CN2484312Y - Tubelide anaerobic baffling reaction apparatus - Google Patents
Tubelide anaerobic baffling reaction apparatus Download PDFInfo
- Publication number
- CN2484312Y CN2484312Y CN01227609U CN01227609U CN2484312Y CN 2484312 Y CN2484312 Y CN 2484312Y CN 01227609 U CN01227609 U CN 01227609U CN 01227609 U CN01227609 U CN 01227609U CN 2484312 Y CN2484312 Y CN 2484312Y
- Authority
- CN
- China
- Prior art keywords
- annulus
- cylinder
- space
- outlet pipe
- flow chamber
- 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
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 relates to a high load anaerobic organisms treatment device for liquid waste or polluted water. The utility model comprises a liquid waste inlet tube, a sludge outlet pipe, a clean water outlet pipe, a methane outlet pipe and a cylinder which has a circular cone bottom. The utility model is characterized in that a round column is fixed on the bottom of the tube. A round ring guide column which separates the space between the neighboring round columns into an upper flow chamber and a lower flow chamber is arranged in the space, and a gap is provided between the bottom of the round ring guide column and the inner wall of the bottom of the round tube. The utility model has the advantages that the structure is simple and the using is convenient.
Description
The utility model relates to a kind of high-load anaerobic biological treatment device that is used for waste water or sewage.It can be used for handling waste water or the sewage that contains middle and high concentration organic pollutant especially.
At present, the anaerobic biological treatment device that is used for waste water or sewage, as the UASB reactor of inventing and being widely used by Dutch professor Lettinga of agriculture university, this reactor can be seen from the synoptic diagram of 3 figure, it contains the cylinder 1 of the band conical bottom of a band waste water inlet pipe 11, pure water inlet pipe 13, methane outlet pipe 14, and the cylinder top has three-phase separating device 4.Waste water enters cylinder 1 from the waste water inlet pipe 11 of bottom, and in the uphill process, successively by Sludge Bed district, sludge suspension floor district and three-phase separation area, last biogas and water are drawn from top methane outlet pipe 14, pure water inlet pipe 13 respectively in tube.This UASB reactor also has following weak point: 1) when load was higher, more anaerobic activated sludge was taken away in top direct draining meeting, made processing efficiency reduce by 2) also there is certain dead angle in this reactor, thus the effective volume load is descended; 3) to containing the sewage disposal of higher suspended sediment concentration, cause the obstruction of three-phase separating device and water port easily, thereby cause difficult treatment.
Also has a kind of anaerobic biological treatment device that is used for waste water or sewage at present, as anaerobic baffled reactor, it can be seen in the synoptic diagram from Fig. 4, have waste water inlet pipe 11 on its housing 1, pure water inlet pipe 13, methane outlet pipe 14, it is horizontally disposed, and the polylith baffle plate is set at Transverse to the flow direction, with upward flow chamber that reactor is being divided at interval with down to the stream chamber, wherein the upward flow chamber is than wide to the stream chamber down, and the flow deflector 16 ' that has 50 ° of inclination angles in the baffle plate bottom that leads to the upward flow chamber, so that water is delivered to the center of upward flow chamber, make active sludge, the sewage thorough mixing.The shortcoming of this device is that processing efficiency is low, improves the load difficulty, and the sludge stream vector is bigger, mud, water distribution inequality.In a word, above-mentioned two kinds of reactors are to handling high concentration organic sewage, as BOD
5When=1000~40000mg/L and greater concn, its efficient is just undesirable.
The purpose of this utility model is to overcome the shortcoming that exists in the above-mentioned prior art, provide a kind of can the processing contain the waste water of middle and high concentration organic pollutant or the anaerobic baffled reaction unit of drum type brake of sewage, so that it has high-level efficiency, high loading and characteristics such as simple in structure, easy to use.
The anaerobic baffled reaction unit of the utility model drum type brake, it contains the cylinder of the band conical bottom of a band waste water inlet pipe, sludge outlet pipe, pure water inlet pipe, methane outlet pipe, be characterized in: be equipped with in the cylinder one group with the concentric annulus post that is solidified as a whole at the bottom of it, and between the adjacent two annulus posts in the contained space, having installed one with one heart can divide the space into the upward flow chamber and down to the annulus guide pillar of stream chamber, leave the gap between the inwall at the bottom of the bottom of annulus guide pillar and the cylinder.
The anaerobic baffled reaction unit of the utility model drum type brake, contained spatial volume equates between the interior adjacent two annulus posts of cylinder, and equals the contained spatial volume of annulus post of cylinder center; Upward flow chamber and down unequal to the volume of stream chamber, and the volume of upward flow chamber is greater than down to the stream chamber.
The anaerobic baffled reaction unit of the utility model drum type brake, the bottom of annulus guide pillar have water conservancy diversion and tiltedly enclose, and the contained spatial height of annulus post and the diameter ratio that are positioned at cylinder center can be 4-6, preferably 3-5 of the quantity of annulus post.
The anaerobic baffled reaction unit of the utility model drum type brake in use, containing the waste water of middle and high concentration organic pollutant or the sewage waste water inlet pipe at center at the bottom of the cylinder enters, the fluid dividing cover and the baffle that are provided with through its pipe end enter the annulus column space R1 that is positioned at cylinder center, this space is anaerobic reactor R1 just, sewage mixes, contacts, reacts at this with anaerobic activated sludge, meanwhile constantly rise again, behind separator, arrive the top of the annulus post at center, outwards overflowed into the space R2 that two annulus posts are surrounded thus; This space that is reactor R2, this fluid be introduced into by the annulus guide pillar be separated into following to stream indoor flowing downward, then from the water conservancy diversion of annulus guide pillar bottom tiltedly at the bottom of circle and the cylinder gap between the inwall change the upward flow chamber over to, upwards the top end to the annulus post promptly overflows into the space R3 that another is surrounded by two annulus posts in this chamber, be reactor R3, after this flow process in the reaction repeated device R2 again in it enters the space R4 that another annulus post and cylinder inner wall are surrounded, i.e. reactor R4 again again; Sewage and anaerobic activated sludge this carry out last mixing, contact, after the reaction, overflow into effluent weir from the cylinder inner wall top, pure water inlet pipe by the effluent weir bottom flows out, and biogas when the turning to of fluid each reactor R1, R2, R3, R4 top separated upwards, and in the top cover of band awl, assemble the back and draw from the methane outlet pipe.
The utility model has the advantages that: 1) the anaerobic baffled reaction unit of the utility model drum type brake can include one group of reactor of connecting in a cylinder, make waste water or sewage by each reactor the time, repeat to flow downward fast, upwards flow at a slow speed, realize that waste water and repeatedly mixing repeatedly of mud contact, constantly carry out the anaerobe reaction, thereby realized high-level efficiency, high loading, therefore made it can be used to handle waste water or the sewage that contains middle and high concentration organic pollutant waste water or biological sewage treatment; 2) the entire treatment process of the utility model device is to carry out in the tandem reactors of sealing for anaerobic sludge, so its loss is less; 3) the compact construction volume of whole device is little, and easy to use, reliable.
To do narration further to the utility model by embodiment also in conjunction with the accompanying drawings below.Accompanying drawing thes contents are as follows:
Fig. 1 and Fig. 2 are respectively the main sectional view and the left views of the anaerobic baffled reaction unit of the utility model drum type brake;
Fig. 3 is the structural representation of existing UASB reactor;
Fig. 4 is the structural representation of existing anaerobic baffled reactor.
Drawing is described as follows: the 1-cylinder; 2-annulus guide pillar; 3-annulus post; The 4-separator; The 5-effluent weir; The 6-top cover; The 7-fluid dividing cover; The 8-baffle; 9-anaerobic sludge water level gauge; The 10-stopple coupon; 11 waste water inlet pipes; 12-sludge outlet pipe; 13 pure water inlet pipes; 14-methane outlet pipe; The 21-water conservancy diversion tiltedly encloses; R1-is positioned at the annulus column space of cylinder center; R2-from cylinder center outwards first by the annulus cylindrical space that is comprised between the adjacent two annulus posts 3; R3-from cylinder center outside second by the annulus cylindrical space that is comprised between the adjacent two annulus posts 3; The annulus cylindrical space of R4-from being comprised between the inwall of outside the 3rd the annulus post 3 of cylinder center with cylinder 1; Under the a-to stream the chamber; B-upward flow chamber; Leave the gap between the bottom of the oblique circle 21 of B-water conservancy diversion and cylinder 1 diapire.
Represent that with solid arrow fluidic flows among Fig. 1.
The structure of the anaerobic baffled reaction unit of embodiment 1. present embodiment drum type brakes can be seen from Fig. 1 and Fig. 2, it contains a band waste water inlet pipe 11, sludge outlet pipe 12, pure water inlet pipe 13, the cylinder 1 of the band conical bottom of methane outlet pipe 14, be equipped with in the cylinder four with the concentric annulus post 3 that fixes as one at the bottom of it, and between the adjacent two annulus posts in the contained space, installed one with one heart and can divide the space into upward flow chamber b and following annulus guide pillar 2 to stream chamber a, the bottom of annulus guide pillar has tiltedly circle 21 of water conservancy diversion, and and cylinder at the bottom of leave gap B between the inwall.
When using the anaerobic baffled reaction unit of the drum type brake of present embodiment, the waste water or the sewage that contain middle and high concentration organic pollutant enter from waste water inlet pipe 11, and fluid dividing cover 7 and baffle 8 of being provided with through its pipe end enter central circular column space R1; In the R1 of this space, sewage mixes with the anaerobic activated sludge limit, contacts, coronite is to rising, has arrived the top of centered cylinder behind separator 4, overflows into the space R2 that two annulus posts 3 are surrounded at this; In the R2 of this space, fluid is introduced into by flowing downward in a of chamber to stream down that annulus guide pillar 2 is separated into, then from the water conservancy diversion of annulus guide pillar bottom tiltedly the gap B between circle 21 and the cylinder diapire change upward flow chamber b over to; Parallel because of the base cone face of the oblique circle 21 of water conservancy diversion with cylinder base cone wall, so fluid can import the middle part of upward flow chamber b through it, promptly overflow into the space R3 that two annulus posts 3 are surrounded on this indoor top that rises to annulus post 3; The flow process in the repeated space R2 again in reactor R3, after this enter the space R4 that is surrounded by annulus post 3 and cylinder inner wall again again, at last overflow into effluent weir 5 at the top, upward flow chamber of space R4, and from 13 outflows of pure water inlet pipe, and biogas fluid when the top of each space R1, R2, R3, R4 turns to separated upwards, and draw from methane outlet pipe 14 after in the top cover 6 of band awl, assembling.What of sludge quantity then can be observed from anaerobic sludge water level gauge 9, and regularly extract out by a slush pump that is connected with sludge outlet pipe 12.The composition of anaerobic sludge and wastewater treatment efficiency then can be from 10 sampling analysis of the stopple coupon on the cylindrical wall.
Claims (4)
1, the anaerobic baffled reaction unit of a kind of drum type brake, it contains the cylinder (1) of the band conical bottom of a band waste water inlet pipe (11), sludge outlet pipe (12), pure water inlet pipe (13), methane outlet pipe (14), it is characterized in that: be equipped with in the cylinder one group with the concentric annulus post (3) that fixes as one at the bottom of it, and between the adjacent two annulus posts in the contained space, having installed one with one heart can divide the space into upward flow chamber (b) and down to the annulus guide pillar (2) of stream chamber (a), leave gap (B) at the bottom of the bottom of annulus guide pillar and the cylinder between the inwall.
2, the anaerobic baffled reaction unit of drum type brake according to claim 1 is characterized in that: in the said cylinder (1), contained spatial volume equates between the adjacent two annulus posts (3), and equals to be positioned at the contained spatial volume of annulus post of cylinder center; Said upward flow chamber (b) and down unequal to the volume of stream chamber (a), and the volume of upward flow chamber (b) is greater than down to stream chamber (a).
3, the anaerobic baffled reaction unit of drum type brake according to claim 1 is characterized in that: the bottom of said annulus guide pillar (2) has water conservancy diversion and tiltedly encloses (21).
4, according to claim 1 and the anaerobic baffled reaction unit of 2 and 3 described drum type brakes, it is characterized in that: in the said cylinder (1), the contained spatial height of annulus post and the diameter ratio that are positioned at the center are 4-6, and the quantity of annulus post (3) is 3-5.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN01227609U CN2484312Y (en) | 2001-06-08 | 2001-06-08 | Tubelide anaerobic baffling reaction apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN01227609U CN2484312Y (en) | 2001-06-08 | 2001-06-08 | Tubelide anaerobic baffling reaction apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2484312Y true CN2484312Y (en) | 2002-04-03 |
Family
ID=33643029
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN01227609U Expired - Fee Related CN2484312Y (en) | 2001-06-08 | 2001-06-08 | Tubelide anaerobic baffling reaction apparatus |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2484312Y (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100506721C (en) * | 2006-07-20 | 2009-07-01 | 清华大学 | Method and device for improving three phase separating efficiency of baffle type anaerobic biological reactor |
CN102079574A (en) * | 2011-02-28 | 2011-06-01 | 中国环境科学研究院 | High-efficiency acid-resistant anaerobic baffled reactor for treating high-concentration organic wastewater |
CN102161529A (en) * | 2011-02-22 | 2011-08-24 | 黑龙江省科学院科技孵化中心 | Anaerobic reciprocating baffling composite digesting device |
CN102531167A (en) * | 2012-02-08 | 2012-07-04 | 牟秀元 | Special diversion anaerobic baffled reactor |
CN102689984A (en) * | 2012-06-25 | 2012-09-26 | 上海理工大学 | Improved anaerobic baffle plate biological sewage treatment equipment |
CN102923851A (en) * | 2012-05-24 | 2013-02-13 | 深圳市启明环境技术有限公司 | Cross flow type anaerobic sludge bed reactor |
CN101774735B (en) * | 2010-01-19 | 2014-07-09 | 江苏金梓环境科技有限公司 | Vertical baffling multifunctional sewage biological treatment system |
CN107585859A (en) * | 2017-09-13 | 2018-01-16 | 长江大学 | Vertical cylindrical ABR reactors |
CN108689475A (en) * | 2018-07-02 | 2018-10-23 | 深圳清华大学研究院 | Fenton oxidation baffled reactor and method for processing organic wastewater |
-
2001
- 2001-06-08 CN CN01227609U patent/CN2484312Y/en not_active Expired - Fee Related
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100506721C (en) * | 2006-07-20 | 2009-07-01 | 清华大学 | Method and device for improving three phase separating efficiency of baffle type anaerobic biological reactor |
CN101774735B (en) * | 2010-01-19 | 2014-07-09 | 江苏金梓环境科技有限公司 | Vertical baffling multifunctional sewage biological treatment system |
CN102161529A (en) * | 2011-02-22 | 2011-08-24 | 黑龙江省科学院科技孵化中心 | Anaerobic reciprocating baffling composite digesting device |
CN102079574A (en) * | 2011-02-28 | 2011-06-01 | 中国环境科学研究院 | High-efficiency acid-resistant anaerobic baffled reactor for treating high-concentration organic wastewater |
CN102531167B (en) * | 2012-02-08 | 2013-06-26 | 牟秀元 | Special diversion anaerobic baffled reactor |
CN102531167A (en) * | 2012-02-08 | 2012-07-04 | 牟秀元 | Special diversion anaerobic baffled reactor |
CN102923851A (en) * | 2012-05-24 | 2013-02-13 | 深圳市启明环境技术有限公司 | Cross flow type anaerobic sludge bed reactor |
CN102689984A (en) * | 2012-06-25 | 2012-09-26 | 上海理工大学 | Improved anaerobic baffle plate biological sewage treatment equipment |
CN102689984B (en) * | 2012-06-25 | 2013-06-26 | 上海理工大学 | Improved anaerobic baffle plate biological sewage treatment equipment |
CN107585859A (en) * | 2017-09-13 | 2018-01-16 | 长江大学 | Vertical cylindrical ABR reactors |
CN107585859B (en) * | 2017-09-13 | 2020-12-01 | 长江大学 | Vertical cylindrical ABR reactor |
CN108689475A (en) * | 2018-07-02 | 2018-10-23 | 深圳清华大学研究院 | Fenton oxidation baffled reactor and method for processing organic wastewater |
CN108689475B (en) * | 2018-07-02 | 2021-02-02 | 深圳清华大学研究院 | Fenton oxidation baffled reactor and organic wastewater treatment method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100480197C (en) | Anaerobic inner circulating reflux type immobilization microorganism fluidized bed reactor | |
CN101691256B (en) | Tri-phase separator of anaerobic reactor | |
CN203866098U (en) | High-efficiency anaerobic and aerobic integrated reactor | |
CN101012084A (en) | Aerobic inner circulating reflux type immobilization microorganism fluidized bed reactor | |
CN2484312Y (en) | Tubelide anaerobic baffling reaction apparatus | |
CN110526395B (en) | Rotational flow anaerobic reactor for wastewater treatment system | |
CN101054234B (en) | Upflow type anaerobic reactor | |
US20150001145A1 (en) | Biofilter for wastewater digestion | |
CN201056518Y (en) | Three-phase separator of upflow type anaerobic reactor | |
CN210313698U (en) | Anaerobic reactor | |
CN102267757B (en) | Biomass three-phase separator device | |
CN105439279A (en) | Biological fluidized bed | |
CN2832804Y (en) | Composite sewage treatment equipment | |
CN201056519Y (en) | Three-phase separator of upflow type anaerobic reactor | |
CN216777998U (en) | Skid-mounted efficient mud-water separation equipment | |
CN111217446B (en) | High-efficient good oxygen biological fluidized bed reactor | |
CN100337938C (en) | Bioreactor for water treatment | |
CN202131146U (en) | Biomass three-phase separator device | |
CN112759201A (en) | Self-maintenance sewage treatment integrated equipment and sewage treatment method thereof | |
CN209081525U (en) | A kind of water-distributing device and anaerobic reactor | |
CN214936396U (en) | Anaerobic reactor | |
CN112777741A (en) | Tank type integrated sewage treatment equipment | |
CN114956324B (en) | Novel internal circulation plug flow anaerobic reactor | |
CN215249842U (en) | External MBR membrane upflow anaerobic reactor | |
CN210367144U (en) | Anaerobic reactor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |