CN205398222U - Anaerobism recombination reaction ware - Google Patents
Anaerobism recombination reaction ware Download PDFInfo
- Publication number
- CN205398222U CN205398222U CN201620176579.1U CN201620176579U CN205398222U CN 205398222 U CN205398222 U CN 205398222U CN 201620176579 U CN201620176579 U CN 201620176579U CN 205398222 U CN205398222 U CN 205398222U
- Authority
- CN
- China
- Prior art keywords
- water distribution
- filler
- cell body
- stainless steel
- phase separator
- 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
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model provides an anaerobism recombination reaction ware, includes reactor cell body, inlet tube, water distribution pipeline, stainless wire net, filler, adjustable three -phase separator, the water distribution pipeline adopts carbon steel or stainless steel, packs and adopts cavity plastics ball, and the separator adopts adjustable three -phase separator, follow supreme distribution inlet tube, water distribution pipeline, stainless wire net, filler, adjustable three -phase separator down in the reactor cell body, the bottom of cell body is the toper to be equipped with pai nikou. The utility model discloses an anaerobism recombination reaction ware will mix, multinomial processing capacity collection in an organic whole such as filtration, hydrolytic acidification, digestion, separation.
Description
Technical field
This utility model relates to a kind of hybrid anaerobic reactor being applied to field of water treatment equipment, mainly for the treatment of high-concentration industrial organic waste water.
Background technology
The discharge of a large amount of industrial wastewaters in recent years causes that the scope that water pollutes is increasing, and water pollution problems is also on the rise, and shortage of water resources has threatened the survival and development of the mankind, and anti-pollution of harnessing the river has become, with water conservation, the target that the mankind pursue jointly.
Anaerobic Microbiological Treatment Technology meets mankind's urgent needs to the energy and wastewater treatment simultaneously.Anaerobic Microbiological Treatment Technology, mainly through the effect of anaerobe, makes the Organic substance in waste water be converted into new microbial cell and gaseous product (C02、H2Or CH4)。H2And CH4There is higher combustion heat value.Therefore, waste water fermentation biologic treating technique reclaims the energy while removing organic pollution, provides a practicable approach for solving environmental problem and energy problem.The treatment technology that Anaerobic Microbiological Treatment Technology combines with benign ecological cycles as a kind of environmental conservation, energy recovery, obtains people and more and more payes attention to.
For high-concentration organic industrial waste water, it is generally adopted anaerobic treatment method.For the various problems that current anaerobic reactor exists, it is necessary to improve hybrid anaerobic reactor.
Utility model content
The purpose of this utility model is to provide a kind of Novel anaerobic compound reactor, has good hydraulic flow state, by constructional improvement so that it is in current in being thoroughly mixed fluidised form, it is thus achieved that stronger disposal ability；The good interception capacity of biosolids, makes microorganism in reactor grow in different regions, contacts with the water inlet of different phase, realize biophasic separation to a certain extent, thus the treatment effect of facility can be stabilized and increased；By textural improvement, extend current flow path in reactor.
The technical solution of the utility model, a kind of hybrid anaerobic reactor, including reactor cell body, water inlet pipe, water distribution pipeline, stainless steel cloth, filler, scalable three phase separator；Water distribution pipeline adopts carbon steel or stainless steel, and filler adopts hollow plastics ball, and separator adopts scalable three phase separator；Water inlet pipe, water distribution pipeline, stainless steel cloth, filler, scalable three phase separator it is distributed from bottom to up in reactor cell body；The bottom of cell body is taper, and is provided with precipitation and mud discharging mouth.
Stainless steel cloth is provided with 3-10 layer.The thickness of filler is 20-60cm.
The structure of water distribution pipeline: reactor cell body bottom sets water distribution pipeline, adopts perforated pipe；Water distribution branch pipe it is provided with between filler and stainless steel cloth.Arm quantity designs according to amount of inlet water, uniform along cell body (cylinder) center water inlet pipe.
