CN202237396U - Water-steam separation device for processing backwashing wastewater of high-speed filter - Google Patents
Water-steam separation device for processing backwashing wastewater of high-speed filter Download PDFInfo
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- CN202237396U CN202237396U CN2011203866440U CN201120386644U CN202237396U CN 202237396 U CN202237396 U CN 202237396U CN 2011203866440 U CN2011203866440 U CN 2011203866440U CN 201120386644 U CN201120386644 U CN 201120386644U CN 202237396 U CN202237396 U CN 202237396U
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Abstract
The utility model discloses a water-steam separation device for processing backwashing wastewater of a high-speed filter, and belongs to the field of a physical measurement device. The device comprises a water inlet pipe, a water outlet pipe and an exhaust pipe, wherein the air inlet of the exhaust pipe is communicated with the upper part of the water inlet pipe; the water inlet of the water outlet pipe is communicated with the lower part of the water inlet pipe; and more than one gas condensation plate is arranged in the exhaust pipe. The water-steam separation device has a simple structure, is used for easily separating liquid and gas in wastewater and condensing the gas to keep the liquid as much as possible and reduce waste of water resources, has the advantages of low cost, small volume, small floor space and less investment, requires no additional investment in the using process, and realizes water consumption reduction and production cost reduction.
Description
Technical field
The utility model belongs to physical measurement device field, particularly a kind of moisture separator of handling the high rate filter backwash waste.
Background technology
In the past in the continuous casting installation for casting running, high rate filter backwash in per 24 hours once, the water spot of no use of the waste water after the backwash can only be drained in vain.Be energy savings; Reduce and consume; Existing conticaster recirculated water has high rate filter and chemical oil remover equipment, is connected on the backwash blow-off pipe of high rate filter on the chemical oil remover inlet channel, can be with the waste water recycling after the high rate filter backwash; Backwash sewage is the same with eddy flow well backwater, in chemical oil remover, handle backwash sewage well through modes such as dosing, deposition, blowdowns.Yet high rate filter needs to feed compressed air in backwash process, utilizes compressed air to break up closely knit filtering layer; And adopt water flushing, gas flushing and the blending rinsed method of air water to make the mutual rubbing of filtrate; Let the dirt that is adsorbed on the filtrate break away from, water backwash again could thoroughly be disposed the suspension that is adsorbed on the filtrate; And, so just realized that filtrate removes the function of suspension, backwash and regeneration utilization with outside its discharge high rate filter.So, be mixed with gas in the backwash sewage of entering chemical oil remover, can cause the fluctuation of chemical oil remover inner aqueous layer big, influence purification of water quality and effect.
The utility model content
The technical problem that the utility model will solve provides and a kind ofly can be easily the liquids and gases in the waste water is separated, liquid has been made full use of and avoided owing to there is the moisture separator of the too fast processing high rate filter backwash waste that next link is exerted an influence of gas and flow rate of liquid.
For solving the problems of the technologies described above, the technical scheme that the utility model adopts is: a kind of moisture separator of handling the high rate filter backwash waste comprises water inlet pipe, outlet pipe and blast pipe; The air inlet of said blast pipe is connected with the top of water inlet pipe, and the water inlet of said outlet pipe is connected with the bottom of water inlet pipe; Be provided with an above condensation of gas plate in the said blast pipe.
Said outlet pipe and blast pipe are all perpendicular to water inlet pipe, and the air inlet of said blast pipe is connected with the water inlet of outlet pipe.
The bottom-up first condensation of gas plate and the second condensation of gas plate of being provided with in said blast pipe.
The said first condensation of gas plate is the annular plate that is provided with along the blast pipe inwall, and said second separating plate is taper, and its outward flange is connected with the inwall of blast pipe through an above dowel.
The first condensation of gas plate is the annular plate that is provided with along the blast pipe inwall, and said second separating plate is the conical plate that has steam vent, and its outward flange is connected with the inwall of blast pipe.
Be provided with the 3rd condensation of gas plate on the top of said blast pipe, said the 3rd condensation of gas plate is provided with steam vent.
Be provided with main delivery port and side delivery port in the said outlet pipe.
