CN106477823A - Domestic water cyclic processing device - Google Patents
Domestic water cyclic processing device Download PDFInfo
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- CN106477823A CN106477823A CN201611028984.XA CN201611028984A CN106477823A CN 106477823 A CN106477823 A CN 106477823A CN 201611028984 A CN201611028984 A CN 201611028984A CN 106477823 A CN106477823 A CN 106477823A
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- Prior art keywords
- room
- water
- screening
- reative cell
- processing device
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 89
- 238000012545 processing Methods 0.000 title claims abstract description 21
- 125000004122 cyclic group Chemical group 0.000 title claims abstract description 18
- 238000012216 screening Methods 0.000 claims abstract description 45
- 238000001914 filtration Methods 0.000 claims abstract description 44
- 238000006386 neutralization reaction Methods 0.000 claims abstract description 28
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 22
- 238000005842 biochemical reaction Methods 0.000 claims abstract description 21
- 238000004062 sedimentation Methods 0.000 claims abstract description 16
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000007599 discharging Methods 0.000 claims abstract description 7
- 230000000694 effects Effects 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 claims abstract description 4
- 239000000126 substance Substances 0.000 claims abstract description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 24
- 150000002500 ions Chemical class 0.000 claims description 13
- 229910052742 iron Inorganic materials 0.000 claims description 12
- 238000001223 reverse osmosis Methods 0.000 claims description 11
- 239000000919 ceramic Substances 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 9
- 238000006243 chemical reaction Methods 0.000 claims description 8
- 239000008213 purified water Substances 0.000 claims description 8
- 239000003921 oil Substances 0.000 claims description 7
- 230000001954 sterilising effect Effects 0.000 claims description 5
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 4
- 239000006004 Quartz sand Substances 0.000 claims description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 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 4
- 239000003830 anthracite Substances 0.000 claims description 4
- 239000000835 fiber Substances 0.000 claims description 4
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 4
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 4
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 3
- 238000005516 engineering process Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 241001148471 unidentified anaerobic bacterium Species 0.000 description 1
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
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
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)
- Separation Using Semi-Permeable Membranes (AREA)
- Physical Water Treatments (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention discloses a kind of domestic water cyclic processing device, including:Screening room, is provided with water inlet in screening ceiling portion, water (flow) direction is provided with least one filter in screening interior, is provided with mud discharging mouth in screening room bottom;Sedimentation basin, is provided with flocculant charging point, and the first fan on sedimentation basin;Primary hydroecium, is provided with filter layer in primary water room;Heavy ion filtering tank, heavy ion filtering tank are accepted the water via the process of primary hydroecium and adsorb the heavy metal harmful substance in water;Biochemical reaction room, is provided with the organic filtration floor that biochemical reaction room can be separated into multiple little reative cells in biochemical reaction room;Decolouring disinfection room, decolouring disinfection room include activated carbon filter layer, and disinfection room;Neutralization chamber, neutralization interior are provided with pH value sensor, are provided with nertralizer in neutralization chamber and add mouth, and the first delivery port.Present configuration is simple, disclosure satisfy that use demand, and can reach good using effect.
Description
Technical field
The present invention relates to water-treatment technology field, specifically a kind of domestic water cyclic processing device.
Background technology
China human mortality is numerous, and freshwater resources are but only a quarter of people from world's mean per capita.As demographic and economic is advised
The day by day expansion of mould and the continuous improvement of living standard of urban and rural population level, the increase of water demand amount and Global climate change and environment
Contradiction between the brought scarcity of fresh water resources of pollution is more and more sharp, particularly China North China, the Northwest and some
In megalopolis, water shortage or even cut off the water supply happens occasionally, and substantially constrains the living safety of resident.Therefore, rational life
Effluent cycle recovery and processing system just arises at the historic moment, but the investment of existing processing system is huge, and the scope of the recycle-water for processing is received
Restrict to a lot.
Content of the invention
The technical problem to be solved in the present invention, is to provide a kind of domestic water cyclic processing device, at least can solve existing
One of the problems referred to above having in the presence of technology.
