JPH047278B2 - - Google Patents
Info
- Publication number
- JPH047278B2 JPH047278B2 JP59085874A JP8587484A JPH047278B2 JP H047278 B2 JPH047278 B2 JP H047278B2 JP 59085874 A JP59085874 A JP 59085874A JP 8587484 A JP8587484 A JP 8587484A JP H047278 B2 JPH047278 B2 JP H047278B2
- Authority
- JP
- Japan
- Prior art keywords
- blow
- nozzle
- upward
- blowing
- draft cylinder
- 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 - Lifetime
Links
- 238000007664 blowing Methods 0.000 claims description 35
- 238000003756 stirring Methods 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 13
- 230000029087 digestion Effects 0.000 claims description 11
- 239000012530 fluid Substances 0.000 claims description 9
- 239000010802 sludge Substances 0.000 description 17
- 239000000835 fiber Substances 0.000 description 13
- 230000000694 effects Effects 0.000 description 12
- 238000013019 agitation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】
[発明の技術分野]
本発明は、消化槽内の汚泥等をガス等の吹出し
による流体吹出しによるリフト効果によつて撹拌
する装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to an apparatus for stirring sludge or the like in a digestion tank using a lift effect caused by blowing out fluid by blowing out gas or the like.
[発明の技術的背景とその問題点]
汚泥の消化槽において、撹拌を行うために、ド
ラフト用筒体内にガス吹込管を中央部に設け、ガ
ス吹込管を通して供給したエアを吹出ノズルから
上方に向つて吸出させ、エアリフト効果によつて
汚泥を誘引し上方へ移送することによつて、消化
槽内の汚泥を撹拌することを行つている。[Technical background of the invention and its problems] In a sludge digestion tank, a gas blowing pipe is provided in the center of the draft cylinder for stirring, and air supplied through the gas blowing pipe is directed upward from a blowing nozzle. The sludge in the digestion tank is stirred by suctioning the sludge upward and transporting it upward by the air lift effect.
従来の撹拌装置の代表例を第7図および第8図
によつて説明すると、50はドラフト用筒体で、
その上下端は開口し、消化槽1内の汚泥液2(第
1図参照)内に竪向に設置されている。筒体50
内中央部にはガス吹込管51が竪向に配置され、
図示しない支持体によつて支持されている。吹込
管51の下部には放射方向にたとえば分岐管52
が設けられ、その先端に設けられた上端開口で下
部は小ドレン孔53のみが開孔された実質的に有
底筒体の竪向吹出ノズル54に連通している。 A representative example of a conventional stirring device will be explained with reference to FIGS. 7 and 8. 50 is a draft cylinder;
Its upper and lower ends are open, and it is vertically installed in the sludge liquid 2 (see FIG. 1) in the digestion tank 1. Cylindrical body 50
A gas blowing pipe 51 is arranged vertically in the inner central part,
It is supported by a support body (not shown). For example, a branch pipe 52 is provided in the lower part of the blow pipe 51 in the radial direction.
is provided, and the upper end opening provided at the tip thereof communicates with a vertical blow-out nozzle 54 which is substantially a bottomed cylindrical body with only a small drain hole 53 opened at the lower part.
このように構成された撹拌装置においては、吹
込管51を通して供給された空気は、分岐管52
を介して各吹出ノズル54に導かれ、その上端開
口から真上に吹出される。この吹出された空気に
よるエアリフト効果によつて、消化槽1内の汚泥
液2がドラフト用筒体50内に誘引され、その内
部を上昇し、上端から叶出される。これによつ
て、汚泥液2には第1図(ただし同図は本発明例
である)とほぼ同様な汚泥液2の流れが生成さ
れ、撹拌操作が行なわれる。 In the stirring device configured in this way, air supplied through the blowing pipe 51 is passed through the branch pipe 52.
The air is guided to each blow-off nozzle 54 through the air, and is blown directly upward from its upper end opening. Due to the air lift effect of the blown air, the sludge liquid 2 in the digestion tank 1 is drawn into the draft cylinder 50, rises inside the draft cylinder 50, and is discharged from the upper end. As a result, a flow of the sludge liquid 2 almost similar to that shown in FIG. 1 (however, this figure shows an example of the present invention) is generated in the sludge liquid 2, and a stirring operation is performed.
