CN105502729B - A kind of water treatment facilities - Google Patents
A kind of water treatment facilities Download PDFInfo
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- CN105502729B CN105502729B CN201510851609.4A CN201510851609A CN105502729B CN 105502729 B CN105502729 B CN 105502729B CN 201510851609 A CN201510851609 A CN 201510851609A CN 105502729 B CN105502729 B CN 105502729B
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- Prior art keywords
- water
- tower
- layer
- filter
- mud discharging
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/283—Treatment of water, waste water, or sewage by sorption using coal, charred products, or inorganic mixtures containing them
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5209—Regulation methods for flocculation or precipitation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Water Treatment By Sorption (AREA)
Abstract
The present invention discloses a kind of water treatment facilities,Including the former pond being sequentially connected,Primary settling tower,Tube settling room,Filter chamber and adsorption chamber,Water intaking filter is provided with former pond,The device includes fetching tank for water and fixed support,Fetching tank for water bottom surface opening is simultaneously provided with grid,There is filter material layer inside,Inlet channel is provided with online flow detection meter,Coagulation dosing device and high-pressure pump,Primary settling tower includes interior,Outer tower and mud discharging passage therebetween,Nei Tanei is relatively arranged in a crossed manner acclivitous deflection plate,Mud collection device and inclined-pipe settler are provided with tube settling room,Filter layer is provided with the middle part of filter chamber,Multilayer adsorption layer is provided with adsorption chamber,The present invention can tentatively be filtered to the raw water at end of fetching water,And the turbidity of raw water is further reduced using primary settling tower,Raw water further flows through tube settling room,Substantially drinking water standard can be reached after the process chambers such as filter chamber,Whole system compact in design,Floor space is small.
Description
Technical field
The present invention relates to water-suppling treatment equipment field, and in particular to a kind of water treatment facilities.
Background technology
The activity of the mankind can be such that substantial amounts of industry, agricultural and domestic refuse is discharged into water, be contaminated water body, at present
The sewage that the whole world there are about billion cubic meter more than 4200 every year is discharged into rivers,lakes and seas, pollutes the fresh water of 5.5 tcms, this phase
When in more than the 14% of global runoff volume, the water pollution aggravated increasingly, forming significant threat to the living safety of the mankind, into
For the major obstacles of human health, economy and social sustainable development, investigated according to authoritative institution of the world, in developing country, respectively
Class disease has 80% to be propagated because antihygienic water has been drunk, every year the global 200d 0 caused by drinking unhygienic water at least
Ten thousand people are dead, therefore water pollution is referred to as " world's number one killer ", at present, in terms of river and the dirty water decontamination handles, form
Various water treatment facilities just play an important role, but in general purifier requires that influent turbidity is not high, for some
The higher water of turbidity is often still extremely difficult to drinking water standard after in general is handled, additionally, due to the complexity of water treatment technology
Property, the defects of cellular construction is various, land occupation resource is big be present in traditional water supply water purification integration apparatus.
The content of the invention
To solve above technical problem, the present invention provides a kind of a kind of water process for being applicable to the higher raw water of turbidity and set
It is standby.
