンのみイオン交換して得られた水素イオン
が増加した酸性水と上記水処理装置から排出され
たスラツジとを混合させることによつて、上記ス
ラツジのPHを所定値以下に低下させたのち、上記
凍結融解処理装置に供給する混合器を備えたこと
を特徴とする凍結融解式スラツジ処理装置。
1. Hydrogen ions obtained by ion-exchanging only the cations of a portion of the effluent water separated from the sludge by the water treatment equipment in a cation-exchange resin packed column are placed in the front stage of the freeze-thaw treatment equipment that has a dehydration equipment in the latter stage. A mixer is provided that lowers the pH of the sludge to a predetermined value or less by mixing the increased acidic water with the sludge discharged from the water treatment equipment, and then supplies the sludge to the freeze-thaw treatment equipment. Freeze-thaw sludge processing equipment characterized by:
JP6861579A 1979-05-29 1979-05-29 Freeze-melt type sludge treatment unit Granted JPS55157397A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6861579A JPS55157397A (en) 1979-05-29 1979-05-29 Freeze-melt type sludge treatment unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6861579A JPS55157397A (en) 1979-05-29 1979-05-29 Freeze-melt type sludge treatment unit

Publications (2)

Publication Number Publication Date
JPS55157397A JPS55157397A (en) 1980-12-08
JPS6157080B2 true JPS6157080B2 (en) 1986-12-05

Family

ID=13378833

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6861579A Granted JPS55157397A (en) 1979-05-29 1979-05-29 Freeze-melt type sludge treatment unit

Country Status (1)

Country Link
JP (1) JPS55157397A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2244488B1 (en) 2008-02-14 2015-07-29 Panasonic Intellectual Property Management Co., Ltd. Speaker and electronic device

Also Published As

Publication number Publication date
JPS55157397A (en) 1980-12-08

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