CN205953661U - Integration column type high -concentration organic wastewater treatment ware - Google Patents
Integration column type high -concentration organic wastewater treatment ware Download PDFInfo
- Publication number
- CN205953661U CN205953661U CN201620940482.3U CN201620940482U CN205953661U CN 205953661 U CN205953661 U CN 205953661U CN 201620940482 U CN201620940482 U CN 201620940482U CN 205953661 U CN205953661 U CN 205953661U
- Authority
- CN
- China
- Prior art keywords
- dividing plate
- aeration
- water
- area
- organic wastewater
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses an integration column type high -concentration organic wastewater treatment ware, including the cylindrical housing body, casing by the intermittent aeration district of district of the anaerobism below the partitions are divided into and top, the anaerobism district establishes UASB reactor, elevator pump and discharge, the discharge passes whole intermittent aeration district perpendicularly, the bottom in intermittent aeration district is equipped with the aeration pipe, the aeration pipe links to each other through the outer aeration fan of control valve and casing, intermittent aeration district by baffle no. 1 cut apart to become not the confined intake the side with go out the water side, establish impeller no. 1, backwash pump and MBR membrane group ware in the intermittent aeration district, MBR membrane group ware links to each other with the outer outlet water pump of casing, elevator pump, control valve no. 1, aeration fan, impeller no. 1, outlet water pump and backwash pump are connected with the outer PLC controller electricity of casing respectively. Process flow one -tenth, structure complicacy, civil construction big, the inconvenient management of investment and the long problem of construction period have been solved to above -mentioned scheme.
Description
Technical field
The utility model is related to field of waste water treatment, and more particularly, to a kind of process that can process high concentrated organic wastewater sets
Standby.
Background technology
High concentrated organic wastewater is the waste water in more than 2000mg/L for the COD, mostly industrial wastewater, and yield is huge, if
Directly discharge, serious environmental pollution can be caused.At present, China's industrial wastewater takes traditional pulling flow type sewage disposal work mostly
Skill, its shortcoming is that floor space is big, construction investment costly, operating cost is high and treatment effect is not sufficiently stable, and disposal ability has
Limit.
UASB (Up-flow Anaerobic Sludge Bed/Blanket) reactor is also known as up-flow anaerobic sludge blanket
Reactor is a kind of anaerobic organism method processing sewage, and it is very big that UASB reactor has a load-bearing capacity, and volumetric loading rate is high, gives up
Hydraulic detention time in UASB reactor for the water is shorter, and contaminant removal efficiency is high, and volume is little, and equipment is simple, and it is convenient to run,
The features such as be easy to management.But UASB reactor has water outlet, and reaction is not thorough, outlet effect difference, it is impossible to directly discharge, needs
It is followed by other operations to continue with.Technics comparing is loaded down with trivial details.
MBR (Membrane Bioractor) reactor is a kind of by membrane separation technique and traditional also known as membrane bioreactor
The combined sewage treatment process of biological processing unit.Its origin is to replace in activated sludge process two with membrane separation technique to sink
Pond, carries out separation of solid and liquid.MBR film group is run under high volumetric loading, low sludge loading, long sludge age, and excess sludge production is extremely low,
Due to sludge age can endless, in theory can achieve zero sludge discharge, efficiently carry out separation of solid and liquid, its separating effect be much better than pass
The sedimentation basin of system, effluent quality is good, goes out aqueous suspension and turbidity close to zero, can direct reuse it is achieved that sewage recycling.
The shortcoming of MBR MBR is poor to the water treatment effect of high concentration, biodegradability difference.
If using continuing with through MBR film again through the pretreated waste water of UASB reactor, after process
Water quality is preferable, stable water outlet, achievable waste water recycling.But such scheme also needs to consider following problem：1st, need to build multiple
Processing unit, leads to the processing technological flow of whole waste water long, complex structure.2nd, project floor space is big, and civil engineering is invested
Greatly.3rd, it is unfavorable for managing, operating cost is high.4th, integration of equipments low degree, the completion time of project is long.