Technical scheme is as follows：
A kind of water treatment facilities, including be sequentially connected former pond, primary settling tower, tube settling room, filter chamber, absorption
Room and clear water reserviors, its key are：
Water intaking filter is provided with the former pond, the water intaking filter includes fetching tank for water and fixed support, institute
State fetching tank for water to be fixed on the fixed support, fetching tank for water bottom surface opening is simultaneously provided with grid, and filter is provided with the fetching tank for water
The bed of material, the fetching tank for water top are connected by inlet channel with the primary settling tower bottom；
The inlet channel is provided with coagulation dosing device, the water inlet pipe between the coagulation dosing device and the former pond
Online flow detection meter is connected with road, the inlet channel between the coagulation dosing device and the primary settling tower is provided with height
Press pump；
The primary settling tower includes Wai Ta and Nei Ta, forms mud discharging passage, the bottom of the interior tower therebetween
Inlet channel is connected with, is intersected from top to bottom provided with least two deflection plates in the Nei Tanei, the deflection plate is inclined upwardly 5-
10 °, the deflection plate lower side is fixedly connected with the tower wall of the interior tower, and the deflection plate upper side edge is respectively equipped with baffle plate, often
The individual deflection plate is respectively equipped with mud discharging mouth with the Nei Ta junctions, the lower edge of the mud discharging mouth and the deflection plate
Lower side is concordant；
It is provided with inclined-pipe settler in the tube settling room, the tube settling room below the inclined-pipe settler leads to
Piping is connected with the interior top of tower；
The filter chamber top is provided with water distributor, and the water distributor water inlet end is connected with the tube settling ceiling portion, institute
State filter chamber bottom and be provided with delivery port, filter layer is provided with the middle part of the filter chamber；
Adsorption layer and vertical water distributor are provided with the adsorption chamber, the both ends of the vertical water distributor pass the absorption respectively
Layer, the upper end of the vertical water distributor is connected with water-locator, the lower end of the vertical water distributor stretch out the adsorption chamber and with the mistake
The delivery port of filter chamber is connected, and the adsorption chamber below the adsorption layer is connected by outlet conduit with the clear water reserviors, the absorption
Diatomite layer that layer includes setting gradually from the bottom up, fluffy cotton layer, layer of silica gel and active carbon layer are the diatomite layer, fluffy
The thickness ratio of cotton layer, layer of silica gel and active carbon layer is 3：2：1.5：1.
Beneficial effect using the technical program is due to that water intaking filter, Neng Gouyou are provided with the water intaking end at water source
The floating object gone in water removal to effect, and have preliminary filtration result to impurity such as other organic pollutions, inorganic pollutions, simultaneously
Can be by online flow monitoring meter Real Time Observation flow of inlet water in water inlet end, and the coagulated agent added in raw water is adjusted according to this
Amount, when with the addition of the raw water after coagulated agent and passing through the deflection plate of primary settling tower, the larger alumen ustum of condensation can preliminary sedimentation exist
On deflection plate and Wai Tazhong is discharged into, now the turbidity of raw water has substantially reduced, and raw water is after the secondary precipitation of tube settling room in water
Impurity be substantially removed, then the raw water after filter chamber filters can reach drinking water standard substantially, and now raw water passes through again
The peculiar smell and poisonous and harmful substance remained after adsorption chamber adsorption filtration in water will be removed further.
As preferred：Above-mentioned water-locator includes star-like branch pipe, and the star-like branch pipe is Samsung branch pipe, between adjacent branch pipe
Angle is 120 °, and the star-like branch pipe external part is connected with same outer endless tube, and interior endless tube, the outer endless tube are provided with the outer endless tube
Connected respectively with the star-like branch pipe with interior endless tube, water distributing pore is respectively equipped with the interior endless tube, outer endless tube and star-like branch pipe.
Using the beneficial effects of the invention are as follows the top that water source can uniformly be distributed to adsorption layer by the narrow meshed water-locator of disc type, and
Larger turbulent water will not be produced.
Back purge system is provided with below above-mentioned adsorption layer.Beneficial effect using this scheme is can effectively to extend adsorption layer
Service life.
Above-mentioned deflection plate is 20-30, is evenly distributed between bottom of towe and the tower top of the interior tower.Using having for this scheme
Beneficial effect is that deflection plate density sets the distance for rationally, shortening alumen ustum sedimentation, is advantageous to accelerate the sedimentation of alumen ustum.
The bottom of towe of above-mentioned outer tower is provided with the first mud discharging pipe, and the first mud discharging pipe is provided with the first mud discharging
Regulating valve.The sludge that outer tower bottom of towe is deposited on using the beneficial effect of this scheme can periodically be discharged by mud discharging pipe.
Above-mentioned tube settling room bottom is provided with sludge collection bucket, and the bottom of the sludge collection bucket is provided with the second mud discharging
Pipe, the second mud discharging pipe are provided with the second mud discharging regulating valve.Beneficial effect using this scheme is can be according to need
Periodical blowdown is wanted, avoids sludge accumulation is excessive from influenceing tube settling effect.
Above-mentioned first mud discharging regulating valve and the second described mud discharging regulation valve opening time are small at intervals of 20-24
When.Beneficial effect using this scheme is periodically to exclude the sludge of deposition, avoids sludge accumulation excessive, influences sedimentation effect.
Sludge-tank, above-mentioned primary settling tower, tube settling are provided with below above-mentioned primary settling tower and the tube settling room
Observation window is equipped with the top of room, filter chamber and the adsorption chamber, the tube settling ceiling portion is provided with automatic exhaust steam valve.Using
The beneficial effect of this scheme is that the sludge of deposition can be concentrated and is emitted in sludge-tank, facilitates worker to concentrate cleaning, worker can pass through
Observation window fast checks purifier inner case.
Above-mentioned filter layer includes manganese layer of sand and the anthracite coal measure being laid on the manganese layer of sand.Using the beneficial effect of this scheme
It is the residual impurity that can further go in water removal, particularly iron, manganese class impurity.
Filtrate in above-mentioned filter material layer is granules of polystyrene, and filtrate intercept net is provided with above the filter material layer.Using this
The beneficial effect of scheme is the weight that filtrate proportion gentlier can effectively mitigate whole intake equipment, facilitates M R, filtrate
The filtrate intercept net of top effectively can prevent filtrate from floating, it is ensured that filter material layer position is fixed and has certain density.
Beneficial effect：
Using the beneficial effects of the invention are as follows due to the water intaking end at water source be provided with water intaking filter, can be effectively
The floating object gone in water removal, and have preliminary filtration result to impurity such as other organic pollutions, inorganic pollutions, while entering
Water end (W.E.) can be by online flow monitoring meter Real Time Observation flow of inlet water, and adjusts the coagulated agent amount added in raw water according to this, adds
When having added the raw water after coagulated agent to pass through primary settling tower, the larger alumen ustum of condensation can settle layer by layer on deflection plate, baffling
It is reasonable that plate density is set, and shortens the distance of alumen ustum sedimentation, is advantageous to accelerate the sedimentation of alumen ustum, reduces the turbidity of raw water, raw water
Drinking water standard can be reached substantially by filter chamber filtering again after the secondary precipitation of tube settling room, now raw water is again through adsorption chamber
The peculiar smell and poisonous and harmful substance remained after adsorption filtration in water will be removed further, and the device is to the iron in water, manganese in addition
There is preferable filtration result Deng impurity, whole system is reasonable in design, compact in design, greatlys save the occupation of land face of structures
Product, is applicable not only to the construction of small-scale water supply plant, can also be used for larger water supply plant by more modes in parallel
Construction.
Brief description of the drawings
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the enlarged drawing in a portions in Fig. 1；
Fig. 3 is water distributor structure schematic diagram；
Fig. 4 is water intaking filter apparatus configuration schematic diagram.
Embodiment
With reference to embodiment and accompanying drawing, the invention will be further described.
As Figure 1-4, a kind of water treatment facilities, including be sequentially connected former pond 5, primary settling tower 1, tube settling
Room 2, filter chamber 3, adsorption chamber 4 and clear water reserviors 20.
The former pond 5 is interior to be provided with water intaking filter 25, and the water intaking filter 25 includes fetching tank for water 251 and fixed
Support 254, the fetching tank for water 251 are fixed on the fixed support 254, and the bottom surface opening of fetching tank for water 251 is simultaneously provided with grid
252, the fetching tank for water 251 is interior to be provided with filter material layer 253, and the top of fetching tank for water 251 passes through inlet channel 6 and the primary settling
The bottom of tower 1 connects, and the filtrate in the filter material layer 253 is granules of polystyrene, and the top of filter material layer 253 is provided with filtrate and intercepted
Net 255.