しかし、この種の撹拌装置では、消化汚泥液が
高濃度でかつ繊維分を多く含み、しかも分岐管5
2が放射方向(半径方向)に張出し、さらに吹出
ノズル54が大きな断面積をもつて上向きに開口
している関係上、消化汚泥の繊維分が分岐管52
および吹出ノズル54にからみつき、ドラフト用
筒体50内を閉塞させ撹拌効果を低下させるとい
う根本的な問題点が残されていた。 However, in this type of stirring device, the digested sludge liquid is highly concentrated and contains a large amount of fiber, and furthermore, the
2 protrudes in the radial direction (radial direction), and the blowing nozzle 54 has a large cross-sectional area and opens upward, so that the fibers of the digested sludge flow into the branch pipe 52.
The fundamental problem remains that the particles get entangled with the blow-off nozzle 54, clogging the inside of the draft cylinder 50 and reducing the stirring effect.
[発明の目的]
本発明の目的は、前記従来の問題点を解決し、
ドラフト用筒体内において閉塞を確実に防止で
き、もつて長期間安定した撹拌を行うことができ
る消化槽のガス撹拌装置を提供することにある。[Object of the invention] The object of the present invention is to solve the above-mentioned conventional problems,
An object of the present invention is to provide a gas agitation device for a digestion tank that can reliably prevent blockage in a draft cylinder and perform stable agitation for a long period of time.
[発明の概要]
この目的を達成するための本第1発明は、両端
開口で竪向のドラフト用筒体とその内部にあつて
液体吹出用の吹出ノズルとを備えたものであつ
て、前記吹出ノズルをそれからの吹出流体流が前
記筒体の内壁に向つて斜め上方の向うように配設
したことを特徴とするものである。[Summary of the Invention] The first invention to achieve this object comprises a vertical drafting cylinder with openings at both ends and a blowing nozzle for blowing out liquid inside the drafting cylinder. The blow-off nozzle is characterized in that the blow-off nozzle is disposed so that the blow-off fluid flow therefrom is directed obliquely upward toward the inner wall of the cylindrical body.
また、第2発明は、両端開口で堅向のドラフト
用筒体とその内部にあつて流体吹出用の吹出ノズ
ルとを備えたものであつて、前記吹出ノズルをそ
れからの吹出流体流が旋回上昇流となるような向
きをもつて前記筒体の内壁に向つて配設したこと
を特徴とするものである。 Further, a second invention is provided with a draft cylinder having openings at both ends and a blowout nozzle disposed inside the drafting cylinder for blowing out fluid, wherein the blowout fluid flow from the blowout nozzle swirls upward. It is characterized in that it is disposed toward the inner wall of the cylindrical body in a direction that creates a flow.
すなわち、本発明は、従来の撹拌装置があくま
でも真上向きに吹出ノズルを配設したもの代え
て、中央からドラフト用筒体の内壁に向けて斜め
上向きに配設したことに主要点がある。 That is, the main point of the present invention is that instead of the conventional stirring device in which the blowing nozzle is arranged directly upward, the blowing nozzle is arranged diagonally upward from the center toward the inner wall of the draft cylinder.
かかる構造によれば、後記具体例で明らかにな
るように、汚泥液の上昇流れに伴つて、その繊維
分は斜め上向きの吹出ノズルの下面に沿つて斜め
上向きに上昇するようになるから、吹出ノズルに
対する付着は殆んどなく、またある横断面をとつ
てみても、吹出ノズルが占める面積が小さくな
り、この面でも上昇流を妨げることはなく、しか
もエアリフト効果も従来例と同一あるいはそれ以
上となる。 According to this structure, as will become clear in the specific examples described later, as the sludge liquid flows upward, its fibers rise diagonally upward along the lower surface of the diagonally upward blowing nozzle. There is almost no adhesion to the nozzle, and even when looking at a certain cross section, the area occupied by the blowout nozzle is small, so the upward flow is not obstructed even in this area, and the air lift effect is the same as or better than the conventional example. becomes.
第2発明では、第1発明の思想と共に、単なる
上昇流ではなく、旋回上昇流となるように吹出す
ものである。これによつて、一層撹拌効果が助長
され、繊維分のからみつきも防止される。 In the second invention, in addition to the idea of the first invention, the air is blown out not as a mere upward flow but as a swirling upward flow. This further promotes the stirring effect and prevents the fibers from becoming entangled.