The cross section of said water inlet pipe, outlet pipe and blast pipe is circular.
The technological progress of adopting technique scheme to obtain is: the utility model is simple in structure, can easily the liquids and gases in the waste water be separated, and with condensation of gas, keep liquid as much as possible, reduces water resource waste; And the utility model is with low cost, and volume is little, takes up an area of to lack, and small investment does not in use have any additional investment again, also can reduce the water consumption, reduces production costs; This utility model makes the backwash waste of high rate filter not contain gas when getting into chemical oil remover as far as possible; And regulated the speed that liquid gets into chemical oil remover; When having guaranteed that backwash sewage gets into chemical oil remover, can not produce huge fluctuation and cause water quality muddy the water surface in the oil expeller; Through this utility model, the separated and discharge of the gas in the backwash sewage, the purified treatment of the calmness in chemical oil remover of the liquid in the backwash sewage guarantees circulating water quality, has reduced energy consumption.
Description of drawings
Fig. 1 is the structural representation of the utility model;
Fig. 2 be Fig. 1 along A-A to cutaway view;
Fig. 3 be Fig. 1 along B-B to cutaway view;
Wherein, the 1, the 3rd condensation of gas plate, 2, the second condensation of gas plate, 3, the first condensation of gas plate, 4, outlet pipe, 5, the side delivery port, 6, steam vent, 7, blast pipe, 8, water inlet pipe, 9, main delivery port.
The specific embodiment
Can know to embodiment shown in Figure 3 according to Fig. 1, handle the moisture separator of high rate filter backwash waste, comprise water inlet pipe 8, outlet pipe 4 and blast pipe 7; The air inlet of said blast pipe 7 is connected with the top of water inlet pipe 8; Said outlet pipe 4 and blast pipe 7 are all perpendicular to water inlet pipe 8; And the air inlet of said blast pipe 7 is connected with the water inlet of outlet pipe 4, and the air inlet of the delivery port of said water inlet pipe 8, blast pipe 7 is connected with the water inlet of outlet pipe 4; The bottom-up first condensation of gas plate 3, the second condensation of gas plate 2 and the 3rd condensation of gas plate 1 of being provided with on the said blast pipe 7; The said first condensation of gas plate 3 is the annular plate that is provided with along blast pipe 7 inwalls; Said second separating plate 2 is a conical plate; And its outward flange is connected with the inwall of blast pipe 7 through four dowels; Be to be provided with the gap between the inwall of outward flange and blast pipe 7 of the said second condensation of gas plate 2 to make things convenient for gas to pass through, said the 3rd condensation of gas plate 1 is positioned at the top of blast pipe 7, and said the 3rd condensation of gas plate 1 is provided with steam vent 6; Be provided with main delivery port 9 and side delivery port 5 in the said outlet pipe 4; The cross section of said water inlet pipe 8, outlet pipe 4, blast pipe 7 and main delivery port 9 is circular.
The utility model adopts the steel plate welding to process.
The water inlet pipe 8 of the utility model is connected with the outlet of high rate filter, accepts the backwash waste that high rate filter is discharged, and this waste water has temperature, so it is the amalgam of liquid water and waste exhaust gases.Backwash waste gets into drainpipe 4 and blast pipe 7 through behind the water inlet pipe 8, because the gravity effect, liquid water can flow to drainpipe 4, and the waste gas body then can move upward along blast pipe 7.The waste gas body runs into condensation liquefy water behind the condensation of gas plate in motion process, this aqueous water can be blended in the liquid along the sidewall of blast pipe 7, and can flow out along drainpipe 4.The liquid water that flows out from drainpipe 4 gets into chemical oil remover equipment.For the liquid in the chemical oil remover equipment is influenced by the liquid in the drainpipe 4, in drainpipe 4, be provided with main delivery port 9 and side delivery port 5.Very fast from the aqueous water flow velocity that main discharge outlet 9 flows out, it gets into chemical oil remover from the bottom, can the water in the chemical oil remover not stired and make muddy like this; The aqueous water flow velocity that from side delivery port 5, flows out is lower, can also can not stir and make muddy the inner water of chemical oil remover directly from the top entering of chemical oil remover.Like this, the waste water of discharging in the high rate filter has obtained utilizing fully again, has reduced the water consumption, has reduced production cost; And the water that from high rate filter, flows out can not impact the water surface in the chemical oil remover, causes water quality to become muddy, guarantees that sewage purifies smoothly.
