CN106746354A - A kind of sewage in-situ processes integrated equipment - Google Patents
A kind of sewage in-situ processes integrated equipment Download PDFInfo
- Publication number
- CN106746354A CN106746354A CN201710046754.4A CN201710046754A CN106746354A CN 106746354 A CN106746354 A CN 106746354A CN 201710046754 A CN201710046754 A CN 201710046754A CN 106746354 A CN106746354 A CN 106746354A
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- Prior art keywords
- storehouse
- sewage
- enriched
- oxygen
- absorption
- Prior art date
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- 239000010865 sewage Substances 0.000 title claims abstract description 40
- 238000000034 method Methods 0.000 title claims abstract description 24
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 60
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 60
- 239000001301 oxygen Substances 0.000 claims abstract description 60
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 47
- 238000010521 absorption reaction Methods 0.000 claims abstract description 43
- 230000004913 activation Effects 0.000 claims abstract description 33
- 244000005700 microbiome Species 0.000 claims description 19
- 230000000694 effects Effects 0.000 claims description 12
- 239000011149 active material Substances 0.000 claims description 11
- 238000005273 aeration Methods 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 102000004169 proteins and genes Human genes 0.000 claims description 3
- 108090000623 proteins and genes Proteins 0.000 claims description 3
- 235000013619 trace mineral Nutrition 0.000 claims description 3
- 239000011573 trace mineral Substances 0.000 claims description 3
- 238000001556 precipitation Methods 0.000 claims 1
- 239000000463 material Substances 0.000 description 11
- 229910001220 stainless steel Inorganic materials 0.000 description 7
- 239000010935 stainless steel Substances 0.000 description 7
- 239000013049 sediment Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 235000013339 cereals Nutrition 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 235000010958 polyglycerol polyricinoleate Nutrition 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000035558 fertility Effects 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 230000000050 nutritive effect Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000005067 remediation Methods 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000003403 water pollutant Substances 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
- C02F1/28—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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F2003/001—Biological treatment of water, waste water, or sewage using granular carriers or supports for the microorganisms
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/004—Apparatus and plants for the biological treatment of water, waste water or sewage comprising a selector reactor for promoting floc-forming or other bacteria
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2203/00—Apparatus and plants for the biological treatment of water, waste water or sewage
- C02F2203/006—Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/06—Nutrients for stimulating the growth of microorganisms
-
- 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
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
-
- 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
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
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)
- Aeration Devices For Treatment Of Activated Polluted Sludge (AREA)
Abstract
The invention discloses a kind of sewage in-situ treatment integrated equipment, it is disposed with multiple water process storehouses, the pipeline that can make drainage flow is provided between two adjacent water process storehouses, the multiple water process storehouse is successively settling banker, activation storehouse, oxygen-enriched storehouse, biochemical bin and absorption storehouse, the sewage sequentially pass through settling banker, activation storehouse, oxygen-enriched storehouse, biochemical bin and absorption storehouse sewage is processed after, finally by absorption storehouse delivery port flow out.Present device uses Integrated design, easy to use, and continuous processing is carried out to sewage by multiple treatment storehouse, and sewage treating efficiency is high.
Description
Technical field
The present invention relates to field of environment protection, more particularly to a kind of sewage in-situ treatment integrated equipment.
Background technology
Microorganism can not only remove water pollutant as the analyst in the ecosystem, to nutritional ingredient in water
Circulation also plays an important role, and some microorganisms for having Special Decomposition conversion capability play important work in river ecosystem restoration
With.One of which microorganism remediation technology is exactly that this technology exists by adding nutriment, promoting the growth of indigenous microorganism
It is widely applied in domestic and international river pollution.But the technology there is also some drawbacks, the nutriment for adding easily is made
Into the secondary pollution in river.The secondary pollution for wanting to avoid the technology from bringing is accomplished by developing some auxiliary equipments avoiding seeking
Foster material is directly added in polluted-water.Simultaneously because the volume that existing water treatment facilities has is excessive, area occupied is excessive,
What is had is integrated not high, and complex operation, fault rate is high.
The content of the invention
To overcome above-mentioned technological deficiency, Integrated design is used the invention discloses one kind, easy to use, the dirt of plug and play
Water in-situ treatment integrated equipment.
