JPS593239B2 - Method and equipment for adding flocculant in sludge treatment - Google Patents
Method and equipment for adding flocculant in sludge treatmentInfo
- Publication number
- JPS593239B2 JPS593239B2 JP55161140A JP16114080A JPS593239B2 JP S593239 B2 JPS593239 B2 JP S593239B2 JP 55161140 A JP55161140 A JP 55161140A JP 16114080 A JP16114080 A JP 16114080A JP S593239 B2 JPS593239 B2 JP S593239B2
- Authority
- JP
- Japan
- Prior art keywords
- flocculant
- sludge
- addition
- pipes
- sludge treatment
- 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
Links
- 239000010802 sludge Substances 0.000 title claims description 30
- 238000000034 method Methods 0.000 title claims description 4
- 238000003756 stirring Methods 0.000 claims description 8
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 239000012530 fluid Substances 0.000 claims 1
- 239000002245 particle Substances 0.000 description 2
- 238000013019 agitation Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/313—Injector mixers in conduits or tubes through which the main component flows wherein additional components are introduced in the centre of the conduit
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】
本発明は汚泥処理に於ける凝集剤添加方法及びその装置
に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for adding a flocculant in sludge treatment.
汚泥処理に際し、高含水率であるため、直接投5 棄等
を行うことができないので機械的もしくは化学機械的に
輸送その他投棄に耐える含水率まで脱水処理を行なつて
いる。When treating sludge, it cannot be directly dumped due to its high moisture content, so it is dehydrated mechanically or chemically mechanically to a moisture content that can withstand transportation or dumping.
汚泥の種別によつては直接機械的脱水が不可能な場合汚
泥に凝集剤を添加撹拌し汚泥粒子をフロック化せしめた
後機械式脱10水を行なつている。しかしこの凝集剤の
添加は凝集剤と汚泥とを混和槽へ供給し、攪拌機にて攪
拌して混合を行なつたり、凝集剤、汚泥を回転ドラムヘ
投入し該ドラムの回転にて攪拌混合したりしている。し
かしこの方法では凝集剤の攪拌に動力15を必要とする
と共に特定箇所に多量の凝集剤を注入するため部分的に
必要以上の凝集剤が汚泥粒子に作用し、高分子凝集剤の
架橋作用が不充分になることがある。本発明はこれに鑑
みて凝集剤添加攪拌に動力を20要することなく均一に
混合でき且簡単な装置で行なわんとしてなしたもので、
以下図示の実施例に基づいて説明する。Depending on the type of sludge, if direct mechanical dewatering is not possible, a flocculant is added to the sludge and stirred to form flocs of sludge particles, followed by mechanical dewatering. However, to add this flocculant, the flocculant and sludge are supplied to a mixing tank and mixed by stirring with an agitator, or the flocculant and sludge are put into a rotating drum and the drum rotates to mix the flocculant and sludge. are doing. However, this method requires 15% of power to stir the flocculant, and because a large amount of flocculant is injected into a specific location, more flocculant than necessary acts on the sludge particles in some areas, and the crosslinking effect of the polymer flocculant is impaired. It may be insufficient. In view of this, the present invention was made with the aim of uniformly mixing the flocculant and stirring without requiring 20% of power, and with a simple device.
The following description will be made based on the illustrated embodiment.
図に於て1は汚泥に対して所要の混合比で凝集剤を添加
混合する添加装置の本体でこれは汚泥供25給移送管の
一部に接続されるよう両端にフランジを具備せしめた管
形状であると共にこの本体1の外周面より本体内に凝集
剤添加管2を多数設ける。In the figure, 1 is the main body of the addition device that adds and mixes flocculant to sludge at the required mixing ratio.This is a pipe equipped with flanges at both ends so as to be connected to a part of the sludge supply 25 supply pipe. In addition to the shape, a large number of flocculant addition pipes 2 are provided inside the main body from the outer peripheral surface of the main body 1.