On said blast pipe 7, be provided with an above condensation of gas plate, guaranteeing overflowing simultaneously of gas, can also keep more liquid like this, play the effect of saving.
In outlet pipe 4, a delivery port can only be arranged, can also be provided with a plurality of delivery ports, help the outflow of liquid like this.
Claims (8)
1. a moisture separator of handling the high rate filter backwash waste is characterized in that comprising water inlet pipe (8), outlet pipe (4) and blast pipe (7); The air inlet of said blast pipe (7) is connected with the top of water inlet pipe (8), and the water inlet of said outlet pipe (4) is connected with the bottom of water inlet pipe (7); Be provided with an above condensation of gas plate in the said blast pipe (7).
2. a kind of moisture separator of handling the high rate filter backwash waste according to claim 1; It is characterized in that said outlet pipe (4) and blast pipe (7) all perpendicular to water inlet pipe (8), and the air inlet of said blast pipe (7) is connected with the water inlet of outlet pipe (4).
3. a kind of moisture separator of handling the high rate filter backwash waste according to claim 1 and 2 is characterized in that the bottom-up first condensation of gas plate (3) and the second condensation of gas plate (2) of being provided with in said blast pipe (7).
4. a kind of moisture separator of handling the high rate filter backwash waste according to claim 3; It is characterized in that the annular plate of the said first condensation of gas plate (3) for being provided with along blast pipe (7) inwall; Said second separating plate (2) is taper, and its outward flange is connected through the inwall of an above dowel with blast pipe (7).
5. a kind of moisture separator of handling the high rate filter backwash waste according to claim 3; It is characterized in that the annular plate of the said first condensation of gas plate (3) for being provided with along blast pipe (7) inwall; Said second separating plate (2) is the conical plate that has steam vent, and its outward flange is connected with the inwall of blast pipe (7).
6. according to claim 4 or 5 described a kind of moisture separators of handling the high rate filter backwash waste; It is characterized in that being provided with the 3rd condensation of gas plate (1) on the top of said blast pipe (7), said the 3rd condensation of gas plate (1) is provided with steam vent (6).
7. according to claim 1 or 2 or 4 or 5 described a kind of moisture separators of handling the high rate filter backwash waste, it is characterized in that being provided with in the said outlet pipe main delivery port (9) and side delivery port (5).
8. according to claim 1 or 2 or 4 or 5 described a kind of moisture separators of handling the high rate filter backwash waste, the cross section that it is characterized in that said water inlet pipe (8), outlet pipe (4) and blast pipe (7) is for circular.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203866440U CN202237396U (en) | 2011-10-12 | 2011-10-12 | Water-steam separation device for processing backwashing wastewater of high-speed filter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011203866440U CN202237396U (en) | 2011-10-12 | 2011-10-12 | Water-steam separation device for processing backwashing wastewater of high-speed filter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202237396U true CN202237396U (en) | 2012-05-30 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011203866440U Expired - Fee Related CN202237396U (en) | 2011-10-12 | 2011-10-12 | Water-steam separation device for processing backwashing wastewater of high-speed filter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202237396U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105627009A (en) * | 2016-03-22 | 2016-06-01 | 江苏沁尔康环境电器有限公司 | Waterway integrated fission |
| CN106116006A (en) * | 2016-03-22 | 2016-11-16 | 江苏沁尔康环境电器有限公司 | A kind of water purifier |
-
2011
- 2011-10-12 CN CN2011203866440U patent/CN202237396U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105627009A (en) * | 2016-03-22 | 2016-06-01 | 江苏沁尔康环境电器有限公司 | Waterway integrated fission |
| CN106116006A (en) * | 2016-03-22 | 2016-11-16 | 江苏沁尔康环境电器有限公司 | A kind of water purifier |
| CN105627009B (en) * | 2016-03-22 | 2018-01-30 | 江苏沁尔康环境电器有限公司 | A kind of water route collection split |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120530 Termination date: 20161012 |