JPH07299500A - Production of inorganic flocculant-mixed sludge and device therefor - Google Patents
Production of inorganic flocculant-mixed sludge and device thereforInfo
- Publication number
- JPH07299500A JPH07299500A JP7045508A JP4550895A JPH07299500A JP H07299500 A JPH07299500 A JP H07299500A JP 7045508 A JP7045508 A JP 7045508A JP 4550895 A JP4550895 A JP 4550895A JP H07299500 A JPH07299500 A JP H07299500A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- inorganic coagulant
- mixed
- powder
- inorganic
- 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)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、下水処理場において使
用される無機凝集剤混合汚泥の製造方法及び装置に関す
るものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and a device for producing an inorganic coagulant-mixed sludge used in a sewage treatment plant.
【0002】[0002]
【従来の技術】下水処理場においては、下水汚泥に消石
灰や生石灰等の無機凝集剤を混合したうえで脱水機に送
り、脱水処理を行っている。このような無機凝集剤は予
め水で溶解しておき、混合槽に導いて汚泥と混合するの
が普通であった。ところがこのような従来技術には、次
のような問題点があった。2. Description of the Related Art At a sewage treatment plant, sewage sludge is mixed with an inorganic coagulant such as slaked lime or quick lime and then sent to a dehydrator for dehydration treatment. It was usual that such an inorganic coagulant was dissolved in water in advance and introduced into a mixing tank to be mixed with sludge. However, such a conventional technique has the following problems.
【0003】第1に、無機凝集剤を溶解するために大量
の水が必要となる。第2に、水に溶解させた無機凝集剤
は常時攪拌していないと沈降し易く、注入する濃度にバ
ラツキが生ずる。第3に、溶解水の分だけ脱水機の負担
が増し、汚泥の呑み込み量が減少する。第4に、溶解水
の分だけ混合槽の容積が大きくなる。第5に、配管内に
無機凝集剤が沈着し易く、配管が閉塞し易い。First, a large amount of water is required to dissolve the inorganic coagulant. Secondly, if the inorganic coagulant dissolved in water is not constantly stirred, it tends to settle, and the injected concentration varies. Thirdly, the load on the dehydrator is increased by the amount of dissolved water, and the swallowing amount of sludge is reduced. Fourth, the volume of the mixing tank increases by the amount of the dissolved water. Fifth, the inorganic coagulant is easily deposited in the pipe, and the pipe is easily blocked.
【0004】[0004]
【発明が解決しようとする課題】本発明は上記した従来
の問題点を解決し、無機凝集剤を溶解するための溶解水
をなくし、従来よりも容易にかつ経済的に無機凝集剤混
合汚泥を得ることができる方法と装置とを提供するため
になされたものである。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems of the prior art, eliminates the dissolved water for dissolving the inorganic coagulant, and makes it easier and more economical to prepare an inorganic coagulant-mixed sludge. This is done to provide a method and apparatus that can be obtained.
【0005】[0005]
【課題を解決するための手段】上記の課題を解決するた
めになされた本発明の無機凝集剤混合汚泥の製造方法
は、無機凝集剤の粉末をエゼクター式またはラインミキ
シング式の混合器の中心部より供給するとともに、その
周囲から流動性のある汚泥を供給して両者を直接混合す
ることを主たる特徴とするものである。また本発明の無
機凝集剤混合汚泥の製造装置は、無機凝集剤粉末の貯槽
と、汚泥貯槽と、無機凝集剤粉末の貯槽から導かれた無
機凝集剤の粉末を中心部より供給するとともに汚泥貯槽
から導かれた流動性のある汚泥をその周囲から供給して
両者を直接混合するエゼクター式またはラインミキシン
グ式の混合器とからなることを特徴とするものである。Means for Solving the Problems The method for producing an inorganic coagulant-mixed sludge of the present invention, which has been made to solve the above-mentioned problems, comprises the steps of mixing an inorganic coagulant powder with an ejector-type or line-mixing-type mixer at the center. The main feature is to supply the sludge with a fluidity from the surroundings and directly mix the both. Further, the apparatus for producing a mixed sludge of inorganic coagulant according to the present invention comprises a storage tank for the inorganic coagulant powder, a sludge storage tank, and a sludge storage tank for supplying the powder of the inorganic coagulant derived from the storage tank for the inorganic coagulant powder and the sludge storage tank. It is characterized by comprising an ejector type or line mixing type mixer which directly supplies the sludge having fluidity derived from the above from its surroundings.
【0006】[0006]
【作用】本発明によれば、消石灰や生石灰等の無機凝集
剤の粉末を溶解水を用いることなく汚泥と直接混合する
ことができるので、溶解水が不要となる経済的効果は大
きく、あわせて脱水機の負担も軽減される。また無機凝
集剤の粉末を汚泥と直接混合するので、配管等の内部に
おける無機凝集剤の沈降がなく、配管が閉塞するおそれ
がない。しかも無機凝集剤の混合比率を容易に調整する
ことができるので、脱水機の安定した運転が可能とな
る。According to the present invention, the powder of the inorganic coagulant such as slaked lime or quick lime can be directly mixed with the sludge without using the dissolving water, so that the dissolving water becomes unnecessary and the economical effect is large. The load on the dehydrator is also reduced. In addition, since the powder of the inorganic coagulant is directly mixed with the sludge, the inorganic coagulant does not settle inside the pipe or the like, and the pipe is not clogged. Moreover, since the mixing ratio of the inorganic coagulant can be easily adjusted, the dehydrator can be stably operated.
【0007】[0007]
【実施例】以下に本発明を図示の実施例によって更に詳
細に説明する。図1、図2は本発明の第1の実施例を示
すものであり、1は無機凝集剤粉末の貯槽、2は汚泥貯
槽、3は混合器、4は汚泥調整槽、5はフィルタープレ
ス等の脱水機である。無機凝集剤粉末の貯槽1には、消
石灰や生石灰等の無機凝集剤の粉末が収納されており、
汚泥貯槽2には水分が例えば93〜98%程度の流動性のあ
る汚泥が収納されている。The present invention will be described below in more detail with reference to the illustrated embodiments. 1 and 2 show a first embodiment of the present invention, wherein 1 is a storage tank for inorganic coagulant powder, 2 is a sludge storage tank, 3 is a mixer, 4 is a sludge adjusting tank, 5 is a filter press, etc. It is a dehydrator. Inorganic coagulant powder storage tank 1 stores inorganic coagulant powder such as slaked lime and quicklime.
The sludge storage tank 2 stores fluid sludge having a water content of, for example, about 93 to 98%.
【0008】第1の実施例では、混合器3としてエゼク
ター式の混合器3が使用されている。この混合器3は図
2に示すように、角αが30〜60°、好ましくは40〜50°
のテーパ状の本体3aの中心に粉末供給ノズル3bを設け、
またその周囲に複数本の汚泥供給ノズル3cを設けたもの
である。ここで角αの角度は、管内付着やつまりが起こ
りにくいように選択されたものである。In the first embodiment, the ejector type mixer 3 is used as the mixer 3. This mixer 3 has an angle α of 30 to 60 °, preferably 40 to 50 °, as shown in FIG.
The powder supply nozzle 3b is provided at the center of the tapered main body 3a of
Further, a plurality of sludge supply nozzles 3c are provided around it. Here, the angle α is selected so that adhesion or clogging in the tube is unlikely to occur.
【0009】そこで汚泥貯槽2から流動性のある汚泥を
混合器3の汚泥供給ノズル3cに導き、これと同時に無機
凝集剤粉末の貯槽1から無機凝集剤の粉末を粉末供給ノ
ズル3bに導いて本体3aの内部に噴出させる。すると無機
凝集剤の粉末は汚泥供給ノズル3cから噴出される汚泥中
に取り込まれて攪拌され、両者は直接均一に混合され
る。なお、汚泥の供給量は汚泥濃度計13および汚泥流
量計14の信号に基づいて、汚泥供給ポンプ15の回転
数制御や流量制御弁6によりコントロールする。また、
無機凝集剤の粉末の供給量はロータリーバルブや定量供
給器7によりコントロールする。このようにして、溶解
水を使用せずに汚泥と無機凝集剤の粉末とが直接混合さ
れた無機凝集剤混合汚泥が製造される。Then, the sludge having fluidity is guided from the sludge storage tank 2 to the sludge supply nozzle 3c of the mixer 3, and at the same time, the inorganic coagulant powder is guided from the storage tank 1 of the inorganic coagulant powder to the powder supply nozzle 3b. Eject inside 3a. Then, the powder of the inorganic coagulant is taken into the sludge ejected from the sludge supply nozzle 3c and stirred, and both are directly and uniformly mixed. The sludge supply amount is controlled by the rotation speed control of the sludge supply pump 15 and the flow control valve 6 based on the signals from the sludge concentration meter 13 and the sludge flow meter 14. Also,
The amount of the inorganic flocculant powder supplied is controlled by a rotary valve or a constant quantity feeder 7. In this way, an inorganic coagulant-mixed sludge in which the sludge and the powder of the inorganic coagulant are directly mixed is produced without using dissolved water.