Technical solution of the present invention is as described below：
A kind of sewage in-situ processes integrated equipment, is disposed with multiple water process storehouses, adjacent two water process storehouses it
Between be provided with the pipeline that can make drainage flow, the multiple water process storehouse is successively settling banker, activation storehouse, oxygen-enriched storehouse, biochemical bin
With absorption storehouse, the sewage sequentially pass through settling banker, activation storehouse, oxygen-enriched storehouse, biochemical bin and absorption storehouse sewage is processed after,
Flowed out finally by the delivery port in absorption storehouse.
The bottom in the settling banker, oxygen-enriched storehouse, biochemical bin and absorption storehouse is funnel-shaped structure, the sewage in-situ treatment
Integrated equipment is additionally provided with blow-off pipe, and the bottom in the settling banker, oxygen-enriched storehouse, biochemical bin and absorption storehouse is exported and blowdown by ball valve
Pipe UNICOM.
Being delivered in the activation storehouse has microorganism active material, and the microorganism active material contains carbon source, trace element
And protein, the active material surface is in loose structure, and particle diameter is 4-10 millimeters, and density is 1.1-1.3 grams/cc.
The activation storehouse is U-shape structure.
The activation storehouse is arranged on oxygen-enriched storehouse top, and the delivery port in the activation storehouse is cell structure.
A settling banker dividing plate for activity is provided with settling banker, the settling banker dividing plate and oxygen-enriched storehouse outer wall constitute one
Individual settling banker outlet conduit, the sewage of the settling banker is flowed into activation storehouse by settling banker outlet conduit, is set in oxygen-enriched storehouse
An oxygen-enriched storehouse dividing plate for activity is equipped with, the oxygen-enriched storehouse dividing plate and biochemical bin outer wall constitute an oxygen-enriched storehouse outlet conduit, institute
The sewage for stating oxygen-enriched storehouse is flowed into biochemical bin by oxygen-enriched storehouse outlet conduit, and a biochemical bin for activity is provided with biochemical bin
Dividing plate, the biochemical bin dividing plate and absorption storehouse outer wall constitute a biochemical bin outlet conduit, and the sewage of the biochemical bin is by life
Change storehouse outlet conduit to flow into absorption storehouse, an absorption storehouse dividing plate for activity, absorption storehouse dividing plate are provided with absorption storehouse
An absorption storehouse outlet conduit is constituted with absorption storehouse inwall, the sewage in the absorption storehouse flows out by adsorbing storehouse outlet conduit.
The bottom in oxygen-enriched storehouse is provided with micropore aeration pipe.
Blast area is provided with the top of oxygen-enriched storehouse, air conduit is provided between the blast area and micropore aeration pipe.
The blast area is separated by dividing plate and is arranged with the first cabin and the second cabin, and air inlet is provided with first cabin
And air blower, air conduit is connected on the air blower, air outlet is provided with second cabin, air inlet and air outlet are distinguished
Positioned at blast area both sides, be additionally provided with the second cabin grid and activation storehouse communicate, first cabin bottom be provided with dividing plate with
Oxygen-enriched storehouse separates, and second cabin and oxygen-enriched storehouse communicate.
The biochemical bin and absorption storehouse bottom are provided with web plate, the web plate specification is 5-10 mesh, screen distance be 3-5 in the least
Rice.
Beneficial effects of the present invention：
(1) equipment uses Integrated design, easy to use, plug and play；
(2) funnel-shaped bottom portion design, enables to sediment effectively to assemble, and spoil disposal is more abundant；
(3) unique U-shape structure microorganism activation storehouse, it can be ensured that water body is sufficiently mixed with microorganism active material, connects
Touch, greatly improve the activity and fertility of microorganism, improve biochemical efficiency；
(4) Low-noise air blower is used, the blinds design in air port is added, the noise of equipment operation can be substantially reduced.
Brief description of the drawings
Fig. 1 is structural representation of the invention；
Fig. 2 is the overlooking the structure diagram of blast area 11 in Fig. 1.
Specific embodiment
Below will the present invention is described in detail by specific embodiment.
Schematic structural view of the invention is as shown in figure 1, a kind of sewage in-situ treatment integrated equipment, is disposed with multiple water
Reason storehouse, is provided with the pipeline that can make water body flow between two adjacent water process storehouses, the multiple water process storehouse is successively heavy
Shallow lake storehouse 2, activation storehouse 3, oxygen-enriched storehouse 4, biochemical bin 5 and absorption storehouse 6.The settling banker 2, oxygen-enriched storehouse 4, biochemical bin 5 and absorption storehouse 6
Bottom is funnel-shaped structure.Sewage in-situ treatment integrated equipment is additionally provided with blow-off pipe 7, the settling banker 2, oxygen-enriched storehouse 4,
The bottom in biochemical bin 5 and absorption storehouse 6 exports 6 and the UNICOM of blow-off pipe 7 by ball valve.The activation storehouse 3 is arranged on oxygen-enriched storehouse 4
Portion, the delivery port in the activation storehouse 3 is cell structure 9.The bottom in oxygen-enriched storehouse 4 is provided with micropore aeration pipe 10.In oxygen-enriched storehouse 4
Top be provided with blast area 11, air conduit 12 is provided between the blast area 11 and micropore aeration pipe 10.The air blast
Plot structure is arranged with the first cabin and the second cabin as shown in Fig. 2 separating 1104 by dividing plate, and air intake is provided with first cabin
Mouth 1101 and air blower 1103, connect air conduit 12 on the air blower 1103, air outlet is provided with second cabin
1102, air inlet 1101 and air outlet 1102 are located at blast area both sides respectively, and grid 17 and activation are additionally provided with the second cabin
Storehouse 3 communicates, and first cabin bottom is provided with dividing plate and separates with oxygen-enriched storehouse 4, and second cabin and oxygen-enriched storehouse 4 communicate.
The biochemical bin 5 and the absorption bottom of storehouse 6 are provided with web plate 13.The direction of arrow in Fig. 1 is water body flow direction
Figure.
The pipeline that water body flow can be allow between each water process storehouse of the invention is common pipeline, it is also possible to by water
Pump operated, it is also possible to complete the flowing of water body using law of connected vessels by dividing plate 15, concrete scheme is as follows：In settling banker 2
It is provided with a settling banker dividing plate 15 for activity, the outer wall in the settling banker dividing plate 15 and oxygen-enriched storehouse 4 constitutes a settling banker and goes out
Waterpipe, the delivery port of the settling banker outlet conduit is arranged on activation storehouse top, and the sewage of the settling banker 2 is gone out by settling banker
Waterpipe is flowed into activation storehouse 3, and an oxygen-enriched storehouse dividing plate 15 for activity, the oxygen-enriched storehouse dividing plate 15 are provided with oxygen-enriched storehouse 4
An oxygen-enriched storehouse outlet conduit is constituted with biochemical bin outer wall, the sewage in the oxygen-enriched storehouse 4 flows into life by oxygen-enriched storehouse outlet conduit
Change in storehouse 5, a biochemical bin dividing plate 15 for activity, the biochemical bin dividing plate 15 and the absorption outer wall of storehouse 6 are provided with biochemical bin 5
A biochemical bin outlet conduit is constituted, the sewage of the biochemical bin 5 is flowed into absorption storehouse 6 by biochemical bin outlet conduit, inhaled
An absorption storehouse dividing plate 15 for activity is provided with attached storehouse 6,6 walls constitute an absorption in absorption storehouse dividing plate 15 and absorption storehouse
Storehouse outlet conduit, the sewage in the absorption storehouse is flowed out by adsorbing storehouse outlet conduit.
When the present invention starts working, sewage enters settling banker 2 by water inlet pipe 1, and settling banker 2 uses stainless steel material
Prepare, the bottom of settling banker 2 is designed using funnel shaped, and after water body enters settling banker 2, water volume flow rate slows down, and can cause water
Large particulate matter in body is precipitated to funnel-shaped bottom portion, and discharge bulky grain is connected with blow-off pipe 7 by the ball valve of the bottom of settling banker 2
Sediment.One pipeline is set between settling banker 2 and activation storehouse 3, and the water body of settling banker 2 enters activation storehouse 3 by the pipeline,
The water inlet of the pipeline is located at the middle and lower part for settling banker 2, and the delivery port of the pipeline is located at the top in activation storehouse 3, according to reality
Need, can be operated by water pump can also carry out water body flow by law of connected vessels.
Being delivered in activation storehouse 3 has microorganism active material, after water body enters activation storehouse 3, swashs with the microorganism in activation storehouse 3
Material living is sufficiently mixed, contacts, stirs, and the characteristic of PGPR microorganisms in water body can be activated using microorganism active material, is made
The PGPR microorganisms obtained in water body can effectively be activated, be bred, and the microorganism after activation is entered with current by grid 9
Oxygen-enriched storehouse 4.Microorganism active material uses the single-size of the composition of nutritive substances such as carbon source, trace element, protein, and surface is in
Many hollow structures, between 4-10 millimeters, between 1.1-1.3 grams/cc, color is in faint yellow or off-white to density to particle diameter
Color, uniform color.Grid 9 is made of stainless steel material, and the spacing of grid 9 can intercept the micro- life of bulky grain between 1-2 millimeters
Thing active material leaves microorganism activation storehouse, while ensureing that water body is passed through into oxygen-enriched storehouse 4.
Oxygen-enriched storehouse 4 is made of stainless steel material, and the bottom in oxygen-enriched storehouse 4 is designed using funnel shaped, and the bottom of oxygen-enriched storehouse 3 is also
Micropore aerating pipe 10 is provided with, water body is by the way that after aeration, the activated sludge of generation is precipitated to funnel-shaped bottom portion, passes through in oxygen-enriched storehouse 4
Ball valve is connected discharge with blow-off pipe 7.In order to more effectively be aerated, the top in oxygen-enriched storehouse 4 is provided with blast area 11, is placed on stainless
On steel steel diaphragm, air is delivered to micropore aeration pipe 10 by blast area 11 by air blower by air conduit 12, and air is from micro-
Hole aeration 10 enters oxygen-enriched storehouse 4, forms tiny bubble, is fully contacted with water body, increases Dissolved Oxygen in Water.Also set in blast area
It is air inlet and air outlet to be equipped with 7, and the two is designed using blinds, with rainproof function.
Water body enters biochemical bin 5 after increased Dissolved Oxygen in Water by oxygen-enriched storehouse 4 by pipeline.Biochemical bin 5 is using stainless
Steel material is made, and the bottom of biochemical bin 5 is designed using funnel shaped, and bottom is provided with web plate 13, the upslide of web plate 13 in biochemical bin 5
Combined stuffing is placed with, the microorganism in water body can be attached to combined stuffing surface, forms biomembrane, after biofilm detachment, sunk
Form sediment to funnel-shaped bottom portion, be connected with blow-off pipe 7 by ball valve.Water body is by entering absorption storehouse 6 after biochemical bin 5.
Absorption storehouse 6 is made of stainless steel material, and the bottom for adsorbing storehouse 6 is designed using funnel shaped, and is provided with stainless steel
Web plate 14, web plate specification is 5-10 mesh, and screen distance is between 3 and 5 millimeters.Sorbing material, adsorption material are placed on stainless steel web plate 14
Material is mainly haydite, volcanic rock, the mixture of activated carbon, and in irregular particle shape, diameter is between 8-15 millimeters.Sorbing material
Surface is loose structure, suspension that can be in adsorbed water body, so as to improve water transparency.Water body leads to after adsorbing storehouse 6
Cross the water outlet of delivery port 16.
In sum, although specific embodiment of the invention is to the present invention have been described in detail, this area is general
Technical staff it is to be understood that above-described embodiment is only the description to the preferred embodiments of the present invention, rather than to the present invention
The limitation of protection domain, persons skilled in the art disclosed herein technical scope in, the change that can be readily occurred in,
Within protection scope of the present invention.
Claims (10)
1. a kind of sewage in-situ processes integrated equipment, it is characterised in that：It is disposed with multiple water process storehouses, two adjacent water
Treatment is provided with the pipeline that can make drainage flow between storehouse, and the multiple water process storehouse is successively settling banker, activation storehouse, oxygen-enriched
Storehouse, biochemical bin and absorption storehouse, the sewage sequentially pass through settling banker, activation storehouse, oxygen-enriched storehouse, biochemical bin and absorption storehouse and sewage are entered
After row treatment, flowed out finally by the delivery port in absorption storehouse.
2. sewage in-situ as claimed in claim 1 processes integrated equipment, it is characterised in that：The settling banker, oxygen-enriched storehouse, biochemistry
The bottom in storehouse and absorption storehouse is funnel-shaped structure, and the sewage in-situ treatment integrated equipment is additionally provided with blow-off pipe, the precipitation
The bottom in storehouse, oxygen-enriched storehouse, biochemical bin and absorption storehouse is exported and blow-off pipe UNICOM by ball valve.
3. sewage in-situ as claimed in claim 1 processes integrated equipment, it is characterised in that：Being delivered in the activation storehouse has micro- life
Thing active material, the microorganism active material contains carbon source, trace element and protein, and the active material surface is in porous
Structure, particle diameter is 4-10 millimeters, and density is 1.1-1.3 grams/cc.
4. sewage in-situ as claimed in claim 1 processes integrated equipment, it is characterised in that：The activation storehouse is U-shape structure.
5. sewage in-situ as claimed in claim 1 processes integrated equipment, it is characterised in that：The activation storehouse is arranged on oxygen-enriched storehouse
Top, the delivery port in the activation storehouse is cell structure.
6. sewage in-situ as claimed in claim 5 processes integrated equipment, it is characterised in that：A work is provided with settling banker
Dynamic settling banker dividing plate, the settling banker dividing plate and oxygen-enriched storehouse outer wall constitute a settling banker outlet conduit, the settling banker
Sewage is flowed into activation storehouse by settling banker outlet conduit, and an oxygen-enriched storehouse dividing plate for activity is provided with oxygen-enriched storehouse, described
Oxygen-enriched storehouse dividing plate and biochemical bin outer wall constitute an oxygen-enriched storehouse outlet conduit, and the sewage in the oxygen-enriched storehouse passes through oxygen-enriched storehouse outlet pipe
Road is flowed into biochemical bin, a biochemical bin dividing plate for activity is provided with biochemical bin, outside the biochemical bin dividing plate and absorption storehouse
Wall constitutes a biochemical bin outlet conduit, and the sewage of the biochemical bin is flowed into absorption storehouse by biochemical bin outlet conduit, inhaled
An absorption storehouse dividing plate for activity is provided with attached storehouse, absorption storehouse dividing plate and absorption storehouse inwall constitute an absorption storehouse water outlet
Pipeline, the sewage in the absorption storehouse is flowed out by adsorbing storehouse outlet conduit.
7. sewage in-situ as claimed in claim 1 processes integrated equipment, it is characterised in that：It is provided with the bottom in oxygen-enriched storehouse micro-
Hole aeration tube.
8. sewage in-situ as claimed in claim 7 processes integrated equipment, it is characterised in that：Drum is provided with the top of oxygen-enriched storehouse
Wind area, air conduit is provided between the blast area and micropore aeration pipe.
9. sewage in-situ as claimed in claim 8 processes integrated equipment, it is characterised in that：The blast area is separated point by dividing plate
The first cabin and the second cabin are provided with, air inlet and air blower are provided with first cabin, air is connected on the air blower
Conduit, air outlet is provided with second cabin, and air inlet and air outlet are located at blast area both sides respectively, on the second cabin also
It is provided with grid and activation storehouse communicates, first cabin bottom is provided with dividing plate and separates with oxygen-enriched storehouse, second cabin and oxygen-enriched
Storehouse communicates.
10. sewage in-situ as claimed in claim 1 processes integrated equipment, it is characterised in that：In the biochemical bin and absorption storehouse
Bottom is provided with web plate, and the web plate specification is 5-10 mesh, and screen distance is 3-5 millimeters.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710046754.4A CN106746354A (en) | 2017-01-22 | 2017-01-22 | A kind of sewage in-situ processes integrated equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710046754.4A CN106746354A (en) | 2017-01-22 | 2017-01-22 | A kind of sewage in-situ processes integrated equipment |
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| Publication Number | Publication Date |
|---|---|
| CN106746354A true CN106746354A (en) | 2017-05-31 |
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| CN201710046754.4A Pending CN106746354A (en) | 2017-01-22 | 2017-01-22 | A kind of sewage in-situ processes integrated equipment |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN118045475A (en) * | 2024-04-16 | 2024-05-17 | 安徽鑫纪源科技有限公司 | Waste gas recovery treatment structure for preparing battery-grade lithium carbonate |
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