JPS6051369B2 - High viscosity sludge dust removal equipment - Google Patents
High viscosity sludge dust removal equipmentInfo
- Publication number
- JPS6051369B2 JPS6051369B2 JP53022514A JP2251478A JPS6051369B2 JP S6051369 B2 JPS6051369 B2 JP S6051369B2 JP 53022514 A JP53022514 A JP 53022514A JP 2251478 A JP2251478 A JP 2251478A JP S6051369 B2 JPS6051369 B2 JP S6051369B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- high viscosity
- dust removal
- removal equipment
- metal
- 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
Landscapes
- Combined Means For Separation Of Solids (AREA)
- Treatment Of Sludge (AREA)
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
港湾や市街地の河川などの堆積したヘドロは、公害の原
因となるので浚渫船により浚渫しているが、一般にこれ
等のヘド川よ有害物を含有するために粘度が大で、その
上多数のゴミが混入している。[Detailed Description of the Invention] Sludge accumulated in rivers in ports and urban areas is dredged by dredgers because it causes pollution, but in general, sludge that has accumulated in rivers in ports and urban areas is dredged by dredgers. And on top of that, a lot of garbage is mixed in.
船から高粘度の浚渫ヘドロを水上管などによつて捨場に
圧送するには高圧のポンプを要し、それはピストン式ポ
ンプが適しているが、これ等のポンプには弁が不可欠で
あるから当然ゴミに因る弁のトラブルが伴う。浚渫ヘド
川こ水を混入して低粘度によれば、弁のない通常の遠心
式ポンプが使用できてトラブルより解放されるが、捨場
での脱水処理が必要となり、経済的に不利となる。本発
明は浚渫された粘度の高いヘドロ中に混入しているゴミ
を、ヘドロの粘度を低下せずに除去する装置であつて、
ゴミによるポンプ弁のトラブルを解消するものである。
高粘度のヘドロ中に混入したゴミを除去する目的で通常
の振動式網篩を使用するとして、ピストルポンプ等の弁
に影響しない程度の大さのゴミを除去するには網目は5
〜1 以下としなければならない。A high-pressure pump is required to pump high-viscosity dredged sludge from a ship to a dumping site via a water pipe, and a piston-type pump is suitable for this purpose, but these pumps naturally require a valve. Valve problems are caused by dust. If the viscosity of water mixed with dredged river water is low, a normal centrifugal pump without a valve can be used and troubles will be avoided, but dewatering treatment at a dumping site will be required, which is economically disadvantageous. The present invention is an apparatus for removing garbage mixed in dredged sludge with high viscosity without reducing the viscosity of the sludge,
This eliminates problems with pump valves caused by dirt.
When using a regular vibrating mesh sieve to remove dust mixed in high viscosity sludge, the mesh size is 5 to remove dust that is small enough not to affect the valves of pistol pumps, etc.
Must be less than or equal to ~1.
しカルこの程度の小網目では、高粘度のヘドロは網目に
付着して通過せず、ヘドロはゴミを包んだまま網上を転
動するのみで、険悪装置の目的は全く達せられない。本
発明の根本原理は、熱した(約100゜C以上)金属製
の管などには、ヘドロが高粘度(200〜500ポイズ
)であつても付着しない現象に基いている。With such a small mesh, the highly viscous sludge sticks to the mesh and does not pass through, and the sludge simply rolls around on the mesh while still encasing dirt, and the purpose of the dangerous device is not achieved at all. The fundamental principle of the present invention is based on the phenomenon that sludge does not adhere to heated (approximately 100° C. or higher) metal pipes, etc., even if the sludge has a high viscosity (200 to 500 poise).
図により、その一例について説明すると、1は金属管で
あつて適当の間隔をあけて複数本が平行して並べてあり
、各管の両端は集合管2に連通し、集合管2には導管3
が取り付けてある。今、導管3の一方より他方へ、蒸気
油などの充分に加熱された流体を通すと、集合管2を経
て金属管1も加熱される。各金属管1の表面温度が常に
約100℃以上になるように流体温度を保ちつつ、並列
した金属管1上に高粘度のヘドロを流すと、ヘド川よ熱
した金属管には付着しない特性に・基き、ヘドロは水の
場合と同様に直ちに管と管との間隙より下方に落下し、
へドロ内に含まれたゴミのみが管1列上に残る。残留し
たゴミは管1を傾斜して設けるか、あるいは管1に振動
を与えることにより、管1の列外に取り出すことができ
・る。本発明では、管と管との間隙を狭めることにより
微小のゴミの除去が可能となる。To explain one example with reference to the figure, 1 is a metal pipe, and a plurality of pipes are arranged in parallel at appropriate intervals, both ends of each pipe are connected to a collecting pipe 2, and a conduit 3 is connected to the collecting pipe 2.
is installed. Now, when a sufficiently heated fluid such as steam oil is passed from one side of the conduit 3 to the other, the metal tube 1 is also heated through the collecting pipe 2. If high viscosity sludge is flowed over the parallel metal tubes 1 while maintaining the fluid temperature so that the surface temperature of each metal tube 1 is always about 100°C or higher, it will not stick to the heated metal tubes. Based on this, sludge immediately falls downward from the gap between the pipes, just like water,
Only the dirt contained in the sludge remains on one row of pipes. The remaining dirt can be taken out of the row of tubes 1 by providing the tubes 1 at an angle or by applying vibration to the tubes 1. In the present invention, fine dust can be removed by narrowing the gap between the tubes.
又管内に流す流体を比熱の大なるものを使用することに
より、冷えたヘドロに接しても管表面を常に約100℃
以上に維持することができる。In addition, by using a fluid with a high specific heat to flow into the pipe, the surface of the pipe is always maintained at approximately 100°C even when it comes into contact with cold sludge.
can be maintained above.
図面は本発明を実施した一例の説明図である。 1は金属管、2は集合管、3は導管。 The drawings are explanatory diagrams of an example of implementing the present invention. 1 is a metal pipe, 2 is a collecting pipe, and 3 is a conduit.
Claims (1)
平行して並べ、該管の各両端を集合管で連通し、集合管
に接続した導管より加熱した蒸気、油などの流体を通し
て各金属管の表面温度を約100℃以上に保たしめ、金
属管の列上に高粘度のヘドロを流し、ヘドロは金属管の
間隙より落下するがヘドロ中のゴミは金属管列上に残る
ようにした、高粘度ヘドロの除塵装置。1. As shown in the figure, multiple metal pipes are arranged in parallel at appropriate intervals, and both ends of the pipes are connected by a collecting pipe, and heated steam, oil, or other fluid is passed through the conduit connected to the collecting pipe. The surface temperature of each metal tube is maintained at approximately 100℃ or higher, and high-viscosity sludge is poured over the row of metal tubes.The sludge falls through the gaps between the metal tubes, but the dirt in the sludge remains on the row of metal tubes. Dust removal equipment for high viscosity sludge.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53022514A JPS6051369B2 (en) | 1978-02-28 | 1978-02-28 | High viscosity sludge dust removal equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP53022514A JPS6051369B2 (en) | 1978-02-28 | 1978-02-28 | High viscosity sludge dust removal equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS54115548A JPS54115548A (en) | 1979-09-08 |
| JPS6051369B2 true JPS6051369B2 (en) | 1985-11-13 |
Family
ID=12084862
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP53022514A Expired JPS6051369B2 (en) | 1978-02-28 | 1978-02-28 | High viscosity sludge dust removal equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6051369B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60188276U (en) * | 1984-05-23 | 1985-12-13 | 株式会社 光合金製作所 | Backflow prevention valve for cold regions |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6058217U (en) * | 1983-09-30 | 1985-04-23 | バブコツク日立株式会社 | Coarse particle separator |
| JP7741379B2 (en) * | 2021-11-19 | 2025-09-18 | 日本製鉄株式会社 | dust remover |
-
1978
- 1978-02-28 JP JP53022514A patent/JPS6051369B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60188276U (en) * | 1984-05-23 | 1985-12-13 | 株式会社 光合金製作所 | Backflow prevention valve for cold regions |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS54115548A (en) | 1979-09-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS6051369B2 (en) | High viscosity sludge dust removal equipment | |
| CN221637402U (en) | Oil-water separator | |
| EP0307397A1 (en) | Apparatus and method for collecting oil from water. | |
| FR2381991A1 (en) | HEAT TRANSFER SYSTEM WITH HEAT TRANSFER FLUID | |
| US4029584A (en) | Pneumatic sludge discharging system | |
| US995446A (en) | Method of snow disposal. | |
| RU2255903C1 (en) | Device for purification of oily waste waters | |
| CN206621831U (en) | A kind of lubricating oil dewatering filtering device | |
| RU22982U1 (en) | OIL PIPELINE FILTER | |
| CN205362063U (en) | Cleaning device | |
| SU398267A1 (en) | IONITE FILTER OF MIXED ACTION WITH INTERNAL IONITIUM REGENERATION | |
| CN113587688A (en) | Multifunctional inclined plate heat exchanger of oil field heating furnace and application method thereof | |
| CN220642685U (en) | An oily wastewater treatment device | |
| SU931243A2 (en) | Stand for washing pipelines | |
| SU556210A1 (en) | Apparatus for washing and thickening the fibrous suspension | |
| SU1122781A1 (en) | Arrangement for cleaning a cooling water basin from oil film | |
| SU795591A1 (en) | Apparatus for passing scapers through pipeline | |
| CN213836488U (en) | A dredging device for highway engineering | |
| RU2238781C1 (en) | Installation for evacuation of water | |
| SU746159A1 (en) | Apparatus for passing separators, scrapers and other flow arrangements through pipeline | |
| SU366871A1 (en) | LIBRARY Leningrad Technological Institute of the Pulp and Paper Industry: ii> & h, '^ "h. * Vy I V.y С: П f ^ L | |
| CN109340568B (en) | A pipeline sand conveying device | |
| SU1255678A1 (en) | Method of removing deposits from hydraulic structure | |
| JPS5499270A (en) | Separation of solid and liquid components of dredged and reclamation slurry | |
| SU1755863A1 (en) | Separation plant |