【0010】図1の実施例では、混合器3は前後2段に
設置されており、前段の混合器3によって製造された無
機凝集剤混合汚泥に対して更に後段の混合器3で汚泥が
混合されている。このように汚泥を段階的に添加して目
的とする濃度の無機凝集剤混合汚泥を製造することもで
きる。またこれとは逆に、前段の混合器3によって製造
された無機凝集剤混合汚泥を後段の混合器3に導き、更
に無機凝集剤の粉末と混合する方法を取ることもでき
る。In the embodiment shown in FIG. 1, the mixer 3 is installed in two stages before and after, and the sludge is mixed with the inorganic coagulant-mixed sludge produced by the mixer 3 in the front stage in the mixer 3 in the rear stage. Has been done. Thus, sludge can be added stepwise to produce an inorganic flocculant-mixed sludge having a desired concentration. On the contrary, a method of introducing the inorganic coagulant mixed sludge produced by the former mixer 3 to the latter mixer 3 and further mixing it with the powder of the inorganic coagulant may be adopted.
【0011】図1の実施例では、このようにして得られ
た無機凝集剤混合汚泥を攪拌機8を備えた汚泥調整槽4
に貯留し、汚泥供給管9を介して更に汚泥を添加して濃
度調整を行ったうえでポンプ10により脱水機5へ送って
いる。このように汚泥調整槽4で最終的な濃度調整を行
う場合には、混合器3によって製造される無機凝集剤混
合汚泥の凝集剤濃度を目的とする濃度よりも高くしてお
くが、このような操作を行わずに混合器3から直接に脱
水機5へ送ることもできる。In the embodiment shown in FIG. 1, the sludge adjusting tank 4 equipped with a stirrer 8 mixes the inorganic coagulant-mixed sludge thus obtained.
The sludge is further stored in the tank, the sludge is further added through the sludge supply pipe 9 to adjust the concentration, and then the sludge is sent to the dehydrator 5 by the pump 10. When the final concentration adjustment is performed in the sludge adjusting tank 4 in this way, the flocculant concentration of the inorganic flocculant-mixed sludge produced by the mixer 3 is set higher than the target concentration. It is also possible to send directly from the mixer 3 to the dehydrator 5 without performing any operation.
【0012】脱水機5では、適正量の無機凝集剤が混合
された無機凝集剤混合汚泥が脱水される。なお、脱水機
5には得られた脱水汚泥の水分測定器11や脱水泥量測定
器12を設けておき、これらの計器による脱水状況をフィ
ードバックして無機凝集剤の混合量をコントロールする
ことが好ましい。一般的には無機凝集剤たとえば消石灰
の添加量は汚泥中の固形分の20〜40%であるから、汚泥
の水分が95%の場合には、汚泥中の固形分は5%とな
り、その20〜40%は1〜2%となる。このため、無機凝
集剤混合汚泥の量は添加前の汚泥を100 %とすると101
〜102%となる。In the dehydrator 5, the inorganic coagulant-mixed sludge mixed with an appropriate amount of inorganic coagulant is dehydrated. It should be noted that the dehydrator 5 is provided with a moisture measuring device 11 and a dehydrating sludge amount measuring device 12 for the obtained dehydrated sludge, and it is possible to control the mixing amount of the inorganic coagulant by feeding back the dehydration condition by these instruments. preferable. Generally, the amount of inorganic coagulant added, such as slaked lime, is 20 to 40% of the solid content in the sludge, so when the water content of the sludge is 95%, the solid content in the sludge becomes 5%. -40% is 1-2%. Therefore, the amount of sludge mixed with inorganic coagulant is 101% if the sludge before addition is 100%.
It will be ~ 102%.
