CN2198038Y - Swirl high efficiency solid and liquid separater - Google Patents
Swirl high efficiency solid and liquid separater Download PDFInfo
- Publication number
- CN2198038Y CN2198038Y CN 94236877 CN94236877U CN2198038Y CN 2198038 Y CN2198038 Y CN 2198038Y CN 94236877 CN94236877 CN 94236877 CN 94236877 U CN94236877 U CN 94236877U CN 2198038 Y CN2198038 Y CN 2198038Y
- Authority
- CN
- China
- Prior art keywords
- high efficiency
- solid
- whirl cylinder
- efficiency solid
- swirl
- 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 - Fee Related
Links
Abstract
The utility model relates to a swirl high efficiency solid and liquid separator. The top of a vertical swirl barrel with a conical bottom is provided with a clear liquid discharge port. Different radial positions of the upper part are respectively provided with a mixture feed inlet and an auxiliary precipitation reagent inlet along the tangent direction, and different height positions of the lower part or the bottom are provided with at least two precipitate outlets.
Description
The utility model relates to a kind of device of finishing the solidliquid mixture separation with cyclone mode.
Common spiral-flow type equipment for separating liquid from solid is to be respectively arranged with mixture charging aperture, clear liquid discharging mouth and sediment outlet on the differing heights position of the vertical shape whirl cylinder that has tapered bottom.Mixed material is entered by tangential charging aperture spin current tube top, and solid content is discharged bottom rotation sinks to naturally owing to difference of specific gravity in tube, and the clear liquid after the separation is emitted by the top.Better to this device separating effect of the big mixed material of difference of specific gravity, but less to difference of specific gravity, or it is slow to be enclosed with the separating rate of mixtures such as the flocculate of a large amount of solvents or gelling thing in the solid content, sedimentary volume is big, and separating effect is undesirable.
The purpose of this utility model is to provide a kind of improved spiral-flow type efficient equipment for separating liquid from solid at the problems referred to above, multiple fields such as water treatment, Industrial Wastewater Treatment, separating substances and recovery be can be widely used in, and solid-liquid separation efficiency and effect improved greatly.
The utility model equipment for separating liquid from solid is provided with the clear liquid discharging mouth at the top of the vertical shape whirl cylinder with tapered bottom, tangentially be provided with a mixed material import and at least one aids precipitation agent import in the Different Diameter on top respectively to the position, in the bottom or the differing heights place of bottom be provided with two sediments outlets at least.Experiment shows, in common rotational flow separation process, if add than great, and not with " inert " mixture of separated object generation chemical reaction as the aids precipitation agent, make its " carrier " of becoming solid content in the separated mixture, can improve the proportion of precipitum, and can squeeze out the moisture that wraps up in the former solid content, can greatly improve sinking speed, improve separating effect.The aids precipitation agent is used repeatedly according to the different separated backs of proportion are capable of circulation.To add the aluminum sulfate precipitate and separate be example with the sand turbidity that contains of 100 milliliters of graduated cylinders, after using this method, sinking speed can be increased to 2～4 seconds by former 500～600 seconds, the solid content clearance that separates is increased to more than 99% by 70～80%, and sedimentary volume also can be compressed to 2～3 milliliters by 10～15 milliliters.Therefore, adopt this device, the volume of present same device is dwindled greatly, separative efficiency greatly improves.
If make the aids precipitation agent on whirl cylinder, the height that highly is higher than the mixture charging aperture is set, will be more favourable to Separation of Solid and Liquid.
Below structure of the present utility model is described, but it is not to be restriction to the utility model scope with example shown in the drawings.
The structure of Fig. 1 the utility model device
The A-A figure of Fig. 2 Fig. 1
As figure, the efficient equipment for separating liquid from solid of this spiral-flow type has a vertical shape whirl cylinder 1 with tapered bottom 7, its top is provided with clear liquid discharging mouth 3, the Different Diameter on top tangentially is provided with mixed material charging aperture 2 and aids precipitation agent import 4 respectively to the position, and the former entrance location is lower than the latter's entrance location.Bottom and bottom at whirl cylinder are respectively equipped with two sediment outlets 5 and 6, and exporting 6 generally speaking is outlets of aids precipitation agent, and outlet 5 is separated solid content outlets.
Claims (2)
1, the efficient equipment for separating liquid from solid of a kind of spiral-flow type, top at the vertical shape whirl cylinder (1) with tapered bottom (7) is provided with clear liquid discharging mouth (3), it is characterized in that tangentially being provided with mixed material charging aperture (2) and at least one aids precipitation agent import (4) respectively to the position in the Different Diameter on whirl cylinder (1) top, in the bottom or the differing heights place of bottom be provided with the outlet of two sediments (5), (6) at least.
2, device as claimed in claim 1 is characterized in that said mixture charging aperture (2) being provided with on whirl cylinder (1) highly is lower than the height of aids precipitation agent import (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 94236877 CN2198038Y (en) | 1994-07-21 | 1994-07-21 | Swirl high efficiency solid and liquid separater |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 94236877 CN2198038Y (en) | 1994-07-21 | 1994-07-21 | Swirl high efficiency solid and liquid separater |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2198038Y true CN2198038Y (en) | 1995-05-24 |
Family
ID=33844743
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 94236877 Expired - Fee Related CN2198038Y (en) | 1994-07-21 | 1994-07-21 | Swirl high efficiency solid and liquid separater |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2198038Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101380525B (en) * | 2007-09-03 | 2012-07-11 | 株式会社东芝 | Solid-liquid separator |
| CN105056588A (en) * | 2015-09-17 | 2015-11-18 | 苏州市玄天环保科技有限公司 | Solid-liquid separator for water body purification |
-
1994
- 1994-07-21 CN CN 94236877 patent/CN2198038Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101380525B (en) * | 2007-09-03 | 2012-07-11 | 株式会社东芝 | Solid-liquid separator |
| US8349177B2 (en) | 2007-09-03 | 2013-01-08 | Kabushiki Kaisha Toshiba | Solid-liquid separator |
| CN105056588A (en) * | 2015-09-17 | 2015-11-18 | 苏州市玄天环保科技有限公司 | Solid-liquid separator for water body purification |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |