CN208038127U - A kind of XS-CSFM intelligent and high-efficiencies bioreactor - Google Patents
A kind of XS-CSFM intelligent and high-efficiencies bioreactor Download PDFInfo
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- CN208038127U CN208038127U CN201820279475.2U CN201820279475U CN208038127U CN 208038127 U CN208038127 U CN 208038127U CN 201820279475 U CN201820279475 U CN 201820279475U CN 208038127 U CN208038127 U CN 208038127U
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- zone
- aerobic zone
- tank body
- aerator
- aerobic
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 40
- 239000007788 liquid Substances 0.000 claims abstract description 31
- 239000010802 sludge Substances 0.000 claims abstract description 30
- 239000010865 sewage Substances 0.000 claims abstract description 28
- 238000009434 installation Methods 0.000 claims abstract description 5
- 238000000926 separation method Methods 0.000 claims abstract 2
- 238000005276 aerator Methods 0.000 claims description 34
- 238000011084 recovery Methods 0.000 claims description 14
- 239000007789 gas Substances 0.000 claims description 9
- 238000005273 aeration Methods 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 238000005352 clarification Methods 0.000 claims 1
- 230000007246 mechanism Effects 0.000 abstract description 4
- 230000000694 effects Effects 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 4
- 238000010606 normalization Methods 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000007726 management method Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 1
- 238000010923 batch production Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000011218 segmentation Effects 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses a kind of XS-CSFM intelligent and high-efficiencies bioreactors, including tank body, the tank base is provided with sludge settling area, anaerobic zone, the inside of the tank body is provided with multi-stage anaerobic area, aerobic zone, gas-liquid separation zone from bottom to top, automatic cycle inside realizing, the anaerobic zone, anoxic zone bottom are respectively arranged with multigroup water feed apparatus, realize segmental influent；The utility model mechanism is simple, and the effect of the abundant denitrogenation dephosphorizing of sewage disposal is realized using in-house each functional areas so that harmful substance greatly reduces in sewage, and accelerates the period of sewage disposal, and installation is few, energy saving, economic, practical, easy to operate.
Description
Technical field
The utility model is related to technical field of sewage treatment equipment, specially a kind of XS-CSFM intelligent and high-efficiencies biological respinse
Device.
Background technology
Domestic sewage of villages and small towns processing is the important content for improving Rural Human Settlements, improving villages and small towns Living consumption,
It is the important symbol of villages and small towns modernization.With villages and small towns improvement of living standard, flush toilet starts to popularize in peasant household, slurry
Increase, the domestic consumption and concentration water supply rate of rural area improve year by year, and domestic sewage of villages and small towns discharge capacity increases year by year.2016
Year China people in the countryside 7.97 hundred million, according to 83 liters of day domestic consumption per capita, emission factor 0.8 is estimated, whole year is accumulative to be needed to handle
153 billion cubic meter of domestic sewage in rural areas accounts for the 31% of national sanitary sewage total emission volumn.From handling rate, year ends 1616, city
City's wastewater treatment rate is 91.9%, and sewage disposal total amount is up to 428.8 billion cubic meters.County town wastewater treatment rate is 85.22%, annual
Sewage disposal total amount is up to 78.9 billion cubic meters.Administrative village wastewater treatment rate is 11.4%, and a large amount of domestic sewage in rural areas are unprocessed
Discharge, it has also become one of the main reason for the environmental pollutions such as rural area, lake and river eutrophication.
According to the Chinese sewage treatment industry market demand and investment consultation report analysis, compared with city, villages and small towns life is dirty
The processing of water has following characteristics：1), without sewage discharge facility；2), without scientific and reasonable planning；3), unprocessed direct row
It puts；4), facility is not perfect, and management lag natural village sanitary sewage disposal is still in the starting stage, and sewage treatment facility is unworthy of
Set is not perfect, and construction relatively lags behind with operational management.
The prior art largely uses the easy device of traditional activated sludge process and a kind of integration of membrane bioreactor dirty
Water treatment facilities and sewage water treatment method, although the easy device operating cost of traditional activated sludge process is relatively low, its
Environmental requirement is not achieved in discharge standard, another membrane bioreactor integrated sewage treating apparatus and sewage water treatment method,
Although disclosure satisfy that the emission request of environmental protection, presence takes up a large area, operating cost is high, operational administrative is complicated, later maintenance
Problem of high cost and unstable effluent quality；Technical problem to be solved in the utility model is to be directed to above-mentioned existing skill
The deficiency of art proposes new technical solution.
Utility model content
The purpose of this utility model is to provide a kind of XS-CSFM intelligent and high-efficiencies bioreactors, to solve above-mentioned background
The problem of being proposed in technology.
To achieve the above object, the utility model provides the following technical solutions：A kind of XS-CSFM intelligent and high-efficiencies biological respinse
Device, including tank body, the inside of the tank body be divided into from the bottom to top sludge settling area, the first aerobic zone, the second aerobic zone and
The top of third aerobic zone, the sludge settling area is equipped with anaerobic zone, the side wall of the tank body corresponding to the sludge settling area
On be fixed with the sludge pipe of inleakage, first aerobic zone is set to the top in sludge settling area, good described first
It is equipped with positioned at the first anoxic zone of tank interior, in first anoxic zone and sludge settling area between oxygen area and sludge settling area
Between be equipped with and be fixed on the first aerator of tank interior, second is equipped between first anoxic zone and the first aerobic zone and is exposed
Device of air is equipped with the second aerobic zone, in first aerobic zone and second in the top of the first aerobic zone of the tank interior
It is equipped with the second anoxic zone between aerobic zone, the third positioned at tank interior is fixed with respectively in the bottom of second anoxic zone
Aerator and the 4th aerator are equipped with the third aerobic zone for being located at tank interior in the top of second aerobic zone,
It is equipped with third anoxic zone between the third aerobic zone and the second aerobic zone, is fixed respectively on the bottom plate of the third anoxic zone
Equipped with the 5th aerator and the 6th aerator, it is equipped with settling section in the top of the third aerobic zone, in the settling section
The side wall of corresponding tank body is equipped with discharge outlet, in first anoxic zone, the bottom of the second anoxic zone and third anoxic zone
It is respectively equipped with the first water feed apparatus, the second water feed apparatus and third water feed apparatus being fixed on tank wall, described first
Be equipped between aerobic zone and the second anoxic zone and be fixed on the first vapor-liquid separating structure in inner tank wall, second aerobic zone with
It is fixed with the second vapor-liquid separating structure between third anoxic zone, is fixed between the third aerobic zone and settling section
Three vapor-liquid separating structures, the trigonum that first vapor-liquid separating structure is contacted with the first aerobic zone are provided with residual air recovery port.
As a kind of optimal technical scheme of the utility model, it is equipped on position of the settling section close to discharge outlet solid
It is higher than discharge outlet due to the top of the weir plate in inner tank wall, the weir plate.
As a kind of optimal technical scheme of the utility model, second vapor-liquid separating structure is contacted with the second aerobic zone
Trigonum be provided with residual air recovery port, the trigonum that the third vapor-liquid separating structure is contacted with third aerobic zone is also equipped with
Residual air recovery port.
As a kind of optimal technical scheme of the utility model, the bottom of first vapor-liquid separating structure and the second anoxic zone
Triangular shape is integrally formed in portion, and second vapor-liquid separating structure is identical as third vapor-liquid separating structure overall structure.
As a kind of optimal technical scheme of the utility model, the first Loss-on-drying device of air, the second aerator, third expose
Device of air, the 4th aerator, the 5th aerator and the 6th aerator gas outlet at be fixed with air flow meter.
As a kind of optimal technical scheme of the utility model, first water feed apparatus, the second water feed apparatus and third
The water inlet of water feed apparatus is fixed with sewage flowmeter.
As a kind of optimal technical scheme of the utility model, shut-off valve is equipped at the residual air recovery port described in each group.
Compared with prior art, the utility model has the beneficial effects that：The utility model is simple in structure, easy to use, profit
The effect of the abundant denitrogenation dephosphorizing of sewage disposal is realized with in-house each functional areas so that harmful substance subtracts significantly in sewage
It is few, and the period of sewage disposal is accelerated, installation is few, energy saving, economic, practical.Each functional areas of mechanism can factory normalization
Batch production realizes that quick dismountable assembling, suitable application region dispersion lack the few economic backward area of ground, sewage quantity.
Description of the drawings
Fig. 1 is the utility model overall structure diagram；
In figure：1- tank bodies, 2- sludge settlings area, the anaerobic zones 3-, the first anoxic zones 4-, the first aerobic zones 5-, the first gas of 6-
Liquid separated structure, the second anoxic zones 7-, the second aerobic zones 8-, the second vapor-liquid separating structures of 9-, 10- thirds anoxic zone, 11- thirds
Aerobic zone, 12- thirds vapor-liquid separating structure, 13- settling sections, 14- weir plates, the first water feed apparatus of 151-, the water inlet dresses of 152- second
It sets, 153- thirds water feed apparatus, the first aerators of 161-, the second aerators of 162-, 163- thirds aerator, 164-
Four aerators, the 5th aerators of 165-, the 6th aerators of 166-, 17- residual air recovery port, 18- discharge outlet, 19- sludge
Pipe, 20- clear water.
Specific implementation mode
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
The every other embodiment obtained, shall fall within the protection scope of the present invention.
Referring to Fig. 1, the utility model provides a kind of technical solution：A kind of XS-CSFM intelligent and high-efficiencies bioreactor, packet
Tank body 1 is included, the inside of tank body 1 is divided into sludge settling area 2, the first aerobic zone 5, the second aerobic zone 8 and third from the bottom to top
The top of aerobic zone 11, sludge settling area 2 is equipped with anaerobic zone, fixes and sets on the side wall of the tank body 1 corresponding to sludge settling area 2
There are the sludge pipe 19 of inleakage, the first aerobic zone 5 to be set to the top in sludge settling area 2, it is heavy with sludge in the first aerobic zone 5
It is equipped with the first anoxic zone 4 being located inside tank body 1 between shallow lake area 2, is equipped between the first anoxic zone 4 and sludge settling area 2 solid
The first aerator 161 inside tank body 1 is equipped with the second aerator between first anoxic zone 4 and the first aerobic zone 5
162, the top of the first aerobic zone 5 inside tank body 1 is equipped with the second aerobic zone 8, in the first aerobic zone 5 and the second aerobic zone 8
Between be equipped with the second anoxic zone 7, the bottom of the second anoxic zone 7 be fixed with respectively the third positioned at tank body 1 inside aeration fill
163 and the 4th aerator 164 are set, the third aerobic zone 11 being located inside tank body 1 is equipped in the top of the second aerobic zone 8,
It is equipped with third anoxic zone 10 between third aerobic zone 11 and the second aerobic zone 8, is fixed respectively on the bottom plate of third anoxic zone 10
Equipped with the 5th aerator 165 and the 6th aerator 166, it is equipped with settling section 13 in the top of third aerobic zone 11, is being clarified
The side wall of tank body 1 corresponding to area 13 is equipped with discharge outlet 18, in the first anoxic zone 4, the second anoxic zone 7 and third anoxic zone 10
Bottom be respectively equipped be fixed on 1 side wall of tank body the first water feed apparatus 151, the second water feed apparatus 152 and third water inlet dress
153 are set, the first vapor-liquid separating structure 6 being fixed on 1 inner wall of tank body is equipped between the first aerobic zone 5 and the second anoxic zone 7,
The second vapor-liquid separating structure 9 is fixed between second aerobic zone 8 and third anoxic zone 10, in third aerobic zone 11 and settling section
Third vapor-liquid separating structure 12 is fixed between 13, the trigonum that the first vapor-liquid separating structure 6 is contacted with the first aerobic zone 5 is set
It is equipped with residual air recovery port 17；By the first water feed apparatus 151, the second water feed apparatus 152, third water feed apparatus 153, segmentation is realized
Water inlet, the first water feed apparatus 151, the second water feed apparatus 152, third water feed apparatus 153 are connected with outside water inlet supervisor, and sludge
Sludge pump connection avoids blocking convenient for the sludge discharge that will be precipitated outside the outer discharge pipe of sludge that settling zone 2 is arranged.
The weir plate 14 being fixed on 1 inner wall of tank body is equipped on the position of discharge outlet 18 in settling section 13, weir plate 14
Topmost it is higher than discharge outlet 18；Convenient for draining clear clear water, play the role of impurity screening；And the second vapor-liquid separating structure
9 trigonums contacted with the second aerobic zone 8 are provided with residual air recovery port 17, third vapor-liquid separating structure 12 and third aerobic zone 11
The trigonum of contact is also equipped with residual air recovery port 17；Coordinate segmental influent, forms exhaust paragraph by paragraph so that exhaust gas discharge is more suitable
Freely；And the bottom of the first vapor-liquid separating structure 6 and the second anoxic zone 7 is integrally formed triangular shape, the second vapor-liquid separating structure 9 with
12 overall structure of third vapor-liquid separating structure is identical, and cooperation residual air recovery port 17 is convenient for exhaust gas being discharged；First Loss-on-drying gas dress simultaneously
The 161, second aerator 162, third aerator 163, the 4th aerator 164, the 5th aerator 165 and the 6th is set to expose
Be fixed with air flow meter at the gas outlet of device of air 166 so that whole aeration is more accurate, convenient for regulation and control, first into
The water inlet of water installations 151, the second water feed apparatus 152 and third water feed apparatus 153 is fixed with sewage flowmeter；Each
It is equipped with shut-off valve at group residual air recovery port 17, facilitates and realizes quick stop and start；Each functional areas can factory normalization batch simultaneously
Production, realizes quick dismountable assembling, and being equipped with sealing ring between each functional areas connection seals antiseepage.
The utility model mechanism is simple, and the abundant denitrogenation dephosphorizing of sewage disposal is realized using in-house each functional areas
Effect so that harmful substance greatly reduces in sewage, and accelerates the period of sewage disposal, and installation is few, energy saving, economic, real
With unattended after, easy to operate, intelligent control commissioning test.Especially each functional areas of mechanism can factory normalization batch life
Production realizes that quick dismountable assembling, suitable application region dispersion lack the few economic backward area of ground, amount.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is appreciated that can these embodiments be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaiied
Change, replace and modification, the scope of the utility model are defined by the appended claims and the equivalents thereof.
Claims (7)
1. a kind of XS-CSFM intelligent and high-efficiencies bioreactor, including tank body (1), it is characterised in that：The inside of the tank body (1)
It is divided into sludge settling area (2), the first aerobic zone (5), the second aerobic zone (8) and third aerobic zone (11), institute from the bottom to top
The top for stating sludge settling area (2) is equipped with anaerobic zone, consolidates on the side wall of the tank body (1) corresponding to the sludge settling area (2)
Surely it is equipped with the sludge pipe (19) of inleakage, first aerobic zone (5) is set to the top of sludge settling area (2), described
It is equipped between first aerobic zone (5) and sludge settling area (2) and is located at internal the first anoxic zone (4) of tank body (1), described first
It is equipped between anoxic zone (4) and sludge settling area (2) and is fixed on internal the first aerator (161) of tank body (1), described first
The second aerator (162) is equipped between anoxic zone (4) and the first aerobic zone (5), first in the tank body (1) inside is aerobic
The top in area (5) is equipped with the second aerobic zone (8), and second is equipped between first aerobic zone (5) and the second aerobic zone (8) and is lacked
Oxygen area (7) is fixed with respectively in the bottom of second anoxic zone (7) positioned at the internal third aerator of tank body (1)
(163) and the 4th aerator (164), it is equipped with that be located at the internal third of tank body (1) good in the top of second aerobic zone (8)
Oxygen area (11) is equipped with third anoxic zone (10), in the third between the third aerobic zone (11) and the second aerobic zone (8)
The 5th aerator (165) and the 6th aerator (166) are fixed on the bottom plate of anoxic zone (10) respectively, in the third
The top of aerobic zone (11) is equipped with settling section (13), the row of being equipped on the side wall of the tank body (1) corresponding to the settling section (13)
The mouth of a river (18) is respectively equipped with fixation in the bottom of first anoxic zone (4), the second anoxic zone (7) and third anoxic zone (10)
In the first water feed apparatus (151), the second water feed apparatus (152) and third water feed apparatus (153) on tank body (1) side wall, in institute
State the first vapor-liquid separating structure for being equipped with and being fixed on tank body (1) inner wall between the first aerobic zone (5) and the second anoxic zone (7)
(6), it is fixed with the second vapor-liquid separating structure (9) between second aerobic zone (8) and third anoxic zone (10), described
Third vapor-liquid separating structure (12), first vapor-liquid separating structure are fixed between three aerobic zones (11) and settling section (13)
(6) trigonum contacted with the first aerobic zone (5) is provided with residual air recovery port (17).
2. a kind of XS-CSFM intelligent and high-efficiencies bioreactor according to claim 1, it is characterised in that：In the clarification
Area (13) is equipped with the weir plate (14) being fixed on tank body (1) inner wall close to the position of discharge outlet (18), the weir plate (14)
Topmost it is higher than discharge outlet (18).
3. a kind of XS-CSFM intelligent and high-efficiencies bioreactor according to claim 1, it is characterised in that：Second gas
The trigonum that liquid separated structure (9) is contacted with the second aerobic zone (8) is provided with residual air recovery port (17), the third gas-liquid separation
The trigonum that structure (12) is contacted with third aerobic zone (11) is also equipped with residual air recovery port (17).
4. a kind of XS-CSFM intelligent and high-efficiencies bioreactor according to claim 1, it is characterised in that：First gas
The bottom of liquid separated structure (6) and the second anoxic zone (7) is integrally formed triangular shape, second vapor-liquid separating structure (9) and the
Three vapor-liquid separating structures (12) overall structure is identical.
5. a kind of XS-CSFM intelligent and high-efficiencies bioreactor according to claim 1, it is characterised in that：Described first exposes
Device of air (161), the second aerator (162), third aerator (163), the 4th aerator (164), the 5th aeration dress
It sets and is fixed with air flow meter at (165) and the gas outlet of the 6th aerator (166).
6. a kind of XS-CSFM intelligent and high-efficiencies bioreactor according to claim 1, it is characterised in that：Described first into
The water inlet of water installations (151), the second water feed apparatus (152) and third water feed apparatus (153) is fixed with the discharge of sewage
Meter.
7. a kind of XS-CSFM intelligent and high-efficiencies bioreactor according to claim 1, it is characterised in that：Described in each group
Residual air recovery port is equipped with shut-off valve at (17).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820279475.2U CN208038127U (en) | 2018-02-28 | 2018-02-28 | A kind of XS-CSFM intelligent and high-efficiencies bioreactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201820279475.2U CN208038127U (en) | 2018-02-28 | 2018-02-28 | A kind of XS-CSFM intelligent and high-efficiencies bioreactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208038127U true CN208038127U (en) | 2018-11-02 |
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ID=63950268
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201820279475.2U Expired - Fee Related CN208038127U (en) | 2018-02-28 | 2018-02-28 | A kind of XS-CSFM intelligent and high-efficiencies bioreactor |
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| Country | Link |
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| CN (1) | CN208038127U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108178306A (en) * | 2018-02-28 | 2018-06-19 | 兴燊环境技术（深圳）有限公司 | A kind of XS-CSFM intelligent and high-efficiencies bioreactor |
-
2018
- 2018-02-28 CN CN201820279475.2U patent/CN208038127U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108178306A (en) * | 2018-02-28 | 2018-06-19 | 兴燊环境技术（深圳）有限公司 | A kind of XS-CSFM intelligent and high-efficiencies bioreactor |
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| Date | Code | Title | Description |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: 518000 102, floor 1, building 7, Yuyuan new village, Yuyuan community, Longcheng street, Longgang District, Shenzhen City, Guangdong Province Patentee after: XINGSHEN ENVIRONMENTAL TECHNOLOGY (SHENZHEN) Co.,Ltd. Address before: 518000 6 103 of Yuyuan new village, Longcheng street Longgang central city, Longgang, Shenzhen, Guangdong Patentee before: XINGSHEN ENVIRONMENTAL TECHNOLOGY (SHENZHEN) Co.,Ltd. |
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| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181102 |