【0013】図3、図4は本発明の第2の実施例を示す
ものであり、ここではラインミキシング式の混合器3が
使用されている。この混合器3は図4に示すように上部
に粉末供給ノズル3bを備えた本体3aの内部に汚泥の流れ
方向に沿って螺旋羽根3dを設けるとともに、本体3aの側
面に汚泥供給ノズル3cを螺旋羽根3dと同様に傾斜させて
設けたものである。この螺旋羽根3dの傾斜角度βは30〜
60°が好ましく、さらに好ましくは40〜50°とする。FIGS. 3 and 4 show a second embodiment of the present invention, in which a line mixing type mixer 3 is used. As shown in FIG. 4, this mixer 3 is provided with a spiral blade 3d along a sludge flow direction inside a main body 3a having a powder supply nozzle 3b on the upper part, and a sludge supply nozzle 3c is spirally provided on a side surface of the main body 3a. Like the blade 3d, the blade 3d is inclined. The inclination angle β of this spiral blade 3d is 30-
It is preferably 60 °, more preferably 40 to 50 °.
【0014】また図5、図6はラインミキシング式の混
合器3を使用する第3の実施例である。ここでは混合器
3として、逆円錐状のスパイラル型混合器であって、30
〜45°の開き角度γおよび10〜30°の流れ角度δを持つ
ものが使用されている。流れ角度δは15〜20°とするこ
とがより好ましい。FIGS. 5 and 6 show a third embodiment in which the line mixing type mixer 3 is used. Here, the mixer 3 is an inverted conical spiral type mixer.
Those with an opening angle γ of ~ 45 ° and a flow angle δ of 10-30 ° are used. The flow angle δ is more preferably 15-20 °.
【0015】上記した第2、第3の実施例でも、汚泥貯
槽2から供給された流動性のある汚泥は汚泥供給ノズル
3cから噴出され、また無機凝集剤粉末の貯槽1から供給
された無機凝集剤粉末は粉末供給ノズル3bから噴出され
て両者は本体3aの内部で直接均一に混合される。なおそ
の他の構成は実施例1と同様である。Also in the above second and third embodiments, the sludge having fluidity supplied from the sludge storage tank 2 is sludge supply nozzle.
The inorganic coagulant powder ejected from 3c and supplied from the tank 1 of the inorganic coagulant powder is ejected from the powder supply nozzle 3b, and both are directly and uniformly mixed inside the main body 3a. The other configurations are similar to those of the first embodiment.
【0016】[0016]
【発明の効果】以上に説明したように、本発明の無機凝
集剤混合汚泥の製造方法及び装置によれば、消石灰や生
石灰等の無機凝集剤の粉末を溶解水を用いることなく汚
泥と直接混合できるので溶解水が不要となり、水道代金
を節減できる経済的効果は非常に大きい。また脱水機の
負担も軽減され、汚泥の呑み込み量の増加を図ることが
できる。また配管等の内部における無機凝集剤の沈降が
なく、配管が閉塞するおそれもない。更に請求項2〜4
の方法を採用すれば、無機凝集剤濃度をより正確にコン
トロールすることが可能となる。As described above, according to the method and apparatus for producing an inorganic coagulant-mixed sludge of the present invention, the powder of the inorganic coagulant such as slaked lime or quick lime is directly mixed with the sludge without using dissolved water. Because it can be done, no dissolved water is needed, and the economic effect of saving the water bill is very large. Further, the load on the dehydrator is reduced, and the amount of sludge swallowed can be increased. In addition, there is no sedimentation of the inorganic coagulant inside the pipe or the like, and there is no risk of the pipe being blocked. Furthermore, claims 2 to 4
By adopting the above method, the concentration of the inorganic coagulant can be controlled more accurately.
【図1】本発明の第1の実施例を示すフローシートであ
る。FIG. 1 is a flow sheet showing a first embodiment of the present invention.
【図2】第1の実施例のエゼクター式の混合器を示す断
面図である。FIG. 2 is a sectional view showing an ejector type mixer of the first embodiment.
【図3】本発明の第2、第3の実施例を示すフローシー
トである。FIG. 3 is a flow sheet showing second and third embodiments of the present invention.
【図4】第2の実施例のラインミキシング式の混合器を
示す断面図である。FIG. 4 is a sectional view showing a line mixing type mixer according to a second embodiment.
