CN103523968A - Integrated water purification device - Google Patents
Integrated water purification device Download PDFInfo
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- CN103523968A CN103523968A CN201310550225.XA CN201310550225A CN103523968A CN 103523968 A CN103523968 A CN 103523968A CN 201310550225 A CN201310550225 A CN 201310550225A CN 103523968 A CN103523968 A CN 103523968A
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- flocculation basin
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 104
- 238000000746 purification Methods 0.000 title abstract description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 57
- 238000005189 flocculation Methods 0.000 claims abstract description 38
- 230000016615 flocculation Effects 0.000 claims abstract description 37
- 239000004576 sand Substances 0.000 claims abstract description 30
- 239000006004 Quartz sand Substances 0.000 claims abstract description 25
- 238000010907 mechanical stirring Methods 0.000 claims abstract description 25
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 20
- 238000003756 stirring Methods 0.000 claims abstract description 14
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 10
- 230000000694 effects Effects 0.000 claims abstract description 7
- 230000001105 regulatory effect Effects 0.000 claims abstract description 7
- 238000001914 filtration Methods 0.000 claims description 34
- 239000003610 charcoal Substances 0.000 claims description 26
- 238000009954 braiding Methods 0.000 claims description 20
- 241000446313 Lamella Species 0.000 claims description 17
- 238000011010 flushing procedure Methods 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 9
- 230000000630 rising effect Effects 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 7
- 239000010802 sludge Substances 0.000 claims description 7
- 238000006243 chemical reaction Methods 0.000 claims description 6
- 239000000701 coagulant Substances 0.000 claims description 6
- 238000011049 filling Methods 0.000 claims description 6
- 238000002386 leaching Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 6
- 238000010992 reflux Methods 0.000 claims description 6
- 238000001179 sorption measurement Methods 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 230000031018 biological processes and functions Effects 0.000 claims description 3
- 230000015572 biosynthetic process Effects 0.000 claims description 3
- 230000015556 catabolic process Effects 0.000 claims description 3
- 238000005352 clarification Methods 0.000 claims description 3
- 238000002425 crystallisation Methods 0.000 claims description 3
- 230000008025 crystallization Effects 0.000 claims description 3
- 238000006731 degradation reaction Methods 0.000 claims description 3
- 230000008676 import Effects 0.000 claims description 3
- 244000005700 microbiome Species 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 abstract description 2
- 231100000719 pollutant Toxicity 0.000 abstract description 2
- 238000004062 sedimentation Methods 0.000 abstract 4
- 239000003651 drinking water Substances 0.000 description 6
- 235000020188 drinking water Nutrition 0.000 description 5
- 241000195493 Cryptophyta Species 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000011001 backwashing Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000007667 floating Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000005325 percolation Methods 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002594 sorbent Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
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Abstract
一种一体化净水设备，包括管式混合器、机械搅拌池、絮凝池、侧向流斜板沉淀池、调节渠、溶气渠、炭砂滤池和集水渠；管式混合器与机械搅拌池相连，管式混合器上设有加药口；机械搅拌池与絮凝池之间设置有配水墙；絮凝池与斜板沉淀池的底部连通；侧向流斜管沉淀池的底面为坡面，侧向流斜板沉淀池的底部设置有集泥槽；侧向流斜板沉淀池与调节渠相连，溶气渠与炭砂滤池的上部相连通，溶气渠中设置有溶气释放器；炭砂滤池内自下至上依次设置有溶气释放器、活性炭滤层、石英砂滤层和反冲洗排水管；炭砂滤池与集水渠的底部相连通。该设备结构紧凑，占地面积小，且操作控制简单方便，有效去除水中污染物质，净化效果好，稳定性高。
An integrated water purification equipment, including a tubular mixer, a mechanical stirring tank, a flocculation tank, a lateral flow inclined plate sedimentation tank, a regulating channel, a dissolved air channel, a carbon sand filter and a water collection channel; the tubular mixer and the mechanical The stirring tank is connected, and the tube mixer is equipped with a dosing port; a water distribution wall is set between the mechanical stirring tank and the flocculation tank; the flocculation tank is connected to the bottom of the inclined plate sedimentation tank; , the bottom of the lateral flow sloping plate sedimentation tank is provided with a mud collection tank; the lateral flow sloping plate sedimentation tank is connected to the regulating channel, the dissolved air channel is connected to the upper part of the carbon sand filter, and the dissolved air channel is provided with a dissolved air release Dissolved air releaser, activated carbon filter layer, quartz sand filter layer and backwash drainage pipe are arranged in sequence from bottom to top in the carbon sand filter; the carbon sand filter is connected with the bottom of the water collection channel. The equipment has a compact structure, a small footprint, and simple and convenient operation and control. It can effectively remove pollutants in water, with good purification effect and high stability.
