CN203065284U - Integrated water purification system for drinking water - Google Patents
Integrated water purification system for drinking water Download PDFInfo
- Publication number
- CN203065284U CN203065284U CN 201320012390 CN201320012390U CN203065284U CN 203065284 U CN203065284 U CN 203065284U CN 201320012390 CN201320012390 CN 201320012390 CN 201320012390 U CN201320012390 U CN 201320012390U CN 203065284 U CN203065284 U CN 203065284U
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- water
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- cleaning systems
- water cleaning
- tube
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 91
- 235000020188 drinking water Nutrition 0.000 title abstract description 5
- 239000003651 drinking water Substances 0.000 title abstract description 5
- 238000000746 purification Methods 0.000 title abstract 4
- 238000001179 sorption measurement Methods 0.000 claims abstract description 24
- 239000006004 Quartz sand Substances 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 16
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000001556 precipitation Methods 0.000 claims abstract description 12
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000003830 anthracite Substances 0.000 claims abstract description 5
- 230000001112 coagulating effect Effects 0.000 claims description 24
- 238000004140 cleaning Methods 0.000 claims description 19
- 238000001914 filtration Methods 0.000 claims description 19
- 239000004744 fabric Substances 0.000 claims description 14
- 238000010521 absorption reaction Methods 0.000 claims description 8
- 239000008399 tap water Substances 0.000 claims description 7
- 235000020679 tap water Nutrition 0.000 claims description 7
- 239000003610 charcoal Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 229920011532 unplasticized polyvinyl chloride Polymers 0.000 claims description 3
- 238000005189 flocculation Methods 0.000 abstract description 11
- 230000016615 flocculation Effects 0.000 abstract description 11
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 5
- 229910052799 carbon Inorganic materials 0.000 abstract description 5
- 230000015271 coagulation Effects 0.000 abstract description 4
- 238000005345 coagulation Methods 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 3
- 238000009287 sand filtration Methods 0.000 abstract description 3
- 230000008901 benefit Effects 0.000 abstract description 2
- 239000000126 substance Substances 0.000 description 13
- 239000003795 chemical substances by application Substances 0.000 description 9
- 239000003245 coal Substances 0.000 description 8
- 230000000694 effects Effects 0.000 description 6
- 238000005096 rolling process Methods 0.000 description 6
- 239000002245 particle Substances 0.000 description 5
- 239000010802 sludge Substances 0.000 description 5
- 238000011010 flushing procedure Methods 0.000 description 4
- 241000195493 Cryptophyta Species 0.000 description 3
- 239000002384 drinking water standard Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 230000035484 reaction time Effects 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 230000008021 deposition Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000000465 moulding Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 241000894007 species Species 0.000 description 2
- FGRBYDKOBBBPOI-UHFFFAOYSA-N 10,10-dioxo-2-[4-(N-phenylanilino)phenyl]thioxanthen-9-one Chemical compound O=C1c2ccccc2S(=O)(=O)c2ccc(cc12)-c1ccc(cc1)N(c1ccccc1)c1ccccc1 FGRBYDKOBBBPOI-UHFFFAOYSA-N 0.000 description 1
- 235000001674 Agaricus brunnescens Nutrition 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000003311 flocculating effect Effects 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
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- 229920005989 resin Polymers 0.000 description 1
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- 238000004062 sedimentation Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
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- Water Treatment By Sorption (AREA)
Abstract
The utility model discloses an integrated water purification system for drinking water. The water purification system is sequentially provided with a coagulation reaction area, an inclined tube precipitation area and a filtration-adsorption area, wherein the coagulation reaction area is provided with polyhedral hollow balls; the inclined tube precipitation area is provided with two layers of inclined tubes; the two layers of inclined tubes are slantwise arranged in opposite directions; and quartz sand anthracite and active carbon are filled in the filtration-adsorption area. The water purification system disclosed by the utility model has the advantage that the turbidity of raw water is reduced and the suspended matters of the raw water are removed by combining polyhedral hollow ball flocculation reaction, double-layer reverse inclined tube precipitation technology, quartz sand filtration and active carbon adsorption, so that the turbidity index and the suspended matter index of the raw water achieve the standards of domestic drinking water.