The inlet channel 6 is provided with coagulation dosing device 9, entering between the coagulation dosing device 9 and the former pond 5
Online flow detection meter 7 is connected with waterpipe 6, the inlet channel between the coagulation dosing device 9 and the primary settling tower 1
6 are provided with high-pressure pump 8.
The primary settling tower 1 includes outer tower 104 and Nei Ta 103, forms mud discharging passage 106 therebetween, described
The bottom of interior tower 103 is connected with inlet channel 6, intersects from top to bottom in the interior tower 103 and is provided with least two deflection plates
102, the deflection plate 102 is 20-30, is evenly distributed between bottom of towe and the tower top of the interior tower 103, the deflection plate 102
It is inclined upwardly 5-10 °, the lower side of deflection plate 102 is fixedly connected with the tower wall of the interior tower 103, on the deflection plate 102
Side is respectively equipped with baffle plate 101, and each deflection plate 102 is respectively equipped with mud discharging mouth with the interior junction of tower 103
105, the lower edge of the mud discharging mouth 105 is concordant with the lower side of deflection plate 102, the dirt being thus deposited on deflection plate 102
Mud can be discharged into mud discharging passage 106 by the mud discharging mouth 105, and is gradually deposited at the bottom of towe of outer tower 104, described
The bottom of towe of outer tower 104 is provided with the first mud discharging pipe 10, and the first mud discharging pipe 10 is adjusted provided with the first mud discharging
Valve 11.
Inclined-pipe settler 202 is provided with the tube settling room 2, the inclined tube of the lower section of inclined-pipe settler 202
Mud chamber 2 is connected by pipeline 15 and the interior top of tower 103, and the bottom of tube settling room 2 is provided with sludge collection bucket 201,
The bottom of the sludge collection bucket 201 is provided with the second mud discharging pipe 16, and the second mud discharging pipe 16 is provided with the second sludge
Emissions adjustment valve 17, the first mud discharging regulating valve 11 and described 17 opening time of the second mud discharging regulating valve interval
For 20-24 hours.
The top of filter chamber 3 is provided with water distributor 18, and the water inlet end of water distributor 18 and the top of tube settling room 2 are logical
Piping is connected, and the bottom of filter chamber 3 is provided with delivery port, and the middle part of filter chamber 3 is provided with filter layer, and the filter layer includes
Manganese layer of sand and the anthracite coal measure being laid on the manganese layer of sand.
Adsorption layer 4 and vertical water distributor 21 are provided with the adsorption chamber 19, the both ends of the vertical water distributor 21 pass respectively
The adsorption layer 4, the upper end of the vertical water distributor 21 are connected with water-locator 22, and the suction is stretched out in the lower end of the vertical water distributor 21
Alcove 19 is simultaneously connected with the delivery port of the filter chamber 3, and the adsorption chamber 19 of the lower section of adsorption layer 4 passes through outlet conduit 24 and institute
Clear water reserviors 20 are stated to connect, the adsorption layer 4 include set gradually from the bottom up diatomite layer 401, fluffy cotton layer 402, silica gel
Layer 403 and active carbon layer 404, the diatomite layer 401, fluffy cotton layer 402, the thickness ratio of layer of silica gel 403 and active carbon layer 404
For 3：2：1.5：1, the lower section of adsorption layer 4 is provided with back purge system 23.
The water-locator 22 includes star-like branch pipe 224, and the star-like branch pipe 224 is Samsung branch pipe, between adjacent branch pipe
Angle is 120 °, and the star-like external part of branch pipe 224 is connected with same outer endless tube 222, and interior endless tube is provided with the outer endless tube 222
223, the outer endless tube 222 and interior endless tube 223 are connected with the star-like branch pipe 224 respectively, in the interior endless tube 223, outer endless tube
222 and star-like branch pipe 224 on be respectively equipped with water distributing pore 221.
From this figure it can be seen that the primary settling tower 1 and the lower section of tube settling room 2 are provided with sludge-tank 13, it is described first
Level sedimentation tower 1, tube settling room 2, the top of filter chamber 3 and the adsorption chamber 19 are equipped with observation window 12, the tube settling
The top of room 2 is provided with automatic exhaust steam valve 14.
Claims (9)
1. a kind of water treatment facilities, including be sequentially connected former pond (5), primary settling tower (1), tube settling room (2), filtering
Room (3), adsorption chamber (19) and clear water reserviors (20), it is characterised in that：
Be provided with water intaking filter (25) in the former pond (5), the water intaking filter (25) include fetching tank for water (251) and
Fixed support (254), the fetching tank for water (251) are fixed on the fixed support (254), and fetching tank for water (251) bottom surface is opened
Mouth is simultaneously provided with grid (252), is provided with filter material layer (253) in the fetching tank for water (251), fetching tank for water (251) top is by entering
Waterpipe (6) is connected with primary settling tower (1) bottom；
The inlet channel (6) is provided with coagulation dosing device (9), between the coagulation dosing device (9) and the former pond (5)
Inlet channel (6) on be connected with online flow detection meter (7), the coagulation dosing device (9) and the primary settling tower (1) it
Between inlet channel (6) be provided with high-pressure pump (8)；
The primary settling tower (1) includes outer tower (104) and interior tower (103), forms mud discharging passage (106) therebetween,
The bottom of the interior tower (103) is connected with inlet channel (6), intersects from top to bottom in the interior tower (103) and is provided with deflection plate
(102), the deflection plate (102) is inclined upwardly 5-10 °, and the deflection plate (102) is 20-30, is evenly distributed on the interior tower
(103) between bottom of towe and tower top, deflection plate (102) lower side is fixedly connected with the tower wall of the interior tower (103), described
Deflection plate (102) upper side edge is respectively equipped with baffle plate (101), and each deflection plate (102) is connected punishment with the interior tower (103)
Not She You mud discharging mouth (105), the lower edge of the mud discharging mouth (105) is concordant with deflection plate (102) lower side；
Be provided with inclined-pipe settler (202) in the tube settling room (2), it is described oblique below the inclined-pipe settler (202)
Pipe mud chamber (2) is by pipeline (15) with being connected at the top of the interior tower (103)；
Water distributor (18) is provided with the top of the filter chamber (3), water distributor (18) water inlet end pushes up with the tube settling room (2)
Portion connects, and filter chamber (3) bottom is provided with delivery port, and filter layer is provided with the middle part of the filter chamber (3)；
Adsorption layer (4) and vertical water distributor (21), the both ends difference of the vertical water distributor (21) are provided with the adsorption chamber (19)
The adsorption layer (4) is passed, the upper end of the vertical water distributor (21) is connected with water-locator (22), under the vertical water distributor (21)
End is stretched out the adsorption chamber (19) and is connected with the delivery port of the filter chamber (3), the adsorption chamber below the adsorption layer (4)
(19) it is connected by outlet conduit (24) with the clear water reserviors (20), the adsorption layer (4) includes what is set gradually from the bottom up
Diatomite layer (401), fluffy cotton layer (402), layer of silica gel (403) and active carbon layer (404) are the diatomite layer (401), fluffy
The thickness ratio of cotton layer (402), layer of silica gel (403) and active carbon layer (404) is 3：2：1.5：1.
A kind of 2. water treatment facilities according to claim 1, it is characterised in that：The water-locator (22) includes star-like branch pipe
(224), the star-like branch pipe (224) is Samsung branch pipe, and the angle between adjacent branch pipe is 120 °, and the star-like branch pipe (224) is stretched
Go out end and be connected with same outer endless tube (222), be provided with interior endless tube (223) in the outer endless tube (222), the outer endless tube (222) and
Interior endless tube (223) is connected with the star-like branch pipe (224) respectively, in interior endless tube (223), outer endless tube (222) and the star-like branch
Water distributing pore (221) is respectively equipped with pipe (224).