Description
Technical field
The present invention relates to the integrated equipment of a kind of integrated form for drinking water treatment, belong to technical field of drinking water treatment.
Background technology
Along with scientific and technical development, people have reached a unprecedented height to the development and utilization of water resources.Meanwhile, pollution of waterhead degree is increasingly sharpened, and source of pollution increase gradually, and along with improving constantly that people live, more and more higher to drinking water quality requirement, feedwater is processed and faced huge challenge.China's water supply plant water supply coverage is wide at present, water supply quality good, but still has in the water supply territorial scope of the Bu from far-off regions water factory such as Some Cities And Towns, rural area, and these Area Inhabitants drinking water safeties can not ensure, have serious hidden danger.And China land resources is deficient, and traditional water supply plant technical process length, complex process, energy consumption is high, floor space is large.
Existing integrative water purifying device mainly with traditional coagulation, precipitation, three water purification unit combination of filtration in same equipment, be equipped with again dosing, sterilization, though take up an area little, but undesirable for low treatment effect turbid, high algae water, the water body of processing has limitation, therefore can not apply on a large scale.As disclosed in CN202576112U " emergent water purifying plant on-vehicle ", this equipment is assemblied in the single-car in compartment, described equipment comprises former water submersible pump, tube settler, the direct contact percolation device of vortex mixed reaction-micro-flocculation, water supply tank, one-level accurate filter, activated charcoal filter, secondary accurate filter, one-level ultraviolet disinfector, direct-drinking water case and the secondary ultraviolet disinfector connecting successively by pipeline, and this equipment also includes delivery machine.
Summary of the invention
The problem existing for existing drinking water treatment technology, the invention provides and a kind ofly can effectively remove various pollutents in water body, the integrative water purifying device that applied widely, treatment effect good, stability is high.
Integrative water purifying device of the present invention, realize by the following technical solutions:
This integrative water purifying device, comprises the tube mixer, mechanical stirring pond, flocculation basin, side flow lamella, adjusting canal, molten gas canal, charcoal sand filter and the braiding channel that connect successively; Tube mixer is connected with mechanical stirring pond, and tube mixer is provided with dosing mouth; Mechanical stirring is provided with agitator in pond, is provided with water distribution wall between mechanical stirring pond and flocculation basin, and both are communicated with by water distribution wall; Between flocculation basin and side flow lamella, be provided with choked flow wall, flocculation basin is communicated with the bottom of inclined-plate clarifying basin by choked flow wall; The bottom surface of lateral flow tube settler is domatic, slope aspect machinery flocculation basin, and the bottom of side flow lamella is provided with mud-collecting slot, and mud-collecting slot is provided with shore pipe, and the swash plate in side flow lamella is horizontal by 60 degree; Side flow lamella is connected with regulating canal, and the top of adjusting canal is provided with and regulates canal to strain hydrophone, regulates canal by this, to strain hydrophone with molten gas canal and is connected, and in molten gas canal, is provided with dissolved air release; Molten gas canal is connected with the top of charcoal sand filter, and the water body in molten gas canal enters charcoal sand filter by the mode of overflow; In charcoal sand filter, be disposed with from bottom to top dissolved air release, gac filtering layer, quartz sand filtering layer and back flushing water shoot, the in-built carbon leaching material of filling out of gac filtering layer, the in-built quartz sand filter media of filling out of quartz sand filtering layer; Charcoal sand filter is connected with the bottom of braiding channel, and the top of braiding channel is provided with braiding channel and strains hydrophone, and the bottom of braiding channel is provided with rising pipe and back flushing water inlet pipe, and rising pipe is strained hydrophone with braiding channel and is communicated with, and back flushing water inlet pipe is provided with blow-down pipe;
By dosing mouth, in tube mixer, add coagulating agent, former water enters mechanical stirring pond after tube mixer fully mixes with coagulating agent, by stirring, form alumen ustum, mechanical stirring pond only arranges lattice, in these lattice, flow velocity gradient G changes, according to stirring rake Board position, large near the velocity gradient g value that stirs paddle board place, from stir paddle board more away from velocity gradient g value less, in mechanical stirring pond, flow rate of water flow reduces gradually along journey, G value also reduces gradually along journey, is conducive to form large and closely knit alumen ustum, alumen ustum enters flocculation basin and flocculates, flocculation basin and lateral flow tube settler are communicated with in bottom, have reduced the impact of water inlet to mechanical flocculation basin pool wall, lateral flow tube settler has solved mud-water separation problem, the bottom slope aspect machinery flocculation basin of lateral flow tube settler, mud is back to mechanical flocculation basin voluntarily, prevent formation mud dead angle area in lateral flow tube settler simultaneously, clear water can be effectively stable be collected in adjusting canal, and most of mud is collected in the mud-collecting slot of lateral flow tube settler bottom, by the shore pipe on mud-collecting slot, discharged, a small amount of sludge reflux is to flocculation basin, mix with water inlet, sludge reflux can promote clarification, the throw out that the suspended substance of alumina blossom particles in mud in can planar water and reaction generate, make suspended substance separated with water with throw out, the throw out that reaction generates plays again crystallization nuclei effect, impel heavy polymers to grow up gradually, accelerate settlement separate, water continues to flow to adjusting canal, regulates the water in canal to enter molten gas canal by regulating canal to strain hydrophone, and the water body in molten gas canal enters charcoal sand filter by the mode of overflow, has prevented that drop from causing breaking of bubble, carbon leaching material in charcoal sand filter is brought into play filtration, absorption and biological action simultaneously, first quartz sand filter media serves as supporting layer, in order to avoid breeze is revealed, secondly, in the operational process of gac, due to the biofilm detachment of activated carbon surface growth and the leakage of abiotic particle, affect effluent quality, quartz sand filter media is set and can effectively guarantees effluent quality, the uneven surface of quartz sand filter media also can provide for the existence of microorganism the good condition of adhering to, and plays biological degradation, after the Filtration Adsorption of gac filtering layer and quartz sand filtering layer, water imports in braiding channel.
The present invention collects the integrated ingenious combinations of technological process such as line-blending, mechanical flocculation, sloping plate deposition, air supporting, the adsorption filtration of charcoal sand, compact construction, and floor space is little, and operation is controlled simple and convenient, effectively remove pollutant in water, good purification, stability is high.
Accompanying drawing explanation
Fig. 1 is the two dimensional structure schematic diagram of integrative water purifying device of the present invention.
Fig. 2 is the A-A diagrammatic cross-section in Fig. 1.
Fig. 3 is the B-B diagrammatic cross-section in Fig. 1.
Fig. 4 is the C-C diagrammatic cross-section in Fig. 1.
Fig. 5 is the structural representation of choked flow wall in the present invention.
In figure: 1, tube mixer, 2, mechanical stirring pond, 3, flocculation basin, 4, side flow lamella, 5, regulate canal, 6, molten gas canal, 7, charcoal sand filter, 8, braiding channel, 9, agitator, 10, water distribution wall, 11, choked flow wall, 12, swash plate, 13, mud-collecting slot, 14, strain hydrophone, 15, dissolved air release, 16, gac filtering layer, 17, quartz sand filtering layer, 18, water inlet pipe, 19, dosing mouth, 20, rising pipe, 21, shore pipe, 22, blow-down pipe, 23, back flushing water inlet pipe, 24, back flushing water shoot.