【図5】第3の実施例のラインミキシング式の混合器を
示す斜視図である。FIG. 5 is a perspective view showing a line mixing type mixer according to a third embodiment.
【図6】第3の実施例のラインミキシング式の混合器の
幾何学形状を示す線図である。FIG. 6 is a diagram showing the geometrical shape of a line mixing mixer according to a third embodiment.
1 無機凝集剤粉末の貯槽、2 汚泥貯槽、3 混合
器、3a 混合器の本体、3b 粉末供給ノズル、3c 汚泥
供給ノズル、3d 螺旋羽根、4 汚泥調整槽、5脱水
機、6 流量制御弁、7 定量供給器、8 攪拌機、9
汚泥供給管、10ポンプ、11 水分測定器、12 脱水汚
泥量測定器、13 汚泥濃度計、 14 汚泥流量計、15
汚泥供給ポンプ1 inorganic flocculant powder storage tank, 2 sludge storage tank, 3 mixer, 3a mixer body, 3b powder supply nozzle, 3c sludge supply nozzle, 3d spiral blade, 4 sludge adjusting tank, 5 dehydrator, 6 flow control valve, 7 fixed quantity feeder, 8 stirrer, 9
Sludge supply pipe, 10 pumps, 11 Moisture measuring instrument, 12 Dewatered sludge amount measuring instrument, 13 Sludge concentration meter, 14 Sludge flow meter, 15
Sludge supply pump
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01F 5/04 C02F 11/00 ZAB A ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display location B01F 5/04 C02F 11/00 ZAB A
Claims (5)
ラインミキシング式の混合器の中心部より供給するとと
もに、その周囲から流動性のある汚泥を供給して両者を
直接混合することを特徴とする無機凝集剤混合汚泥の製
造方法。1. An inorganic coagulant powder is supplied from the central part of an ejector type or line mixing type mixer, and fluid sludge is supplied from the periphery thereof to directly mix the two. Method for producing sludge mixed with inorganic coagulant.
集剤混合汚泥を後段のエゼクター式またはラインミキシ
ング式の混合器に導き、更に流動性のある汚泥と混合す
ることを特徴とする無機凝集剤混合汚泥の製造方法。2. An inorganic coagulation characterized in that the sludge mixed with an inorganic coagulant produced by the method of claim 1 is introduced into an ejector-type or line-mixing-type mixer in the subsequent stage and further mixed with a fluid sludge. Method for producing agent-mixed sludge.
集剤混合汚泥を後段のエゼクター式またはラインミキシ
ング式の混合器に導き、更に無機凝集剤の粉末と混合す
ることを特徴とする無機凝集剤混合汚泥の製造方法。3. Inorganic coagulation, wherein the inorganic coagulant-mixed sludge produced by the method of claim 1 is introduced into an ejector-type or line-mixing-type mixer in the subsequent stage and further mixed with the powder of the inorganic coagulant. Method for producing agent-mixed sludge.
高い無機凝集剤混合汚泥を製造して汚泥調整槽に貯留し
ておき、これに汚泥を混入して目的とする濃度の無機凝
集剤混合汚泥とすることを特徴とする無機凝集剤混合汚
泥の製造方法。4. An inorganic coagulant having a desired concentration by producing an inorganic coagulant-mixed sludge having a high inorganic coagulant concentration by the method of claim 1 and storing the sludge in a sludge adjusting tank and mixing the sludge with the sludge. A method for producing an inorganic coagulant-mixed sludge, which is a mixed sludge.
無機凝集剤粉末の貯槽から導かれた無機凝集剤の粉末を
中心部より供給するとともに汚泥貯槽から導かれた流動
性のある汚泥をその周囲から供給して両者を直接混合す
るエゼクター式またはラインミキシング式の混合器とか
らなることを特徴とする無機凝集剤混合汚泥の製造装
置。5. A storage tank for inorganic coagulant powder, and a sludge storage tank,
Inorganic coagulant powder that is introduced from the storage tank of the inorganic coagulant powder is supplied from the center and fluid sludge that is introduced from the sludge storage tank is supplied from the surrounding area to directly mix the two. An apparatus for producing an inorganic coagulant-mixed sludge, comprising:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP04550895A JP3145601B2 (en) | 1994-03-09 | 1995-03-06 | Method and apparatus for producing sludge mixed with inorganic coagulant |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP6-38117 | 1994-03-09 | ||
| JP3811794 | 1994-03-09 | ||
| JP04550895A JP3145601B2 (en) | 1994-03-09 | 1995-03-06 | Method and apparatus for producing sludge mixed with inorganic coagulant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH07299500A true JPH07299500A (en) | 1995-11-14 |
| JP3145601B2 JP3145601B2 (en) | 2001-03-12 |
Family
ID=26377307
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP04550895A Expired - Fee Related JP3145601B2 (en) | 1994-03-09 | 1995-03-06 | Method and apparatus for producing sludge mixed with inorganic coagulant |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3145601B2 (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003305307A (en) * | 2002-04-15 | 2003-10-28 | Ebara Corp | Table feeder and treatment system for wastewater, sludge and liquid waste equipped therewith |
| JP2004098048A (en) * | 2002-07-18 | 2004-04-02 | Shinwa Yosetsu:Kk | Purification apparatus |
| JP2005007250A (en) * | 2003-06-17 | 2005-01-13 | Fumiyoshi Yoshioka | Sludge treatment apparatus and sludge treatment method |
| JP2006167583A (en) * | 2004-12-15 | 2006-06-29 | Taiheiyo Cement Corp | Sludge treatment method, sludge treatment system, and sludge flocculant addition device |
| JP2007069167A (en) * | 2005-09-09 | 2007-03-22 | Kurita Water Ind Ltd | Emulsion polymer primary or secondary diluter |
| CN100374271C (en) * | 2005-12-16 | 2008-03-12 | 华南理工大学 | Application method of aluminum-containing inorganic salt as anti-slip agent for synthetic rubber dehydration screw extruder |
| JP2009000669A (en) * | 2007-06-19 | 2009-01-08 | Nippon Solid Co Ltd | Water mixing equipment |
| JP2011078904A (en) * | 2009-10-07 | 2011-04-21 | Masanori Aritomi | Polluted water treatment apparatus, and operation control method |
| JP2018043194A (en) * | 2016-09-14 | 2018-03-22 | 好史 大良 | Water treatment method and apparatus |
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| KR101234808B1 (en) | 2011-01-25 | 2013-02-19 | (주)으뜸산업 | Sewage treatment system |
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| JPS5239574A (en) * | 1975-09-20 | 1977-03-26 | Kloeckner Humboldt Deutz Ag | Manufacture of ecomonically useful and homogeneous powder mixture |
| JPS5784800A (en) * | 1980-11-14 | 1982-05-27 | Hitachi Kiden Kogyo Ltd | Addition of flocculant in treatment of sludge and apparatus therefor |
| JPS6087838A (en) * | 1983-10-17 | 1985-05-17 | Marusei Jukogyo Kk | Solid liquid mixing equipment |
| JPS6342799A (en) * | 1986-08-07 | 1988-02-23 | Nippon Steel Corp | Sludge treatment by fine coke powder |
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Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003305307A (en) * | 2002-04-15 | 2003-10-28 | Ebara Corp | Table feeder and treatment system for wastewater, sludge and liquid waste equipped therewith |
| JP2004098048A (en) * | 2002-07-18 | 2004-04-02 | Shinwa Yosetsu:Kk | Purification apparatus |
| JP2005007250A (en) * | 2003-06-17 | 2005-01-13 | Fumiyoshi Yoshioka | Sludge treatment apparatus and sludge treatment method |
| JP2006167583A (en) * | 2004-12-15 | 2006-06-29 | Taiheiyo Cement Corp | Sludge treatment method, sludge treatment system, and sludge flocculant addition device |
| JP2007069167A (en) * | 2005-09-09 | 2007-03-22 | Kurita Water Ind Ltd | Emulsion polymer primary or secondary diluter |
| CN100374271C (en) * | 2005-12-16 | 2008-03-12 | 华南理工大学 | Application method of aluminum-containing inorganic salt as anti-slip agent for synthetic rubber dehydration screw extruder |
| JP2009000669A (en) * | 2007-06-19 | 2009-01-08 | Nippon Solid Co Ltd | Water mixing equipment |
| JP2011078904A (en) * | 2009-10-07 | 2011-04-21 | Masanori Aritomi | Polluted water treatment apparatus, and operation control method |
| JP2018043194A (en) * | 2016-09-14 | 2018-03-22 | 好史 大良 | Water treatment method and apparatus |
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