Utility model content
In order to solve the problems, such as prior art, the utility model provide a kind of by UASB reactor and MBR film group device
It is incorporated into the integrated pillar high concentrated organic wastewater processor in same housing.
To achieve these goals, the technical solution adopted in the utility model is：A kind of integration pillar high concentration is organic
Waste water treater；Including housing, UASB reactor and MBR film group device；Described housing is cylindrical；Described enclosure interior is by dividing plate
It is divided into two parts up and down of closing；The lower section of described dividing plate is anaerobic zone；The top of dividing plate is intermittent aerating area；Described UASB
Reactor is arranged on anaerobic zone；UASB reactor is connected with the pretreatment pool outside housing by pipeline；The top of described anaerobic zone
It is provided with the elevator pump of the waste water lifting after UASB reactor for treatment to intermittent aerating area；Described dividing plate is provided with one and vertically passes through
Wear the discharge in whole intermittent aerating area；One end of described discharge is arranged on the top of anaerobic zone, and the other end extends to housing
Outward；The bottom in described intermittent aerating area is provided with some equally distributed aeration tubes；Described aeration tube passes through control valve one and sets
Aeration fan outside housing is connected；Described intermittent aerating area is divided into the influent side do not closed and water outlet side by dividing plate one；Institute
The bottom stating intermittent aerating area is provided with the impeller one that the waste water that elevator pump conveying comes up is pushed to water outlet side from influent side；Institute
The bottom stating water outlet side is provided with and will be transmitted back to the reflux pump of influent side after sludge agitation；Described MBR film group device is arranged on water outlet side
Top and the water going out after water pump is connected after processing being arranged on outside housing discharge；Described elevator pump, control valve one, aeration
Blower fan, impeller one, go out water pump and reflux pump is electrically connected with the PLC being arranged on outside housing respectively.
After technique scheme, sewage enters anaerobic zone after pretreatment through UASB reactor for treatment, and anaerobism is anti-
Waste water after answering enters intermittent aerating area and carries out biochemical treatment, then the suction micro-filtration water outlet through MBR film group device, effluent quality
Height, and water stabilization, can be used for processing the water yield and pollutant levels change industrial wastewater greatly.
Integrated pillar high concentrated organic wastewater processor has advantages below：1st, to spatial development in the way of three-dimensional,
Greatly save floor space, improve oxygen transformation efficiency and utilization ratio.2nd, decrease the construction investment that multiple units reduce.
3rd, through UASB reactor, entering organic matter of water is degraded, the biogas recoverable of generation simultaneously improves the biodegradability of waste water.
Even if the 4, the leaving water temperature of anaerobic reaction also provides favourable temperature conditionss it is ensured that intermittent aerating area exists for follow-up biochemical treatment
Winter also can effectively be run.5th, utilize aeration and the microbial action in intermittent aerating area, effectively eliminate anaerobic reaction and produce
Foul smell, it is to avoid secondary pollution and foul smell are individually processed.6th, integrated, high degree of automation, operation, safeguard simple and convenient.
7th, batch production can make, in-site installation, short construction period, greatly save up-front investment.
Brief description
Fig. 1 is the schematic diagram of integrated pillar high concentrated organic wastewater processor erectility.
Fig. 2 is the schematic diagram of the vertical view state in integrated pillar high concentrated organic wastewater processor intermittent aerating area.
Specific embodiment
To the utility model, preferred scheme is further elaborated below in conjunction with the accompanying drawings：
As depicted in figs. 1 and 2, a kind of integration pillar high concentrated organic wastewater processor.Including cylindrical housing
1st, UASB reactor 2 and MBR film group device 3.Described enclosure interior is divided into two parts up and down of closing by dividing plate 5；Described dividing plate
Lower section be anaerobic zone 4；The intermittent aerating area 6 of the top of dividing plate 5.
UASB reactor is arranged on anaerobic zone；UASB reactor is connected with the pretreatment pool 7 outside housing by pipeline.Described
The top of anaerobic zone is provided with the elevator pump 8 of the waste water lifting after UASB reactor for treatment to intermittent aerating area.On described dividing plate
It is provided with a discharge 9 extending vertically through whole intermittent aerating area, one end of described discharge is arranged on the top of anaerobic zone, separately
One end extends to outside housing.