For above-mentioned purpose is reached, the technical scheme is that and be achieved in that:
A kind of domestic water cyclic processing device, including:
Screening room, is provided with water inlet in the screening ceiling portion, water (flow) direction is provided with least one in the screening interior
Individual filter, is provided with mud discharging mouth in screening room bottom;
Sedimentation basin, is provided with flocculant charging point, and the first fan on the sedimentation basin, the sedimentation basin accept via
The flocculant that the water that the screening room is filtered is filled in the flocculant charging point and the effect of the air that the first fan is poured
Under carry out preliminary suspended particulate removal;
Primary hydroecium, is provided with filter layer in the primary water room, goes forward side by side for accepting the water processed via the sedimentation basin
The profound suspended particulate of row is removed;
Heavy ion filtering tank, the heavy ion filtering tank are accepted the water via the primary hydroecium process and adsorb the huge sum of money in water
Category harmful substance;
Biochemical reaction room, is provided with the biochemical reaction room and the biochemical reaction room can be separated into multiple little reative cells
Organic filtration layer;
Decolouring disinfection room, the decolouring disinfection room include activated carbon filter layer, and disinfection room;
Neutralization chamber, the neutralization interior are provided with pH value sensor, are provided with nertralizer in the neutralization chamber and add mouth, Yi Ji
One delivery port.
As restriction, also include:
Reverse osmosis cell, the reverse osmosis cell include the negative-ion fiber film that the reverse osmosis cell is separated into two chambeies, close to
The chamber of the neutralization chamber is accepted the water of the indoor neutralization of the neutralization and carries out salinity and small organic molecule filtration, in another chamber
Bottom is provided with valve;
Purified water collecting room, the purified water collecting room are connected with another chamber described via valve, and are received in the pure water
Collection room bottom is provided with the second delivery port.
As limiting further, three filters are disposed with the screening interior along water (flow) direction, respectively
The screening room is separated into four cells by the first screening net, the second screening net and the 3rd screening net, three filters,
The mud discharging mouth is respectively communicated with and arranges in four cell bottoms.
Used as further limiting, the first screening net includes to be formed with thereon the first iron net of multiple first meshes,
And the oil suction felt being covered in first iron net.
Used as further limiting, the second screening net and the 3rd screening net include to be formed with multiple second thereon respectively
Two the second iron nets of mesh, and two pieces of oil suction felts being covered each by second iron net, second mesh
Diameter is less than the diameter of the first mesh.
Used as restriction, the filter layer is made up of quartz sand, anthracite, particles of silicon carbide.
As restriction, in the heavy ion filtering tank, ceramic particle is filled with.
Used as restriction, the organic filtration floor is included laterally with by the biochemical reaction in the biochemical reaction room
Room is separated into the first organic filtration floor of the first little reative cell and the second reative cell, and indoor with by the located at the second reaction
Two reative cells are longitudinally separated into anti-zigzag the second organic filtration layer of the 3rd reative cell and the second little reative cell, also include to set
Indoor little anti-so that the 3rd reative cell is divided transversely into the 3rd little reative cell, the 4th little reative cell and the 5th in the 3rd reaction
Answer two the 3rd organic filtration floor of room;The first little reative cell, the second little reative cell and the 3rd little reative cell are all connected
The second fan of filling air, the 4th little reative cell and the 5th little reative cell is had to be anaerobic room.
As limiting further, the first organic filtration layer, the second organic filtration layer and the 3rd organic filtration
Layer all includes ceramic grid, and the biomembrane for being overlying on the pottery grid outer surface.
Used as restriction, the sterilization interior is filled with ozone, and is provided with the ultraviolet lamp that can send ultraviolet.
The present invention due to employing above-mentioned structure, its compared with prior art, acquired technological progress is:
(1)The present invention is by setting gradually screening room, sedimentation basin, primary hydroecium, heavy ion filtering tank, biochemical reaction room, decolouring
Domestic water circular treatment can be become primary domestic water by disinfection room, neutralization chamber, that is, be used for rinsing;
(2)Water can be continued with into pure water by arranging reverse osmosis cell, and purified water collecting room again by the present invention, with
Normal use for domestic water.
