CN205419905U - Sewage dynamic load processing apparatus - Google Patents
Sewage dynamic load processing apparatus Download PDFInfo
- Publication number
- CN205419905U CN205419905U CN201521029879.9U CN201521029879U CN205419905U CN 205419905 U CN205419905 U CN 205419905U CN 201521029879 U CN201521029879 U CN 201521029879U CN 205419905 U CN205419905 U CN 205419905U
- Authority
- CN
- China
- Prior art keywords
- main body
- apparatus main
- pipe
- water inlet
- water
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Abstract
The utility model discloses a sewage dynamic load processing apparatus, including the device main part, the left sub -unit connection inlet tube of device main part, the inlet tube is connected with the water inlet main pipe who installs the main part lower part, the upper portion on device main part right side sets up the outlet pipe, and the outlet pipe is responsible for with the play water that installs the main part lower part and is connected, the utility model discloses can realize coming water variation in load within range at a broad, it is unchangeable basically that the device low reaches remain operating load throughout, and treatment effeciency that like this can whole water factory provides very big assurance, the stable of low reaches biochemical system microorganism populations has been guaranteed and has grown that this is most important to stabilizing of treatment effect to the stability of lotus, the biochemical operation degree of difficulty in low reaches has been simplified in the stability of load, provides the precondition for realizing becoming more meticulous operateing.
Description
Technical field
This patent relates to field of waste water treatment, is specifically related to a kind of sewage dynamic load processing means.
Background technology
Current sewage disposal technology has defined diversified treatment technology, although currently having numerous sewage treatment technologies, but these technology all assume that a stable operating mode designs and calculates, the water load variations that face actual for sewage disposal system does not has special design and equipment, typically can only be amplified by entirety and tackle；Being currently included MBBR technique in interior most of technological designs is all a kind of fixed connected mode, does not make full use of special process actual motion change under the conditions of different load, does not the most play this technique practical capacity to reply load variations；Design under being both for a kind of static state or being the operating mode of stable state, the load variations problem (coming water concentration and changes in flow rate) generally faced for sewage disposal system, there is presently no special technology or equipment is tackled.
Summary of the invention
The purpose of this utility model be to solve in prior art not for a kind of static state or be stable state operating mode under the defect of design.
This utility model adopts the following technical scheme that
A kind of sewage dynamic load processing means, including apparatus main body (1), the bottom in described apparatus main body (1) left side connects water inlet pipe (3), and water inlet pipe (3) is responsible for (10) with the water inlet of apparatus main body (1) bottom and is connected；The top on described apparatus main body (1) right side arranges outlet pipe (2), and outlet pipe (2) is connected with the water outlet main pipe (11) of apparatus main body (1) bottom；The inside of described apparatus main body (1) arranges Moveable packings reaction zone (8), and the bottom of described apparatus main body (1) arranges aerating system (9)；Described aerating system (9) is connected to compressed air supervisor (12) by pipeline；Described water inlet pipe (3) arranges electrically operated valve one (4), and described aerating system (9) is connected on the pipeline of compressed air supervisor (12) arrange electrically operated valve two (5), and described outlet pipe (2) arranges electrically operated valve three (6).
Described water inlet supervisor (10), water outlet main pipe (11) and compressed air supervisor (12) all be arranged in parallel, and water outlet main pipe (11) is in water inlet supervisor (10) bottom, and compressed air supervisor (12) is in water outlet main pipe (11) bottom.
Described apparatus main body (1) can be multiple series connection, and apparatus main body (1) is by the water inlet pipe of the upper connecting line of outlet pipe (2) to another apparatus main body.
Electrically operated valve four (7) is set on the pipeline of the water inlet pipe being connected to another apparatus main body on described outlet pipe (2).
Operation principle of the present utility model: reach to absorb water load variations by application biological moving bed technique (MBBR) technology of innovation formula, reaches the effect keeping downstream load stable, specifically by sewage dynamic load processing means.
The biological moving bed technique (MBBR) run by sewage dynamic load processing means is a kind of biochemical process utilizing mobile model filler, filler becomes biomembranous carrier, and form the microflora of the composition such as multiple different oxygen and autotrophic type microorganism to the C degrading in sewage, N, the pollutant such as P, thus reach to purify the effect of sewage.The outstanding feature of this technique is, owing to make use of the mobility filler with very bigger serface, and the quantity that not only ensure that microorganism but also the efficient mass transfer effect that simultaneously ensure that between biomembrane and sewage, high load capacity can be born, and capacity of resisting impact load is strong.
Multistage MBBR processing unit is attached by this utility model sewage dynamic load processing means by multiple pipeline, and realize the multiple connection in series-parallel form of each processing unit and off-line by the valve on pipeline and presence switches, in conjunction with aerating system under comprehensive robot control system(RCS) is uniformly controlled, according to different industry controls (the different water yields and concentration levels), the degree of depth of adjusting process and form, realize stablizing the purpose of water outlet, ensure that the process load of downstream processes remains at a relatively minizone, thus keep water outlet quality steadily in the long term.
Comprehensive robot control system(RCS) system utilizes flow and the concentration sensor parameter of upstream, by selecting suitable operational mode after computing, automatic adjustment system operational mode, it is ensured that operate steadily intelligence.
The beneficial effects of the utility model: in the range of this utility model can be implemented in a wider water load variations, device downstream remains that operating load is basically unchanged, so can provide the biggest guarantee with the treatment effeciency of whole water factory；Lotus stablize the stable growth that ensure that downstream biochemical system microbial population (especially nitrifier so needs the strain of stable conditions of existence), treatment effect is stablized most important by this；Stablizing of load simplifies the operation difficulty that downstream is biochemical, provides precondition for realizing lean operation.
Accompanying drawing explanation
Fig. 1 is described sewage dynamic load processing means structure；
Fig. 2 is described apparatus main body structure chart.
Description of reference numerals
1 apparatus main body；2 outlet pipes；3 water inlet pipes；4 electrically operated valves one；5 electrically operated valves two；6 electrically operated valves three；7 electrically operated valves four；8 Moveable packings reaction zones；9 aerating systems；10 water inlet supervisors；11 water outlet main pipe；12 compressed air supervisors.
Detailed description of the invention
This utility model is further illustrated below in conjunction with the accompanying drawings with preferred embodiment of the present utility model.
Such as Fig. 1-2, a kind of sewage dynamic load processing means, including apparatus main body 1, the bottom on the left of described apparatus main body 1 connects water inlet pipe 3, and water inlet pipe 3 is responsible for 10 with the water inlet of apparatus main body 1 bottom and is connected；Top on the right side of described apparatus main body 1 arranges outlet pipe 2, and outlet pipe 2 is connected with the water outlet main pipe 11 of apparatus main body 1 bottom；The inside of described apparatus main body 1 arranges Moveable packings reaction zone 8, and the bottom of described apparatus main body 1 arranges aerating system 9；Described aerating system 9 is connected to compressed air supervisor 12 by pipeline；Described water inlet pipe 3 arranges electrically operated valve 1, and described aerating system 9 is connected on the pipeline of compressed air supervisor 12 arrange electrically operated valve 25, and described outlet pipe 2 arranges electrically operated valve 36.
Described water inlet supervisor 10, water outlet main pipe 11 and compressed air supervisor 12 be arranged in parallel, and water outlet main pipe 11 is in water inlet supervisor 10 bottoms, and compressed air supervisor 12 is in water outlet main pipe 11 bottom.
Described apparatus main body 1 can be multiple series connection, and apparatus main body 1 is by the water inlet pipe of connecting line on outlet pipe 2 to another apparatus main body.
On the pipeline of the water inlet pipe being connected to another apparatus main body on described outlet pipe 2, electrically operated valve 47 is set.
Operation principle of the present utility model: reach to absorb water load variations by application biological moving bed technique (MBBR) technology of innovation formula, reaches the effect keeping downstream load stable, specifically by sewage dynamic load processing means.
The biological moving bed technique (MBBR) run by sewage dynamic load processing means is a kind of biochemical process utilizing mobile model filler, filler becomes biomembranous carrier, and form the microflora of the composition such as multiple different oxygen and autotrophic type microorganism to the C degrading in sewage, N, the pollutant such as P, thus reach to purify the effect of sewage.The outstanding feature of this technique is, owing to make use of the mobility filler with very bigger serface, and the quantity that not only ensure that microorganism but also the efficient mass transfer effect that simultaneously ensure that between biomembrane and sewage, high load capacity can be born, and capacity of resisting impact load is strong.
Multistage MBBR processing unit is attached by this utility model sewage dynamic load processing means by multiple pipeline, and realize the multiple connection in series-parallel form of each processing unit and off-line by the valve on pipeline and presence switches, in conjunction with aerating system under comprehensive robot control system(RCS) is uniformly controlled, according to different industry controls (the different water yields and concentration levels), the degree of depth of adjusting process and form, realize stablizing the purpose of water outlet, ensure that the process load of downstream processes remains at a relatively minizone, thus keep water outlet quality steadily in the long term.
Comprehensive robot control system(RCS) system utilizes flow and the concentration sensor parameter of upstream, by selecting suitable operational mode after computing, automatic adjustment system operational mode, it is ensured that operate steadily intelligence.
In the range of this utility model can be implemented in a wider water load variations, device downstream remains that operating load is basically unchanged, and so can provide the biggest guarantee with the treatment effeciency of whole water factory；Lotus stablize the stable growth that ensure that downstream biochemical system microbial population (especially nitrifier so needs the strain of stable conditions of existence), treatment effect is stablized most important by this；Stablizing of load simplifies the operation difficulty that downstream is biochemical, provides precondition for realizing lean operation.
The above, only this utility model preferred embodiment, therefore the scope that this utility model is implemented can not be limited according to this, the equivalence change i.e. made according to this utility model the scope of the claims and description with modify, all should still belong in the range of this utility model contains.
Claims (4)
1. a sewage dynamic load processing means, it is characterised in that: including that apparatus main body (1), the bottom in described apparatus main body (1) left side connect water inlet pipe (3), water inlet pipe (3) is responsible for (10) with the water inlet of apparatus main body (1) bottom and is connected；The top on described apparatus main body (1) right side arranges outlet pipe (2), and outlet pipe (2) is connected with the water outlet main pipe (11) of apparatus main body (1) bottom；The inside of described apparatus main body (1) arranges Moveable packings reaction zone (8), and the bottom of described apparatus main body (1) arranges aerating system (9)；Described aerating system (9) is connected to compressed air supervisor (12) by pipeline；Described water inlet pipe (3) arranges electrically operated valve one (4), and described aerating system (9) is connected on the pipeline of compressed air supervisor (12) arrange electrically operated valve two (5), and described outlet pipe (2) arranges electrically operated valve three (6).
Sewage dynamic load processing means the most according to claim 1, it is characterized in that: described water inlet supervisor (10), water outlet main pipe (11) and compressed air supervisor (12) all be arranged in parallel, water outlet main pipe (11) is in water inlet supervisor (10) bottom, and compressed air supervisor (12) is in water outlet main pipe (11) bottom.
Sewage dynamic load processing means the most according to claim 1, it is characterised in that: described apparatus main body (1) can be multiple series connection, and apparatus main body (1) is by the water inlet pipe of the upper connecting line of outlet pipe (2) to another apparatus main body.
Sewage dynamic load processing means the most according to claim 3, it is characterised in that: electrically operated valve four (7) is set on the pipeline of the water inlet pipe being connected to another apparatus main body on described outlet pipe (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521029879.9U CN205419905U (en) | 2015-12-10 | 2015-12-10 | Sewage dynamic load processing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521029879.9U CN205419905U (en) | 2015-12-10 | 2015-12-10 | Sewage dynamic load processing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205419905U true CN205419905U (en) | 2016-08-03 |
Family
ID=56516782
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521029879.9U Expired - Fee Related CN205419905U (en) | 2015-12-10 | 2015-12-10 | Sewage dynamic load processing apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205419905U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106348264A (en) * | 2016-09-29 | 2017-01-25 | 浙江省林业科学研究院 | Device for countercurrent recovering phosphoric acid from chemical activation material |
-
2015
- 2015-12-10 CN CN201521029879.9U patent/CN205419905U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106348264A (en) * | 2016-09-29 | 2017-01-25 | 浙江省林业科学研究院 | Device for countercurrent recovering phosphoric acid from chemical activation material |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Jacob-Lopes et al. | Biomass production and carbon dioxide fixation by Aphanothece microscopica Nägeli in a bubble column photobioreactor | |
| Tang et al. | Perfusion culture of hybridoma cells for hyperproduction of IgG2a monoclonal antibody in a wave bioreactor‐perfusion culture system | |
| EA200801974A1 (en) | METHOD OF INDUSTRIAL PRODUCTION OF BIOCATALIZERS IN THE FORM OF ENZYMES OR MICROORGANISMS IMMOBILIZED IN GEL ON THE BASIS OF POLYVINYL ALCOHOL, THEIR APPLICATION AND DEVICE FOR THEIR PRODUCTION | |
| Park et al. | Hydrogen sulfide removal utilizing immobilized Thiobacillus sp. IW with Ca-alginate bead | |
| CN205419905U (en) | Sewage dynamic load processing apparatus | |
| CN104512960B (en) | A kind of integrated apparatus of biological wastewater treatment and method of wastewater treatment | |
| CN216712108U (en) | Device for rapidly enriching and culturing anaerobic ammonium oxidation bacteria | |
| Yang et al. | Kinetics and stability of GM‐CSF production by recombinant yeast cells immobilized in a fibrous‐bed bioreactor | |
| CN203728638U (en) | MBBR (moving bed biofilm reactor) integrated autotrophic nitrogen removal device | |
| CN104609549B (en) | A kind of remove the method for ammonia nitrogen in waste water | |
| CN110759465A (en) | Membrane aeration aerobic granular sludge reactor and method for culturing aerobic granular sludge and synchronously denitrifying and decarbonizing aerobic granular sludge | |
| Prachanurak et al. | Modelling of biofilm growth for photosynthetic biomass production in a pipe-overflow recirculation bioreactor | |
| CN205419907U (en) | Novel sewage dynamic load handles device | |
| CN110342634A (en) | The micro- oxygen sludge bed process of membrane aeration biomembrane and its wastewater treatment method | |
| CN105217779A (en) | A kind of Mobile biological bed of packings reactor and using method | |
| CN106348445B (en) | The sewage-treatment plant and method of multistage good anaerobism | |
| CN105060624A (en) | Sewage treatment biochemical reaction tank | |
| CN210656885U (en) | A slope shakes pipe for aerobic bacteria cultivates | |
| CN207259230U (en) | A kind of Anammox reaction unit using aerogenesis regulation and control inflow | |
| CN205398226U (en) | Moving bed biofilm - membrane biological fluidized bed sewage treatment system | |
| CN204601992U (en) | Biological method flue gas desulfurization control system | |
| CN206318778U (en) | A kind of vertical biomass generator | |
| CN204939189U (en) | A kind of sewage disposal biochemical reaction tank | |
| Shanahan et al. | Acetate and ammonium diffusivity in membrane-aerated biofilms: improving model predictions using experimental results | |
| CN208747758U (en) | A kind of Water Ecological Recovery fluidized bed |
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: 20160803 Termination date: 20171210 |