Embodiment
As depicted in figs. 1 and 2, integrative water purifying device of the present invention mainly comprises tube mixer 1, mechanical stirring pond 2, flocculation basin 3, side flow lamella 4, adjusting canal 5, molten gas canal 6, charcoal sand filter 7 and the braiding channel 8 connecting successively.Tube mixer 1 one end is connected with water inlet pipe 18, and one end is connected with mechanical stirring pond 2, and tube mixer 1 is provided with dosing mouth 19, by dosing mouth 19, in tube mixer 1, adds coagulating agent.In mechanical stirring pond 2, be provided with agitator 9, between mechanical stirring pond 2 and flocculation basin 3, be provided with water distribution wall 10, both are communicated with by water distribution wall 10.Between flocculation basin 3 and side flow lamella 4, be provided with choked flow wall 11, flocculation basin 3 is communicated with the bottom of inclined-plate clarifying basin 4 by choked flow wall 11, and as shown in Figure 5, choked flow wall 11 is I shape, and its upper and lower is equipped with breach, so that.Machinery flocculation basin 2 and lateral flow tube settler 4 are communicated with in bottom, can reduce the impact to mechanical flocculation basin 2 pool walls into water, the bottom surface of lateral flow tube settler 4 is domatic, be certain slope, slope aspect machinery flocculation basin 2, therefore mud can be back to flocculation basin 2 voluntarily, can prevent the interior formation mud of lateral flow tube settler 4 dead angle area simultaneously.The bottom of side flow lamella 4 is provided with mud-collecting slot 13, and mud-collecting slot 13 is provided with shore pipe 21.As shown in Figure 3, the swash plate in side flow lamella 12 is horizontal by 60 °.Side flow lamella 4 is connected with regulating canal 5, and the top of adjusting canal 5 is provided with strains hydrophone 14, regulates canal 5 to be connected by straining hydrophone 14 with molten gas canal 6, in molten gas canal 6, is provided with dissolved air release 15.Molten gas canal 6 is connected with the top of charcoal sand filter 7, and the water body in molten gas canal 6 enters charcoal sand filter 7 by the mode of overflow, can prevent that drop from causing breaking of bubble.As shown in Figure 4, in charcoal sand filter 7, be disposed with from bottom to top dissolved air release 15, gac filtering layer 16, quartz sand filtering layer 17 and back flushing water shoot 24.The interior filling carbon leaching material of gac filtering layer 16, the in-built quartz sand filter media of filling out of quartz sand filtering layer 17.Carbon leaching material is brought into play filtration, absorption and biological action simultaneously; First quartz sand filter media can serve as supporting layer, in order to avoid breeze leakage, secondly, in the operational process of gac, due to the biofilm detachment of activated carbon surface growth and the leakage of abiotic particle, affect effluent quality, quartz sand thickness is set and can effectively guarantees effluent quality.Finally, the uneven surface of quartz sand filter media also can provide for the existence of microorganism the good condition of adhering to, and plays certain biological degradation.On the water surface, there is air supporting process in charcoal sand filter 7, in underwater, occur to filter and adsorption process, and be the integrated of conventional processing and advanced treatment, can save investment and working cost.
Water enters charcoal sand filter 7 by molten gas canal 6 overflows, Filtration Adsorption effect through gac filtering layer 16 with quartz sand filtering layer 17, after filtering, water imports in braiding channel 8, and the top of braiding channel 8 is also provided with strains hydrophone, and the water being collected is strained hydrophone by this and discharged by rising pipe 12.The bottom of braiding channel 8 is provided with rising pipe 20 and back flushing water inlet pipe 23, and back flushing water inlet pipe 23 is provided with blow-down pipe 22, and rising pipe 20 is communicated with the hydrophone of straining in braiding channel.
Agitator 9 adopts perpendicular axis type, utilizes agitator drive motor to stir water.2, mechanical stirring pond arranges lattice, and in these lattice, flow velocity gradient G changes, according to stirring rake Board position, large near the velocity gradient g value that stirs paddle board place, from stir paddle board more away from velocity gradient g value less.In mechanical stirring pond 2, flow rate of water flow reduces gradually along journey,
g valuealso along journey, reduce gradually, be conducive to form large and closely knit alumen ustum.