従つてこの本体径は汚泥供給移送管3の径と同径もしく
は少し大径となるように定める。30本体外周に設ける
凝集剤添加管2は本体外周面に軸心に沿つて螺旋状に点
々として多数配列すると共に本体内を移送される汚泥が
この添加管2によつて渦流が生じる径を有し、且下流方
向に傾斜させ、さらにはこの添加管2の先端が本体1の
内35面より少しの間隙を有するようにしてその長さを
定めるもので、この各添加管2は本体1に固定してもよ
いが第4図に示すように本体外周に突設したボス1aに
添加管2を気密的摺動自在に嵌挿しロツクボルト1b等
の係止具にて任意の突出量位置で可調整的に固定する方
式であつてもよい。Therefore, the diameter of the main body is determined to be the same as or slightly larger than the diameter of the sludge supply transfer pipe 3. 30 A large number of flocculant addition pipes 2 provided on the outer periphery of the main body are arranged in a spiral pattern along the axis along the outer peripheral surface of the main body, and the sludge transferred inside the main body has a diameter that causes a vortex flow due to the addition pipes 2. The length of each addition tube 2 is determined so that the tip of the addition tube 2 has a slight gap from the inner 35 surface of the main body 1. Although it may be fixed, as shown in Fig. 4, the addition tube 2 can be slidably inserted into the boss 1a protruding from the outer periphery of the main body in an airtight manner, and the protrusion amount can be adjusted to any desired position using a locking tool such as a lock bolt 1b. It may be fixed in an adjustable manner.
尚多数の凝集剤添加管2の外端には凝集剤供給管4が接
続されるものである。而して上述の如く構成する装置に
於て凝集剤を添加混合するには本体内に所要の圧力、流
速にて汚泥を移送せしめつつ各添加管2より汚泥量に対
し所定の割合で凝集剤を少量づつ添加すると汚泥中の浮
遊物は下流方向に傾斜した添加管に引掛らずに流下する
と共に汚泥はこの添加管外周面に衝突して恰も攪拌棒の
如き作用してその下流側に渦流(乱流)が生じて撹拌さ
れる。Furthermore, a flocculant supply pipe 4 is connected to the outer ends of the many flocculant addition pipes 2. To add and mix the flocculant in the apparatus configured as described above, the flocculant is added to the sludge amount from each addition pipe 2 at a predetermined ratio to the amount of sludge while the sludge is transferred into the main body at the required pressure and flow rate. When sludge is added little by little, the suspended matter in the sludge flows down the addition pipe that is tilted in the downstream direction without being caught, and the sludge collides with the outer circumferential surface of this addition pipe, acting like a stirring bar, creating a vortex flow downstream. (turbulent flow) is generated and stirred.
この渦流が生じている中もしくはその附近に凝集剤が少
量づつ添加されるため均一な凝集剤添加と共に混合撹拌
が効率的に行なわれるものである。また添加管の本体内
への突出量を変えることにより混合攪拌を汚泥質、凝集
剤添加量等に応じて最も効率的な混合撹拌が行なわれる
。Since the flocculant is added little by little in or near the vortex, uniform addition of the flocculant and efficient mixing and agitation are achieved. Furthermore, by changing the amount of protrusion of the addition pipe into the main body, the most efficient mixing and stirring can be performed depending on the quality of the sludge, the amount of flocculant added, etc.
本発明による時は汚泥を輸送するようになした管状本体
内にその外周面より下流方向に傾斜せしめて多数の凝集
剤添加管を設け、この添加管外周により汚泥流に乱流を
生ぜしめると共に各添加管より凝集剤を少量ずつ本体内
の多数位置より移送汚泥中に添加するため凝集剤の添加
が均一で、しかも混合攪拌も外部の撹拌動力が不要で且
つ簡単な構造で効率的な添加混合が行える利点がある。According to the present invention, a large number of flocculant addition pipes are provided in a tubular body designed to transport sludge and are inclined downstream from the outer peripheral surface of the main body, and the outer periphery of the addition pipes creates turbulence in the sludge flow. A small amount of flocculant is added from each addition tube to the transported sludge from multiple locations within the main body, so the flocculant is added uniformly, and mixing and stirring does not require external stirring power, and the simple structure allows for efficient addition. It has the advantage of being able to be mixed.
第1図は概略図、第2図は正面図、第3図は縦断側面図
、第4図は一部拡大断面図である。
1・・・・・・本体、1a・・・・・・ボス、1b・・
・・・・ロツクボルト、2・・・・・・凝集剤添加管、
3・・・・・・汚泥供給移送管、4・・・・・・凝集剤
供給管。1 is a schematic diagram, FIG. 2 is a front view, FIG. 3 is a vertical side view, and FIG. 4 is a partially enlarged sectional view. 1...Body, 1a...Boss, 1b...
... Lock bolt, 2 ... Coagulant addition pipe,
3...Sludge supply transfer pipe, 4...Flocculant supply pipe.
Claims (1)
て該本体内にその流下方向に傾斜せしめあらゆる方向か
ら多数突設した凝集剤添加管にてカルマン渦流を生ぜし
めると共に該渦流中に各添加管より凝集剤を添加し均一
な添加攪拌混合を強制的に行うようになしたことを特徴
とする汚泥処理に於ける凝集剤の添加方法。 2 汚泥移送管に接続されるようになした管状の本体に
その外周面のあらゆる角度よりその内部に突入するよう
多数の凝集剤添加管を配設すると共にこの各添加管を汚
泥流下方向に傾斜せしめ、且流体中にカルマン渦流を発
生せしめる程度の長さを突出せしめてなることを特徴と
する汚泥処理に於ける凝集剤添加装置。[Scope of Claims] 1. A Karman vortex is generated by the flowing energy of the sludge transferred within the tubular body through a large number of flocculant addition pipes which are inclined in the direction of flow and protrude from all directions within the body. 1. A method for adding a flocculant in sludge treatment, characterized in that the flocculant is added from each addition pipe into a vortex flow, and uniform addition stirring and mixing is forcibly performed. 2 A large number of flocculant addition pipes are arranged in a tubular body connected to a sludge transfer pipe so as to protrude into the interior from all angles of the outer peripheral surface, and each of these addition pipes is inclined in the downward direction of sludge flow. 1. A flocculant addition device for sludge treatment, characterized in that the flocculant addition device is protruded to a length sufficient to cause a Karman vortex flow in the fluid.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55161140A JPS593239B2 (en) | 1980-11-14 | 1980-11-14 | Method and equipment for adding flocculant in sludge treatment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55161140A JPS593239B2 (en) | 1980-11-14 | 1980-11-14 | Method and equipment for adding flocculant in sludge treatment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5784800A JPS5784800A (en) | 1982-05-27 |
| JPS593239B2 true JPS593239B2 (en) | 1984-01-23 |
Family
ID=15729347
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55161140A Expired JPS593239B2 (en) | 1980-11-14 | 1980-11-14 | Method and equipment for adding flocculant in sludge treatment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS593239B2 (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6044006A (en) * | 1983-08-19 | 1985-03-08 | Ebara Corp | Separation of fine particle in suspension |
| JPS63258626A (en) * | 1987-04-16 | 1988-10-26 | Aoki Kensetsu:Kk | Viscous material stirring/mixing method and its device |
| JP3145601B2 (en) * | 1994-03-09 | 2001-03-12 | 日本碍子株式会社 | Method and apparatus for producing sludge mixed with inorganic coagulant |
| FR2728892B1 (en) * | 1995-01-04 | 1997-03-14 | Bernard Thierry | PROCESS FOR PRODUCING A PYROTECHNIC COMPOSITION |
| KR100858957B1 (en) | 2007-09-18 | 2008-09-17 | 주식회사 덕영엔지니어링 | Powder conveying device and powder conveying method |
| FI20105230A7 (en) * | 2010-03-10 | 2011-09-11 | Wetend Tech Oy | Method and apparatus for mixing different flows into a process fluid flow |
-
1980
- 1980-11-14 JP JP55161140A patent/JPS593239B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5784800A (en) | 1982-05-27 |
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