A kind of 3. water treatment facilities according to claim 1 or 2, it is characterised in that：It is provided with below the adsorption layer (4) anti-
Flusher (23).
A kind of 4. water treatment facilities according to claim 1, it is characterised in that：The bottom of towe of the outer tower (104) is provided with the
One mud discharging pipe (10), the first mud discharging pipe (10) are provided with the first mud discharging regulating valve (11).
A kind of 5. water treatment facilities according to claim 4, it is characterised in that：Tube settling room (2) bottom is provided with
Sludge collection bucket (201), the bottom of the sludge collection bucket (201) are provided with the second mud discharging pipe (16), the second sludge row
Put pipe (16) and be provided with the second mud discharging regulating valve (17).
A kind of 6. water treatment facilities according to claim 5, it is characterised in that：The first mud discharging regulating valve (11)
With the second described mud discharging regulating valve (17) opening time at intervals of 20-24 hours.
A kind of 7. water treatment facilities according to claim 1 or 5, it is characterised in that：The primary settling tower (1) and inclined tube
Sludge-tank (13), the primary settling tower (1), tube settling room (2), filter chamber (3) and the suction are provided with below mud chamber (2)
Observation window (12) is equipped with the top of alcove (19), automatic exhaust steam valve (14) is provided with the top of the tube settling room (2).
A kind of 8. water treatment facilities according to claim 7, it is characterised in that：The filter layer includes manganese layer of sand and laying
Anthracite coal measure on the manganese layer of sand.
A kind of 9. water treatment facilities according to claim 7, it is characterised in that：Filtrate in the filter material layer (253) is
Granules of polystyrene, filter material layer (253) top are provided with filtrate intercept net (255).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510851609.4A CN105502729B (en) | 2015-11-28 | 2015-11-28 | A kind of water treatment facilities |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510851609.4A CN105502729B (en) | 2015-11-28 | 2015-11-28 | A kind of water treatment facilities |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105502729A CN105502729A (en) | 2016-04-20 |
| CN105502729B true CN105502729B (en) | 2018-02-16 |
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| CN201510851609.4A Expired - Fee Related CN105502729B (en) | 2015-11-28 | 2015-11-28 | A kind of water treatment facilities |
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Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105502713A (en) * | 2015-11-30 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterwork water purification treatment equipment |
| CN105461091A (en) * | 2015-11-30 | 2016-04-06 | 綦江县狮子桥供水有限公司 | Water treating equipment for waterworks |
| CN105502714A (en) * | 2015-11-30 | 2016-04-20 | 綦江县狮子桥供水有限公司 | Waterwork water purification treatment equipment with water taking and filtering device |
| CN105347564A (en) * | 2015-11-30 | 2016-02-24 | 綦江县狮子桥供水有限公司 | Tap water plant integrated water purification equipment with water getting and filtering device |
| CN105347565A (en) * | 2015-11-30 | 2016-02-24 | 綦江县狮子桥供水有限公司 | Integrated water purifying device of tap water plant |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090095690A1 (en) * | 2007-10-14 | 2009-04-16 | Mccabe Derald L | Solids removal system and method |
| CN201240953Y (en) * | 2008-07-08 | 2009-05-20 | 甘臻 | Integral water purifying apparatus |
| CN201770557U (en) * | 2010-09-01 | 2011-03-23 | 浙江沃特水处理设备有限公司 | Integrated water purifying device |
| US9056266B2 (en) * | 2012-07-21 | 2015-06-16 | Don M. Buckner | Method and system to separate solids from liquids |
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- 2015-11-28 CN CN201510851609.4A patent/CN105502729B/en not_active Expired - Fee Related
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| CN105502729A (en) | 2016-04-20 |
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