CN2761594Y - Program control pulse flushing type high turbidity integrated water purifier - Google Patents
Program control pulse flushing type high turbidity integrated water purifier Download PDFInfo
- Publication number
- CN2761594Y CN2761594Y CNU2005200329547U CN200520032954U CN2761594Y CN 2761594 Y CN2761594 Y CN 2761594Y CN U2005200329547 U CNU2005200329547 U CN U2005200329547U CN 200520032954 U CN200520032954 U CN 200520032954U CN 2761594 Y CN2761594 Y CN 2761594Y
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- Prior art keywords
- pipe
- water
- reaction chamber
- clarification
- tube
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 43
- 238000011010 flushing procedure Methods 0.000 title abstract description 6
- 238000006243 chemical reaction Methods 0.000 claims abstract description 23
- 238000005352 clarification Methods 0.000 claims abstract description 15
- 238000005273 aeration Methods 0.000 claims abstract description 14
- 238000009826 distribution Methods 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims abstract description 3
- 239000000706 filtrate Substances 0.000 claims description 14
- 239000000919 ceramic Substances 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- 229920006327 polystyrene foam Polymers 0.000 claims description 3
- 230000000630 rising effect Effects 0.000 claims description 3
- 239000010802 sludge Substances 0.000 claims description 3
- 238000003860 storage Methods 0.000 claims description 2
- 239000000463 material Substances 0.000 abstract description 8
- 239000010840 domestic wastewater Substances 0.000 abstract 1
- 239000010842 industrial wastewater Substances 0.000 abstract 1
- 238000004062 sedimentation Methods 0.000 abstract 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000011403 purification operation Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Biological Treatment Of Waste Water (AREA)
Abstract
本实用新型公开了一种程控脉冲冲洗型高浊度一体化净水器，属于水处理设备；旨在提供一种既能除浊又可去除有机污染，能够产生气垫脉冲冲洗滤料，自动化程度较高的一体化净水器。包括反应、澄清、沉淀及过滤部分，反应室和输泥管固定在本体内，中央集泥斗通过输泥管固定在反应室内，进水管、排泥管与反应室、环行输泥管连通；澄清环板上方有澄清水管；斜管托架上有斜管，该管上方有空气管及带曝气头并与输气管连通的布气管；空气管的上端有电磁阀、下端与进气管和冲洗排水管连通；曝气头的上方有滤头板、与出水槽连通的集水槽，出水槽与出水管连通；滤头板与曝气头之间有滤料，滤料的上、下方有液位传感器。本实用新型主要用于处理工业或生活废水。
The utility model discloses a program-controlled pulse flushing type high-turbidity integrated water purifier, which belongs to water treatment equipment; it aims to provide a filter material capable of removing turbidity and organic pollution, capable of generating air cushion pulse flushing, and has a high degree of automation. Higher integrated water purifier. Including the reaction, clarification, sedimentation and filtration parts, the reaction chamber and the mud delivery pipe are fixed in the body, the central mud collection hopper is fixed in the reaction chamber through the mud delivery pipe, and the water inlet pipe and the mud discharge pipe are connected with the reaction chamber and the circular mud delivery pipe; There is a clarification water pipe above the clarification ring plate; there is an inclined pipe on the inclined pipe bracket, and above the pipe is an air pipe and an air distribution pipe with an aeration head and connected with the air pipe; the upper end of the air pipe has a solenoid valve, and the lower end is connected to the air intake pipe and The flushing drainage pipe is connected; above the aeration head, there is a filter head plate and a sump connected to the water outlet tank, and the water outlet tank is connected to the water outlet pipe; there is a filter material between the filter head plate and the aeration head, and there is a filter material above and below the filter material. liquid level sensor. The utility model is mainly used for treating industrial or domestic waste water.
Description
Technical field: the utility model relates to a kind for the treatment of plant that can carry out turbidity removal and biochemical treatment to the former water of high turbidity, organically-polluted water, relates in particular to the high turbidity integral water purifier of a kind of program control pulse wash type.
Background technology: at present, widely popular light filter material integral water purifier mostly adopts fixing porous water pipe to add mechanical stirring or washes the lightweight floating filter material with rotating the mode that perforated tube sprays water, can only turbidity removal, and it is extremely low to the clearance of BOD in the organically-polluted water and COD, and mostly be manual operation, complicated operation.
