CN205575772U - Handle horizontal baffling formula reactor of anaerobism of high suspended solid waste water - Google Patents
Handle horizontal baffling formula reactor of anaerobism of high suspended solid waste water Download PDFInfo
- Publication number
- CN205575772U CN205575772U CN201620341902.6U CN201620341902U CN205575772U CN 205575772 U CN205575772 U CN 205575772U CN 201620341902 U CN201620341902 U CN 201620341902U CN 205575772 U CN205575772 U CN 205575772U
- Authority
- CN
- China
- Prior art keywords
- reactor
- waste water
- deflection plate
- casing
- high suspended
- 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.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
The utility model discloses a handle horizontal baffling formula reactor of anaerobism of high suspended solid waste water, including the reactor box, the inside baffling board that is the ripple type that is equipped with of reactor box, reactor box outside are equipped with inlet pipe, feeder hopper, discharging pipe, liquid storage tank and towards the sediment device, the utility model discloses in the use, waste water gets into the reactor through the feed inlet, the level stream and the back reaction ware after the end motion, discharge from the discharge gate at last, waste water reacts production marsh gas at this in -process, the horizontal baffling mode of adoption reduces the block effect of traditional baffling formula reactor to the dross by a wide margin to it rushes out the reactor to stop district with a small amount of dross from the dross through the natural pond liquid in the circulating pump extraction liquid storage tank. The utility model discloses simple structure, the cost is low, and the treatment effeciency is high, has solved the easy problem at baffling formula reactor scumming jam reactor of high suspended solid especially, has huge market perspective.
Description
Technical field
This utility model belongs to environmental project technical field of sewage, is specifically related to a kind of high suspended matter that processes and gives up
The anaerobic horizontal baffling formula reactor of water.
Background technology
Nowadays, anaerobic baffled formula reactor (ABR) is a kind of efficient anaerobic reactor, is mainly used in
In the technical process that waste water processes.Apply this reactor can by waste water complicated Organic substance (saccharide, fat,
Protein) it is converted into the short-chain fatty acid (acetic acid, propanoic acid, butanoic acid) of simple in construction and is further converted to clear
The clean energy " biogas ", processed waste water is degraded, so being more beneficial for follow-up because of wherein complicated Organic substance
Waste water treatment process runs.
The operation principle of anaerobic baffled formula reactor is to arrange multiple vertical deflection plate in reactor will react
Device is divided into several compartments, and waste water is entered reactor by charging aperture, successively from a compartment flow to last every
Room, finally gets rid of from discharging opening.Anaerobic baffled reactor has a simple in construction, low cost, stable and
The feature of convenient management.
The application of anaerobic baffled formula reactor is quite varied, can obtain good effect during processing waste water
Really.But, anaerobic baffled formula reactor also has certain defect.Such as: be vertically arranged deflection plate when using
During reactor, in waste water substantial amounts of float can pile up in the reactor formed scum silica frost cannot discharge, along with use
The growth of time, scum silica frost can result in blockage in the reactor, reactor can be caused to damage, add inspection time serious
Accomplish this.Nowadays, the way of such issues that many people solve is before waste water enters reactor, by float mistake
Filter off.This way not only labor intensive, inefficiency and substantial amounts of Organic substance in float can be filtered off, make
Obtain large amount of organic to be wasted, cause reactor biogas output on the low side.Therefore, high suspended matter waste water is being processed
When, need to strengthen float mobility in reactor to avoid blocking, flushing cinder system to be designed
Blanket insurance card float is discharged smoothly.
Utility model content
In order to solve the deficiencies in the prior art, the purpose of this utility model is that proposing a kind of high suspended matter that processes gives up
The anaerobic horizontal baffling formula reactor of water.This structure of reactor is simple, has current existing baffled reactor
Advantage, and by the novel deflection plate that is provided with and slag flushing device, it is possible to effectively avoid scum silica frost to block,
And high suspended matter in waste water can be discharged smoothly, greatly reduce cost and improve the efficiency of process.
To achieve the above object, the technical solution adopted in the utility model is:
A kind of anaerobic horizontal baffling formula reactor processing high suspended matter waste water, including reactor casing, its feature
Be: described reactor box house is provided with deflection plate, be provided with outside reactor casing feed pipe, feed hopper,
Discharge nozzle, liquid storage tank and slag flushing device；Described feed pipe from feeding funnel bottom part stretch out with reactor casing front end
Side is connected, and waste water flows to reactor casing from feed hopper by feed pipe；Described discharge nozzle and liquid storage tank be positioned at into
Material pipe homonymy, described discharge nozzle be connected on the upside of reactor casing end and extend inside liquid storage tank, liquid storage tank
Use water seal that discharge nozzle is partially submerged；Reactor casing is connected by pipeline by described slag flushing device with liquid storage tank
Connecing, slag flushing device includes the flushing cinder mouth with reactor casing junction and is positioned at the immersible pump within liquid storage tank, logical
Cross unlatching immersible pump and scum silica frost is gone out discharging opening by flushing cinder mouth by the biogas slurry in liquid storage tank；Described reactor casing
Top be provided with for biogas discharge exhaustor, in the reactor wastewater fermentation produce biogas arrange from exhaustor
Go out.
Further, described deflection plate is ripple type, and on described deflection plate, the crest of ripple and the angle of trough are
Preferred 90 °, baffle material can be made up of rustless steel or PE plate.
Further, the number of described deflection plate is the odd number more than 3；The number of deflection plate is set as odd number,
Feed pipe mouth and the discharging mouth of pipe can be made to be positioned at the homonymy of reactor casing.
Further, described deflection plate is staggered front to back layout at reactor box house, and waste water is in reactor casing
Portion walks around deflection plate and flows.
Further, bottom and the top of deflection plate contact with bottom and the top of reactor casing, deflection plate
The sidewall of side and reactor casing contacts, and the opposite side of deflection plate reserves necessarily with the sidewall of reactor casing
Space；Deflection plate can use with the way of contact of reactor casing and weld or bonding.
Further, described flushing cinder mouth is between two deflection plates and slightly above the discharging mouth of pipe, beneficially flushing cinder mouth
In waste water high suspended matter is rushed in discharge nozzle.
Further, the number of described flushing cinder mouth is identical with the number of deflection plate, each after first compartment
Compartment is designed with flushing cinder mouth, improves the efficiency of flushing cinder.
Further, at flushing cinder mouth biogas slurry flow to this in reactor casing waste water flow to identical, flushing cinder mouth
High suspended matter is rushed at discharge nozzle by the flow direction of waste water in reactor casing of waste water out.
The beneficial effects of the utility model are:
(1) deflection plate of the present utility model is ripple type so that waste water flow process ratio in the reactor is general
Logical anaerobic baffled reactor is much bigger, also enhances waste water mixed effect in this reactor, improves
Treatment effeciency to waste water.
(2) this utility model is provided with slag flushing device, the biogas slurry in liquid storage tank is passed through by opening immersible pump
Scum silica frost is gone out discharging opening by flushing cinder mouth, can be discharged by the scum silica frost that inside reactor is piled up in time, prevents substantial amounts of floating
Slag muck manufactures into reactor plugs and has damaged reactor, well solves the problem that scum silica frost is piled up, and adds anti-
Answer the service life of device.
(3) each compartment of this utility model is interconnected, and waste water can be allowed to be evenly distributed in reactor, keep away
Exempt from front end and be easily acidified the malnourished phenomenon in rear end, improve the stability of reactor.
Accompanying drawing explanation
Fig. 1 is complete structure schematic diagram of the present utility model；
Fig. 2 is top plan view of the present utility model；
Fig. 3 is elevation cross-sectional view of the present utility model；
Fig. 4 is piping diagram of the present utility model.
In figure: 1, reactor casing；2, feed pipe；3, discharge nozzle；4, deflection plate；5, flushing cinder mouth；6、
Liquid storage tank；7, immersible pump；8, exhaustor；9, slag flushing device；10, feed hopper.
Detailed description of the invention
In order to make the purpose of utility model, technical scheme and advantage clearer, below in conjunction with the accompanying drawings to this practicality
Novel it is further elaborated.
In the present embodiment, refering to Fig. 1-4, a kind of anaerobic horizontal baffling formula reaction processing high suspended matter waste water
Device, including reactor casing 1, it is characterised in that: described reactor casing 1 is internal is provided with deflection plate 4, instead
Device casing 1 outside is answered to be provided with feed pipe 2, feed hopper 10, discharge nozzle 3, liquid storage tank 6 and slag flushing device 9；
Described feed pipe 2 stretches out bottom feed hopper 10 and is connected on the downside of reactor casing 1 front end, and waste water is from charging
Bucket 10 flows to reactor casing 1 by feed pipe 2；Described discharge nozzle 3 is positioned at feed pipe 2 with liquid storage tank 6
Homonymy, described discharge nozzle 3 be connected on the upside of reactor casing 1 end and to extend liquid storage tank 6 internal, liquid storage
Pond 6 uses water seal by partially submerged for discharge nozzle 3；Described slag flushing device 9 is by reactor casing 1 and liquid storage tank 6
Being connected by pipeline, slag flushing device 9 includes the flushing cinder mouth 5 with reactor casing 1 junction and is positioned at liquid storage
Immersible pump 7 within pond 6, will be floating by flushing cinder mouth 5 by the biogas slurry in liquid storage tank 6 by opening immersible pump 7
Slag rushes in discharge nozzle 3；The top of described reactor casing 1 is provided with the exhaustor 8 discharged for biogas, in reaction
The biogas that in device, wastewater fermentation produces is discharged from exhaustor 8.
As a kind of prioritization scheme of the present utility model, described deflection plate 4 is in ripple type, on described deflection plate 4
The crest of ripple and the angle of trough are preferred 90 °, and the material of deflection plate 4 can be by rustless steel or PE plate
Make.
As a kind of prioritization scheme of the present utility model, the number of described deflection plate 4 is the odd number more than 3；Will
The number of deflection plate 4 is set as odd number, so that feed pipe 2 mouthfuls and discharge nozzle 3 mouthfuls are positioned at reactor casing
The homonymy of 1.
As a kind of prioritization scheme of the present utility model, described deflection plate 4 is staggered front to back in reactor casing 1
Arranging, waste water is walked around deflection plate 4 inside reactor casing 1 and is flow to last compartment from the first compartment.
As a kind of prioritization scheme of the present utility model, the bottom of deflection plate 4 and top and reactor casing 1
Bottom and top contact, and the side of deflection plate 4 and the sidewall of reactor casing 1 contact, deflection plate 4
The sidewall of opposite side and reactor casing 1 reserve a fixed gap；Deflection plate 4 contacts with reactor casing 1
Mode can use welds or bonding.
As a kind of prioritization scheme of the present utility model, described flushing cinder mouth 5 is between two deflection plates 4 and omits
Higher than the waste water in discharge nozzle 3 mouthfuls, beneficially flushing cinder mouth 5, high suspended matter is rushed in discharge nozzle 3.
As a kind of prioritization scheme of the present utility model, the number of described flushing cinder mouth 5 and the number phase of deflection plate 4
With, each compartment after first compartment is designed with flushing cinder mouth 5, improves the efficiency of flushing cinder.
As a kind of prioritization scheme of the present utility model, at flushing cinder mouth 5 flow direction of biogas slurry with this at reactor casing
In 1 waste water flow to identical, flushing cinder mouth 5 biogas slurry out in reactor casing 1 flow direction of waste water by height
Float rushes at discharge nozzle 3.
In the present embodiment, it is internal that waste water enters reactor casing 1 from feed hopper 10 by feed pipe 2, useless
Water is walked around deflection plate 4 in reactor casing 1 and is flow in last compartment by first compartment.Work as waste water
Liquid level reached the position of discharge nozzle 3 mouthfuls after, waste water can be discharged in liquid storage tank through discharge nozzle 3, meanwhile,
The biogas produced after wastewater fermentation in this process is discharged from exhaustor 8.Water seal is used to go out in liquid storage tank 6
Material pipe 3 is partially submerged, it is ensured that the anaerobic environment of this reactor.Under normal conditions, the float in waste water
Can flow along with the current of waste water, finally discharge from discharge nozzle 3.But when the suspension in reactor casing 1
During the phenomenon that the more appearance of thing is piled up, the valve of slag flushing device 9 can be opened, and start immersible pump 7, biogas slurry
Extracted out by liquid storage tank 6 by immersible pump 7, through flushing cinder mouth 5, the float in reactor casing 1 formed impact,
Thus float is rushed at discharge nozzle 3 and discharges reactor.This utility model simple in construction, be possible not only to avoid by
Piling up, in float, the reactor plugs caused causes reactor to damage, it is also possible to effectively improve the process to waste water
Efficiency, and have good stability, use can be widely popularized.
Of the present utility model ultimate principle, principal character and of the present utility model advantage have more than been shown and described.
Skilled person will appreciate that of the industry, this utility model is not restricted to the described embodiments, above-described embodiment and
Principle of the present utility model is simply described, without departing from this utility model spirit and scope described in description
Under premise, this utility model also has various changes and modifications, and these changes and improvements both fall within claimed
In the range of this utility model.This utility model claims scope by appending claims and equivalent circle thereof
Fixed.
Claims (8)
1. process an anaerobic horizontal baffling formula reactor for high suspended matter waste water, including reactor casing (1),
It is characterized in that: described reactor casing (1) is internal is provided with deflection plate (4), and reactor casing (1) is outside
It is provided with feed pipe (2), feed hopper (10), discharge nozzle (3), liquid storage tank (6) and slag flushing device (9)；Institute
State feed pipe (2) to stretch out be connected on the downside of reactor casing (1) front end from feed hopper (10) bottom；Described
Discharge nozzle (3) and liquid storage tank (6) are positioned at the homonymy of feed pipe (2), described discharge nozzle (3) and reactor
It is connected on the upside of casing (1) end and extends liquid storage tank (6) inside；Described slag flushing device (9) is by reactor
Casing (1) is connected by pipeline with liquid storage tank (6), and slag flushing device (9) includes and reactor casing (1)
The flushing cinder mouth (5) of junction and be positioned at the immersible pump (7) that liquid storage tank (6) is internal；Described reactor casing (1)
Top be provided with for biogas discharge exhaustor (8).
A kind of anaerobic horizontal baffling formula reactor processing high suspended matter waste water the most according to claim 1,
It is characterized in that: described deflection plate (4) in ripple type, the crest of deflection plate (4) ripple and the angle of trough
It is 90 °.
A kind of anaerobic horizontal baffling formula reactor processing high suspended matter waste water the most according to claim 2,
It is characterized in that: the number of described deflection plate (4) is the odd number more than 3.
A kind of anaerobic horizontal baffling formula reactor processing high suspended matter waste water the most according to claim 3,
It is characterized in that: described deflection plate (4) is arranged at reactor casing (1) alternate internal.
A kind of anaerobic horizontal baffling formula reactor processing high suspended matter waste water the most according to claim 4,
It is characterized in that: bottom and the top of deflection plate (4) contact with bottom and the top of reactor casing (1),
The side of deflection plate (4) and the sidewall of reactor casing (1) contact, the opposite side of deflection plate (4) with
The sidewall of reactor casing (1) reserves a fixed gap.
A kind of anaerobic horizontal baffling formula reactor processing high suspended matter waste water the most according to claim 5,
It is characterized in that: described flushing cinder mouth (5) is higher than the position of discharge nozzle (3) and is positioned at two deflection plates (4)
Between.
A kind of anaerobic horizontal baffling formula reactor processing high suspended matter waste water the most according to claim 6,
It is characterized in that: the number of described flushing cinder mouth (5) is identical with the number of deflection plate (4).
A kind of anaerobic horizontal baffling formula reactor processing high suspended matter waste water the most according to claim 7,
It is characterized in that: the interior flow direction flowing out biogas slurry of described flushing cinder mouth (5) and reactor casing (1) interior waste water at this
Flow to identical.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620341902.6U CN205575772U (en) | 2016-04-21 | 2016-04-21 | Handle horizontal baffling formula reactor of anaerobism of high suspended solid waste water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620341902.6U CN205575772U (en) | 2016-04-21 | 2016-04-21 | Handle horizontal baffling formula reactor of anaerobism of high suspended solid waste water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205575772U true CN205575772U (en) | 2016-09-14 |
Family
ID=56860754
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620341902.6U Expired - Fee Related CN205575772U (en) | 2016-04-21 | 2016-04-21 | Handle horizontal baffling formula reactor of anaerobism of high suspended solid waste water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205575772U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111847626A (en) * | 2020-07-27 | 2020-10-30 | 南昌航空大学 | Device for pretreating complex heavy metal in electroplating cleaning wastewater by catalytic oxidation method and using method thereof |
-
2016
- 2016-04-21 CN CN201620341902.6U patent/CN205575772U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111847626A (en) * | 2020-07-27 | 2020-10-30 | 南昌航空大学 | Device for pretreating complex heavy metal in electroplating cleaning wastewater by catalytic oxidation method and using method thereof |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203307190U (en) | Anaerobic reactor | |
| CN205575772U (en) | Handle horizontal baffling formula reactor of anaerobism of high suspended solid waste water | |
| CN211393926U (en) | High-density air floatation equipment | |
| CN204643958U (en) | Modernization pig house wastewater reuse approach anaerobic reaction system | |
| CN203833929U (en) | Complete mixed anaerobic bioreactor | |
| CN206407970U (en) | Biogas recirculation anaerobic reactor | |
| CN206069667U (en) | Environmentally friendly feces, sewage purification bucket | |
| CN205662439U (en) | High efficiency manure pit | |
| CN106381262B (en) | Feed liquid circulation fluidizes installation for fermenting | |
| CN202973059U (en) | Novel periodic blowdown flash tank | |
| CN207973542U (en) | The oil-water separation tank of municipal swill separator | |
| CN203095663U (en) | Integrated air floating device | |
| CN202558696U (en) | Normal-temperature anaerobic device | |
| CN202124627U (en) | Overflow type dry anaerobic fermentation tank | |
| CN202246661U (en) | Full-automatic methane tank | |
| CN201317773Y (en) | Automatic anti-crusting marsh gas tank | |
| CN206127284U (en) | Biogas anaerobic fermentation device | |
| CN205576132U (en) | Can arrange anaerobism baffling formula reactor of dross | |
| CN218188540U (en) | Asphalt flue gas purification system of asphalt mixing plant | |
| CN203999126U (en) | A kind of hydrolysis acidification pool | |
| CN202209895U (en) | Steam-water mixing device for recycling steam heat during slag stewing | |
| CN203007271U (en) | Household pregnant-type liquid communicating vessel methane tank | |
| CN207091046U (en) | A kind of portable sewage disposal device | |
| CN209853840U (en) | Composite artificial wet land | |
| CN210048639U (en) | Three manure pits of check of integral type |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| 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: 20160914 Termination date: 20180421 |