CN210915406U - Air-float purifying equipment - Google Patents
Air-float purifying equipment Download PDFInfo
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- CN210915406U CN210915406U CN201921975117.6U CN201921975117U CN210915406U CN 210915406 U CN210915406 U CN 210915406U CN 201921975117 U CN201921975117 U CN 201921975117U CN 210915406 U CN210915406 U CN 210915406U
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Abstract
The utility model discloses an air supporting clarification plant, including adjacent coagulation reaction district, contact reaction district, dross disengagement zone and the clear water district that sets up in proper order, the clear water district is through wet return connection dissolved air pump, dissolved air pump is through dissolved air outlet pipe intercommunication gas-liquid separator jar, gas-liquid separator jar is through releasing water pipe intercommunication dissolved air water releaser, dissolved air water releaser sets up contact reaction district bottom, dross disengagement zone top is provided with scrapes the foam maker, dross disengagement zone bottom is provided with the siltation district, the siltation district with the dross disengagement zone passes through isolating device intercommunication or separates, the siltation district is provided with row's silt pipe. The utility model provides an air supporting clarification plant separates siltation district and dross disengagement zone through isolating device, and the silt in siltation district is got rid of through arranging the silt pipe, prevents that silt from being inhaled by the collector pipe and arrives the clear water district side by side, ensures that air supporting clarification plant exhaust clear water reaches emission standard.
Description
Technical Field
The utility model belongs to the technical field of industrial sewage treatment technique and specifically relates to an air supporting clarification plant is related to.
Background
The air-float purifying equipment is a water treatment equipment which can make air pass through or produce lots of fine bubbles in water to make air be attached to suspended particles in the form of high-dispersion fine bubbles to make the density be less than that of water, and utilize buoyancy principle to make it float on the water surface, and the suspended particles are accumulated to form lots of floating slags to float on the water surface, then the floating slags are removed by foam-scraping machine so as to implement solid-liquid separation. The air-flotation purification device is particularly suitable for the separation of very fine particles with a particle density close to or less than 1. The scum of the air floatation purifying equipment can not be scraped completely by the scum scraping machine, the scum remaining on the water surface sinks to the bottom of the scum separation area along with the breaking of bubbles, and the sunk scum is sucked by the water collecting pipe at the bottom of the scum separation area along with the fluctuation of water flow and is discharged into the clear water area, so that the water is discharged with the sludge. The phenomenon is particularly remarkable on small-water-volume air-floating purification equipment, and directly influences the quality of effluent and the standard discharge effect.
In view of the above-mentioned phenomena, it is a common practice to arrange a conical hopper at the bottom of the scum separation area and periodically discharge the residual sludge; secondly, the container pump and the slag scraping device are closed in a delayed mode after the sewage inlet pipe is closed, and scum on the surface is scraped to the maximum extent; thirdly, when the mud is discharged, the machine is stopped to empty the separation area and the clean water area, and clean tap water is refilled. The first method works well, but increases the complexity and cost of the equipment; the second method only relatively prolongs the effective running time and does not thoroughly solve the problem; the third method, though thorough, is not controllable and wastes water resources, increasing operating costs.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide an air supporting clarification plant, the sediment of automatic clearance income dross disengagement zone bottom ensures that air supporting purifier exhaust clear water reaches emission standard.
In order to achieve the purpose, the utility model provides an air supporting clarification plant, including coagulation reaction district, contact reaction district, dross disengagement zone and the clear water district of adjacent setting in proper order, the clear water district is through wet return connection dissolved air pump, dissolved air pump is through dissolving gas outlet pipe intercommunication gas-liquid separator jar, gas-liquid separator jar is through releasing water pipe intercommunication dissolved air water releaser, dissolved air water releaser sets up contact reaction district bottom, dross disengagement zone top is provided with the froth scraper, dross disengagement zone bottom is provided with the siltation district, the siltation district with the dross disengagement zone passes through isolating device intercommunication or separates, the siltation district is provided with row's silt pipe.
Optionally, the separating means is a shutter, and translation of the shutter can connect or separate the fouling zone and the scum separating zone.
Optionally, the separating device is a grid plate, the grid plate is formed by splicing a plurality of grid bars, and the grid bars are rotated to be spaced from each other or contacted with each other, so that the deposition area and the scum separation area are communicated or separated.
Optionally, the siltation area is communicated with the contact reaction area through a flushing sewage pipe, and the flushing sewage pipe is provided with a flushing sewage solenoid valve.
Optionally, the siltation area is provided with a waterproof vent valve, and the waterproof vent valve and the silt discharge pipe are arranged at intervals.
