CN202070201U - Rotary solid-liquid separator - Google Patents
Rotary solid-liquid separator Download PDFInfo
- Publication number
- CN202070201U CN202070201U CN2011201708230U CN201120170823U CN202070201U CN 202070201 U CN202070201 U CN 202070201U CN 2011201708230 U CN2011201708230 U CN 2011201708230U CN 201120170823 U CN201120170823 U CN 201120170823U CN 202070201 U CN202070201 U CN 202070201U
- Authority
- CN
- China
- Prior art keywords
- case
- suspension
- shell
- waste slag
- liquid separator
- 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
- 239000007788 liquid Substances 0.000 title claims abstract description 16
- 239000002699 waste material Substances 0.000 claims abstract description 12
- 238000007599 discharging Methods 0.000 claims description 6
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 claims description 3
- 239000000725 suspension Substances 0.000 abstract description 13
- 239000007787 solid Substances 0.000 abstract description 7
- 238000001556 precipitation Methods 0.000 abstract description 6
- 239000002893 slag Substances 0.000 abstract 4
- 239000000463 material Substances 0.000 abstract 3
- 239000002245 particle Substances 0.000 abstract 2
- 239000008187 granular material Substances 0.000 description 4
- 238000005352 clarification Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000006194 liquid suspension Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Landscapes
- Separation Of Solids By Using Liquids Or Pneumatic Power (AREA)
Abstract
The utility model relates to a rotary solid-liquid separator, which is provided with a conical case with the smaller upper part and the larger lower part, wherein a material outlet, a material inlet and a waste slag outlet are sequentially arranged on the side wall of the case from top to bottom, the circle center part of the upper end of the case is provided with a small hole, the upper end of the case is provided with an electric motor and a speed controller, the bottom of the electric motor is connected with a rotating shaft, the rotating shaft passes through the case and is downwards connected with a U-shaped support rod surrounding the rotating shaft, blades are arranged on the support rod, and the bottom of the support rod is provided with a balance disc in a circular disc shape. When the rotary solid-liquid separator is sued, small solid particles in suspension are fast precipitated, the suspension is separated into clarified liquid at the upper part and the waste slag at the bottom, the clarified liquid and the waste slag are respectively discharged from the material outlet and the waste slag outlet, and the clarified liquid is obtained. The precipitation speed of the small solid particles in the suspension is accelerated, the precipitation time and the precipitation space are saved, and the cost is reduced.
Description
Technical field
The utility model relates to a kind of solid-liquid separating equipment, especially can quicken the rotary solid-liquid separator of separating solids and liquid.
Background technology
Along with the continuous increase of industrial expansion and water consumption, the separation of liquid suspension more and more receives publicity.At present, the separation of suspension mainly contains dual mode, and a kind of is to adopt precipitation mode to carry out, and the sedimentation basin of its use takes up room greatly, and settling velocity is slow; Another kind of separate mode is the mode that adopts chemical settling, needs to use a large amount of chemicals, and cost is high and easily pollute.
The utility model content
In order to overcome the deficiency of existing suspension separate mode, the utility model provides a kind of rotary solid-liquid separator, has improved the settling velocity of solid granule in the suspension, has saved the time and the space of precipitation, has reduced cost.
The technical scheme that its technical problem that solves the utility model adopts is: this separator has a up-small and down-big coniform shell, be disposed with discharging opening, charging aperture and waste residue outlet on the sidewall of shell from top to bottom, the upper end circle centre position of shell has aperture, the upper end of shell is provided with motor and speed control, the bottom of motor is connected with turning cylinder, turning cylinder passes shell and is connected with U-shaped support bar round turning cylinder downwards, blade is installed on the support bar, and the bottom of support bar is provided with discoid balancing frame.During use, add suspension to be separated from charging aperture, actuating motor, turning cylinder drives the blade rotation by support bar, and, the solid granule in the suspension being precipitated rapidly by speed control control rotary speed, suspension is separated into the liquid of top clarification and the waste residue of bottom, discharge the liquid that obtains clarifying by discharging opening and waste residue outlet respectively.
The beneficial effects of the utility model are, have improved the settling velocity of solid granule in the suspension, have saved the time and the space of precipitation, have reduced cost.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is a structural principle schematic diagram of the present utility model.
Among the figure, 1. shell, 2. speed control, 3. motor, 4. turning cylinder, 5. support bar, 6. blade, 7. discharging opening, 8. charging aperture, 9. waste residue outlet, 10. balancing frame.
The specific embodiment
In Fig. 1, this separator has a up-small and down-big coniform shell 1, be disposed with discharging opening 7, charging aperture 8 and waste residue outlet 9 on the sidewall of shell 1 from top to bottom, the upper end circle centre position of shell 1 has aperture, the upper end of shell 1 is provided with motor 3 and speed control 2, the bottom of motor 3 is connected with turning cylinder 4, turning cylinder 4 passes shell 1 and is connected with U-shaped support bar 5 round turning cylinder 4 downwards, blade 6 is installed on the support bar 5, and the bottom of support bar 5 is provided with discoid balancing frame 10.During use, add suspension to be separated from charging aperture 8, actuating motor 3, turning cylinder 4 drives blade 6 rotations by support bar 5, and, the solid granule in the suspension being precipitated rapidly by speed control 2 control rotary speeies, suspension is separated into the liquid of top clarification and the waste residue of bottom, discharge the liquid that obtains clarifying by discharging opening 7 and waste residue outlet 9 respectively.
Claims (1)
1. rotary solid-liquid separator, this separator have a up-small and down-big coniform shell (1), are disposed with discharging opening (7), charging aperture (8) and waste residue outlet (9) on the sidewall of shell (1) from top to bottom; It is characterized in that: the upper end circle centre position of shell (1) has aperture, the upper end of shell (1) is provided with motor (3) and speed control (2), the bottom of motor (3) is connected with turning cylinder (4), turning cylinder (4) passes shell (1) and is connected with U-shaped support bar (5) round turning cylinder (4) downwards, blade (6) is installed on the support bar (5), and the bottom of support bar (5) is provided with discoid balancing frame (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201708230U CN202070201U (en) | 2011-05-18 | 2011-05-18 | Rotary solid-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201708230U CN202070201U (en) | 2011-05-18 | 2011-05-18 | Rotary solid-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202070201U true CN202070201U (en) | 2011-12-14 |
Family
ID=45108317
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201708230U Expired - Fee Related CN202070201U (en) | 2011-05-18 | 2011-05-18 | Rotary solid-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202070201U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102749439A (en) * | 2012-07-03 | 2012-10-24 | 长安大学 | Test and evaluation device for segregation of fresh concrete |
| CN111569479A (en) * | 2020-05-12 | 2020-08-25 | 张家港凯铭锌业有限公司 | Zinc oxide powder precipitation device |
-
2011
- 2011-05-18 CN CN2011201708230U patent/CN202070201U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102749439A (en) * | 2012-07-03 | 2012-10-24 | 长安大学 | Test and evaluation device for segregation of fresh concrete |
| CN102749439B (en) * | 2012-07-03 | 2015-04-22 | 长安大学 | Test and evaluation device for segregation of fresh concrete |
| CN111569479A (en) * | 2020-05-12 | 2020-08-25 | 张家港凯铭锌业有限公司 | Zinc oxide powder precipitation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111214 Termination date: 20120518 |