JPS5750600A - Floating and concentrating method of sludge - Google Patents
Floating and concentrating method of sludgeInfo
- Publication number
- JPS5750600A JPS5750600A JP55126994A JP12699480A JPS5750600A JP S5750600 A JPS5750600 A JP S5750600A JP 55126994 A JP55126994 A JP 55126994A JP 12699480 A JP12699480 A JP 12699480A JP S5750600 A JPS5750600 A JP S5750600A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- pressurized water
- tank
- sludges
- change
- 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
- 239000010802 sludge Substances 0.000 title abstract 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 5
- 239000007788 liquid Substances 0.000 abstract 2
- 239000012141 concentrate Substances 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
Landscapes
- Physical Water Treatments (AREA)
- Treatment Of Sludge (AREA)
Abstract
PURPOSE: To efficiently concentrate sludges, which is difficult to be concentrated without using chemicals by providing a mixing tank in which pressurized water dissolving evacuated gas is admixed with sludges and a mixing tank in which pressurized water dissolving unevacuated gas is admixed with sludges followed by evaculation.
CONSTITUTION: Usualy a pressurized water C is introduced through a change-over valve 15 to an ejetor that is the first mixer 4 without evacuation. While pressurized water is spouted from a nozzle in the inside of the ejector, the sludge A is sucked from a sludge tank 1 to the ejector and a mixed liquid E is flowed into floating concentration tank 6 to form froth layers by the sludge particles. In the worse condition of the sludge, by operating the change-over valves 11W15 and a sludge supplying pump 2, sludge A and the pressurized water C are poured into the second mixing vessels 3 respectively through the change-over valves 11 or said valve 14 and then are mixed under the pressure above the atomosphere. The mixing liquid E is transported to evacuating apparatus 5 and evacuated and thereafter is poured into the floating concentration tank 6.
COPYRIGHT: (C)1982,JPO&Japio
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55126994A JPS6014634B2 (en) | 1980-09-12 | 1980-09-12 | Sludge flotation concentration method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55126994A JPS6014634B2 (en) | 1980-09-12 | 1980-09-12 | Sludge flotation concentration method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5750600A true JPS5750600A (en) | 1982-03-25 |
| JPS6014634B2 JPS6014634B2 (en) | 1985-04-15 |
Family
ID=14949023
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55126994A Expired JPS6014634B2 (en) | 1980-09-12 | 1980-09-12 | Sludge flotation concentration method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6014634B2 (en) |
-
1980
- 1980-09-12 JP JP55126994A patent/JPS6014634B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6014634B2 (en) | 1985-04-15 |
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