Optionally, a coagulation water outlet pipe is arranged above the dissolved gas water releaser, and the contact reaction area is communicated with the coagulation reaction area through the coagulation water outlet pipe.
Optionally, a stirring device is arranged in the coagulation reaction zone, and the coagulation reaction zone is filled with water through a sewage pipe.
Optionally, the lower part of the scum separation zone and the lower part of the contact reaction zone are separated by a guide plate, and the upper part of the scum separation zone is communicated with the upper part of the contact reaction zone.
Optionally, be provided with between the dross disengagement zone with the clear water district and be used for collecting the dross collecting region through the dross that the scum machine scraped off, the dross collecting region is provided with the scum pipe.
The utility model provides an air supporting clarification plant is including adjacent coagulation reaction district, contact reaction district, dross disengagement zone and the clear water district that sets up in proper order, the clear water district passes through wet return coupling dissolved air pump, dissolved air pump is through dissolving gas outlet pipe intercommunication gas-liquid separator jar, gas-liquid separator jar is through releasing water pipe intercommunication dissolved air water releaser, dissolved air water releaser sets up contact reaction district bottom, dross disengagement zone top is provided with the froth scraper, dross disengagement zone bottom is provided with the siltation district, the siltation district with the dross disengagement zone passes through isolating device intercommunication or separates, the siltation district is provided with row's silt pipe. The utility model provides an air supporting clarification plant separates siltation district and dross disengagement zone through isolating device, and the silt in siltation district is got rid of through arranging the silt pipe, prevents that silt from being inhaled by the collector pipe and arrives the clear water district side by side, ensures that air supporting clarification plant exhaust clear water reaches emission standard.
Drawings
FIG. 1 is a schematic view of an air flotation purification apparatus according to an embodiment of the present invention;
FIG. 2 is a schematic view of a grating plate in a closed state;
fig. 3 is a schematic view of a grating plate in an open state.
Wherein: 1-coagulation reaction zone, 2-contact reaction zone, 3-scum separation zone, 4-scum collection zone, 5-clear water zone, 6-siltation zone, 7-foam scraper, 8-dissolved air pump, 9-gas-liquid separator tank, 10-dissolved air water releaser, 11-return pipe, 12-return electromagnetic valve, 13-dissolved air outlet pipe, 14-release outlet pipe, 15-release electromagnetic valve, 16-sludge discharge pipe, 17-waterproof vent valve, 18-grid plate, 181-grid bar, 182-rotating shaft, 183-driving belt, 19-flushing sewage discharge pipe, 20-flushing sewage discharge electromagnetic valve, 21-coagulation outlet pipe, 22-stirring device, 23-sewage pipe, 24-guide plate, 25-slag discharge pipe, 26-a water collecting pipe, 27-a water collecting electromagnetic valve, 28-a clean water pipe, 29-a throttle valve, 30-a vent pipe, 31-an automatic exhaust valve and 32-a frame.
Detailed Description
The following description of the embodiments of the present invention will be described in more detail with reference to the drawings. Advantages and features of the present invention will become apparent from the following description and claims. It should be noted that the drawings are in simplified form and are not to precise scale, and are provided for convenience and clarity in order to facilitate the description of the embodiments of the present invention.
The utility model provides an air supporting clarification plant, figure 1 is the utility model discloses an air supporting purifier schematic diagram that embodiment provided refers to figure 1, air supporting clarification plant includes: the coagulation reaction area 1, the contact reaction area 2, the scum separation area 3 and the clear water area 5 are adjacently arranged in sequence, sewage is led into the coagulation reaction area 1 through a sewage pipe 23, and ions in the sewage react with the input medicines to form fine suspended particles. A stirring device 22 is arranged in the coagulation reaction zone 1, and the stirring device 22 enables sewage and the added medicines to uniformly and rapidly react. The lower part of the scum separation zone 3 is separated from the lower part of the contact reaction zone 2 by a guide plate 24, and the upper part of the scum separation zone 3 is communicated with the upper part of the contact reaction zone 2. The top of the scum separation area 3 is provided with a scum scraper 7, a scum collection area 4 used for collecting scum scraped by the scum scraper 7 is arranged between the scum separation area 3 and the clear water area 5, and the scum collection area 4 is provided with a scum discharge pipe 25. The clear water area 5 is provided with a clear water pipe 28 for discharging clear water, and the clear water pipe 28 is provided with a throttle valve 29. The clean water area is communicated with the scum separation area 3 through a water collecting pipe 26, and a water collecting electromagnetic valve 27 is arranged on the water collecting pipe 26.
Clear water district 5 connects dissolved air pump 8 through wet return 11, be provided with backward flow solenoid valve 12 on the wet return 11, be provided with breather pipe 30 intercommunication atmosphere on the dissolved air pump 8, dissolve in air pump 8 can be with the clear water suction pump in clear water district 5, the negative pressure that the impeller of high-speed rotation produced in the pump also mixes the air with the clear water in passing through breather pipe 30 suction pump simultaneously, forms high pressure dissolved air water. The dissolved air pump 8 is communicated with a gas-liquid separator tank 9 through a dissolved air water outlet pipe 13, the gas-liquid separator tank 9 is communicated with a dissolved air water releaser 10 through a release water pipe 14, and the dissolved air water releaser 10 is arranged at the bottom of the contact reaction zone 2. An automatic exhaust valve 31 is arranged at the top of the gas-liquid separator tank 9, and a release electromagnetic valve 15 is arranged on the release water outlet pipe 14. A coagulation water outlet pipe 21 is arranged above the dissolved gas water releaser 10, and the contact reaction area 2 is communicated with the coagulation reaction area 1 through the coagulation water outlet pipe 21. The bottom of the scum separation area 3 is provided with a deposition area 6, the deposition area 6 and the scum separation area 3 are communicated or separated through an isolating device, and the deposition area 6 is provided with a sludge discharge pipe 16.
The isolating device is a shutter plate, and the siltation area and the scum separation area can be communicated or separated by translating the shutter plate. Fig. 2 is a schematic view of a grid plate in a closed state, fig. 3 is a schematic view of a grid plate in an open state, see fig. 1-3, the separating device is a grid plate 18, the grid plate 18 is formed by splicing a plurality of grid bars 181, the cross section of the grid bars 181 is in a diamond shape, and the plurality of grid bars 181 are spliced in contact with each other to form the separating device to separate the sedimentation zone 6 from the scum separation zone 3. When the grating 181 is rotated, the grating 181 is spaced apart, in the form of louvers, to connect the sedimentation zone 6 to the dross separation zone 3. The sedimentation zone 6 is communicated with the contact reaction zone 2 through a flushing sewage discharge pipe 19, and the flushing sewage discharge pipe 19 is provided with a flushing sewage discharge electromagnetic valve 20. The siltation area 6 is provided with a waterproof vent valve 17, and the waterproof vent valve 17 and the silt discharge pipe 16 are arranged at intervals. One end of the grid bar 181 is provided with a rotating shaft 182, the rotating shaft 182 is arranged outside the scum separation area 3 and the deposition area 6, and the rotating shaft 182 is in transmission connection through a transmission belt 183.
The utility model provides an air supporting clarification plant during operation, start dissolved air pump 8, the clear water of clear water district 5 is in the pump is inhaled through back flow 11 by dissolved air pump 8 this moment, the negative pressure that high-speed rotatory impeller produced in the pump is simultaneously also mixed with the clear water in passing through breather pipe 30 suction pump, form high-pressure dissolved air water, high-pressure dissolved air water gets into gas-liquid separation jar 9 through dissolved air water outlet pipe 13, gas-liquid separation jar 9 releases high-pressure dissolved air water to contact reaction district 21 bottom through releasing water pipe 14 and dissolved air water releaser 10, dissolved air water releaser 10 releases high-pressure dissolved air water to contact reaction district 21 bottom, form continuous intensive microbubble and rise gradually in the contact reaction district; sewage is led into the coagulation reaction zone 1 through a sewage pipe 23, ions in the sewage react with the input drugs to form fine suspended particles, and the sewage containing the fine suspended particles in the coagulation reaction zone 1 enters the contact reaction zone 2 through a coagulation water outlet pipe 21; tiny suspended solid particles and microbubble contact come-up, get into dross separation zone 3 jointly, accomplish solid-liquid separation, and the dross of solid is scraped into dross collecting region 4 through scraping the foam machine 7, discharges through scum pipe 25, and mud cake further processing is made through the dehydration again, and the clear water of dross separation zone 3 passes through collector pipe 26 and gets into clear water district 5, and the clear water is most to be discharged through clear water pipe 28, and the minority is passed through back flow 11 and is recycled.
Air supporting clarification plant's dross can't all scrape totally through scum machine 7, remaining dross will get into the siltation district 6 along with the breaing out of bubble through grid plate 18 on the surface of water, the silt when siltation district 6 gathers to certain extent, grid plate 18 is closed and is distinguished siltation district 6 and dross disengagement zone 3 partition, silt is got rid of through arranging silt pipe 16, through waterproof breather valve 17 balanced pressure during the elimination, most silt is got rid of the back through arranging silt pipe 16, open grid plate 18 slightly, the clear water gets into and washes siltation district 6, the sewage of taking silt after washing is through washing 19 secondary purification of blow off pipe.
In summary, the embodiment of the present invention provides an air-floating purification apparatus, which includes: coagulation reaction district 1, contact reaction district 2, dross disengagement zone 3 and the clear water district 5 that adjacent set up in proper order, clear water district 5 passes through wet return 11 and connects dissolved air pump 8, dissolved air pump 8 is through dissolved air outlet pipe 13 intercommunication gas-liquid separator jar 9, gas-liquid separator jar 9 is through releasing water pipe 14 intercommunication dissolved air water releaser 10, dissolved air water releaser 10 sets up contact reaction district 2 bottoms, dross disengagement zone 3 tops are provided with scum 7, dross disengagement zone bottom is provided with siltation district 6, siltation district 6 with dross disengagement zone 3 passes through isolating device intercommunication or partition, siltation district 6 is provided with row's silt pipe 16. The utility model provides an air supporting clarification plant separates siltation district and dross disengagement zone through isolating device, and the silt in siltation district is got rid of through arranging the silt pipe, prevents that silt from being inhaled by the collector pipe and arrives the clear water district side by side, ensures that air supporting clarification plant exhaust clear water reaches emission standard.
The above description is only for the preferred embodiment of the present invention, and does not limit the present invention. Any technical personnel who belongs to the technical field, in the scope that does not deviate from the technical scheme of the utility model, to the technical scheme and the technical content that the utility model discloses expose do the change such as the equivalent replacement of any form or modification, all belong to the content that does not break away from the technical scheme of the utility model, still belong to within the scope of protection of the utility model.
Claims (9)
1. An air-flotation purification apparatus, comprising: the coagulation reaction district, contact reaction district, dross disengagement zone and the clear water district that adjacent set up in proper order, the clear water district passes through wet return coupling dissolved air pump, dissolved air pump is through dissolving gas outlet pipe intercommunication gas-liquid separator jar, gas-liquid separator jar is through releasing water pipe intercommunication dissolved air water releaser, dissolved air water releaser sets up contact reaction district bottom, dross disengagement zone top is provided with the froth scraper, dross disengagement zone bottom is provided with the siltation district, the siltation district with the dross disengagement zone passes through isolating device intercommunication or separates, the siltation district is provided with row's silt pipe.
2. The air flotation purification apparatus according to claim 1, wherein the separation device is a shutter, and wherein the displacement of the shutter enables communication or separation between the fouling zone and the froth separation zone.
3. The air-flotation purification apparatus according to claim 1, wherein the separation device is a grid plate formed by a plurality of grid strips, and the grid strips are rotated to be spaced apart or in contact with each other, thereby communicating or separating the deposition zone and the froth separation zone.
4. The air-flotation purification equipment as recited in claim 2 or 3, wherein the siltation area is communicated with the contact reaction area through a flushing sewage discharge pipe, and a flushing sewage discharge electromagnetic valve is arranged on the flushing sewage discharge pipe.
5. The air-flotation purification apparatus according to claim 1, wherein the siltation area is provided with a waterproof vent valve spaced from the sludge discharge pipe.
6. The air-flotation purification equipment as claimed in claim 1, wherein a coagulation water outlet pipe is arranged above the dissolved gas water releaser, and the contact reaction zone and the coagulation reaction zone are communicated through the coagulation water outlet pipe.
7. The air-flotation purification device according to claim 1, wherein a stirring device is arranged in the coagulation reaction zone, and the coagulation reaction zone is filled with water through a sewage pipe.
8. The air flotation purification apparatus according to claim 1, wherein the lower portion of the froth separation zone and the lower portion of the contact reaction zone are separated by a baffle plate, and the upper portion of the froth separation zone and the upper portion of the contact reaction zone are in communication.
9. The air-flotation purification apparatus according to claim 1, wherein a scum collection area is arranged between the scum separation area and the clean water area, and the scum collection area is provided with a scum discharge pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921975117.6U CN210915406U (en) | 2019-11-15 | 2019-11-15 | Air-float purifying equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921975117.6U CN210915406U (en) | 2019-11-15 | 2019-11-15 | Air-float purifying equipment |
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| Publication Number | Publication Date |
|---|---|
| CN210915406U true CN210915406U (en) | 2020-07-03 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201921975117.6U Active CN210915406U (en) | 2019-11-15 | 2019-11-15 | Air-float purifying equipment |
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| CN (1) | CN210915406U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112850963A (en) * | 2021-01-21 | 2021-05-28 | 山东共享环境管理咨询有限公司 | Sewage filtering and deslagging device |
-
2019
- 2019-11-15 CN CN201921975117.6U patent/CN210915406U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112850963A (en) * | 2021-01-21 | 2021-05-28 | 山东共享环境管理咨询有限公司 | Sewage filtering and deslagging device |
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