CN201981032U - Continuous seriflux flotation purifying processor - Google Patents
Continuous seriflux flotation purifying processor Download PDFInfo
- Publication number
- CN201981032U CN201981032U CN2011200839704U CN201120083970U CN201981032U CN 201981032 U CN201981032 U CN 201981032U CN 2011200839704 U CN2011200839704 U CN 2011200839704U CN 201120083970 U CN201120083970 U CN 201120083970U CN 201981032 U CN201981032 U CN 201981032U
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- CN
- China
- Prior art keywords
- slurries
- outer case
- seriflux
- good
- outlet
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- Expired - Fee Related
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Abstract
The utility model discloses a continuous seriflux flotation purifying processor which is characterized in that an outer box body is supported by a bracket, a seriflux balance cylinder is arranged in the middle part of the inner part of the outer box body, the periphery of the seriflux blance cylinder is provided with a good pulp cylinder, the upper end of the outer part of the good pulp cylinder is provided with a floating slag groove arranged around the good pulp cylinder, the bottom of the floating slag groove is connected with a floating slag outlet arranged at one side of the outer box body through pipes, the lower end of the outer part of the good pulp cylinder is provided with a conic air storing chamber arranged around the good pulp cylinder, the periphery of the conic air storing chamber is provided with a plurality of micro-air film pipes; with the adoption of above arrangements, the seriflux processed by the continuous seriflux flotation purifying processor is not only meet the standard of the required seriflux quality but also can be continuously discharged.
Description
Technical field
The utility model relates to a kind of continous way slurries floatation purification treatment facility, is the purifying treatment machine that a kind of greasy dirt, printing ink ion, cotton-shaped class and the irregular bag that can isolate continuously in the slurries held the weight material in slurries under the arm specifically.
Background technology
At present, handle the slurries purification apparatus that the slurries relevant industries generally adopt, its complex structure, floor space is big, cost is high, power consumption is high, generally adopt Wen Qiulishi and air-dissolved treatment process, cause impurity separating effect in the production process slurries, the rate of removing is low and go out slurries quality instability, and causes phenomenons such as environmental pollution easily.
Summary of the invention
In order to overcome above-mentioned shortcoming, it is high and go out the slurries steady quality that the purpose of this utility model provides a kind of rate of removing, and the continous way slurries floatation purification handler of non-environmental-pollution.
To achieve these goals, outer case of the present utility model is by stent support, bosom position in outer case is provided with the slurries surge drum, periphery at the slurries surge drum is provided with good slurry tube, be provided with around it scum silica frost groove in the outer upper ends of good slurry tube, the bottom of scum silica frost groove is connected with the scum silica frost outlet that is located at outer case one side by pipeline, be provided with taper air storage chamber around it in the outside lower end of good slurry tube, periphery at the taper air storage chamber is provided with many little air film pipes, inlet mouth is located at the bottom of taper air storage chamber, good slurries outlet is located at the bottom of slurries surge drum, manhole and sediment outlet are located at upper and lower one side of outer case respectively, slurry inlet is located at outside one side of outer case along tangent line, and the slurries vision slit is located at the outside opposite side of outer case, and tensimeter is located at top one side of outer case.
By above setting, the utility model has changed the processing mode with Wen Qiulishi and air-dissolved, and adopt the sudden and violent gas mode of totally-enclosed microporous membrane, slurries enter in the outer case and produce a large amount of microbubbles by many little air film pipes, in the process that microbubble rises, the greasy dirt in the slurries, printing ink ion and cotton-shaped light impurity thing are separated out with the slurries separation rapidly, be suspended in the slurries upper surface bubble and discharge automatically.Bottom then sinking, heavy hard impurity discharges at any time.The utility model is handled slurries, has both reached required slurries quality standard, again can continuous blow-down.
Description of drawings
Fig. 1, be the utility model cross-sectional view.
Fig. 2, be the schematic cross-section of the little air film pipe of the utility model.
Among the figure 1, outer case 2, support 3, slurries surge drum 4, good slurry tube 5, scum silica frost groove 6, scum silica frost outlet 7, taper air storage chamber 8, little air film pipe 9, inlet mouth 10, good slurries outlet 11, manhole 12, sediment outlet 13, slurry inlet 14, tensimeter 15, slurries vision slit 16, little pore 17, through hole 18, microporous membrane skeleton body
Embodiment
As Fig. 1, shown in 2, outer case 1 of the present utility model is supported by support 2, bosom position in outer case 1 is provided with slurries surge drum 3, periphery at slurries surge drum 3 is provided with good slurry tube 4, be provided with around it scum silica frost groove 5 in the outer upper ends of good slurry tube 4, the bottom of scum silica frost groove 5 is connected with the scum silica frost outlet 6 that is located at outer case 1 one sides by pipeline, be provided with taper air storage chamber 7 around it in the outside lower end of good slurry tube 4, periphery at taper air storage chamber 7 is provided with many little air film pipes 8, inlet mouth 9 is located at the bottom of taper air storage chamber 7, good slurries outlet 10 is located at the bottom of slurries surge drum 3, manhole 11 and sediment outlet 12 are located at upper and lower one side of outer case 1 respectively, slurry inlet 13 is located at outside one side of outer case 1 along tangent line, slurries vision slit 15 is located at the outside opposite side of outer case, and tensimeter 14 is located at top one side of outer case 1.Be provided with microporous membrane skeleton body 18 in the inside of described little air film pipe 8, a plurality of little pores 16 are located on the outer wall of little air film pipe 8.
By above setting, the utility model adopts totally enclosed, in the outer case 1 micro-pressure is arranged during normal the operation, when slurries enter outer case 1 from slurry inlet 13, slurries are done tangent line along outer case 1 inwall in the direction of the clock and are flowed, separate out a large amount of microbubbles by little air film pipe 8, in the microbubble uphill process, form foam, with the printing ink in the slurries, the greasy dirt ion, bag such as floss and light impurity is held under the arm in foam, and foam constantly separates under the effect of minute-pressure, come-up enters scum silica frost groove 5, overflowed continuously outside the outer case 1 by scum silica frost outlet 6, heavy hard impurity thing outer case 1 bottom that then sinks is discharged outside the outer case 1 by sediment outlet 12, slurries then enter good slurry tube 4 inside by a plurality of through holes 17 of good slurry tube 4 bottoms, overflow into slurries surge drum 3, behind the current stabilization, slurries are discharged by the good slurries outlet 10 of slurries surge drum 3 bottoms.
Claims (2)
1. continous way slurries floatation purification handler, it is characterized in that: outer case is by stent support, bosom position in outer case is provided with the slurries surge drum, periphery at the slurries surge drum is provided with good slurry tube, be provided with around it scum silica frost groove in the outer upper ends of good slurry tube, the bottom of scum silica frost groove is connected with the scum silica frost outlet that is located at outer case one side by pipeline, be provided with taper air storage chamber around it in the outside lower end of good slurry tube, periphery at the taper air storage chamber is provided with many little air film pipes, inlet mouth is located at the bottom of taper air storage chamber, good slurries outlet is located at the bottom of slurries surge drum, manhole and sediment outlet are located at upper and lower one side of outer case respectively, slurry inlet is located at outside one side of outer case along tangent line, and the slurries vision slit is located at the outside opposite side of outer case, and tensimeter is located at top one side of outer case.
2. continous way slurries floatation purification handler according to claim 1 is characterized in that: be provided with the microporous membrane skeleton body in the inside of described little air film pipe, a plurality of little pores are located on the outer wall of little air film pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200839704U CN201981032U (en) | 2011-03-15 | 2011-03-15 | Continuous seriflux flotation purifying processor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200839704U CN201981032U (en) | 2011-03-15 | 2011-03-15 | Continuous seriflux flotation purifying processor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201981032U true CN201981032U (en) | 2011-09-21 |
Family
ID=44608496
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200839704U Expired - Fee Related CN201981032U (en) | 2011-03-15 | 2011-03-15 | Continuous seriflux flotation purifying processor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201981032U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110841806A (en) * | 2019-11-21 | 2020-02-28 | 清华大学 | Flotation method for fine particle mineral powder |
-
2011
- 2011-03-15 CN CN2011200839704U patent/CN201981032U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110841806A (en) * | 2019-11-21 | 2020-02-28 | 清华大学 | Flotation method for fine particle mineral powder |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110921 Termination date: 20180315 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |