CN105347570B - Water factory's integrative water purifying device - Google Patents
Water factory's integrative water purifying device Download PDFInfo
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- CN105347570B CN105347570B CN201510855915.5A CN201510855915A CN105347570B CN 105347570 B CN105347570 B CN 105347570B CN 201510855915 A CN201510855915 A CN 201510855915A CN 105347570 B CN105347570 B CN 105347570B
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 101
- 238000001179 sorption measurement Methods 0.000 claims abstract description 38
- 238000007599 discharging Methods 0.000 claims description 34
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 20
- 239000010802 sludge Substances 0.000 claims description 12
- 230000015271 coagulation Effects 0.000 claims description 9
- 238000005345 coagulation Methods 0.000 claims description 9
- 230000001105 regulatory effect Effects 0.000 claims description 9
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 7
- 239000011572 manganese Substances 0.000 claims description 7
- 229910052748 manganese Inorganic materials 0.000 claims description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 6
- 229920000742 Cotton Polymers 0.000 claims description 6
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 239000004576 sand Substances 0.000 claims description 6
- 239000000741 silica gel Substances 0.000 claims description 6
- 229910002027 silica gel Inorganic materials 0.000 claims description 6
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 3
- 239000003830 anthracite Substances 0.000 claims description 3
- 239000003245 coal Substances 0.000 claims description 3
- 238000001514 detection method Methods 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 238000010926 purge Methods 0.000 claims description 3
- 239000002384 drinking water standard Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract 1
- 230000009286 beneficial effect Effects 0.000 description 12
- 238000004062 sedimentation Methods 0.000 description 7
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 238000010276 construction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 231100000614 poison Toxicity 0.000 description 2
- 230000007096 poisonous effect Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000003911 water pollution Methods 0.000 description 2
- 230000001413 cellular effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000035622 drinking Effects 0.000 description 1
- 239000013505 freshwater Substances 0.000 description 1
- 150000002696 manganese Chemical class 0.000 description 1
- 230000000644 propagated effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Landscapes
- Water Treatment By Sorption (AREA)
Abstract
The present invention discloses a kind of water factory's integrative water purifying device,Including the former pond being sequentially connected,Primary settling tower,Tube settling room,Filter chamber and adsorption chamber,Primary settling tower includes inner tower and outside tower,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,Tube settling room bottom is connected by pipeline with primary settling top of tower,Filter chamber top is provided with the water distributor being connected with tube settling room top,Middle part is provided with filter layer,Bottom is provided with delivery port,Multilayer adsorption layer and vertical water distributor are provided with adsorption chamber,The upper end of vertical water distributor passes adsorption layer and connects water-locator,Lower end is stretched out adsorption chamber and is connected with the delivery port of filter chamber,The present invention greatly reduces the turbidity of raw water 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 factory's integrative water purifying device.
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, it is net that the present invention provides a kind of water factory's integration for being applicable to the higher raw water of turbidity
Wetting system.
Technical scheme is as follows：
A kind of water factory's integrative water purifying device, including former pond, primary settling tower, tube settling room, the mistake being sequentially connected
Filter chamber, adsorption chamber and clear water reserviors, its key are：The former pond is connected by inlet channel and the primary settling tower bottom
Connect, the inlet channel is provided with coagulation dosing device, on the inlet channel between the coagulation dosing device and the former pond
Online flow detection meter is connected with, the inlet channel between the coagulation dosing device and the primary settling tower is provided with high pressure
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 can be by online flow monitoring meter Real Time Observation flow of inlet water, and according to this
Regulation add raw water in coagulated agent amount, with the addition of the raw water after coagulated agent pass through primary settling tower deflection plate when, coagulate
The larger alumen ustum meeting preliminary sedimentation of knot on deflection plate and is discharged into Wai Tazhong, and now the turbidity of raw water has substantially reduced, raw water warp
Impurity after the secondary precipitation of tube settling room in water has been substantially removed, then the raw water after filter chamber filters can reach substantially
Drinking water standard, the peculiar smell and poisonous and harmful substance that now raw water remains after adsorption chamber adsorption filtration in water again will be further
Remove.
As preferred：Above-mentioned water-locator includes star-like branch pipe, and the star-like branch pipe external part is connected with same outer endless tube, should
Interior endless tube is provided with outer endless tube, the outer endless tube and interior endless tube are connected with the star-like branch pipe respectively, in the interior endless tube, outer shroud
Water distributing pore is respectively equipped with pipe and star-like branch pipe.Using the beneficial effects of the invention are as follows the narrow meshed water-locator energy of disc type is uniform
The top that water source is distributed to adsorption layer, and larger turbulent water will not be produced.
Above-mentioned star-like branch pipe is Samsung branch pipe, and the angle between adjacent branch pipe is 120 °.Using the beneficial effect of this scheme
Be outer endless tube and interior endless tube fixation it is more firm.
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.
Beneficial effect：
Using the beneficial effects of the invention are as follows can be by online flow monitoring meter Real Time Observation flow of inlet water, and adjust according to this
The coagulated agent amount added in raw water, when with the addition of the raw water after coagulated agent and passing through primary settling tower, the larger alumen ustum of condensation
It can be settled layer by layer on deflection plate, it is reasonable that deflection plate density is set, and shortens the distance of alumen ustum sedimentation, is advantageous to accelerate alumen ustum
Sedimentation, the turbidity of raw water is reduced, raw water can reach substantially by filter chamber filtering again after the secondary precipitation of tube settling room drinks
Water quality standard, the peculiar smell and poisonous and harmful substance that now raw water remains after adsorption chamber adsorption filtration in water again will further be gone
Remove, the device has preferable filtration result to impurity such as the iron in water, manganese in addition, and whole system is reasonable in design, and layout is tight
Gather, greatly save the floor space of structures, be applicable not only to the construction of small-scale water supply plant, more parallel connections can also be passed through
Mode be used for larger water supply plant 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.
Embodiment
With reference to embodiment and accompanying drawing, the invention will be further described.
As Figure 1-3, a kind of water factory's integrative water purifying device, 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 pass through inlet channel 6 and the primary settling
The bottom of tower 1 connects, and 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 water inlet between the coagulation dosing device 9 and the primary settling tower 1
Pipeline 6 is 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 factory's integrative water purifying device, including be sequentially connected former pond (5), primary settling tower (1), tube settling room
(2), filter chamber (3), adsorption chamber (19) and clear water reserviors (20), it is characterised in that：The former pond (5) passes through inlet channel (6)
It is connected with primary settling tower (1) bottom, the inlet channel (6) is provided with coagulation dosing device (9), coagulation dosing dress
Put and online flow detection meter (7), the coagulation dosing device are connected with the inlet channel (6) between (9) and the former pond (5)
(9) inlet channel (6) between the primary settling tower (1) is 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.
2. water factory's integrative water purifying device according to claim 1, it is characterised in that：The water-locator (22) includes star-like
Branch pipe (224), star-like branch pipe (224) external part are connected with same outer endless tube (222), are provided with the outer endless tube (222) interior
Endless tube (223), the outer endless tube (222) and interior endless tube (223) are connected with the star-like branch pipe (224) respectively, in the inner ring
Water distributing pore (221) is respectively equipped with pipe (223), outer endless tube (222) and star-like branch pipe (224).
3. water factory's integrative water purifying device according to claim 2, it is characterised in that：The star-like branch pipe (224) is three
Prong pipe, the angle between adjacent branch pipe is 120 °.
4. water factory's integrative water purifying device according to claim 1 or 2, it is characterised in that：Set below the adsorption layer (4)
There is back purge system (23).
5. water factory's integrative water purifying device according to claim 1, it is characterised in that：The bottom of towe of the outer tower (104) is set
There is the first mud discharging pipe (10), the first mud discharging pipe (10) is provided with the first mud discharging regulating valve (11).
6. water factory's integrative water purifying device according to claim 5, it is characterised in that：Tube settling room (2) bottom
Provided with sludge collection bucket (201), the bottom of the sludge collection bucket (201) is provided with the second mud discharging pipe (16), and described second is dirty
Mud delivery pipe (16) is provided with the second mud discharging regulating valve (17).
7. water factory's integrative water purifying device according to claim 6, it is characterised in that：The first mud discharging regulating valve
(11) and the second described mud discharging regulating valve (17) opening time is at intervals of 20-24 hours.
8. water factory's integrative water purifying device according to claim 4, it is characterised in that：The primary settling tower (1) and tiltedly
It is provided with sludge-tank (13) below pipe mud chamber (2), the primary settling tower (1), tube settling room (2), filter chamber (3) and described
Observation window (12) is equipped with the top of adsorption chamber (19), automatic exhaust steam valve (14) is provided with the top of the tube settling room (2).
9. water factory's integrative water purifying device according to claim 1, it is characterised in that：The filter layer include manganese layer of sand and
The anthracite coal measure being laid on the manganese layer of sand.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510855915.5A CN105347570B (en) | 2015-11-28 | 2015-11-28 | Water factory's integrative water purifying device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510855915.5A CN105347570B (en) | 2015-11-28 | 2015-11-28 | Water factory's integrative water purifying device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105347570A CN105347570A (en) | 2016-02-24 |
| CN105347570B true CN105347570B (en) | 2018-02-16 |
Family
ID=55323666
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510855915.5A Expired - Fee Related CN105347570B (en) | 2015-11-28 | 2015-11-28 | Water factory's integrative water purifying device |
Country Status (1)
| Country | Link |
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| CN (1) | CN105347570B (en) |
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
- 2015-11-28 CN CN201510855915.5A patent/CN105347570B/en not_active Expired - Fee Related
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| Publication number | Publication date |
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| CN105347570A (en) | 2016-02-24 |
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Effective date of registration: 20180115 Address after: 400023 Chongqing Jiangbei District Wujiang Road No. 18 1-1 (room 1-6) Applicant after: CHONGQING HEHUANG TECHNOLOGY CONSULTING Co.,Ltd. Address before: Jianshan village Chongqing city Qijiang County Gunan town 401421 three agency Applicant before: QIJIANG SHIZIQIAO WATER SUPPLY CO.,LTD. |
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Effective date of registration: 20200511 Address after: 400800 first floor, Kechuang building, Wansheng Economic Development Zone, Qijiang District, Chongqing Patentee after: Chongqing Mibu Environmental Protection Technology Co.,Ltd. Address before: 400023 Chongqing Jiangbei District Wujiang Road No. 18 1-1 (room 1-6) Patentee before: CHONGQING HEHUANG TECHNOLOGY CONSULTING Co.,Ltd. |
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Granted publication date: 20180216 Termination date: 20211128 |