(3)By three filters being disposed with screening interior along water (flow) direction, can filter sump oil, miscellaneous successively
Thing silt and bulky grain suspending sundries.
(4)By filter layer to be arranged to be made up of quartz sand, anthracite, particles of silicon carbide, can be effectively isolated in water
Suspended particle.
(5)By ceramic particle will be filled with heavy ion filtering tank, can effectively adsorb the heavy metal nuisance in water
Matter.
(6)By arranging the first little reative cell, the second little reative cell, the 3rd little reative cell, the 4th little reative cell and the 5th
Little reative cell, degraded most of the nitrogen capable of circulation, phosphorus organic matter.
(7)By ceramic grid is arranged, the organic matter after degraded is can support and filters;By covering in ceramic grid outer surface
There is biomembrane, the mutual propagation that can effectively completely cut off aerobic bacterium and anaerobic bacteria forms independent aerobic/anaerobic environment.
(8)By ozone being filled with sterilization interior, and be provided with the ultraviolet lamp that can send ultraviolet, kill can sterilization
Bacterium operation is simpler.
To sum up, present configuration is simple, disclosure satisfy that use demand, and can reach good using effect.
Description of the drawings
Accompanying drawing is used for providing a further understanding of the present invention, and constitutes a part for specification, the reality with the present invention
Example is applied together for the present invention is explained, be not construed as limiting the invention.
Fig. 1 is the use state figure of the domestic water cyclic processing device described in the embodiment of the present invention.
In figure:
1- screens room, and 111- first screens net, and 112- second screens net, and 113- the 3rd screens net, and 12- water inlet, 13- sludge are arranged
Put mouth, the first water pump of 14-, 2- sedimentation basin, 21- flocculant charging point, the first fan of 22-, 3- primary hydroecium, 31- filter layer,
The second water pump of 32-, 4- heavy ion filtering tank, 5- biochemical reaction room, the second fan of 51-, 52- organic filtration layer, 521- first
Little reative cell, the second little reative cell, the 3rd little reative cell, the 4th little reative cell of 522-, the 5th little reative cell, the 3rd water pump of 53-,
6- decolouring disinfection room, 61- activated carbon filter layer, 62- disinfection room, the 4th water pump of 63-, 7- neutralization chamber, 71-PH value sensor, 72-
5th water pump, the first delivery port of 73-, 8- reverse osmosis cell, 81- negative-ion fiber film, 82- valve, 9- purified water collecting room, 91-
Second delivery port.
Specific embodiment
With reference to the accompanying drawings and examples, the present invention is expanded on further.In the following detailed description, only by explanation
Mode describes some one exemplary embodiment of the present invention.Undoubtedly, one of ordinary skill in the art will recognize,
In the case of without departing from the spirit and scope of the present invention, can be to be repaiied to described embodiment with a variety of modes
Just.Therefore, accompanying drawing is inherently illustrative with description, rather than for limiting scope of the claims.
As shown in figure 1, according to the domestic water cyclic processing device of the present embodiment, its overall structure includes to screen room 1, sinks
Shallow lake pond 2, primary hydroecium 3, heavy ion filtering tank 4, biochemical reaction room 5, decolouring disinfection room 6, neutralization chamber 7, specifically, in screening room
1 top is provided with water inlet 12, water (flow) direction is provided with least one filter in screening room 1, in screening 1 bottom of room
Mud discharging mouth 13 is provided with, and on concrete structure, in the present embodiment, in screening room 1, three mistakes is disposed with along water (flow) direction
Filter device, the respectively first screening net 111, second screen net 112 and the 3rd screening net 113, and three filters will screen room 1
Four cells are separated into, mud discharging mouth 13 is respectively communicated with and arranges in four cell bottoms, the first screening net 111 includes shape thereon
Becoming has the first iron net of multiple first meshes, and the oil suction felt being covered in the first iron net, the second screening net 112 and the 3rd
Screening net 113 includes to be formed with thereon two the second iron nets of multiple second meshes respectively, and is covered each by the second iron net
On two pieces of oil suction felts, the diameter of the second mesh is less than the diameter of the first mesh.