Inclined-plate clarifying basin 4 adopts lateral flow, and with respect to anisotropic flow, in precipitation process, mudflow and water (flow) direction are in 90 °, contribute to the downslide of mud; With respect to concurrent, can solve well mud-water separation problem, clear water can be effectively stable is collected in and regulates canal 5, and most of mud is collected in mud-collecting slot 13 and discharged by shore pipe 21, a small amount of sludge reflux, to flocculation basin 3, mixes with water inlet.Sludge reflux can promote clarification, and the throw out that the alumina blossom particles in mud is a kind of sorbent material, the suspended substance in can planar water and reaction generate, makes it separated with water.Meanwhile, the throw out that reaction generates plays again crystallization nuclei effect, impels heavy polymers to grow up gradually, accelerates settlement separate.
Former water enters in tube mixer 1 by water inlet pipe 18, by dosing mouth 19, in tube mixer 1, add coagulating agent, through tube mixer 1, fully mix, first enter mechanical stirring pond 2, by agitator 9, stir and form alumen ustum, enter flocculation basin 3 and flocculate, then pass through side flow lamella 4, impurity particle is sunken to inclined-plate clarifying basin 4 bottoms and forms mud, and precipitating sludge is mainly collected in mud accumulation area and discharges, and small part is back to mechanical stirring pond 2.Water continues to flow to adjusting canal 5, regulates the water in canal 5 to enter molten gas canal 6 by straining hydrophone 14, and then water molten gas in molten gas canal 6 enter charcoal sand filter 7, and scum silica frost floats on the water surface of charcoal sand filter 7.Air supporting is in molten gas canal 6, to discharge microbubble by dissolved air release 15, and after drainage enters, microbubble adheres on flco, thereby realizes the mandatory floating of flco, reaches solid-liquid separation.The pollutents such as suspended solids in water body, lipid, algae are mainly removed in air supporting.Through air supporting, filtration, adsorption treatment, obtain water outlet.
In the time of need to carrying out backwash to gac filtering layer 16 and quartz sand filtering layer 17, first by blow-down pipe 22 by the water emptying in charcoal sand filter 7, and then carry out back flushing.When back flushing is carried out, by the valve open on back flushing water inlet pipe 23 and back flushing water shoot 24, valve closes on blow-down pipe 22, backwashing water enters charcoal sand filter 7 by back flushing water inlet pipe 23, gac filtering layer 16 and quartz sand filtering layer 17 are carried out to backwash, and backwash water is discharged by back flushing water shoot 24.
Claims (1)
1. an integrative water purifying device, comprises the tube mixer, mechanical stirring pond, flocculation basin, side flow lamella, adjusting canal, molten gas canal, charcoal sand filter and the braiding channel that connect successively; It is characterized in that: tube mixer is connected with mechanical stirring pond, and tube mixer is provided with dosing mouth; Mechanical stirring is provided with agitator in pond, is provided with water distribution wall between mechanical stirring pond and flocculation basin, and both are communicated with by water distribution wall; Between flocculation basin and side flow lamella, be provided with choked flow wall, flocculation basin is communicated with the bottom of inclined-plate clarifying basin by choked flow wall; The bottom surface of lateral flow tube settler is domatic, slope aspect machinery flocculation basin, and the bottom of side flow lamella is provided with mud-collecting slot, and mud-collecting slot is provided with shore pipe, and the swash plate in side flow lamella is horizontal by 60 degree; Side flow lamella is connected with regulating canal, and the top of adjusting canal is provided with and regulates canal to strain hydrophone, regulates canal by this, to strain hydrophone with molten gas canal and is connected, and in molten gas canal, is provided with dissolved air release; Molten gas canal is connected with the top of charcoal sand filter, and the water body in molten gas canal enters charcoal sand filter by the mode of overflow; In charcoal sand filter, be disposed with from bottom to top dissolved air release, gac filtering layer, quartz sand filtering layer and back flushing water shoot, the in-built carbon leaching material of filling out of gac filtering layer, the in-built quartz sand filter media of filling out of quartz sand filtering layer; Charcoal sand filter is connected with the bottom of braiding channel, and the top of braiding channel is provided with braiding channel and strains hydrophone, and the bottom of braiding channel is provided with rising pipe and back flushing water inlet pipe, and rising pipe is strained hydrophone with braiding channel and is communicated with, and back flushing water inlet pipe is provided with blow-down pipe;
By dosing mouth, in tube mixer, add coagulating agent, former water enters mechanical stirring pond after tube mixer fully mixes with coagulating agent, by stirring, form alumen ustum, mechanical stirring pond only arranges lattice, in these lattice, flow velocity gradient G changes, according to stirring rake Board position, large near the velocity gradient g value that stirs paddle board place, from stir paddle board more away from velocity gradient g value less, in mechanical stirring pond, flow rate of water flow reduces gradually along journey, G value also reduces gradually along journey, is conducive to form large and closely knit alumen ustum, alumen ustum enters flocculation basin and flocculates, flocculation basin and lateral flow tube settler are communicated with in bottom, have reduced the impact of water inlet to mechanical flocculation basin pool wall, lateral flow tube settler has solved mud-water separation problem, the bottom slope aspect machinery flocculation basin of lateral flow tube settler, mud is back to mechanical flocculation basin voluntarily, prevent formation mud dead angle area in lateral flow tube settler simultaneously, clear water can be effectively stable be collected in adjusting canal, and most of mud is collected in the mud-collecting slot of lateral flow tube settler bottom, by the shore pipe on mud-collecting slot, discharged, a small amount of sludge reflux is to flocculation basin, mix with water inlet, sludge reflux can promote clarification, the throw out that the suspended substance of alumina blossom particles in mud in can planar water and reaction generate, make suspended substance separated with water with throw out, the throw out that reaction generates plays again crystallization nuclei effect, impel heavy polymers to grow up gradually, accelerate settlement separate, water continues to flow to adjusting canal, regulates the water in canal to enter molten gas canal by regulating canal to strain hydrophone, and the water body in molten gas canal enters charcoal sand filter by the mode of overflow, has prevented that drop from causing breaking of bubble, carbon leaching material in charcoal sand filter is brought into play filtration, absorption and biological action simultaneously, first quartz sand filter media serves as supporting layer, in order to avoid breeze is revealed, secondly, in the operational process of gac, due to the biofilm detachment of activated carbon surface growth and the leakage of abiotic particle, affect effluent quality, quartz sand filter media is set and can effectively guarantees effluent quality, the uneven surface of quartz sand filter media also can provide for the existence of microorganism the good condition of adhering to, and plays biological degradation, after the Filtration Adsorption of gac filtering layer and quartz sand filtering layer, water imports in braiding channel.
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| CN105002960A (en) * | 2015-08-12 | 2015-10-28 | 陈栋 | Staggered floor reclaimed water reuse system for high-rise public building |
| CN107055954A (en) * | 2017-03-30 | 2017-08-18 | 山东建筑大学 | A kind of charcoal circular form pool water cleaning systems and method |
| CN108083507A (en) * | 2017-12-31 | 2018-05-29 | 广州市市政工程设计研究总院 | A kind of integrated form Water feeding treatment device and processing method |
| CN108658306A (en) * | 2018-06-28 | 2018-10-16 | 上海市地矿建设有限责任公司 | Integrated sewage treating apparatus |
| CN108675519A (en) * | 2018-05-18 | 2018-10-19 | 沈阳建筑大学 | A kind of waste water treatment system for fowl processing wastewater |
| CN109205952A (en) * | 2018-10-26 | 2019-01-15 | 江门市新会区猫淘鹰贸易有限公司 | A kind of water process purification system |
| CN109368860A (en) * | 2018-11-16 | 2019-02-22 | 金山环保集团有限公司 | It is a kind of high turbid except the cabinet type water purifier of algae |
| CN110170184A (en) * | 2019-06-28 | 2019-08-27 | 西南石油大学 | A kind of three-in-one filter device for TEG Dehydration Processing |
| CN110655231A (en) * | 2019-10-12 | 2020-01-07 | 云南树业科技有限公司 | Integrated water treatment equipment |
| CN112551765A (en) * | 2020-12-30 | 2021-03-26 | 苏州苏沃特环境科技有限公司 | River water purification treatment system and process |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2352525Y (en) * | 1997-12-12 | 1999-12-08 | 聂法玉 | Integrated water treatment equipment |
| ES2224853A1 (en) * | 2003-05-21 | 2005-03-01 | Santiago Lopez Martinez | Purification of oil mill water comprises flotation, homogenization, settling, filtration, degassing and oxidation, for disposal in drains |
| CN201952311U (en) * | 2011-01-20 | 2011-08-31 | 山东建筑大学 | Water purifying system of floating filter tank |
| CN203007068U (en) * | 2012-12-27 | 2013-06-19 | 成都源创环保工程有限公司 | Multifunctional wastewater treatment device |
-
2013
- 2013-11-08 CN CN201310550225.XA patent/CN103523968B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2352525Y (en) * | 1997-12-12 | 1999-12-08 | 聂法玉 | Integrated water treatment equipment |
| ES2224853A1 (en) * | 2003-05-21 | 2005-03-01 | Santiago Lopez Martinez | Purification of oil mill water comprises flotation, homogenization, settling, filtration, degassing and oxidation, for disposal in drains |
| CN201952311U (en) * | 2011-01-20 | 2011-08-31 | 山东建筑大学 | Water purifying system of floating filter tank |
| CN203007068U (en) * | 2012-12-27 | 2013-06-19 | 成都源创环保工程有限公司 | Multifunctional wastewater treatment device |
Non-Patent Citations (1)
| Title |
|---|
| 王志勇等: "多功能絮凝浮沉水处理实验装置设计", 《实验技术与管理》, vol. 29, no. 12, 31 December 2012 (2012-12-31), pages 78 - 84 * |
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105002960A (en) * | 2015-08-12 | 2015-10-28 | 陈栋 | Staggered floor reclaimed water reuse system for high-rise public building |
| CN107055954A (en) * | 2017-03-30 | 2017-08-18 | 山东建筑大学 | A kind of charcoal circular form pool water cleaning systems and method |
| CN107055954B (en) * | 2017-03-30 | 2020-10-09 | 山东建筑大学 | Biochar circulation type copolymerization air flotation tank water purification system and method |
| CN108083507A (en) * | 2017-12-31 | 2018-05-29 | 广州市市政工程设计研究总院 | A kind of integrated form Water feeding treatment device and processing method |
| CN108675519A (en) * | 2018-05-18 | 2018-10-19 | 沈阳建筑大学 | A kind of waste water treatment system for fowl processing wastewater |
| CN108675519B (en) * | 2018-05-18 | 2021-10-29 | 沈阳建筑大学 | A wastewater treatment system for poultry processing wastewater |
| CN108658306A (en) * | 2018-06-28 | 2018-10-16 | 上海市地矿建设有限责任公司 | Integrated sewage treating apparatus |
| CN109205952A (en) * | 2018-10-26 | 2019-01-15 | 江门市新会区猫淘鹰贸易有限公司 | A kind of water process purification system |
| CN109368860A (en) * | 2018-11-16 | 2019-02-22 | 金山环保集团有限公司 | It is a kind of high turbid except the cabinet type water purifier of algae |
| CN110170184A (en) * | 2019-06-28 | 2019-08-27 | 西南石油大学 | A kind of three-in-one filter device for TEG Dehydration Processing |
| CN110655231A (en) * | 2019-10-12 | 2020-01-07 | 云南树业科技有限公司 | Integrated water treatment equipment |
| CN112551765A (en) * | 2020-12-30 | 2021-03-26 | 苏州苏沃特环境科技有限公司 | River water purification treatment system and process |
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| CN103523968B (en) | 2015-02-25 |
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