Summary of the invention: in order to overcome the deficiencies in the prior art, the utility model aims to provide a kind ofly can turbidity removal can remove organic contamination again, and can utilize electric time variable control to produce air cushion pulse flushing filtrate, integral water purifier easy and simple to handle, that level of automation is higher.
The technical solution of the utility model comprises reaction, clarification, tube settling and filtration fraction, reaction chamber and ring-like dredging tube are fixed on intrinsic bottom, central authorities' sludge hopper is fixed in the reaction chamber by the dredging tube that is communicated with it, and water inlet pipe, shore pipe are communicated with reaction chamber, the dredging tube that goes in ring respectively; Fixedly have porous clarification ring flat-plate between the inwall of the outer rim of reaction chamber and body, there is the clarification water pipe that is fixed on the body top of plate; The inclined tube carriage is positioned at the reaction chamber top and is fixed on the inwall of body, and inclined tube is installed on the frame, and there is the external blast main of the basis of passing to the top of inclined tube, and the upper end of this blast main is connected to magnetic valve, lower end and is communicated with inlet pipe and flush discharge pipe respectively; The gas distribution pipe that has some aeration heads is positioned at body, and passes body and be connected with pneumatic tube; Upper fixed at aeration head has filter head plate, and the upper fixed of this plate has the water leg that is communicated with effluent trough, and the bottom of effluent trough is communicated with rising pipe; Be some lightweight floating filter materials between filter head plate and aeration head, the upper and lower of filtrate is respectively to lead to this external liquid level sensor.
Filtrate comprises matter ceramic grain filter and polystyrene foam particles filtrate clearly, is water storage space between filter head plate, the water leg; Blast main is arranged in parallel for how ring-like or multitube on the top of inclined tube, and external at this is vertical shaft type or for sleeping in box; Gas distribution pipe is ring-like or multitube is arranged in parallel.
Compared with the prior art, the utility model is owing to organically be combined in water purification operations such as traditional reaction, clarification, tube settling and biological aerated filter among the equipment, realized that the pulse flushing combines with aeration, can only turbidity removal thereby overcome existing equipment, can not remove the limitation of organic pollutant, increase functions of the equipments, improved cleaning water.
Description of drawings:
Accompanying drawing is a structural representation of the present utility model.
Among the figure: water inlet pipe 1 body 2 reative cells 3 inclined tube carriages 4 inclined tubes 5 filtrates 6 filter head plates 7 water legs 8 effluent troughs 9 outlet pipes 10 centralized buckets 11 dredging tubes 12 buckets 13 belt dredging tube 14 discharge pipelines 15 flush discharge pipes 16 air inlet pipe 17 air hoses 18 magnetic valves 19 liquid level sensors 20,21 aeration heads, 22 gas distribution pipes, 23 appendixs, 24 suspended body flowmeters, 25 electrically operated valves, 26 clarification ring flat-plates, 27 clarification water pipes, 28 basic 29 gutters, 30 blow-down pipes 31
Embodiment: the utility model is described in further detail below in conjunction with accompanying drawing and specific embodiment:
As shown in the figure, funnelform reaction chamber 3 and the ring-like dredging tube 14 that is provided with some through holes are welded on the bottom in the body 2, constitute bucket 13 by the space between reaction chamber 3 and the body 2; Central authorities' sludge hopper 11 is welded on the reaction chamber 3 and with bucket 13 by the dredging tube 12 that is communicated with it and is communicated with.Water inlet pipe 1 passes the bottom that body 2 tangentially enters reaction chamber 3 and is communicated with it, and shore pipe 15 passes body 2 and is communicated with ring-like dredging tube 14.Have porous clarification ring flat-plate 27 and be welded between the inwall of reaction chamber 3 outer rims and body 2, and bucket 13 is divided into upper and lower two chambeies; Clarification water pipe 28 is welded on the body 2 and with the epicoele of bucket 13 and is communicated with.Inclined tube carriage 4 is positioned at reaction chamber 3 tops and is welded on the inwall of body 2, and the inclined tube 5 that is 60 ° of inclination angles is installed on this.There is the blast main 18 that passes to outside the body 2 top of inclined tube 5, and the upper end of this blast main is connected to magnetic valve 19, lower end and is communicated with inlet pipe 17 and flush discharge pipe 16 respectively.The gas distribution pipe 23 that has some aeration heads 22 is positioned at body 2, and passes body 2 and be connected with pneumatic tube 24.Filter head plate 7 is positioned at the top of aeration head 22 and is welded on the body 2, is some lightweight floating filter materials 6 between this plate and the aeration head 22, and the upper and lower of this filtrate is respectively the liquid level sensor 21,20 that leads to outside the body 2; Filtrate 6 is light ceramic filtrate and polystyrene foam particles filtrate, and filter head plate 7 is mainly used in the buoyancy of carrying filtrate 6.The water leg 8 that the superiors' structure of equipment is made up of perforated tube or groove, this slot welding is connected on the top of filter head plate 7, and its two ends are communicated with effluent trough 9.Effluent trough 9 is a ring shaped slot, and its bottom is communicated with rising pipe 10.
For the ease of realizing procedure auto-control, on water inlet pipe 1, shore pipe 15, flush discharge pipe 16, inlet pipe 17, pneumatic tube 24 and the clarification water pipe 28 electrically operated valve 26 is housed all, the hypomere of pneumatic tube 24 also is equipped with suspended body flowmeter 25; Utility appliance lift pump outside magnetic valve 19, liquid level sensor 20 and 21, electrically operated valve 26 and the water purifier, air compressor machine, high pressure positive blower, dispensing kit etc. all link to each other with the time variable control cabinet.Because equipment self weight is bigger, whole equipment is installed on the basis 29 by body 2; Around basis 29, ring-like waterways 30 can be set also and be used to accept the waste water that shore pipe 15, flush discharge pipe 16 and blow-down pipe 31 are discharged.
Claims (4)
1. high turbidity integral water purifier of program control pulse wash type, comprise reaction, clarification, tube settling and filtration fraction, it is characterized in that: reaction chamber (3) and ring-like dredging tube (14) are fixed on the bottom in the body (2), central authorities' sludge hoppers (11) are fixed in the reaction chamber (3) by the dredging tube (12) that is communicated with it, and water inlet pipe (1), shore pipe (15) are communicated with reaction chamber (3), the dredging tube (14) that goes in ring respectively; Fixedly have porous clarification ring flat-plate (27) between the inwall of the outer rim of reaction chamber (3) and body (2), there is the clarification water pipe (28) that is fixed on the body (2) top of plate; Inclined tube carriage (4) is positioned at reaction chamber (3) top and is fixed on the inwall of body (2), inclined tube (5) is installed on the frame, there is the blast main (18) that passes to outside the body (2) top of inclined tube (5), and the upper end of this blast main is connected to magnetic valve (19), lower end and is communicated with inlet pipe (17) and flush discharge pipe (16) respectively; The gas distribution pipe (23) that has some aeration heads (22) is positioned at body (2), and passes body (2) and be connected with pneumatic tube (24); Upper fixed at aeration head (22) has filter head plate (7), and the upper fixed of this plate has the water leg (8) that is communicated with effluent trough (9), and the bottom of effluent trough (9) is communicated with rising pipe (10); Be some lightweight buoyant filtrates (6) between filter head plate (7) and aeration head (22), the upper and lower of filtrate (6) is respectively to lead to body (2) outer liquid level sensor (21), (20).
2. the high turbidity integral water purifier of program control pulse wash type according to claim 1 is characterized in that: filtrate (6) comprises matter ceramic grain filter and polystyrene foam particles filtrate clearly, is water storage space between filter head plate (7), the water leg (8).
3. the high turbidity integral water purifier of program control pulse wash type according to claim 1 is characterized in that: blast main (18) how ring-likely is on the top of inclined tube (5) or multitube is arranged in parallel, and is vertical shaft type or for sleeping in box outside body (2).
4. the high turbidity integral water purifier of program control pulse wash type according to claim 1 is characterized in that: gas distribution pipe (23) is arranged in parallel for ring-like or multitube.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2005200329547U CN2761594Y (en) | 2005-01-21 | 2005-01-21 | Program control pulse flushing type high turbidity integrated water purifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2005200329547U CN2761594Y (en) | 2005-01-21 | 2005-01-21 | Program control pulse flushing type high turbidity integrated water purifier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2761594Y true CN2761594Y (en) | 2006-03-01 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2005200329547U Expired - Fee Related CN2761594Y (en) | 2005-01-21 | 2005-01-21 | Program control pulse flushing type high turbidity integrated water purifier |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2761594Y (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102050552A (en) * | 2010-10-27 | 2011-05-11 | 贵州绿色环保设备工程有限责任公司 | Novel high-turbidity and biochemical integrated water purifier |
| CN101182087B (en) * | 2007-11-05 | 2011-11-30 | 上海市政工程设计研究总院 | Integrated biology aerobic sedimentation tank |
| CN102886163A (en) * | 2012-09-28 | 2013-01-23 | 天津晟远环境有限公司 | Pulsed airlift sludge discharge device |
| CN105621505A (en) * | 2016-03-25 | 2016-06-01 | 中国水产科学研究院渔业机械仪器研究所 | Seawater purification system for shellfish keep-alive transport vehicle |
| CN108163963A (en) * | 2018-01-24 | 2018-06-15 | 广州市环境保护工程设计院有限公司 | A kind of filler for biological gaseous-waste holdup system |
| CN108423796A (en) * | 2018-01-24 | 2018-08-21 | 广州市环境保护工程设计院有限公司 | A kind of biology delay facility |
| CN108423837A (en) * | 2018-01-24 | 2018-08-21 | 广州市环境保护工程设计院有限公司 | A kind of filler improving biological gaseous-waste holdup system percolation effect |
| CN108558121A (en) * | 2018-01-24 | 2018-09-21 | 广州市环境保护工程设计院有限公司 | A kind of high diafiltration biology delay facility |
| CN108558021A (en) * | 2018-01-24 | 2018-09-21 | 广州市环境保护工程设计院有限公司 | A kind of filler for biological delaying basin |
-
2005
- 2005-01-21 CN CNU2005200329547U patent/CN2761594Y/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101182087B (en) * | 2007-11-05 | 2011-11-30 | 上海市政工程设计研究总院 | Integrated biology aerobic sedimentation tank |
| CN102050552A (en) * | 2010-10-27 | 2011-05-11 | 贵州绿色环保设备工程有限责任公司 | Novel high-turbidity and biochemical integrated water purifier |
| CN102886163A (en) * | 2012-09-28 | 2013-01-23 | 天津晟远环境有限公司 | Pulsed airlift sludge discharge device |
| CN102886163B (en) * | 2012-09-28 | 2014-07-30 | 宜兴市荣盛达环保有限公司 | Pulsed airlift sludge discharge device |
| CN105621505A (en) * | 2016-03-25 | 2016-06-01 | 中国水产科学研究院渔业机械仪器研究所 | Seawater purification system for shellfish keep-alive transport vehicle |
| CN108163963A (en) * | 2018-01-24 | 2018-06-15 | 广州市环境保护工程设计院有限公司 | A kind of filler for biological gaseous-waste holdup system |
| CN108423796A (en) * | 2018-01-24 | 2018-08-21 | 广州市环境保护工程设计院有限公司 | A kind of biology delay facility |
| CN108423837A (en) * | 2018-01-24 | 2018-08-21 | 广州市环境保护工程设计院有限公司 | A kind of filler improving biological gaseous-waste holdup system percolation effect |
| CN108558121A (en) * | 2018-01-24 | 2018-09-21 | 广州市环境保护工程设计院有限公司 | A kind of high diafiltration biology delay facility |
| CN108558021A (en) * | 2018-01-24 | 2018-09-21 | 广州市环境保护工程设计院有限公司 | A kind of filler for biological delaying basin |
| CN108163963B (en) * | 2018-01-24 | 2020-12-11 | 广州市环境保护工程设计院有限公司 | Filler for biological retention system |
| CN108558121B (en) * | 2018-01-24 | 2020-12-11 | 广州市环境保护工程设计院有限公司 | High percolation bioretention facility |
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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: 20060301 |