CN202063770U - Novel biofilm reactor - Google Patents
Novel biofilm reactor Download PDFInfo
- Publication number
- CN202063770U CN202063770U CN2011200439167U CN201120043916U CN202063770U CN 202063770 U CN202063770 U CN 202063770U CN 2011200439167 U CN2011200439167 U CN 2011200439167U CN 201120043916 U CN201120043916 U CN 201120043916U CN 202063770 U CN202063770 U CN 202063770U
- Authority
- CN
- China
- Prior art keywords
- membrane
- water
- sewage
- reactor
- dividing plate
- 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
Images
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
The utility model discloses a novel biofilm reactor which solves the problems of a reactor membrane component in the prior art that the membrane hanging is inconvenient, blockage is easy, a sewage treatment process cannot be flexibly changed and reliability is lacked. According to the reactor, the membrane component can be flexibly detached and changed, so that a membrane hole is effectively prevented from being blocked, and the treatment process can be flexibly changed according to incoming water quality and water outlet requirements; and the biofilm reactor mainly comprises water inlets, a valve, a reaction container, a division board, the membrane component, a filter mesh, a sewage funnel, a sewage pipe and water outlets. The novel biofilm reactor is characterized in that the division board, a detachable biofilm and the sewage funnel are arranged in a shell body, and a plurality of water inlets are arranged for changing the sewage treatment process.
Description
Technical field
The utility model relates to a kind of biofilm reactor, mainly adopts the microbial film processing mode to carry out the processing of sewage.
Background technology
Water is the human lives, produce in requisite resource, along with economy in the global range and Increase of population, the demand of water is presented the trend that increases gradually.On the other hand, the pollution of water body and the atrophy at water source have produced the contradiction between water supply and the need water, and water has become the restraining factors of modern society and Economic development.
Municipal sewage as a resource is meant that municipal effluent and trade effluent reach certain water quality standard through suitably handling, and makes it to become the part of urban water resource, reaches the purpose that makes full use of water resources and alleviate ambient pollution burden.
China is as water big country and one of 13 poor-water states in the world, and under the limited prerequisite of gross amount of water resources, the new water resources of simple exploitation is not all right, and increasing income develops simultaneously with throttling is only the effective way that solves this difficult problem.
Biomembrance process is to utilize the microorganism (be microbial film) of apposition growth in some solids surface to carry out the method that organic sewage is handled.The ecosystem that microbial film is made up of aerobic bacteria, anerobe, amphimicrobe, fungi, protozoon and the algae etc. of highly dense, its solid dielectric that adheres to is called filtrate or carrier.Microorganism growth accumulative carrier (generally claiming filler) is set in sewage treatment structure, under the condition of oxygenation, microorganism is at the poly-formation microbial film that adheres to of filling surface, when the sewage of process oxygenation (oxygenate apparatus is made up of water treatment aeration blower fan and aerator) flows through filler with certain flow velocity, microorganism in the microbial film absorbs the organism in the water of decomposition, sewage is purified, and microorganism also obtains propagation simultaneously, and microbial film thickens thereupon.When microbial film rises to certain thickness, be restricted to the oxygen of microbial film internal divergence, its surface has been still oxygen condition, and internal layer then can be anoxic even anaerobic state, and finally causes biomembranous coming off.
Microorganism is along the general designation of the epontic bioremediation of solid (can claim carrier) in the waste water.Because of microbial population grows into the mucous membrane shape along solid surface, so name.When waste water contacted with microbial film, pollutent was transferred on the film from water, thereby obtained handling.
The utility model content
For overcoming above-mentioned the deficiencies in the prior art, the utility model provides a kind of new-type biofilm reactor, this reactor can change the kind and the quantity of film as required arbitrarily, also can change water treatment process, therefore be applicable to the processing of multiple sewage, and have simple in structure, cost is low, easy to operate, fenestra is difficult for stopping up, and blowdown is characteristics easily.
The technical scheme that its technical problem that solves the utility model adopts is:
A kind of novel membrane-biological membrane reactor, comprise housing, water-in, reaction vessel, dividing plate, membrane module, filter screen, sewage draining exit, valve, water outlet, it is characterized in that, described housing is provided with a plurality of water-ins in the top, inside is provided with dividing plate, dividing plate is provided with the membrane module pickup groove, and detachable microbial film is housed on the pickup groove; Described reactor bottom is provided with a plurality of discharge funnel for sludges arranged side by side, and the discharge funnel for sludge bottom is connected with blow-off line, and is provided with valve.3-7 dividing plate is installed in the described reaction vessel, reaction vessel is divided into the unit for treating water of 2-6 U type.Each described unit for treating water top is furnished with a water-in, and each described water-in all is furnished with valve.The dividing plate of the side that described U type unit for treating water sewage is up is provided with 3-5 membrane module pickup groove.The up side of described U type unit for treating water sewage below membrane module, is provided with 1 filter screen pickup groove.Each described U type unit for treating water below connects a funnel type sewage draining exit, and each sewage draining exit all is furnished with 1 valve.Described water outlet is located at reactor top, is higher than last group membrane module, is lower than the upper edge of lower rim fixed dividing plate.
The beneficial effect of the technical scheme that utility model embodiment provides is:
This novel membrane-biological membrane reactor can come to require to change water treatment process according to influent quality, water outlet by the quantity of dismounting dividing plate, switch inlet valve, increase and decrease membrane module, has saved unnecessary cost.Membrane module in the reactor also can be replaced to adapt to different types of waste water.Filter screen in the reactor and U type structure can effectively prevent the fenestra blocking problem.The funnel type sewage draining exit of reactor bottom makes things convenient for the settling discharging.Last draining helps reactor in underground installation.
Description of drawings
In order to be illustrated more clearly in the technical solution of the utility model, to do one to the accompanying drawing that uses among the embodiment below introduces simply, apparently, below listed accompanying drawing only be embodiment of the present utility model, for those of ordinary skills, under the prerequisite of not paying creative work, can also obtain other accompanying drawing according to these accompanying drawings.
Fig. 1 is the synoptic diagram of embodiment 1.
Fig. 2 is the synoptic diagram of embodiment 2.
Fig. 3 is the synoptic diagram of embodiment 3.
Fig. 4 is the synoptic diagram of embodiment 4.
In the accompanying drawing, the assembly of each label representative is as follows:
1. inhalent siphon, 2. valve, 3. reactor wall, 4. membrane module, 5. dividing plate, 6. filter screen, 7. settling collection funnel, 8. settling vent pipe, 9. rising pipe.
Embodiment
For making the purpose of this utility model, technical scheme and advantage clearer, the utility model embodiment is described in further detail below in conjunction with accompanying drawing.
Embodiment 1
The embodiment synoptic diagram is seen Fig. 1.The utility model provides a kind of novel membrane-biological membrane membrane bioreactor, wherein in the reactor wall 3 dividing plate 5 is housed, and dividing plate 5 is detachable, and reactor is divided into a plurality of U type reaction members.Each reaction member top all is equipped with inhalent siphon 1, and each inhalent siphon all is furnished with opening-closing valve 2 separately.Filter screen 6 is equipped with in bottom at U type reaction member, and there is detachable membrane module 4 filter screen 6 tops.Settling collection funnel 7 is arranged at the reaction member bottom, and funnel connects settling vent pipe 8.Reactor top is provided with rising pipe 9.
The embodiment synoptic diagram is seen Fig. 2.Open first water intaking valve 2, other water intaking valves are closed, and are the sewage feeding reactor that 20～25NTU, COD300-500mg/L, ammonia nitrogen 50-80mg/L contain active sludge with turbidity.When sewage passed through U type channel bottom, sludge settling was collected precipitation collection funnel 7.Sewage is up, and during through filter screen 6, unprecipitated suspended substance is blocked in the sewage.Sewage continues up, by five tunic assemblies 4, enters next processing unit successively, is finally flowed out by water outlet 9.Sedimentary mud is discharged through precipitation collection funnel 7 and precipitation vent pipe 8, refluxes.The sewage turbidity of discharging is that 0NTU, COD are 30-50mg/L, ammonia nitrogen 20mg/L.
The embodiment synoptic diagram is seen Fig. 3.Open the 3rd water intaking valve 2, other water intaking valves are closed, and are the sewage feeding reactor that 20～25NTU, COD100-200mg/L, ammonia nitrogen 40-60mg/L contain active sludge with turbidity.When sewage passed through U type channel bottom, sludge settling was collected precipitation collection funnel 7.Sewage is up, and during through filter screen 6, unprecipitated suspended substance is blocked in the sewage.Sewage continues up, by five tunic assemblies 4, enters next processing unit successively, is finally flowed out by water outlet 9.Sedimentary mud is discharged through precipitation collection funnel 7 and precipitation vent pipe 8, refluxes.The sewage turbidity of discharging is that 0NTU, COD are 30-50mg/L, ammonia nitrogen 25mg/L.
The embodiment synoptic diagram is seen Fig. 4.Open first water intaking valve 2, other water intaking valves are closed, and are the sewage feeding reactor that 20～25NTU, COD100-200mg/L, ammonia nitrogen 40-60mg/L contain active sludge with turbidity.When sewage passed through U type channel bottom, sludge settling was collected precipitation collection funnel 7.Sewage is up, and during through filter screen 6, unprecipitated suspended substance is blocked in the sewage.Sewage continues up, by trilamellar membrane assembly 4, enters next processing unit successively, is finally flowed out by water outlet 9.Sedimentary mud is discharged through precipitation collection funnel 7 and precipitation vent pipe 8, refluxes.The sewage turbidity of discharging is that 0NTU, COD are 30-50mg/L, ammonia nitrogen 20-25mg/L.
The above only is preferred embodiment of the present utility model, and is in order to restriction the utility model, not all within spirit of the present utility model and principle, any modification of being done, is equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.