なお、本発明は、エア吹出しによるもののほ
か、他の流体、たとえば水、もしくは汚泥液を吹
出す例も包含するものである。 Note that the present invention includes not only air blowing but also blowing out other fluids, such as water or sludge liquid.
[発明の具体例]
以下本発明を第1図〜第6図に示すエアリフト
効果による具体例によつてさらに詳説する。[Specific Examples of the Invention] The present invention will be further explained in detail below using specific examples based on the air lift effect shown in FIGS. 1 to 6.
<第1具体例>
第1図〜第4図は第1具体例を示したもので、
3はドラフト用筒体で、その内部にガス吹込管4
が配置されている。ガス吹込管4は、上部の蓋体
5にあるいはさらにサポート管6(第2図)を介
して槽1の底部に支持されている。<First Specific Example> Figures 1 to 4 show the first specific example.
3 is a draft cylinder, inside which is a gas blowing pipe 4.
is located. The gas blowing pipe 4 is supported at the bottom of the tank 1 by an upper lid 5 or further via a support pipe 6 (FIG. 2).
ガス吹込管4の途中に、高さ方向に一個所また
は間隔を置いて複数個所に1または好ましくは複
数のガス吹出ノズル7,7…が設けられている。
ノズル7は、ガス吹込管4内に連通し、叶出口は
水平切断した平面的にみて楕円形状をなしてい
る。またノズル7は、ガス吹込管4から放射方向
に張り出して、ドラフト用筒体3の内壁に向い
て、斜め上方に配設されている。なお、吹込管4
およびサポート管6は、短管をフランジを介して
連設したもので、また吹込管4とサポート管6と
の間は仕切板8によつて仕切られている。 In the middle of the gas blowing pipe 4, one or preferably a plurality of gas blowing nozzles 7, 7, . . . are provided at one location or at multiple locations spaced apart in the height direction.
The nozzle 7 communicates with the inside of the gas blowing pipe 4, and the leaf outlet has an elliptical shape when viewed in a horizontally cut plane. Further, the nozzle 7 protrudes radially from the gas blowing pipe 4 and is disposed obliquely upward toward the inner wall of the draft cylinder 3. In addition, the blowing pipe 4
The support pipe 6 is formed by connecting short pipes via flanges, and the blow pipe 4 and the support pipe 6 are separated by a partition plate 8.
かかる撹拌装置において、ガス吹込管4にたと
えば空気Aを圧送すると、空気Aはガス吹込管4
から向きを変えガス吹出ノズル7に至り、ドラフ
ト用筒体3の内壁面に向つて放射方向の斜め上方
に吹出され、やがて垂直方向に向う。その結果、
エアリフト効果によつて、ドラフト用筒体3の下
端開口から汚泥液が誘引され、ドラフト用筒体3
内を上昇し、上端開口から吐出される。したがつ
て、消化槽1内の汚泥液2には、第1図のような
流れが形成され、撹拌操作が行なわれる。 In such a stirring device, when air A, for example, is forced into the gas blowing pipe 4, the air A flows through the gas blowing pipe 4.
The gas then changes its direction and reaches the gas blowing nozzle 7, where it is blown obliquely upward in the radial direction toward the inner wall surface of the draft cylinder 3, and then in the vertical direction. the result,
Due to the air lift effect, sludge liquid is attracted from the lower end opening of the draft cylinder 3.
It rises inside and is discharged from the upper end opening. Therefore, a flow as shown in FIG. 1 is formed in the sludge liquid 2 in the digestion tank 1, and a stirring operation is performed.
本発明に従えば、吹出ノズル7が放射方向に斜
め上方に向いて設けられる。したがつて、第2図
矢印で示すように、吹出ノズル7の傾斜下面に当
るように上昇してきた汚泥液は、吹出ノズル7の
傾斜下面に沿つて上昇するので、汚泥の繊維分が
流れと共に付着することなくそのまま上昇せられ
る。したがつて、繊維分の吹出ノズル7への付着
によるドラフト用筒体3内の閉塞が防止される。 According to the present invention, the blow-off nozzle 7 is provided facing obliquely upward in the radial direction. Therefore, as shown by the arrow in FIG. 2, the sludge liquid that has risen so as to hit the inclined lower surface of the blowing nozzle 7 rises along the inclined lower surface of the blowing nozzle 7, so that the fibers of the sludge are removed with the flow. It can be lifted as it is without sticking. Therefore, clogging of the inside of the draft cylinder 3 due to adhesion of fibers to the blow-off nozzle 7 is prevented.
一方、図示例のように、吹出ノズル7は全長に
わたつて一様な管状であることが、繊維分の付着
を一層防止できる点で好ましい。ここで、第7図
および第8図の従来例について振り返つてみる
と、分岐管52に上昇して当つた繊維分は、周方
向は一部沿つて上昇するものの、分岐管52の長
さ方向の沿う流れは一切なく、この点で付着が生
じ易く、また吹出ノズル54の低面に当る繊維分
はそこで滞留しがちである。これに対して、本発
明例では、上昇流が円滑で、繊維分の付着がな
い。 On the other hand, as shown in the illustrated example, it is preferable that the blow-off nozzle 7 has a uniform tubular shape over its entire length, since this can further prevent the adhesion of fibers. Now, looking back at the conventional examples shown in FIGS. 7 and 8, the fibers that rise and hit the branch pipe 52 rise along a part of the circumference, but in the longitudinal direction of the branch pipe 52. There is no flow along this point, and adhesion tends to occur at this point, and the fibers that hit the lower surface of the blow-off nozzle 54 tend to stay there. On the other hand, in the example of the present invention, the upward flow is smooth and there is no adhesion of fibers.
<第2具体例>
第5図は、吹込管4の下端部4aを円錐状とな
し、第1具体例のようなサポート管6を使用しな
い例で、しかも吹出ノズル7の下面を下端部51
aの下面と面一とした例である。この例によれ
ば、第2図例において吹出ノズル7の吹込管4へ
の取付部において、あるいは従来例における吹込
管51の底面において生じがちな繊維分の付着が
確実に防止される。<Second Specific Example> FIG. 5 shows an example in which the lower end 4a of the blowing pipe 4 is conical and the support pipe 6 as in the first specific example is not used.
This is an example where it is flush with the bottom surface of a. According to this example, the adhesion of fibers that tends to occur at the attachment portion of the blow-off nozzle 7 to the blow-in pipe 4 in the example of FIG. 2 or on the bottom surface of the blow-in pipe 51 in the conventional example is reliably prevented.
<第3具体例>
第6図は、ドラフト用筒体3内において上昇旋
回流を生起させるべく、吹出ノズル7Aを、ドラ
フト用筒体3の接線方向に沿わせ、かつ放射方向
に斜め上方に向けた例である。なお、第6図のみ
では、上方に向いていることが明らかでないが、
第3図等と同様に上方に向けてある。<Third Specific Example> In FIG. 6, the blowing nozzle 7A is aligned along the tangential direction of the drafting cylinder 3 and diagonally upward in the radial direction in order to generate an upward swirling flow within the drafting cylinder 3. This is an example aimed at Although it is not clear from Figure 6 that it is facing upward,
It is oriented upward as in Figure 3.
本例によれば、単に上昇流のみでなく、旋回流
も与えられるものであるので、ドラフト筒体3内
での上昇撹拌力は大きなものとなり、繊維分によ
る付着、閉塞は完全といつていい程防止される。 According to this example, not only an upward flow but also a swirling flow is provided, so the upward stirring force within the draft cylinder 3 is large, and the adhesion and blockage by fibers can be said to be completely eliminated. This will be prevented.
[発明の効果]
以上の通り、本発明は吹出流体流が放射方向に
斜め上方に向うようにしたので、汚泥の繊維分等
による付着・閉塞が確実に防止される。[Effects of the Invention] As described above, in the present invention, since the blown fluid flow is directed diagonally upward in the radial direction, adhesion and clogging due to sludge fibers, etc. can be reliably prevented.
また、第2発明によれば、旋回上昇流が生起さ
れるものであるため、旋回効果も加わつて、付
着・閉塞防止効果が一層顕在化される。 Further, according to the second invention, since a swirling upward flow is generated, a swirling effect is also added, and the effect of preventing adhesion and clogging becomes even more pronounced.
さらに、上昇流が吹出部における圧損が極力小
さくなり円滑となる結果、消化槽内の液の撹拌効
果が向上する利点もある。 Furthermore, as a result of the upward flow becoming smooth with minimal pressure loss at the blow-off section, there is also the advantage that the stirring effect of the liquid in the digestion tank is improved.
第1図は本発明装置の全体概要図、第2図は第
1具体例に従う撹拌装置の詳細を示す縦断面図、
第3図はその要部拡大縦断面図、第4図は水平半
断面図、第5図は第2具体例の縦断面図、第6図
は第3具体例(第2発明)の水平断面図、第7図
は従来例の縦断面図、第8図はその水平断面図で
ある。
1……消化槽、3……ドラフト用筒体、4……
ガス吹込管、7,7A……ガス吹出ノズル、A…
…空気。
FIG. 1 is an overall schematic diagram of the device of the present invention, and FIG. 2 is a longitudinal sectional view showing details of the stirring device according to the first specific example.
Fig. 3 is an enlarged vertical cross-sectional view of the main part, Fig. 4 is a horizontal half-sectional view, Fig. 5 is a vertical cross-sectional view of the second specific example, and Fig. 6 is a horizontal cross-sectional view of the third specific example (second invention). 7 are longitudinal sectional views of the conventional example, and FIG. 8 is its horizontal sectional views. 1... Digestion tank, 3... Draft cylinder, 4...
Gas blowing pipe, 7,7A...Gas blowing nozzle, A...
…air.
Claims (1)
にあつて流体吹出用の吹出ノズルとを備えたもの
であつて、前記吹出ノズルをそれからの吹出流体
流が前記筒体の内壁に向つて斜め上方の向うよう
に配設したことを特徴とする消化槽の撹拌装置。 2 両端開口で堅向のドラフト用筒体とその内部
にあつて液体吹出用の吹出ノズルとを備えたもの
であつて、前記吹出ノズルをそれからの吹出流体
流が旋回上昇流となるような向きをもつて前記筒
体の内壁に向つて配設したことを特徴とする消化
槽の撹拌装置。[Scope of Claims] 1. A device comprising a vertical draft cylinder with openings at both ends and a blow-out nozzle disposed inside the draft cylinder for blowing out fluid, wherein the blow-out nozzle is connected to the blow-out fluid flow from the cylinder. A stirring device for a digestion tank, characterized in that it is arranged diagonally upward toward the inner wall of the body. 2. A draft cylinder with openings at both ends and a straight-facing draft cylinder, and a blow-out nozzle disposed inside the draft cylinder for blowing out liquid, the blow-out nozzle being oriented so that the blowing fluid flow from it becomes a swirling upward flow. A stirring device for a digestion tank, characterized in that the stirring device is disposed toward the inner wall of the cylindrical body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59085874A JPS60227887A (en) | 1984-04-27 | 1984-04-27 | Stirrer for digestion tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP59085874A JPS60227887A (en) | 1984-04-27 | 1984-04-27 | Stirrer for digestion tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS60227887A JPS60227887A (en) | 1985-11-13 |
| JPH047278B2 true JPH047278B2 (en) | 1992-02-10 |
Family
ID=13871041
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP59085874A Granted JPS60227887A (en) | 1984-04-27 | 1984-04-27 | Stirrer for digestion tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS60227887A (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2470070B (en) | 2009-05-08 | 2012-05-16 | Coldharbour Marine Ltd | Liquid pump apparatus and method |
| US10711807B2 (en) | 2010-06-29 | 2020-07-14 | Coldharbour Marine Limited | Gas lift pump apparatus with ultrasonic energy generator and method |
| GB2497954A (en) | 2011-12-22 | 2013-07-03 | Coldharbour Marine Ltd | Gas lift pump with a sonic generator |
| GB2521258B8 (en) | 2013-10-14 | 2020-02-26 | Coldharbour Marine Ltd | Apparatus and method |
| JP6104829B2 (en) * | 2014-02-25 | 2017-03-29 | 株式会社東芝 | Anaerobic water treatment system |
-
1984
- 1984-04-27 JP JP59085874A patent/JPS60227887A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS60227887A (en) | 1985-11-13 |
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