Description
Technical field
The utility model relates to a kind of water purifying plant, and specifically a kind of tap water integrated purifying system belongs to the water purifying plant field.
Background technology
Existing tap water water purifying plant is to utilize the coagulating district of water purifier water cleaning systems front end to carry out the hybrid reaction of flocculation agent mostly, utilize the region intermediate of water cleaning systems to carry out tube settling, utilize the quartz sand filtration layer of the Background Region of water cleaning systems to carry out the suspended substance filtration, collect water outlet at last.Because what coagulating adopted is rolling type gravity flow alr mode, reaction efficiency is low, the flocculation alumen ustum that forms is little and big or small inhomogeneous, caused that coagulating district volume is big, long reaction time is not enough, precipitation zone adopts the individual layer tube settling to cause that efficient is low, the settling region floor space big, precipitate halfway drawback, filtrating area also is simple quartz sand filtration, though removed most suspended substance, but the peculiar smell in the water, algae, mushroom fine particle can't be removed, and cause processing back water quality to be difficult to meet fully drinking water standard.
Summary of the invention
In order to address the above problem, the utility model has designed a kind of tap water integrated purifying system, utilize the flocculation reaction of multiaspect hollow ball, double-deck oppositely Inclined-tube Settling Technology, quartz sand, hard coal to filter and combine with charcoal absorption, with turbidity and the suspended substance removal of former water, make the turbidity of water quality and indicator of suspended solids reach drinking water standard.
The technical solution of the utility model is:
A kind of tap water integrated purifying system, described water cleaning systems is provided with coagulating district, tube settling district and Filtration Adsorption district successively; Described coagulating district is provided with the multiaspect hollow ball; Described tube settling district is provided with two-layer inclined tube, is reverse direction between the described two-layer inclined tube and is obliquely installed; Described Filtration Adsorption district is provided with quartz sand, ANTHRACITE FILTER MEDIA and charcoal absorption material from top to bottom successively.
Further, described multiaspect hollow ball is the UPVC multiaspect hollow ball of diameter 50-120 millimeter.
Further, the bottom in described coagulating district is provided with shore pipe; Described coagulating district is provided with a plurality of branch reaction zones that are communicated with successively.
Further, to be 60 ° of angle lappings with respect to vertical direction oblique for described two-layer inclined tube.
Further, the bottom in described tube settling district is provided with sludge hopper, and the top is provided with water leg.
Further, top one side in described Filtration Adsorption district is provided with cloth tank and water distributor, and links to each other with described water leg, and the bottom is provided with water collector, and water collector is connected with water outlet.
Further, described charcoal absorption material is arranged in the casing that has mesh.
Further, be provided with the cloth waterwall between described coagulating district and the tube settling district.
Further, top, described tube settling district is provided with clear water behind the rectangle water leg collecting precipitation.
Further, described gac is placed in the casing that has mesh, and the side is provided with drain hole, can regularly take out regeneration.
Source water enters the coagulating district from bottom of device, be provided with line mixer at device water-in pipeline, add certain density flocculation agent at the mixing tank water-in, adding concentration looks water quality and is not all 3-8ppm, add water behind the flocculation agent in the coagulation district up and down rolling type flow, in each reaction is individual, place the multiaspect hollow ball, the multiaspect hollow ball is suspended in the water, and the collision that under the drive of current, does not stop rolling, drive collision, combination, the reaction moulding of flocculation agent and suspended substance, forming uniformly at last, the precipitation alumen ustum enters the tube settling district.Water enters the tube settling district and finishes by the cloth waterwall, current presentation layer stream mode, and inclined tube is to tilt 60 degree angles to be laid, and two-layer presenting in the other direction lays.The precipitation threshold species precipitate is to the sludge hopper of bottom, pond and by the regular spoil disposal of shore pipe.Current enter cloth tank and the water distributor in Filtration Adsorption district by water leg; water distributor adopts the tube-type micropore water distribution uniformity; suspended substance is filtered by quartz sand and the interception of hard coal particle; when current during through granulated active carbon, gac utilizes its extremely strong micro-porous adsorption ability that the finely ground particles in the water, algae walk, smell substance absorption are removed.During back flushing, water is from the slit of loosen down quartz sand, hard coal, gac, and suspended substance is got rid of by the current flushing.
In the coagulating district, set up the multiaspect hollow ball, in each reaction zone, place the multiaspect hollow ball of some amount, the multiaspect hollow ball rotation of ceaselessly rolling in water flows process, the water quality that adds behind the flocculating settling agent has been formed strong mixing effect, greatly increased the chance of flocculation agent and suspended substance mixing combination in the water, reach good reaction effect, thereby make reaction times and reaction compartment reduce 1/3rd, handle same water quality and the water yield and reduced by 1/3rd space and investment cost.
Change the individual layer inclined tube into bilayer in precipitation zone and be folded to the tube settling pattern, increase the device height and reduced floor space, because mud bigger deposition efficiency of the bigger weight of the formed particle of mud in dirty precipitation process is higher, sedimentation effect improves 20% under the same volume.
At filtrating area the filtration of quartz sand hard coal is combined with charcoal absorption, set up the granulated active carbon adsorption zone at quartz sand ANTHRACITE FILTER MEDIA bottom, movable body structure is made in the charcoal absorption district, can regularly take out and regenerate.Can guarantee that through the water quality that above operation is handled turbidity is up to standard, the limpid free from extraneous odour of water quality.
Advantage of the present utility model is: place the multiaspect hollow ball and improve coagulation effect in the coagulating district, reduces by 1/3rd reaction times and space; The settling region adopts double-deck inclined tube reversed arrangement deposition efficiency to improve 20%; Filtrating area will filter with adsorption function in one, and it is better to handle back water quality, and gac can regularly take out regeneration, and Operation and Maintenance is good, and is durable for a long time; With turbidity and the suspended substance removal of former water, make the turbidity of water quality and indicator of suspended solids reach drinking water standard.Design science, rational in infrastructure, compact efficient, the cleaning water height, purifying water effect is good, install simple, stable and reliable operation, strong shock resistance, the industrial and mining enterprises, drinking water of rural area safety technique, army etc. that are specially adapted to away from the city are the water purifying treatment of drinking water source with the surface water.
The utility model is described in further detail below in conjunction with drawings and Examples.
Description of drawings
Fig. 1 is the sectional view of the utility model embodiment water cleaning systems;
Fig. 2 is the vertical view of the utility model embodiment water cleaning systems;
Among the figure: 1-coagulating district, 2-tube settling district, 3-Filtration Adsorption district, 4-multiaspect hollow ball, 5-inclined tube, 6-sludge hopper, 7-quartz sand hard coal, 8-water distributor, 9-gac, 10-casing, 11-water-in, 12-cloth waterwall, 13-water leg, 14-shore pipe, 15-water collector, 16-water outlet, 17-gac feeding tube, 18-manhole, 19-cloth tank.
Embodiment
Below preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein only is used for description and interpretation the utility model, and be not used in restriction the utility model.
As shown in Figure 1, a kind of tap water integrated purifying system, described water cleaning systems is provided with coagulating district 1, tube settling district 2 and Filtration Adsorption district 3 successively.
Described coagulating district 1 is provided with multiaspect hollow ball 4, the UPVC multiaspect hollow ball that described multiaspect hollow ball 4 is diameter 50-120 millimeter; The bottom in described coagulating district 1 is provided with shore pipe 14; Described coagulating district 1 is provided with a plurality of branch reaction zones that are communicated with successively;
Described tube settling district 2 is provided with two-layer inclined tube 5, is reverse direction between the described two-layer inclined tube 5 and is obliquely installed, and it is oblique that described two-layer inclined tube 5 is 60 ° of angle lappings with respect to vertical direction; The top in described tube settling district 2 is provided with water leg 13, and the bottom in described tube settling district 2 is provided with sludge hopper 6, and sludge hopper 6 is connected with shore pipe 14;
Top one side in described Filtration Adsorption district 3 is provided with cloth tank 19, and link to each other with described water leg 13, described Filtration Adsorption district 3 is provided with quartz sand 7 and gac 9 from top to bottom successively, described gac 9 is arranged in the casing 10 that has mesh, the casing side is provided with drain hole, can regularly take out regeneration; The bottom in described Filtration Adsorption district 3 is provided with water collector 15, and water collector 15 is connected with water outlet 16; The top in described Filtration Adsorption district 3 is provided with gac feeding tube 17, by gac feeding tube 17 gac is joined in the casing 10, between quartz sand 7 and the gac 9 one deck anthracite coal measure can also be set again, improves filter effect; One side in described Filtration Adsorption district 3 is provided with manhole 18, convenient maintenance;
Coagulating district 1 one side bottoms of described water cleaning systems are provided with water-in 11, water-in 11 places are provided with line mixer, be provided with cloth waterwall 12 between described coagulating district 1 and the tube settling district 2, cloth waterwall 12 is provided with water distributing pore, is provided with the cloth tank between described tube settling district 2 and the Filtration Adsorption district 3.
Described water cleaning systems outside is provided with the horizontal square metal cabinet, and material is carbon steel, and is interior anticorrosion with health level Resins, epoxy.
Source water enters the coagulating district from bottom of device, be provided with line mixer at device water-in pipeline, water-in at line mixer adds certain density flocculation agent, adding concentration looks water quality and is not all 3-8ppm, add water behind the flocculation agent in the coagulating district up and down rolling type flow, in dividing reaction zone, each places equal diameter multiaspect hollow ball, the multiaspect hollow ball is suspended in the water, and the collision that under the drive of current, does not stop rolling, drive the collision of flocculation agent and suspended substance, in conjunction with, the reaction moulding, forming uniformly at last, the precipitation alumen ustum enters the tube settling district.Water enters the tube settling district and finishes by the cloth waterwall, current presentation layer stream mode, and inclined tube is to tilt 60 degree angles to be laid, and two-layer presenting in the other direction lays.The precipitation threshold species precipitate is to the mud-collecting slot of bottom, pond and by the regular spoil disposal of shore pipe.Current by the water leg on top after filtration the cloth tank of adsorption zone flow into the Filtration Adsorption district from top to bottom; water distribution adopts the tube-type micropore water distribution uniformity; suspended substance is filtered by quartz sand and the interception of hard coal particle; when current during through granulated active carbon, gac utilizes its extremely strong micro-porous adsorption ability that the finely ground particles in the water, algae walk, smell substance absorption are removed.During back flushing, water is from the slit of loosen down quartz sand, hard coal, gac, and suspended substance is got rid of by the current flushing.
It should be noted that at last: the above only is preferred embodiment of the present utility model, be not limited to the utility model, although with reference to previous embodiment the utility model is had been described in detail, for a person skilled in the art, it still can be made amendment to the technical scheme that aforementioned each embodiment puts down in writing, and perhaps part technical characterictic wherein is equal to replacement.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
Claims (9)
1. tap water integrated purifying system, described water cleaning systems is provided with coagulating district, tube settling district and Filtration Adsorption district successively, it is characterized in that: described coagulating district is provided with the multiaspect hollow ball, described tube settling district is provided with two-layer inclined tube, be reverse direction between the described two-layer inclined tube and be obliquely installed, described Filtration Adsorption district is provided with quartz sand ANTHRACITE FILTER MEDIA and charcoal absorption material from top to bottom successively.
2. water cleaning systems according to claim 1, it is characterized in that: described multiaspect hollow ball is the UPVC multiaspect hollow ball of diameter 50-120 millimeter.
3. water cleaning systems according to claim 1, it is characterized in that: it is oblique that described two-layer inclined tube is 60 ° of angle lappings with respect to vertical direction.
4. water cleaning systems according to claim 1, it is characterized in that: the bottom in described tube settling district is provided with mud-collecting slot, and the top is provided with water leg.
5. water cleaning systems according to claim 4, it is characterized in that: top one side in described Filtration Adsorption district is provided with the cloth tank, and links to each other with described water leg, and the bottom is provided with water collector, and water collector is connected with water outlet.
6. water cleaning systems according to claim 1, it is characterized in that: described gac is arranged in the casing that has mesh.
7. according to any described water cleaning systems of claim 1-6, it is characterized in that: be provided with the cloth waterwall between described coagulating district and the tube settling district.
8. according to any described water cleaning systems of claim 1-6, it is characterized in that: top, described tube settling district is provided with clear water behind the tube-type micropore collecting precipitation.
9. according to any described water cleaning systems of claim 1-6, it is characterized in that: the bottom in described coagulating district is provided with shore pipe; Described coagulating district is provided with a plurality of branch reaction zones that are communicated with successively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320012390 CN203065284U (en) | 2013-01-10 | 2013-01-10 | Integrated water purification system for drinking water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320012390 CN203065284U (en) | 2013-01-10 | 2013-01-10 | Integrated water purification system for drinking water |
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| Publication Number | Publication Date |
|---|---|
| CN203065284U true CN203065284U (en) | 2013-07-17 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN 201320012390 Expired - Fee Related CN203065284U (en) | 2013-01-10 | 2013-01-10 | Integrated water purification system for drinking water |
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| CN (1) | CN203065284U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104609676A (en) * | 2015-02-13 | 2015-05-13 | 西安建筑科技大学 | Device for quickly improving water quality of urban water body |
| CN105565553A (en) * | 2015-12-22 | 2016-05-11 | 解艳超 | Zero-emission purifying and recycling system of cyanide-containing heavy metal wastewater |
| CN107055725A (en) * | 2017-05-04 | 2017-08-18 | 冯路亭 | Integral water purifying device |
| CN108083489A (en) * | 2017-10-31 | 2018-05-29 | 夹江县盛世东方陶瓷有限公司 | A kind of waste water circulatory system |
| CN108423788A (en) * | 2018-05-25 | 2018-08-21 | 浙江工业大学 | Without medicament secondary waterpower coagulation assisted pond |
| CN111675359A (en) * | 2020-05-06 | 2020-09-18 | 浙江省水利河口研究院 | Simple automatic treatment device and treatment method for dealing with sudden high turbidity of drinking water in rural areas |
-
2013
- 2013-01-10 CN CN 201320012390 patent/CN203065284U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104609676A (en) * | 2015-02-13 | 2015-05-13 | 西安建筑科技大学 | Device for quickly improving water quality of urban water body |
| CN105565553A (en) * | 2015-12-22 | 2016-05-11 | 解艳超 | Zero-emission purifying and recycling system of cyanide-containing heavy metal wastewater |
| CN107055725A (en) * | 2017-05-04 | 2017-08-18 | 冯路亭 | Integral water purifying device |
| CN107055725B (en) * | 2017-05-04 | 2020-07-03 | 贵州黔成电器制造有限公司 | Integrated water purifying device |
| CN108083489A (en) * | 2017-10-31 | 2018-05-29 | 夹江县盛世东方陶瓷有限公司 | A kind of waste water circulatory system |
| CN108423788A (en) * | 2018-05-25 | 2018-08-21 | 浙江工业大学 | Without medicament secondary waterpower coagulation assisted pond |
| CN108423788B (en) * | 2018-05-25 | 2024-04-09 | 浙江工业大学 | Non-medicament secondary hydraulic reinforced coagulating sedimentation tank |
| CN111675359A (en) * | 2020-05-06 | 2020-09-18 | 浙江省水利河口研究院 | Simple automatic treatment device and treatment method for dealing with sudden high turbidity of drinking water in rural areas |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130717 Termination date: 20160110 |