The bottom in intermittent aerating area is provided with some equally distributed aeration tubes 10；Described aeration tube passes through control valve 1
It is connected with the Aeration fan 12 being located at outside housing.Described intermittent aerating area is divided into influent side 14 He do not closed by dividing plate 1
Water outlet side 15；The bottom in described intermittent aerating area is provided with the waste water that elevator pump 8 conveying comes up and is pushed to water outlet side from influent side
Impeller 1.The bottom of described water outlet side is provided with and will be transmitted back to the reflux pump 17 of influent side after sludge agitation.Described MBR film
Water after processing is discharged after water pump 18 is connected by the top that group device is arranged on water outlet side with being arranged on going out outside housing.Described carry
Rise pump, control valve one, Aeration fan, impeller one, go out water pump and reflux pump respectively with the PLC 19 being arranged on outside housing
Electrical connection.
UASB reactor includes Sludge Bed 20, water distributor 21, three phase separator 22 and collection chamber 23；Described Sludge Bed and cloth
Water pipe is arranged on the bottom of anaerobic zone；Described water distributor is arranged in Sludge Bed；Water distributor is connected with pretreatment pool；Described three-phase
Separator is arranged on the middle part of anaerobic zone；Described collection chamber is arranged on the top of three phase separator；The top of collection chamber and gas collection
Pipe 9 is connected.It is provided between the top of described three phase separator and Sludge Bed and the waste water of anaerobic zone is carried out secondary back process
Return duct 25.The bottom of described housing is provided with mud discharging pipe 26.
Improve as further, also include in the intermittent aerating area of integrated pillar high concentrated organic wastewater processor every
Plate 2 27, dividing plate 3 28 and impeller 2 29；Influent side is separated into the first-class area not closed by described dividing plate two and dividing plate three
30th, second area 31 and the 3rd stream area 32；Described dividing plate two and dividing plate one do not close identical not the sealing with dividing plate three of extreme direction
Closed end is in opposite direction；Described impeller two is arranged on the blind end against dividing plate three in second area；Described impeller one is arranged
Against the blind end of dividing plate one in the 3rd stream area；Described impeller two is electrically connected with PLC.Using the technical program
Afterwards, the runner of waste water is lengthened out, the runner of lengthening so that in equipment waste water experience aerobic, the anoxic repeatedly of longer time
Environment, can more thoroughly remove pollutant.
The lower section of MBR film group device is provided with aeration tube 2 33 near the water inlet of MBR film group device, described aeration tube two passes through
Control valve 2 34 is connected with Aeration fan 12；Described control valve two is electrically connected with PLC.After aforesaid way, a side
Face provide MBR film group device water outlet needs wash away aeration, on the other hand increased content in water for the air and then increased
The dissolution rate of oxygen and utilization ratio.
The step that high-concentration sewage is processed using the technical program：First the waste water drainage of high concentration is entered into pretreatment
Carry out in pond 7 precipitating, adjust etc. anticipates, and then enters the bottom of anaerobic zone through inlet channel water conservancy diversion, by water distributor
21 bottoms that waste water is uniformly uniformly distributed in equipment as far as possible, anaerobic zone bottom is the higher Sludge Bed 20 of concentration, organic matter
After high concentration sludge bed 20 reaction, produce methane and carbon dioxide and rise, anaerobic grain sludge or floc sludge are in rising
It is in suspended state in the presence of current and bubble, that is, gas and liquid mixture rises, then carry out separating by three phase separator 22,
Mud sinks down into Sludge Bed 20 after separating, and the water after process enters the settling zone on top, and the biogas of rising is entered by collection chamber 23
Row is collected, and arranges through discharge 9 is outer, the biogas emitting can be used for generating electricity and other purposes.Separate through three phase separator 22
The settling zone mud being formed afterwards or water are back to anaerobic zone Sludge Bed 20 through return duct 25, and the remaining mud of Sludge Bed 20 is through dirt
Mud blow-off pipe 26 is discharged outside housing.Waste water after processing through anaerobic reaction is transported to the first-class area of influent side by elevator pump 8
Interior, then it is pushed in second area by impeller two, waste water is pushed to the 3rd stream area and water outlet side by last impeller one；Useless
Water in the intermittent aerating area process of circulation, realize being sick of by the switch that PLC controls control valve one and Aeration fan and
The switching of aerobic two kinds of environment, in this region, waste water experiences aerobic environment, anaerobic environment repeatedly, sufficiently removes in sewage
Organic matter, nitrogen, the pollutant such as phosphorus.Process after the waste water completing is processed again by MBR film group device 3 and then discharged by going out water pump
Housing, and then complete the process work to waste water.
The utility model is not limited to above-mentioned preferred forms, and anyone can show that other are various under this enlightenment
The product of form, however, making any change in its shape or structure, every have skill identical or similar to the present application
Art scheme, all falls within protection domain of the present utility model.
Claims (6)
1. a kind of integration pillar high concentrated organic wastewater processor；Including housing (1), UASB reactor (2) and MBR film group device
(3)；It is characterized in that：Described housing is cylindrical；Described enclosure interior is divided into two parts up and down of closing by dividing plate (5)；
The lower section of described dividing plate is anaerobic zone (4)；The intermittent aerating area (6) of the top of dividing plate (5)；Described UASB reactor is arranged on to be detested
Oxygen area；UASB reactor is connected with the pretreatment pool (7) outside housing by pipeline；The top of described anaerobic zone is provided with UASB is anti-
Waste water lifting after answering device to process is to the elevator pump (8) in intermittent aerating area；Described dividing plate be provided with one extend vertically through whole between
Have a rest the discharge (9) of aeration zone；One end of described discharge is arranged on the top of anaerobic zone, and the other end extends to outside housing；Institute
The bottom stating intermittent aerating area is provided with some equally distributed aeration tubes (10)；Described aeration tube pass through control valve one (11) with
The Aeration fan (12) being located at outside housing is connected；Described intermittent aerating area is divided into, by dividing plate one (13), the influent side do not closed
And water outlet side (15) (14)；The bottom in described intermittent aerating area is provided with the waste water that elevator pump (8) conveying comes up and pushes away from influent side
Deliver to the impeller one (16) of water outlet side；The bottom of described water outlet side is provided with and will be transmitted back to the reflux pump of influent side after sludge agitation
(17)；The top that described MBR film group device is arranged on water outlet side will process it with being arranged on going out after water pump (18) is connected outside housing
Water afterwards is discharged；Described elevator pump, control valve one, Aeration fan, impeller one, go out water pump and reflux pump respectively be arranged on shell
External PLC (19) electrical connection.
2. according to claim 1 integration pillar high concentrated organic wastewater processor it is characterised in that：Described UASB is anti-
Device is answered to include Sludge Bed (20), water distributor (21), three phase separator (22) and collection chamber (23)；Described Sludge Bed and water distributor set
Put the bottom in anaerobic zone；Described water distributor is arranged in Sludge Bed；Water distributor is connected with pretreatment pool；Described three phase separator
It is arranged on the middle part of anaerobic zone；Described collection chamber is arranged on the top of three phase separator；The top of collection chamber and discharge (9) phase
Connection.
3. according to claim 2 integration pillar high concentrated organic wastewater processor it is characterised in that：Described three-phase separate
From being provided with the return duct (25) that the waste water of anaerobic zone is carried out secondary back process between the top of device (22) and Sludge Bed.
4. according to claim 2 integration pillar high concentrated organic wastewater processor it is characterised in that：Described housing
Bottom is provided with mud discharging pipe (26).
5. according to claim 2 integration pillar high concentrated organic wastewater processor it is characterised in that：Also include dividing plate
Two (27), dividing plate three (28) and impeller two (29)；Described dividing plate two and dividing plate three influent side is separated into not closing first
Stream area (30), second area (31) and the 3rd stream area (32)；Described dividing plate two and dividing plate one do not close extreme direction identical with every
The not blind end of plate three is in opposite direction；Described impeller two is arranged on the blind end against dividing plate three in second area；Described push away
Stream device one is arranged on the blind end in the 3rd stream area against dividing plate one；Described impeller two is electrically connected with PLC.
6. according to claim 2 integration pillar high concentrated organic wastewater processor it is characterised in that：Described MBR film
The lower section of group device is provided with aeration tube two (33) near the water inlet of MBR film group device, described aeration tube two passes through control valve two
(34) it is connected with Aeration fan (12)；Described control valve two is electrically connected with PLC.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620940482.3U CN205953661U (en) | 2016-08-25 | 2016-08-25 | Integration column type high -concentration organic wastewater treatment ware |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620940482.3U CN205953661U (en) | 2016-08-25 | 2016-08-25 | Integration column type high -concentration organic wastewater treatment ware |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205953661U true CN205953661U (en) | 2017-02-15 |
Family
ID=57980161
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620940482.3U Active CN205953661U (en) | 2016-08-25 | 2016-08-25 | Integration column type high -concentration organic wastewater treatment ware |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205953661U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106115918A (en) * | 2016-08-25 | 2016-11-16 | 河南力诚环保科技有限公司 | Integration pillar high concentrated organic wastewater processor |
-
2016
- 2016-08-25 CN CN201620940482.3U patent/CN205953661U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106115918A (en) * | 2016-08-25 | 2016-11-16 | 河南力诚环保科技有限公司 | Integration pillar high concentrated organic wastewater processor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101205109A (en) | Apparatus for treating chemical fiber waste water by anaerobic method | |
| CN101323482A (en) | Deep well aeration film bioreactor waste water treatment process and apparatus | |
| CN201932988U (en) | Anaerobic/aerobic contact oxidation membrane bioreactor | |
| CN108002660A (en) | Depth waste water treatment system and sewage water treatment method | |
| CN206512058U (en) | A kind of efficient villages and small towns waste water treating and reutilizing device | |
| CN101386445A (en) | Water pump-driving baffling internal circulation bioreactor and use method thereof | |
| CN208022860U (en) | Depth waste water treatment system | |
| CN201538734U (en) | Sewage treatment device | |
| CN204211537U (en) | The double oxygen MBR membrane bioreactor of integration | |
| CN206289048U (en) | Sewage combination biochemistry and sludge static state deposition separating treatment integrated apparatus | |
| CN204079721U (en) | A kind of sewage disposal device adopting pure oxygen aeration and remaining oxygen reuse | |
| CN105693039A (en) | UASB-MBR(up-flowa naerobic sludge bed-membrane bioractor) based high-concentration organic wastewater treatment equipment | |
| CN202610021U (en) | External anaerobic membrane bioreactor | |
| CN205528307U (en) | High concentration organic wastewater equipment based on UASB -MBR | |
| CN203238141U (en) | Sewage biological treatment membrane filtration system | |
| CN111056710B (en) | Sewage advanced treatment and resource recovery system and method for anaerobic ectopic electric release iron membrane bioreactor | |
| CN205953661U (en) | Integration column type high -concentration organic wastewater treatment ware | |
| CN202063766U (en) | Top end gradation particle sludge purification bed | |
| CN106115918A (en) | Integration pillar high concentrated organic wastewater processor | |
| CN203284290U (en) | Domestic sewage purification tank treatment system | |
| CN105693036A (en) | Intelligent sewage treatment system | |
| CN104609554A (en) | Purification device and method for reclaiming and reusing breeding wastewater | |
| CN103819062A (en) | MBR (membrane biological reactor) sewage treatment equipment for integrated fluidizing pool | |
| CN205023939U (en) | Novel gas lift formula circulation immoblilization biofilm reactor | |
| CN203346179U (en) | Oxygen-increasing device, self-flow oxygen-increasing biological filter, self-flow oxygen-enriching ecological bed and sewage treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |