CN105384250B - Novel anaerobic aerobic integratedization reactor - Google Patents

Novel anaerobic aerobic integratedization reactor Download PDF

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Publication number
CN105384250B
CN105384250B CN201510896017.4A CN201510896017A CN105384250B CN 105384250 B CN105384250 B CN 105384250B CN 201510896017 A CN201510896017 A CN 201510896017A CN 105384250 B CN105384250 B CN 105384250B
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aerobic
anaerobic
phase
reactor
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CN105384250A (en
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戚恺
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Suzhou Clear Industry Co Ltd
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Suzhou Clear Industry Co Ltd
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00Biological treatment of water, waste water, or sewage
    • C02F3/30Aerobic and anaerobic processes
    • C02F3/301Aerobic and anaerobic treatment in the same reactor
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2203/00Apparatus and plants for the biological treatment of water, waste water or sewage
    • C02F2203/006Apparatus and plants for the biological treatment of water, waste water or sewage details of construction, e.g. specially adapted seals, modules, connections

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  • Life Sciences & Earth Sciences (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biological Treatment Of Waste Water (AREA)

Abstract

The invention discloses Novel anaerobic aerobic integratedization reactors, including reactor body (1), the reactor body (1) includes the aerobic zone (11) being sequentially distributed from top to bottom and anaerobic zone (12), anaerobic zone (12) the lower part connection water inlet pipe (3), aerobic zone (11) the top connection outlet pipe (8), the anaerobic zone (12) is equipped with Sludge Bed (5), the lower section setting water distribution system (4) of the Sludge Bed (5), the water distribution system (4) is connected to the water inlet pipe (3), three-phase separating device (2) is equipped between the aerobic zone (11) and the anaerobic zone (12), the three-phase separating device (2) includes several three phase separators, the gas collecting tube (21) of the three phase separator is connected to gas chamber (6).Novel anaerobic aerobic integratedization reactor provided by the invention, which has a compact structure and a reasonable design, good sewage processing effect save sewage disposal investment.

Description

Novel anaerobic aerobic integratedization reactor
Technical field
The present invention relates to technical field of sewage, more particularly to a kind of Novel anaerobic aerobic integratedization reactor.
Background technology
The technique that anaerobic and aerobic are combined can greatly reduce operating cost by anaerobic pretreatment, and utilize Aerobic Process for Treatment Reach excellent effluent quality.
The technique that existing anaerobic and aerobic are combined use two individual processing units, generally front and rear arrangement, two Numerous connections such as pipeline, instrument are needed between a processing unit, are taken up a large area, especially for the sewage disposal economy of small flow Property is not high.
Invention content
It is an object of the present invention to provide a kind of Novel anaerobic aerobic integratedization reactor, which has a compact structure and a reasonable design, sewage High treating effect.
Based on the above problem, technical solution provided by the invention is:
Novel anaerobic aerobic integratedization reactor, including reactor body, the reactor body include from top to bottom according to The aerobic zone and anaerobic zone of secondary distribution, the anaerobic zone lower part connect water inlet pipe, and the aerobic zone top connects outlet pipe, described Anaerobic zone is equipped with Sludge Bed, the lower section setting water distribution system of the Sludge Bed, and the water distribution system is connected to the water inlet pipe, institute It states and three-phase separating device is equipped between aerobic zone and the anaerobic zone, the three-phase separating device includes several three phase separations Device, the gas collecting tube of the three phase separator is connected to gas chamber, through three phase separation after the anaerobic zone processing of the reacted device lower part of sewage Device realizes gas-liquid-solid three-phase separation, and wherein gas is delivered to gas chamber through gas collecting tube, and anaerobic zone water outlet enters reactor top Aerobic zone carries out Aerobic Process for Treatment, is discharged after Aerobic Process for Treatment by outlet pipe.
In one of which embodiment, the aerobic zone is equipped with aerobe turntable processing unit, the aerobe Turntable processing unit includes several biological rotating disks.
In one of which embodiment, the biological rotating disk include turntable and be arranged on the turntable several three Tie up filler module.
Compared with prior art, it is an advantage of the invention that:
1. traditional horizontally separated arrangement of aerobic-anaerobic is made into the cloth up and down of integral type by technical solution using the present invention It puts, it is compact-sized, reduce floor space, save sewage disposal input;
2. technical solution using the present invention, aerobic zone is arranged on anaerobic zone top, can effectively solve anaerobic reaction generation Stink overflows scattered the problem of influencing environment;
3. using the further technical solution of the present invention, aerobic biological rotating disk processing unit, Ke Yiyan are set in aerobic zone Long aerobic sludge retention time solves the adverse effect that carbon source is insufficient, aerobic sludge sludge age is short after anaerobism, can also avoid Oxygen area and the string mud of anaerobic zone.
Description of the drawings
In order to illustrate the technical solution of the embodiments of the present invention more clearly, required use in being described below to embodiment Attached drawing be briefly described, the accompanying drawings in the following description is only some embodiments of the present invention, for the common skill in this field For art personnel, without creative efforts, other attached drawings are can also be obtained according to these attached drawings.
Fig. 1 is the structure diagram of Novel anaerobic aerobic integratedization reactor embodiment of the present invention;
Wherein:
1st, reactor body;11st, aerobic zone;12nd, anaerobic zone;
2nd, three-phase separating device;21st, gas collecting tube;
3rd, water inlet pipe;
4th, water distribution system;
5th, Sludge Bed;
6th, gas chamber;
7th, aerobe turntable processing unit;
8th, outlet pipe.
Specific embodiment
Said program is described further below in conjunction with specific embodiment.It should be understood that these embodiments are for illustrating The present invention and be not limited to limit the scope of the invention.The implementation condition used in embodiment can be done according to the condition of specific producer Further adjustment, the implementation condition being not specified is usually the condition in routine experiment.
Referring to Fig. 1, it is the structure diagram of the embodiment of the present invention, a kind of Novel anaerobic aerobic integratedization reactor is provided, It includes reactor body 1, which includes the aerobic zone 11 being sequentially distributed from top to bottom and anaerobic zone 12, anaerobism 12 lower part of area connects water inlet pipe 3, and connection outlet pipe 8 in 11 top of aerobic zone is equipped with Sludge Bed 5, in Sludge Bed 5 in anaerobic zone 12 Lower section sets water distribution system 4, which is connected to water inlet pipe 3, three-phase separate is set between aerobic zone 11 and anaerobic zone 12 From device 2, three-phase separating device 2 includes several three phase separators, and the gas collecting tube 21 of three phase separator is connected to gas chamber 6.
Aerobic zone uses contact oxidation technology in this example, and aerobic biological rotating disk processing unit is preferably set in aerobic zone 11 7, which includes several biological rotating disks;Biological rotating disk includes turntable and is arranged on turntable Several three-dimensional filler modules, can be reduced using aerator using aerobe rotating-table apparatus 7, gas stripping is avoided to cause String mud problem.
The operation principle of the present invention:Sewage is entered the water distribution system 4 of 12 bottom of anaerobic zone by water inlet pipe 3, and sewage leads to upwards The process generation anaerobic reaction of the Sludge Bed 5 comprising granule sludge or floc sludge, waste water and mud granule contact is crossed, in anaerobism The biogas generated under state causes internal cycle, is attached on mud granule in some gases that sludge blanket is formed, attachment and The gas not adhered to rises to 12 top of anaerobic zone, rises to three-phase separating device 2, and attachment and the gas without adhering to are received Collect the gas collecting tube 21 of three phase separator, and then gas chamber 6 is delivered to by gas collecting tube 21, and through the processing water of three phase separator separation Aerobic Process for Treatment is carried out into aerobic zone 11, is discharged after the processing of aerobe turntable processing unit 7 by outlet pipe 8.
Such as 6m wide, 12m long, 10 meters of high integrated reactors of design handle water day for handling beer food sewage It measures as 1000m3/ d, COD 2000mg/l, BOD 1800mg/l, NH in water inlet3- N35mg/l, TN 50mg/l, go out after processing Water water quality reaches brewing industry pollutant emission standard (GB19821-2005).
The foregoing examples are merely illustrative of the technical concept and features of the invention, its object is to allow the person skilled in the art to be Present disclosure can be understood and implemented according to this, it is not intended to limit the scope of the present invention.It is all smart according to the present invention The equivalent transformation or modification that refreshing essence is done, should be covered by the protection scope of the present invention.

Claims (2)

1. Novel anaerobic aerobic integratedization reactor, including reactor body (1), it is characterised in that:The reactor body (1) Including the aerobic zone (11) being sequentially distributed from top to bottom and anaerobic zone (12), anaerobic zone (12) the lower part connection water inlet pipe (3), Aerobic zone (11) top connection outlet pipe (8), the anaerobic zone (12) is equipped with Sludge Bed (5), under the Sludge Bed (5) Side's setting water distribution system (4), the water distribution system (4) are connected to the water inlet pipe (3), the aerobic zone (11) and the anaerobism Three-phase separating device (2) is equipped between area (12), the three-phase separating device (2) includes several three phase separators, and described three The gas collecting tube (21) of phase separator is connected to gas chamber (6);
The aerobic zone (11) includes equipped with aerobe turntable processing unit (7), the aerobe turntable processing unit (7) Several biological rotating disks.
2. Novel anaerobic aerobic integratedization reactor according to claim 1, it is characterised in that:The biological rotating disk includes Turntable and several three-dimensional filler modules being arranged on the turntable.
CN201510896017.4A 2015-12-08 2015-12-08 Novel anaerobic aerobic integratedization reactor Active CN105384250B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510896017.4A CN105384250B (en) 2015-12-08 2015-12-08 Novel anaerobic aerobic integratedization reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510896017.4A CN105384250B (en) 2015-12-08 2015-12-08 Novel anaerobic aerobic integratedization reactor

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Publication Number Publication Date
CN105384250A CN105384250A (en) 2016-03-09
CN105384250B true CN105384250B (en) 2018-06-29

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113651433A (en) * 2021-09-07 2021-11-16 恒臻(无锡)生物科技有限公司 Leather wastewater treatment system and method

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4563281A (en) * 1984-07-09 1986-01-07 Syracuse University Anaerobic contactor
KR20010105549A (en) * 2000-05-16 2001-11-29 제성호 method for sewage disposal and arrangement therefor
PT2254842T (en) * 2008-01-28 2016-12-22 Biowater Tech As Method and device for the treatment of waste water
CN101570380A (en) * 2009-06-11 2009-11-04 德威华泰(北京)科技有限公司 Combined sewage treatment device
CN202226756U (en) * 2011-10-19 2012-05-23 东北石油大学 Enhanced treatment device for sludge digestion supernatant
CN103663850A (en) * 2012-09-14 2014-03-26 苏州克莱尔环保科技有限公司 Biological rotating disc integrated domestic sewage treatment equipment
CN104909448A (en) * 2014-03-12 2015-09-16 陈辅利 Biocarrier equipped biological rotating disc
CN204474409U (en) * 2015-01-29 2015-07-15 苏州科技学院 Rectilinear anaerobic aerobic integratedization reactor

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