CN106587537A - Integrated equipment for high-concentration wastewater treatment - Google Patents

Integrated equipment for high-concentration wastewater treatment Download PDF

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Publication number
CN106587537A
CN106587537A CN201710006121.0A CN201710006121A CN106587537A CN 106587537 A CN106587537 A CN 106587537A CN 201710006121 A CN201710006121 A CN 201710006121A CN 106587537 A CN106587537 A CN 106587537A
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China
Prior art keywords
pond
pipeline
aerobic
access port
electric control
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Granted
Application number
CN201710006121.0A
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Chinese (zh)
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CN106587537B (en
Inventor
廖勇强
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Guangdong Silu Environmental Protection Technology Co ltd
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Guangdong Silv Environmental Protection Engineering Co Ltd
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Priority to CN201710006121.0A priority Critical patent/CN106587537B/en
Publication of CN106587537A publication Critical patent/CN106587537A/en
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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
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/002Grey water, e.g. from clothes washers, showers or dishwashers
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/005Black water originating from toilets
    • 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)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Microbiology (AREA)
  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

Integrated equipment for high-concentration wastewater treatment comprises an integrated wastewater treatment box, wherein multiple wastewater treatment separation tanks are arranged in the integrated wastewater treatment box, a port which facilitates maintenance and can be covered for sealing is formed in the top of each wastewater treatment separation tank, the wastewater treatment separation tanks sequentially comprise an acid and base adjusting dosage separation tank, a first-stage anaerobic biochemical separation tank, a second-stage facultative biochemical separation tank and a third-stage aerobic biochemical separation tank from a front end wastewater inlet to a water outlet, the wastewater inlet is arranged at the bottom of the acid and base adjusting dosage separation tank, the water outlet is arranged at the upper part of the third-stage aerobic biochemical separation tank, and the wastewater treatment separation tanks are provided with a wastewater circulating pipeline system communicated with the wastewater treatment separation tanks. The equipment is compact in structure, occupies a small area, can adapt treatment of wastewater with different concentrations and is efficient, green and energy-saving in wastewater treatment.

Description

High concentration wastewater treatment integration apparatus
Technical field
The present invention relates to sewage treatment equipment technical field, particularly high concentration wastewater treatment integration apparatus.
Background technology
Sanitary sewage mainly includes two parts, and a part is the high strength domestic sewage of lavatory flushing feces, another part It is the water for kitchen use in addition to flushing supply, the sanitary sewage of the low concentration such as laundry and slurry.It is general by two parts at present Waste water is processed together, but has so undoubtedly increased the process load of processing system.Simultaneously as economy is developed rapidly, entirely Mankind's urbanization process is accelerated, and people's productive life is more concentrated, and part concentration zones do not set up centralized sewage disposal to set Apply, at present main centralized sewage treatment facility generally existing floor space is big, and operating cost is high.
The content of the invention
In order to overcome the disadvantages mentioned above of prior art, it is an object of the invention to provide a kind of compact conformation, floor space is little , it is suitable for variable concentrations wastewater treatment, the high concentration wastewater treatment integration apparatus of waste-water treatment efficient green energy conservation.
The technical solution adopted for the present invention to solve the technical problems is:
High concentration wastewater treatment integration apparatus, including integrated wastewater treatment integrated cabinet, wherein:Set in the integrated cabinet Several wastewater treatments are equipped with every pond, the wastewater treatment is both provided with easy access ground and can cover the passage of sealing every pond top Mouthful, the wastewater treatment is followed successively by soda acid from front end waste water inlet port to discharge outlet and reconciles plus connective pond, the life of one-level anaerobism every pond Change every pond, two grades of facultative anaerobic biochemicals every pond and three-level aerobic biochemical every pond, the soda acid reconciles plus connective bottom of pond portion is provided with into useless Water inlet port, three-level aerobic biochemical is provided with discharge outlet every pond top, and the wastewater treatment is provided with connection wastewater treatment every pond Every the waste water circulation tubing in pond, the one-level anaerobic biological every pond include main anaerobic biological every pond and secondary anaerobic biological every Pond, two grades of facultative anaerobic biochemicals every pond include main facultative anaerobic biochemical every pond and secondary facultative anaerobic biochemical every pond, the three-level aerobic biochemical every Pond includes main aerobic biochemical every pond and secondary aerobic biochemical every pond.
As a further improvement on the present invention:The soda acid reconciles plus the passway in connective pond is provided with chemicals dosing plant, institute State one-level anaerobic biological and anaerobe filler is provided with pond, two grades of facultative anaerobic biochemicals are provided with and oxygen life in pond Thing filler, the three-level aerobic biochemical is provided with aerobe filler in pond, and two grades of facultative anaerobic biochemicals are every pond and three-level Aerobic biochemical is both provided with aerator every bottom of pond portion, and the aerator is connected by pipeline with air pump.
As a further improvement on the present invention:The waste water circulation tubing includes several waste water circulation electric control pumps Body, the automatically controlled pump housing of the waste water circulation includes main electric control pump, main anaerobism electric control pump, and secondary anaerobism is intake electric control pump, secondary anaerobic effluent Electric control pump, secondary and oxygen water outlet electric control pump, the aerobic electric control pump of master, secondary aerobic water inlet electric control pump, secondary outputted aerobic water electric control pump, the master The water inlet of electric control pump accesses soda acid and reconciles plus connective pond by pipeline, and outlet accesses the of main anaerobism cross valve by pipeline One access port, the second access port of the main anaerobism cross valve accesses the water inlet of secondary anaerobism water inlet electric control pump by pipeline, the Three access ports access main and oxygen cross valve the first access port by pipeline, and the 4th access port accesses main anaerobic biological by pipeline Every pond, the outlet of the secondary anaerobism water inlet electric control pump passes through the first access port of pipeline auxiliary connection anaerobism three-way valve, the pair By pipeline auxiliary connection anaerobic effluent electric control pump, the 3rd access port accesses pair by pipeline to be detested second access port of anaerobism three-way valve Every pond, the outlet of the secondary anaerobic effluent electric control pump passes through the first access port of pipeline auxiliary connection and oxygen cross valve to oxygen biochemistry, Described secondary and oxygen cross valve the second access port accesses secondary and oxygen water outlet electric control pump water inlet by pipeline, and the 3rd access port leads to Piping accesses secondary aerobic water inlet electric control pump, and the 4th access port accesses secondary facultative anaerobic biochemical every pond by pipeline, and the secondary and oxygen goes out The outlet of water electric control pump is accessed the 3rd of the second access port of main simultaneous oxygen cross valve, the master and oxygen cross valve by pipeline and is connect Entrance accesses the water inlet of the aerobic electric control pump of master by pipeline, and the 4th access port accesses main facultative anaerobic biochemical every pond, institute by pipeline The outlet for stating the aerobic electric control pump of master accesses the first access port for leading aerobic three-way valve by pipeline, the aerobic three-way valve of the master Second access port accesses the outlet of secondary outputted aerobic water electric control pump by pipeline, and the 3rd access port accesses the aerobic life of master by pipeline Change every pond, the water inlet of the secondary outputted aerobic water electric control pump accesses the second access port of secondary aerobic three-way valve by pipeline, described First access port of secondary aerobic three-way valve accesses the outlet of secondary aerobic water inlet electrically-controlled valve by pipeline, and the 3rd access port is by pipe Road accesses secondary aerobic biochemical every pond, and the automatically controlled pump housing of waste water circulation is connected by control line with wastewater treatment cycle controller, described The water quality detection sensor of COD and BOD that each wastewater treatment is both provided with detecting waste strength every pond.
Compared with prior art, the invention has the beneficial effects as follows:Body of the present invention is arranged by several wastewater treatments every pond Change in wastewater treatment integrated cabinet one, compact conformation, floor space is little;Multi-stage biochemical is provided with every pond, by biologic packing material Evolution decomposition is carried out to poisonous and harmful substance in waste water, active mud evolution wastewater treatment is compared more efficient and green Energy-conservation;Simultaneously multi-stage biochemical is both provided with major and minor biochemistry every pond every pond, can be according to the waste water of variable concentrations, by controlling waste water The automatically controlled pump housing of circulation of cycle cooling plating drum so that pending waste water stream enters different major and minor biochemistry every pond so that the present invention High concentration wastewater treatment can not only be suitable for, low concentration wastewater process is also suitable, scope of application scope is wide, can be widely applied to waste water Green energy conservation process application.
Description of the drawings
Fig. 1 is the facade structures schematic diagram of the present invention;
Fig. 2 is the overlooking the structure diagram of the present invention.
Specific embodiment
In conjunction with description of the drawings, the present invention is further described with embodiment:
With reference to Fig. 1 and Fig. 2, high concentration wastewater treatment integration apparatus, including integrated wastewater treatment integrated cabinet 1, wherein:Institute State in integrated wastewater treatment integrated cabinet 1 and be provided with several wastewater treatments every pond, the wastewater treatment all sets every pond top Being equipped with easy access ground can cover the passway of sealing, and the wastewater treatment is every pond 11 from front end waste water inlet port 2 to discharge outlet 3 Be followed successively by soda acid reconcile plus connective pond 4, one-level anaerobic biological every 5, two grades of pond facultative anaerobic biochemical every pond 6 and three-level aerobic biochemical every pond 7, the soda acid reconciles plus the bottom of connective pond 4 is provided with into waste water inlet port 2, and three-level aerobic biochemical is provided with row every the top of pond 7 The mouth of a river 3, the wastewater treatment is provided with waste water circulation tubing of the connection wastewater treatment every pond, the one-level anaerobism life every pond Change every pond 5 including main anaerobic biological every pond 51 and secondary anaerobic biological every pond 52, two grades of facultative anaerobic biochemicals include main simultaneous oxygen every pond 6 Every pond 61 and secondary facultative anaerobic biochemical every pond 62, the three-level aerobic biochemical includes that main aerobic biochemical is good every pond 71 and pair to biochemistry every pond 7 Oxygen biochemistry is every pond 72.
The soda acid reconciles plus the passway in connective pond 4 is provided with chemicals dosing plant 8, and the one-level anaerobic biological is in pond 5 Anaerobe filler 9 is provided with, two grades of facultative anaerobic biochemicals are provided with and oxygen biologic packing material 10 in pond 6, the three-level Aerobic biochemical is provided with aerobe filler 11 in pond 4, and two grades of facultative anaerobic biochemicals are every pond 6 and three-level aerobic biochemical every pond 7 bottoms are both provided with aerator 12, and the aerator 12 is connected by pipeline with air pump 13.
The waste water circulation tubing includes the automatically controlled pump housing of several waste water circulations, the automatically controlled pump housing bag of the waste water circulation Include main electric control pump 14, main anaerobism electric control pump 15, secondary anaerobism water inlet electric control pump 16, secondary anaerobic effluent electric control pump 17, secondary and oxygen water outlet Electric control pump 18, the aerobic electric control pump 19 of master, secondary aerobic water inlet electric control pump 20, secondary outputted aerobic water electric control pump 21, the main electric control pump 14 Water inlet soda acid accessed by pipeline reconcile plus connective pond 4, outlet accesses the first of main anaerobism cross valve 22 by pipeline Access port, the second access port of the main anaerobism cross valve 22 accesses the water inlet of secondary anaerobism water inlet electric control pump 16 by pipeline, 3rd access port accesses main and oxygen cross valve 23 the first access port by pipeline, and the 4th access port accesses main anaerobism by pipeline Every pond 51, the outlet of the secondary anaerobism water inlet electric control pump 16 is accessed biochemistry by the first of pipeline auxiliary connection anaerobism three-way valve 24 Mouthful, by pipeline auxiliary connection anaerobic effluent electric control pump 17, the 3rd access port leads to the second access port of the secondary anaerobism three-way valve 24 Piping accesses secondary anaerobic biological every pond 52, and the outlet of the secondary anaerobic effluent electric control pump 17 is by pipeline auxiliary connection and oxygen four First access port of port valve 25, described secondary and oxygen cross valve 25 second access ports access secondary and oxygen water outlet electric control pump by pipeline 18 water inlet, the 3rd access port accesses secondary aerobic water inlet electric control pump 20 by pipeline, and the 4th access port is accessed secondary by pipeline Every pond 62, described secondary and oxygen water outlet electric control pump 18 outlet accesses main and oxygen cross valve 23 second to facultative anaerobic biochemical by pipeline The water inlet that 3rd access port of access port, the master and oxygen cross valve 23 passes through the aerobic electric control pump 19 of pipeline access master, the 4th Access port accesses main facultative anaerobic biochemical every pond 61 by pipeline, and the outlet of the aerobic electric control pump 19 of the master is accessed by pipeline to be led First access port of oxygen three-way valve 26, the second access port of the aerobic three-way valve 26 of the master accesses secondary outputted aerobic water electricity by pipeline The outlet of control pump 21, the 3rd access port accesses main aerobic biochemical every pond 71 by pipeline, the secondary outputted aerobic water electric control pump 21 Water inlet the second access port of secondary aerobic three-way valve 27, the first access port of the secondary aerobic three-way valve 27 are accessed by pipeline The outlet of secondary aerobic water inlet electrically-controlled valve 20 is accessed by pipeline, the 3rd access port accesses secondary aerobic biochemical every pond by pipeline 72, the automatically controlled pump housing of waste water circulation is connected by control line with wastewater treatment cycle controller, and described each wastewater treatment is every pond It is provided with the water quality detection sensor of the COD and BOD of detection waste strength.
Operation principle of the present invention:
By soda acid reconcile plus connective pond chemicals dosing plant adjust waste water pH value so that its pH value can adapt to subsequent biochemical every Biologic packing material growing environment demand in pond, while by soda acid mediation plus the water quality detection sensor in connective pond, detection band COD the and BOD values of waste strength are processed, and different waste water circulation processing modes are carried out for variable concentrations waste water.
When high-concentration waste water is processed, the automatically controlled pump housing of waste water circulation is controlled by wastewater treatment cycle controller so that high Concentration waste water successively Jing circulating lines flow through main anaerobiosiss every pond, secondary anaerobic biological every pond, secondary facultative anaerobic biochemical every pond, master and oxygen Biochemistry is every pond, main aerobic biochemical every pond and secondary aerobic biochemical every pond, the discharge outlet pipeline for finally arranging every pond from secondary aerobic biochemical Flow out, high-concentration waste water is after the multistage major and minor biochemical biologic packing material in pond carries out purification decomposition, and it is net that discharge outlet flows out Change water energy and enough reach recycle-water or industrial discharge water quality standard, meet general high-concentration waste Water warfare requirement.
When low concentration wastewater is processed, the automatically controlled pump housing of waste water circulation is controlled by wastewater treatment cycle controller so that low Concentration waste water successively Jing circulating lines flow through main anaerobiosiss every pond, main facultative anaerobic biochemical every pond and main aerobic biochemical every pond, finally The discharge outlet pipeline that the main aerobic biochemicals of Jing are arranged every pond flows out, due to low concentration wastewater COD and BOD value it is relatively low, without the need for Jing It is secondary biochemical every pond process, it becomes possible to reach recycle-water or industrial discharge water quality standard, process waste water faster, efficiency high.
In sum, one of ordinary skill in the art is read after file of the present invention, technology according to the present invention scheme with Technology design makes other various corresponding conversion schemes without the need for creative mental work, belongs to the model that the present invention is protected Enclose.

Claims (3)

1. high concentration wastewater treatment integration apparatus, including integrated wastewater treatment integrated cabinet, it is characterised in that:It is described integrated Several wastewater treatments are provided with casing every pond, the wastewater treatment can cover close with being both provided with easy access every pond top The passway of envelope, the wastewater treatment every pond be followed successively by from front end waste water inlet port to discharge outlet soda acid reconcile plus connective pond, one Level anaerobic biological every pond, two grades of facultative anaerobic biochemicals every pond and three-level aerobic biochemical every pond, the soda acid reconciles plus connective bottom of pond portion sets It is equipped with into waste water inlet port, three-level aerobic biochemical is provided with discharge outlet every pond top, and the wastewater treatment is provided with connection every pond , every the waste water circulation tubing in pond, the one-level anaerobic biological is every pond including main anaerobic biological every pond and secondary anaerobism for wastewater treatment Biochemistry every pond, two grades of facultative anaerobic biochemicals every pond include main facultative anaerobic biochemical every pond and secondary facultative anaerobic biochemical every pond, the three-level is aerobic It is biochemical to include main aerobic biochemical every pond and secondary aerobic biochemical every pond every pond.
2. high concentration wastewater treatment integration apparatus according to claim 1, it is characterised in that:The soda acid mediation dosing The passway in pond is provided with chemicals dosing plant, the one-level anaerobic biological is provided with anaerobe filler in pond, described two Level facultative anaerobic biochemical is provided with and oxygen biologic packing material in pond, and the three-level aerobic biochemical is provided with aerobe in pond and fills out Material, two grades of facultative anaerobic biochemicals are both provided with aerator every pond and three-level aerobic biochemical every bottom of pond portion, and the aerator leads to Piping is connected with air pump.
3. high concentration wastewater treatment integration apparatus according to claim 1, it is characterised in that:The waste water circulation pipeline System includes the automatically controlled pump housing of several waste water circulations, and the automatically controlled pump housing of the waste water circulation includes main electric control pump, main anaerobism electric control pump, Secondary anaerobism is intake electric control pump, secondary anaerobic effluent electric control pump, secondary and oxygen water outlet electric control pump, the aerobic electric control pump of master, it is secondary it is aerobic enter water power Control pump, secondary outputted aerobic water electric control pump, the water inlet of the main electric control pump accesses soda acid and reconciles plus connective pond by pipeline, outlet First access port of main anaerobism cross valve is accessed by pipeline, the second access port of the main anaerobism cross valve is accessed by pipeline Secondary anaerobism is intake the water inlet of electric control pump, and the 3rd access port accesses the first access port of main simultaneous oxygen cross valve by pipeline, and the 4th Access port accesses main anaerobic biological every pond by pipeline, and the outlet of the secondary anaerobism water inlet electric control pump is detested by pipeline auxiliary connection First access port of oxygen three-way valve, the second access port of the secondary anaerobism three-way valve is automatically controlled by pipeline auxiliary connection anaerobic effluent Pump, the 3rd access port accesses secondary anaerobic biological every pond by pipeline, and the outlet of the secondary anaerobic effluent electric control pump passes through pipeline First access port of auxiliary connection and oxygen cross valve, described secondary and oxygen cross valve the second access port accesses secondary and oxygen and goes out by pipeline The water inlet of water electric control pump, the 3rd access port accesses secondary aerobic water inlet electric control pump by pipeline, and the 4th access port is connect by pipeline Enter secondary facultative anaerobic biochemical every pond, described secondary and oxygen water outlet electric control pump outlet connects by the second of the main simultaneous oxygen cross valve of pipeline access 3rd access port of entrance, the master and oxygen cross valve accesses the water inlet of the aerobic electric control pump of master, the 4th access port by pipeline Main facultative anaerobic biochemical is accessed every pond by pipeline, the outlet of the aerobic electric control pump of the master accesses the aerobic three-way valve of master by pipeline First access port, the second access port of the aerobic three-way valve of the master passes through the outlet that pipeline accesses secondary outputted aerobic water electric control pump, 3rd access port accesses main aerobic biochemical every pond by pipeline, and the water inlet of the secondary outputted aerobic water electric control pump is accessed by pipeline Second access port of secondary aerobic three-way valve, the first access port of the secondary aerobic three-way valve by pipeline access pair it is aerobic enter water power The outlet of control valve, the 3rd access port accesses secondary aerobic biochemical every pond by pipeline, and the automatically controlled pump housing of waste water circulation passes through control line It is connected with wastewater treatment cycle controller, described each wastewater treatment is both provided with detecting the COD and BOD of waste strength every pond Water quality detection sensor.
CN201710006121.0A 2017-01-05 2017-01-05 High-concentration wastewater treatment integrated equipment Active CN106587537B (en)

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Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1093343A (en) * 1994-03-17 1994-10-12 孙乔良 Automatic and quick wastewater purification system by biological method
JP2002011495A (en) * 2000-06-29 2002-01-15 Nippon Steel Corp Method for removing nitrogen and phosphor from wastewater
CN2680657Y (en) * 2004-02-26 2005-02-23 北京碧海行动投资有限公司 Waste water treatment system integrating modular optimization technologies
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CN203360117U (en) * 2013-07-17 2013-12-25 郑州大学 Multipoint inflowing circulation A/O sewage treatment system
CN103588352A (en) * 2013-09-03 2014-02-19 北京工业大学 Two-stage backflow simultaneous nitrogen and phosphorus removal device and technology for denitrification phosphorus removal, shortcut nitrification and anaerobic ammonia oxidation of municipal sewage
CN103787555A (en) * 2013-01-25 2014-05-14 浙江商达环保有限公司 Intelligent rural sewage integrated treatment method
CN103964573A (en) * 2014-01-09 2014-08-06 上海理工大学 Ceramic bioreactor and sewage treatment method thereof
CN203938563U (en) * 2014-05-29 2014-11-12 凯天环保科技股份有限公司 A kind of microkinetic integrated sewage treating apparatus
CN204111420U (en) * 2014-10-16 2015-01-21 武汉都市环保工程技术股份有限公司 Multipoint water feeding improvement sequencing batch activated sludge system
CN104355408A (en) * 2014-11-11 2015-02-18 玉溪师范学院 A2O (anaeroxic-anoxic-oxic) sewage treatment device and A2O sewage treatment method
CN104402184A (en) * 2014-11-28 2015-03-11 宁波圆周率环境科技有限公司 Multi-stage oxidization treatment technology for sludge
CN105060489A (en) * 2015-09-10 2015-11-18 天津泰达新水源科技开发有限公司 A2O (Anaerobic-Anoxic-Oxic) system of denitrification and dephosphorization for sewage treatment
CN106007258A (en) * 2016-07-29 2016-10-12 东南大学 Six-box integrated two-sludge denitrifying phosphorus removal system and technology

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1093343A (en) * 1994-03-17 1994-10-12 孙乔良 Automatic and quick wastewater purification system by biological method
JP2002011495A (en) * 2000-06-29 2002-01-15 Nippon Steel Corp Method for removing nitrogen and phosphor from wastewater
CN2680657Y (en) * 2004-02-26 2005-02-23 北京碧海行动投资有限公司 Waste water treatment system integrating modular optimization technologies
CN102583912A (en) * 2012-03-30 2012-07-18 陈宏� Technology and system for treating roasted eel industrial sewage
CN103787555A (en) * 2013-01-25 2014-05-14 浙江商达环保有限公司 Intelligent rural sewage integrated treatment method
CN203360117U (en) * 2013-07-17 2013-12-25 郑州大学 Multipoint inflowing circulation A/O sewage treatment system
CN103408143A (en) * 2013-08-26 2013-11-27 盐城工学院 Sub-grid adjustable anaerobic-anoxic-aerobic biochemical reactor
CN103588352A (en) * 2013-09-03 2014-02-19 北京工业大学 Two-stage backflow simultaneous nitrogen and phosphorus removal device and technology for denitrification phosphorus removal, shortcut nitrification and anaerobic ammonia oxidation of municipal sewage
CN103964573A (en) * 2014-01-09 2014-08-06 上海理工大学 Ceramic bioreactor and sewage treatment method thereof
CN203938563U (en) * 2014-05-29 2014-11-12 凯天环保科技股份有限公司 A kind of microkinetic integrated sewage treating apparatus
CN204111420U (en) * 2014-10-16 2015-01-21 武汉都市环保工程技术股份有限公司 Multipoint water feeding improvement sequencing batch activated sludge system
CN104355408A (en) * 2014-11-11 2015-02-18 玉溪师范学院 A2O (anaeroxic-anoxic-oxic) sewage treatment device and A2O sewage treatment method
CN104402184A (en) * 2014-11-28 2015-03-11 宁波圆周率环境科技有限公司 Multi-stage oxidization treatment technology for sludge
CN105060489A (en) * 2015-09-10 2015-11-18 天津泰达新水源科技开发有限公司 A2O (Anaerobic-Anoxic-Oxic) system of denitrification and dephosphorization for sewage treatment
CN106007258A (en) * 2016-07-29 2016-10-12 东南大学 Six-box integrated two-sludge denitrifying phosphorus removal system and technology

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Address after: 510000 unit 210, No. 22, Yinli street, shatai Road, Tianhe District, Guangzhou, Guangdong Province (office only) (not for plant use)

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Address before: Room 412, No. 28, Yinli Street, Tianhe District, Guangzhou City, Guangdong Province, 510000

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Denomination of invention: High-concentration wastewater treatment integrated equipment

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