In the present embodiment, flocculant charging point 21, and the first fan 2 is provided with sedimentation basin 2, sedimentation basin 2 is accepted
The flocculant that fills in flocculant charging point 21 of water filtered via screening room 1 and the work of air that pours of the first fan 2
With under carry out preliminary suspended particulate removal, in the present embodiment, the little interior of screening after the 3rd screening net 113 is screened is provided with first
Water pump 14, will screen in the water suction sedimentation basin 2 after little lab screening.
In the present embodiment, in primary hydroecium 3, filter layer 31 is provided with, for accepting the water processed via sedimentation basin 2 simultaneously
The suspended particulate for carrying out profound level is removed, and on concrete structure, filter layer 31 is made up of quartz sand, anthracite, particles of silicon carbide, this
In embodiment, in the primary hydroecium 3 after filter layer 31 is filtered, the second water pump 32 is provided with, after filtering in primary hydroecium 3
In water suction heavy ion filtering tank 4.In the present embodiment, heavy ion filtering tank 4 is accepted the water via the process of primary hydroecium 3 and is adsorbed
Heavy metal harmful substance in water, on concrete structure, is filled with ceramic particle in heavy ion filtering tank 4.
In the present embodiment, it is provided with and biochemical reaction room 5 can be separated into having for multiple little reative cells in biochemical reaction room 5
Machine thing filter layer 52, on concrete structure, organic filtration floor 52 is included laterally with by biochemical reaction room in biochemical reaction room 5
5 the first organic filtration layers for being separated into the first little reative cell 521 and the second reative cell 521, and indoor located at the second reaction
So that the second reative cell to be longitudinally separated into anti-zigzag the second organic filtration layer of the 3rd reative cell and the second little reative cell 521,
Also include located at the 3rd reaction interior so that the 3rd reative cell is divided transversely into the 3rd little reative cell 521, the 4th little reative cell 522
Two the 3rd organic filtration layers with the 5th little reative cell 522;First little reative cell 521, the second little reative cell 521 and the 3rd
Little reative cell 521 is all communicated with the second fan 51 of filling air, and the 4th little reative cell 522 and the 5th little reative cell 522 are
Anaerobic room.In the present embodiment, the first organic filtration layer, the second organic filtration layer and the 3rd organic filtration layer all include pottery
Porcelain grid, and it is overlying on the biomembrane of ceramic grid outer surface.
In the present embodiment, decolouring disinfection room 6 includes activated carbon filter layer 61, and disinfection room 62;Filling in disinfection room 62
There is ozone, and the ultraviolet lamp that can send ultraviolet is provided with, the 3rd water pump 53 is provided with biochemical reaction room 5, by biochemistry
In reative cell 5 in the water suction neutralization chamber 7 of reaction.In the present embodiment, pH value sensor 71 is provided with neutralization chamber 7, in neutralization
Room 7 is provided with nertralizer and adds mouth, and the first delivery port 73, is provided with the 4th water pump 63 in decolouring disinfection room 6, will decolourize
In water suction neutralization chamber 7 after sterilization, meta-alkalescence, via in neutralization chamber 7 and after water, can be used for primary domestic water, i.e.,
For bath etc..
In the present embodiment, reverse osmosis cell 8 includes the negative-ion fiber film 81 that reverse osmosis cell 8 is separated into two chambeies, close
The water of the interior neutralization of neutralization chamber 7 is accepted in the chamber of neutralization chamber 7 and salinity and small organic molecule filtration is carried out, in another bottom of chamber portion
Valve 82 is provided with, and the 5th water pump 72 is provided with neutralization chamber 7, by the water suction reverse osmosis cell 8 in neutralization chamber 7;This
In embodiment, purified water collecting room 9 is connected with another chamber via valve 82, and is provided with second in 9 bottom of purified water collecting room
Delivery port 91.
The schematic specific embodiment of the present invention is the foregoing is only, is not limited to the scope of the present invention.Any
Those skilled in the art, the equivalent variations that is made on the premise of the design without departing from the present invention and principle and modification, all
The scope of protection of the invention should be belonged to.
Claims (10)
1. a kind of domestic water cyclic processing device, it is characterised in that include:
Screening room, is provided with water inlet in the screening ceiling portion, water (flow) direction is provided with least one in the screening interior
Individual filter, is provided with mud discharging mouth in screening room bottom;
Sedimentation basin, is provided with flocculant charging point, and the first fan on the sedimentation basin, the sedimentation basin accept via
The flocculant that the water that the screening room is filtered is filled in the flocculant charging point and the effect of the air that the first fan is poured
Under carry out preliminary suspended particulate removal;
Primary hydroecium, is provided with filter layer in the primary water room, goes forward side by side for accepting the water processed via the sedimentation basin
The profound suspended particulate of row is removed;
Heavy ion filtering tank, the heavy ion filtering tank are accepted the water via the primary hydroecium process and adsorb the huge sum of money in water
Category harmful substance;
Biochemical reaction room, is provided with the biochemical reaction room and the biochemical reaction room can be separated into multiple little reative cells
Organic filtration layer;
Decolouring disinfection room, the decolouring disinfection room include activated carbon filter layer, and disinfection room;
Neutralization chamber, the neutralization interior are provided with pH value sensor, are provided with nertralizer in the neutralization chamber and add mouth, Yi Ji
One delivery port.
2. domestic water cyclic processing device according to claim 1, it is characterised in that also include:
Reverse osmosis cell, the reverse osmosis cell include the negative-ion fiber film that the reverse osmosis cell is separated into two chambeies, close to
The chamber of the neutralization chamber is accepted the water of the indoor neutralization of the neutralization and carries out salinity and small organic molecule filtration, in another chamber
Bottom is provided with valve;
Purified water collecting room, the purified water collecting room are connected with another chamber described via valve, and are received in the pure water
Collection room bottom is provided with the second delivery port.
3. domestic water cyclic processing device according to claim 1 and 2, it is characterised in that:In the indoor edge of the screening
Water (flow) direction is disposed with three filters, the respectively first screening net, the second screening net and the 3rd screening net, and described three
The screening room is separated into four cells by individual filter, and the mud discharging mouth is respectively communicated with and sets in four cell bottoms
Put.
4. domestic water cyclic processing device according to claim 3, it is characterised in that:The first screening net includes which
On be formed with the first iron net of multiple first meshes, and the oil suction felt being covered in first iron net.
5. domestic water cyclic processing device according to claim 4, it is characterised in that:The second screening net and the 3rd
Screening net includes to be formed with thereon two the second iron nets of multiple second meshes respectively, and is covered each by second iron net
On two pieces of oil suction felts, the diameter of second mesh is less than the diameter of the first mesh.
6. domestic water cyclic processing device according to claim 1, it is characterised in that:The filter layer by quartz sand,
Anthracite, particles of silicon carbide composition.
7. domestic water cyclic processing device according to claim 1, it is characterised in that:Fill out in the heavy ion filtering tank
It is filled with ceramic particle.
8. domestic water cyclic processing device according to claim 1, it is characterised in that:The organic filtration layer includes
Laterally so that the biochemical reaction room to be separated into the of the first little reative cell and the second reative cell in the biochemical reaction room
One organic filtration layer, and indoor so that the second reative cell is longitudinally separated into the 3rd reative cell and second little located at the second reaction
Anti- zigzag the second organic filtration layer of reative cell, also includes indoor with will be horizontal for the 3rd reative cell located at the 3rd reaction
It is separated into two the 3rd organic filtration layers of the 3rd little reative cell, the 4th little reative cell and the 5th little reative cell;Described first
Little reative cell, the second little reative cell and the 3rd little reative cell are all communicated with the second fan of filling air, the 4th little reaction
Room and the 5th little reative cell are anaerobic room.
9. domestic water cyclic processing device according to claim 8, it is characterised in that:First organic filtration
Layer, the second organic filtration layer and the 3rd organic filtration layer all include ceramic grid, and are overlying on the pottery grid appearance
The biomembrane in face.
10. domestic water cyclic processing device according to claim 1, it is characterised in that:The sterilization interior is filled with
Ozone, and it is provided with the ultraviolet lamp that can send ultraviolet.
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CN201611028984.XA CN106477823A (en) | 2016-11-22 | 2016-11-22 | Domestic water cyclic processing device |
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CN201611028984.XA CN106477823A (en) | 2016-11-22 | 2016-11-22 | Domestic water cyclic processing device |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108409041A (en) * | 2018-03-26 | 2018-08-17 | 韩秀英 | A kind of sanitary sewage multi-stage treatment units |
CN109422416A (en) * | 2017-08-22 | 2019-03-05 | 江苏佳鑫环保工程有限公司 | A kind of integrated sewage treating apparatus and its method |
CN110357313A (en) * | 2019-08-16 | 2019-10-22 | 丽江尚源水业有限公司 | A kind of efficient absorption and filter method producing pure water |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1090356A (en) * | 1993-01-29 | 1994-08-03 | 铁岭市环境保护科学研究所 | Closed ciculation method for water used in producing paper by regenerated pulp |
CN203238140U (en) * | 2013-05-13 | 2013-10-16 | 天津中海汇通科技有限公司 | Multi-stage deep wastewater circulating treatment system |
CN104193081A (en) * | 2014-07-25 | 2014-12-10 | 席北斗 | Device for filtering sewage step by step and method for treating sewage by using device |
CN204058150U (en) * | 2014-08-22 | 2014-12-31 | 天津亿安瑞科技有限公司 | A kind of recycled water in family recycling and processing equipment |
CN104803560A (en) * | 2015-04-23 | 2015-07-29 | 河南鑫饰板业有限公司 | Method for manufacturing precipitated lignin from production waste water of man-made fiber boards |
CN106007201A (en) * | 2016-07-05 | 2016-10-12 | 嘉兴悟净环保科技有限公司 | Livestock and poultry breeding wastewater treating technology |
CN206204113U (en) * | 2016-11-22 | 2017-05-31 | 安一方 | A kind of household water cyclic processing device |
-
2016
- 2016-11-22 CN CN201611028984.XA patent/CN106477823A/en not_active Withdrawn
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1090356A (en) * | 1993-01-29 | 1994-08-03 | 铁岭市环境保护科学研究所 | Closed ciculation method for water used in producing paper by regenerated pulp |
CN203238140U (en) * | 2013-05-13 | 2013-10-16 | 天津中海汇通科技有限公司 | Multi-stage deep wastewater circulating treatment system |
CN104193081A (en) * | 2014-07-25 | 2014-12-10 | 席北斗 | Device for filtering sewage step by step and method for treating sewage by using device |
CN204058150U (en) * | 2014-08-22 | 2014-12-31 | 天津亿安瑞科技有限公司 | A kind of recycled water in family recycling and processing equipment |
CN104803560A (en) * | 2015-04-23 | 2015-07-29 | 河南鑫饰板业有限公司 | Method for manufacturing precipitated lignin from production waste water of man-made fiber boards |
CN106007201A (en) * | 2016-07-05 | 2016-10-12 | 嘉兴悟净环保科技有限公司 | Livestock and poultry breeding wastewater treating technology |
CN206204113U (en) * | 2016-11-22 | 2017-05-31 | 安一方 | A kind of household water cyclic processing device |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109422416A (en) * | 2017-08-22 | 2019-03-05 | 江苏佳鑫环保工程有限公司 | A kind of integrated sewage treating apparatus and its method |
CN108409041A (en) * | 2018-03-26 | 2018-08-17 | 韩秀英 | A kind of sanitary sewage multi-stage treatment units |
CN110357313A (en) * | 2019-08-16 | 2019-10-22 | 丽江尚源水业有限公司 | A kind of efficient absorption and filter method producing pure water |
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