Claims (7)
1. novel membrane-biological membrane reactor, comprise housing, water-in, reaction vessel, dividing plate, membrane module, filter screen, sewage draining exit, valve, water outlet, it is characterized in that, described housing is provided with a plurality of water-ins in the top, inside is provided with dividing plate, dividing plate is provided with the membrane module pickup groove, and detachable microbial film is housed on the pickup groove; Described reactor bottom is provided with a plurality of discharge funnel for sludges arranged side by side, and the discharge funnel for sludge bottom is connected with blow-off line, and is provided with valve.
2. novel membrane-biological membrane reactor according to claim 1 is characterized in that, 3-7 dividing plate is installed in the described reaction vessel, reaction vessel is divided into the unit for treating water of 2-6 U type.
3. novel membrane-biological membrane reactor according to claim 2 is characterized in that, each described unit for treating water top is furnished with a water-in, and each described water-in all is furnished with valve.
4. novel membrane-biological membrane reactor according to claim 3 is characterized in that, the dividing plate of the side that described U type unit for treating water sewage is up is provided with 3-5 membrane module pickup groove.
5. novel membrane-biological membrane reactor according to claim 4 is characterized in that, the up side of described U type unit for treating water sewage below membrane module, is provided with 1 filter screen pickup groove.
6. novel membrane-biological membrane reactor according to claim 5 is characterized in that, each described U type unit for treating water below connects a funnel type sewage draining exit, and each sewage draining exit all is furnished with 1 valve.
7. novel membrane-biological membrane reactor according to claim 6 is characterized in that described water outlet is located at reactor top, is higher than last group membrane module, is lower than the upper edge of lower rim fixed dividing plate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200439167U CN202063770U (en) | 2011-02-22 | 2011-02-22 | Novel biofilm reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011200439167U CN202063770U (en) | 2011-02-22 | 2011-02-22 | Novel biofilm reactor |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202063770U true CN202063770U (en) | 2011-12-07 |
Family
ID=45057639
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011200439167U Expired - Fee Related CN202063770U (en) | 2011-02-22 | 2011-02-22 | Novel biofilm reactor |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202063770U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104211173A (en) * | 2014-09-30 | 2014-12-17 | 许中华 | Modularized intelligent anaerobic reaction system |
| CN108579440A (en) * | 2018-05-19 | 2018-09-28 | 郭学章 | A kind of depth sewage disposal ceramic film component |
-
2011
- 2011-02-22 CN CN2011200439167U patent/CN202063770U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104211173A (en) * | 2014-09-30 | 2014-12-17 | 许中华 | Modularized intelligent anaerobic reaction system |
| CN108579440A (en) * | 2018-05-19 | 2018-09-28 | 郭学章 | A kind of depth sewage disposal ceramic film component |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN111675435A (en) | Integrated sewage treatment equipment based on A/O-MBBR (anaerobic-anoxic-aerobic-moving bed biofilm reactor) process and sewage treatment method | |
| CN106116045A (en) | A kind of efficiently villages and small towns waste water treating and reutilizing device and technique thereof | |
| CN101792242A (en) | Treatment process of waste water of dairy products | |
| CN105836970B (en) | Sewage treatment device | |
| CN217809127U (en) | Kitchen garbage effluent disposal system | |
| CN209835892U (en) | Domestic sewage purification device | |
| CN106673257A (en) | Micropolluted raw water treatment integrated plant | |
| CN202063770U (en) | Novel biofilm reactor | |
| CN202988918U (en) | Multi-stage multi-section combined type high concentration chemical wastewater treatment system | |
| CN209835881U (en) | Distributed household type integrated sewage treatment device suitable for rural areas | |
| CN208933187U (en) | A kind of integration distributing high-efficiency wastewater treatment system | |
| CN114906986B (en) | Integrated sewage treatment device and method with adjustable process | |
| CN216808506U (en) | Kitchen and kitchen garbage and wastewater treatment system | |
| CN104671612A (en) | Sequence flow return type sewage treatment method and treatment device | |
| CN211367130U (en) | Multipoint balanced distributed backflow sewage treatment device | |
| CN104355396B (en) | Type sequence intermittent biofiltration particle reaction device and technique thereof | |
| CN114014492A (en) | Low carbon nitrogen ratio sewage treatment system | |
| CN207903981U (en) | A kind of efficient up-flow biological reaction apparatus | |
| CN207811366U (en) | A kind of sewage disposal system | |
| CN111908603A (en) | Novel anaerobic biological filter wastewater treatment equipment and wastewater treatment method thereof | |
| CN206457381U (en) | A kind of papermaking sewage treatment system | |
| CN205999219U (en) | A kind of sewage disposal device based on MBBR technique | |
| CN217377665U (en) | Purification tank equipment for separating and treating liquid dung | |
| CN104261562B (en) | Biological bed treatment unit and method under a kind of 360 degree of rotating waters | |
| CN204111419U (en) | Biological bed treatment unit under a kind of 360 degree of rotating waters |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111207 Termination date: 20130222 |