The beneficial effects of the utility model: this utility model is hybrid anaerobic reactor, are integrated in one multinomial process functions such as mixing, filtration, hydrolysis acidification, digestion, separation.Technique is processed by several anaerobic reactors a kind of efficient anaerobic that is composited in an equipment.Hybrid anaerobic reactor its underpart is water distribution, mud-water separation district, and central reaction zone is made up of the biomembrane of filler and attachment thereof, it is possible to keep significantly high microorganism concn；Due to the existence of filler, the bubble carrying mud secretly collides therewith in uphill process, and quickening mud separates with bubble, reduces sludge loss.Top sets three phase separator, gas and water, mud three phase separation, and under gravity, mud falls after rise to reaction zone.Treatment effect of the present utility model is proven very outstanding, specifically has following features: hydraulics is good, anti-shock loading；The interception capacity of good biosolids, organic loading is high；The startup time is short, runnability is reliable and stable；Three phase separation is effective, contaminant removal efficiency is high；Volume of equipment load is high, and floor space is little；Energy consumption is low, and operating cost is little, easy to maintenance.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
Detailed description of the invention
Below in conjunction with accompanying drawing and example, this utility model is described further.Hybrid anaerobic reactor basic structure is as shown in drawings.Mud discharging mouth 1, water inlet supervisor 2, wire gauze 3, filler 4, water outlet 5, biogas 6, three phase separator 7, water distribution branch pipe 8, water inlet 9.
Hybrid anaerobic reactor, including reactor cell body, water distribution pipeline, stainless steel cloth, filler, scalable three phase separator.
The integrated baffling type anaerobic reactor (ABR) of this utility model, anaerobic filter (AF), upflow anaerobic sludge blanket reactor (UASB), be composited a kind of new and effective anaerobic reactor by several anaerobic reactors in an equipment.
For taper bucket bottom reactor cell body, bottom is provided with discharge pipeline, discharges the solid suspension of excess sludge and sedimentation.
Reactor lower part sets water distribution pipeline, adopts perforated pipe；Setting up water distribution branch pipe between filler and stainless steel cloth, arm quantity designs according to amount of inlet water, uniform along body centre water inlet pipe.
On water inlet supervisor top, stainless steel cloth is set.On the one hand by designing the rational spacing of stainless steel cloth, angle, make waste water repeatedly baffling up and down, reduce dead band, also function to retain the effect of float, tentatively realize the separation that solid-liquid is biphase, reduce the stifled risk of packing layer dirt.Increase inside reactor Zero-valent Iron on the other hand, by consuming the hydrion that acidifying produces, and anaerobe combined effect, reduce influent COD and pH value, provide advantage for follow-up Aerobic Process for Treatment.
Reaction zone adopts hollow plastics ball, and packing layer makes the ability of reactor accumulation microorganism be greatly increased, and improves anaerobic treatment effect.Different according to water quality treatment, different filler can be loaded at packing layer, to reach to remove different pollutant purpose.
Three phase separator adopts controllability three phase separator, by driving hand lever and telescopic arm, regulates reflecting plate and horizontal direction angle, improves gas, solid and liquid three phase separation effect.
In hybrid anaerobic reactor cell body, water distribution pipeline, stainless steel cloth, filler, scalable three phase separator constitute water distribution area, reaction zone and Disengagement zone.
1, water distribution area: reactor lower part sets water distribution pipeline, water inlet current with slower speed along water distribution pipe even into reactor, formed at stainless steel cloth each cut off in make up and down and precipitation motion, make waste water repeatedly baffling, minimizing dead band up and down.Owing to sewage is under the effect of stainless steel cloth, current make the total length of current flow path in reactor increase around stainless steel cloth flowing, and the settlement action of the stop of stainless steel cloth and mud in addition, biosolids is retained effectively.Inside reactor Zero-valent Iron is increased by stainless steel cloth, by consuming the hydrion that acidifying produces, and anaerobe combined effect, reduce influent COD and pH value, provide advantage for follow-up Aerobic Process for Treatment.
2, reaction zone: adopt hollow plastics ball, packing layer makes the ability of reactor accumulation microorganism be greatly increased, and improves anaerobic treatment effect.This utility model adopts hollow plastics ball, and real surface amasss the advantages such as height, easy to be filmed, long service life, and filler can carry out selecting to replace according to water quality treatment situation.
3, Disengagement zone: adopt controllability three phase separator, by driving hand lever and telescopic arm, regulates reflecting plate and horizontal direction angle, improves gas, solid and liquid three phase separation effect.
Waste water enters water distribution area, and by intaking, perforated pipe enters stainless steel silk web area, enters packing layer after repeatedly baffling, after being attached to the anaerobe on filler and processing, realizes gas, solid and liquid three phase separation by top three phase separator.Recoverable after the collection and confinement of gases produced, the solid suspension of excess sludge and sedimentation is deposited on bottom cone bucket, is discharged by discharge pipeline.
Claims (4)
1. a hybrid anaerobic reactor, is characterized in that including reactor cell body, water inlet pipe, water distribution pipeline, stainless steel cloth, filler, scalable three phase separator；Water distribution pipeline adopts carbon steel or stainless steel, and filler adopts hollow plastics ball, and separator adopts scalable three phase separator；Water inlet pipe, water distribution pipeline, stainless steel cloth, filler, scalable three phase separator it is distributed from bottom to up in reactor cell body；The bottom of cell body is taper, and is provided with mud discharging mouth.
2. hybrid anaerobic reactor according to claim 1, is characterized in that stainless steel cloth is provided with 3-10 layer.
3. hybrid anaerobic reactor according to claim 1, is characterized in that the thickness of filler is 20-60cm.
4. hybrid anaerobic reactor according to claim 1, is characterized in that reactor cell body bottom sets water distribution pipeline, adopts perforated pipe；Water distribution branch pipe it is provided with between filler and stainless steel cloth.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620176579.1U CN205398222U (en) | 2016-03-08 | 2016-03-08 | Anaerobism recombination reaction ware |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620176579.1U CN205398222U (en) | 2016-03-08 | 2016-03-08 | Anaerobism recombination reaction ware |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205398222U true CN205398222U (en) | 2016-07-27 |
Family
ID=56442030
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620176579.1U Active CN205398222U (en) | 2016-03-08 | 2016-03-08 | Anaerobism recombination reaction ware |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205398222U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114749112A (en) * | 2021-01-11 | 2022-07-15 | 中国石油化工股份有限公司 | Fluidized bed reactor |
-
2016
- 2016-03-08 CN CN201620176579.1U patent/CN205398222U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114749112A (en) * | 2021-01-11 | 2022-07-15 | 中国石油化工股份有限公司 | Fluidized bed reactor |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN201245503Y (en) | Multi-cycle efficient anaerobic waste water treating device | |
| CN202089869U (en) | High-efficient composite reaction device for anaerobic organism | |
| CN203999140U (en) | A kind of moving-bed type decentralized sewage treatment device | |
| CN105692894A (en) | Novel anaerobic electrochemical membrane bioreactor system and water treatment method thereof | |
| CN202390287U (en) | Internal iron-carbon UASB-SBR (Upflow Anaerobic Sludge Blanket-Sequencing Batch Reactor) coupling system for treatment of printing and dyeing wastewater | |
| CN202829702U (en) | Anaerobic system used for treating garbage dialysate | |
| CN107384753B (en) | High-efficiency anaerobic fermentation dynamic membrane bioreactor | |
| CN106698661A (en) | Anaerobic reactor for treating high-load garbage leachate | |
| CN201033264Y (en) | High-efficiency water clarifying processing equipment | |
| CN100567176C (en) | Utilize the method and the equipment thereof for the treatment of refuse simultaneously of organism pressure anaerobic method and waste water | |
| CN204454736U (en) | A kind of high efficiency anaerobic reactor | |
| CN203568938U (en) | Domestic sewage treatment system | |
| CN1174815A (en) | High-effect anaerobic treatment device for waste water and method thereof | |
| CN111333281B (en) | Integrated sewage treatment device and treatment process for garbage transfer station sewage | |
| CN205398222U (en) | Anaerobism recombination reaction ware | |
| CN108946939A (en) | A kind of distributed domestic sewage treatment equipment and its technique | |
| CN101774688A (en) | Anaerobic reactor for treating high-concentration chemical industry sewage | |
| CN207792955U (en) | Medium-sized and small enterprises life sewage treatment and reuse equipment | |
| CN215161957U (en) | Novel multi-functional high-speed sedimentation tank | |
| CN214457495U (en) | Self-maintenance sewage treatment integrated equipment | |
| CN111320340B (en) | Bioreactor for treating garbage transfer station pressed leachate | |
| CN214612022U (en) | Landfill leachate handles integrated device | |
| CN204848578U (en) | A hobbing cutter formula agitating unit for unifying sewage treatment device | |
| CN210945262U (en) | Cosmetic production wastewater treatment system | |
| CN108585197B (en) | Village-to-home-level mud film coupling sewage treatment device and treatment method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |