CN2603804Y - Anaerobic reactor - Google Patents

Anaerobic reactor Download PDF

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Publication number
CN2603804Y
CN2603804Y CNU032155603U CN03215560U CN2603804Y CN 2603804 Y CN2603804 Y CN 2603804Y CN U032155603 U CNU032155603 U CN U032155603U CN 03215560 U CN03215560 U CN 03215560U CN 2603804 Y CN2603804 Y CN 2603804Y
Authority
CN
China
Prior art keywords
pipe
feed
tank
tank body
blow
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
Application number
CNU032155603U
Other languages
Chinese (zh)
Inventor
类延录
王吉辉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JINAN BENYUAN ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
Original Assignee
JINAN BENYUAN ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by JINAN BENYUAN ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd filed Critical JINAN BENYUAN ENVIRONMENTAL PROTECTION ENGINEERING Co Ltd
Priority to CNU032155603U priority Critical patent/CN2603804Y/en
Application granted granted Critical
Publication of CN2603804Y publication Critical patent/CN2603804Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

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  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

An anaerobic reactor belongs to wastewater treatment technology field. The reactor is mainly made up with a tank that includes a biogas pipe, a blow-down pipe, an anti-explosive port, a feed pipe, a feed distributor, a central pipe, a three-phase separator and a feed outlet. The anti-explosive port is arranged the top of outside tank, the blow-down pipe is extended outward on the bottom of the tank. A middle container and an inner container is arranged in the tank from outside to inner, the bottom of the middle container is fixed on the bottom of tank by a stent and the bottom of inner container is connected with the bottom of tank to fix. The top of the middle container and the inner container connects with each other and space exists between the top of containers and tank. The feed inlet is connected with the inner container by the feed distributor, the central pipe is fixed in the middle of the tank and is linked with the feed distributor, the blow-down pipe, the feed distributor and feed pipe respectively, the feed outlet is arranged on the lower part of the central pipe. The utility model can remove COD in wastewater at high percent and does not need external power, recycling operation, low-cost, steady performance, easy to operate and safe.

Description

A kind of anaerobic reactor
(1) technical field
The utility model belongs to technical field of waste water processing, particularly a kind of anaerobism reflecting device.
(2) background technology
Anaerobic reactor is the necessaries of anaerobism sewage disposal, and anaerobic reactor commonly used at present is a contact anaerobism reflecting device.The contact anaerobic reactor has stronger adaptability to potato alcohol, but shortcoming is: 1, additional power need be set promote circulation, equipment energy consumption is big, running cost is high; 2, the charging cross section is big, and pulse power is little; 3, because of reasons in structure, the suspended matter that dynamically ferments is difficult for precipitation, water outlet suspended matter concentration height, and the COD clearance in the waste water is low.
(3) summary of the invention
The utility model is at the deficiencies in the prior art, provides that a kind of charging cross section is little, pulse power big, high and do not need to be provided with additional power, internal-circulation type anaerobic reactor that circular flow is good to the COD clearance in the waste water.
The utility model is achieved through the following technical measures.
This reactor mainly is made up of tank body, tank body includes the biogas pipe, blow-off pipe, venting, feed-pipe, feed distributor, pipe core, triphase separator, discharge nozzle, wherein, venting is arranged on the upper end of tank body outside, blow-off pipe is drawn outside jar by tank base, it is characterized in that, courage and inner bag during ecto-entad is provided with in tank body, middle courage bottom is fixed by support and tank base, the lower end and the tank base of inner bag are connected and fixed, in courage communicate with the upper end of inner bag and and the tank body inner top between leave the space, a jar intravital feed-pipe is communicated with inner bag by feed distributor, the top that triphase separator is arranged on outside the middle courage is communicated with discharge nozzle.
In the middle of described pipe core was arranged in the tank body, its bottom was connected with tank base, and the bottom is communicated with blowdown divider and blow-off pipe respectively, the middle part is communicated with feed distributor and feed-pipe, the bottom is provided with discharge port, and open top is connected with the tank body top by bracing frame.
Middle courage bottom has through hole.
The utility model forms internal recycle by inner bag and middle courage are set with feed-pipe, feed distributor, pipe core, triphase separator and discharge nozzle, makes that reactor does not need the recycle system is set in addition, has saved working cost, and running cost reduces greatly; Integral reactor distribution cross section increases from inside to outside gradually, and flow velocity reduces gradually, helps the precipitation of suspended substance, has guaranteed microbial strains quantity and growth conditions, has improved the clearance of COD; Inner bag contains sectional area, and to account for the ratio of reactor total sectional area less, and the water inlet cross section is little, and pulse power is big, and dynamically water distribution is even, and microorganism and organism contact area are big, the waste water treatment efficiency height.Principle of work is as follows: waste water is pumped into feed-pipe, enter inner bag by feed distributor, when the inner bag feed liquid is full, just overflow in the middle courage, enter between middle courage and the cylindrical shell by middle courage bottom, through triphase separator suspended substance is separated the postprecipitation awl end again, gas delivery is to the tank top, and the water after the processing enters discharge nozzle, connect discharge port by pipe core, finished the internal recycle operation.Use the utlity model has that the charging cross section is little, pulse power is big, high and do not need to be provided with additional power to the COD clearance in the waste water, working cost is low, stable performance, advantage such as easy to operate, safe.
(4) description of drawings
Accompanying drawing is the utility model structural representation.
Wherein, 1, cone, 2, cylindrical shell, 3, feed-pipe, 4, feed distributor, 5, middle courage, 6, inner bag, 7, pipe core, 8, the biogas pipe, 9, triphase separator, 10, discharge nozzle, 11, end socket, 12, blowdown divider, 13, venting, 14, blow-off pipe, 15, collection chamber, 16, discharge port.
(5) embodiment
Embodiment: as shown in drawings, the potato alcohol production line of 20,000 tons of throughput, two 5000 cubic metres of volumetrical internal-circulation anaerobic reactors have been adopted, the cylindrical shell 2 of reactor is welded as a whole with cone 1 and end socket 11, constituted a tank body, feed-pipe 3 enters in the tank body and is connected with feed distributor 4, in courage 5 and inner bag 6 be provided with from outside to inside, inner bag 6 and middle courage 5 tops communicate, and and the tank body inner top between leave the space, form collection chamber 15, triphase separator 9 is installed in the top between cylindrical shell 2 and the middle courage 5, is communicated with discharge nozzle 10, and discharge nozzle 10 connects pipe core 7, the bottom of pipe core 7 is connected with tank base, the bottom is communicated with blowdown divider 12 and blow-off pipe 14 respectively, and the middle part is communicated with feed distributor 4 and feed-pipe 3, and the bottom is provided with discharge port 16, open top is connected with the tank body top by bracing frame; Biogas pipe 8 connects a jar intravital top collection chamber 15, at the outside end socket of tank body top venting 13 is set; The blow-off pipe 14 that is arranged on pot bottom is connected with blowdown divider 12.The waste water that with COD is 55000mg/l is squeezed into the bottom that jar intravital feed distributor 4 enters inner bag 6 by feed-pipe 3, waste water is courage 5 from the top of inner bag 6 enters, arrive the triphase separator 9 of cylindrical shell 2 internal upper parts by the through hole of middle courage bottom, enter discharge nozzle 10, discharge from discharge port 16 by pipe core 7, the liquid COD that discharges is 5000mg/l, clearance is 91%, improve 12% than contact anaerobic reactor with scale, saved be equipped with the 7.5KW motor follow two of environment protecting pumps, economize on electricity 28.8%.

Claims (3)

1, a kind of anaerobic reactor, mainly form by tank body, tank body includes the biogas pipe, blow-off pipe, venting, feed-pipe, feed distributor, pipe core, triphase separator, discharge nozzle, wherein, venting is arranged on the upper end of tank body outside, blow-off pipe is drawn outside jar by tank base, it is characterized in that, courage and inner bag during ecto-entad is provided with in tank body, middle courage bottom is fixed by support and tank base, the lower end and the tank base of inner bag are connected and fixed, in courage communicate with the upper end of inner bag and and the tank body inner top between leave the space, the intravital feed-pipe of jar is communicated with inner bag by feed distributor, and middle courage bottom has through hole, and the top in the courage outside was communicated with discharge nozzle during triphase separator was arranged on.
2, a kind of anaerobic reactor according to claim 1, it is characterized in that, in the middle of described pipe core is arranged in the tank body, its bottom is connected with tank base, the bottom is communicated with blowdown divider and blow-off pipe respectively, and the middle part is communicated with feed distributor and feed-pipe, and the bottom is provided with discharge port, open top is connected with the tank body top by bracing frame.
3, a kind of anaerobic reactor according to claim 1 is characterized in that, middle courage bottom has through hole.
CNU032155603U 2003-03-10 2003-03-10 Anaerobic reactor Expired - Fee Related CN2603804Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU032155603U CN2603804Y (en) 2003-03-10 2003-03-10 Anaerobic reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU032155603U CN2603804Y (en) 2003-03-10 2003-03-10 Anaerobic reactor

Publications (1)

Publication Number Publication Date
CN2603804Y true CN2603804Y (en) 2004-02-18

Family

ID=34160329

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU032155603U Expired - Fee Related CN2603804Y (en) 2003-03-10 2003-03-10 Anaerobic reactor

Country Status (1)

Country Link
CN (1) CN2603804Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101234826B (en) * 2007-08-29 2012-12-12 大冶有色金属公司 Sulfuration recovery processing method and device for high-acidity high-arsenic high-cadmium waste water
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
CN103833128A (en) * 2014-01-23 2014-06-04 陈际平 Vertical baffled acidify anaerobic digestor

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101234826B (en) * 2007-08-29 2012-12-12 大冶有色金属公司 Sulfuration recovery processing method and device for high-acidity high-arsenic high-cadmium waste water
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
CN103833128A (en) * 2014-01-23 2014-06-04 陈际平 Vertical baffled acidify anaerobic digestor

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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