CN104891738A - Ecological treatment method of municipal sewage - Google Patents

Ecological treatment method of municipal sewage Download PDF

Info

Publication number
CN104891738A
CN104891738A CN201510275447.4A CN201510275447A CN104891738A CN 104891738 A CN104891738 A CN 104891738A CN 201510275447 A CN201510275447 A CN 201510275447A CN 104891738 A CN104891738 A CN 104891738A
Authority
CN
China
Prior art keywords
aeration
sewage
zones
water
tank
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.)
Granted
Application number
CN201510275447.4A
Other languages
Chinese (zh)
Other versions
CN104891738B (en
Inventor
黄平娜
王荣辉
邓竹
叶选荣
张群新
赖苑玉
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.)
Guangdong Meiyan Jixiang Hydropower Co Ltd
Original Assignee
Guangdong Meiyan Jixiang Hydropower 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 Guangdong Meiyan Jixiang Hydropower Co Ltd filed Critical Guangdong Meiyan Jixiang Hydropower Co Ltd
Priority to CN201510275447.4A priority Critical patent/CN104891738B/en
Publication of CN104891738A publication Critical patent/CN104891738A/en
Application granted granted Critical
Publication of CN104891738B publication Critical patent/CN104891738B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention discloses an ecological treatment method of municipal sewage, which comprises the following steps: pretreating municipal sewage, filtering the municipal sewage, carrying out biological treatment on the municipal sewage, and sending the municipal sewage into an aeration tank to perform aeration reaction. In the municipal sewage pretreatment process, when the sewage passes through the grid, large impurities are removed; the sewage is enhanced by a water inlet pump station to enter an aeration-desilting-oil removal tank, thereby removing sand and floating oil in the sewage; and in the municipal sewage biological treatment process, return sludge and the filtered sewage are sufficiently mixed in a 4-6m-deep ecological treatment tank, the activated sludge adsorbs the pollutants within 3-5 minutes, and the phosphorus-accumulating bacterium releases phosphorus, thereby performing biological dephosphorization. The method can implement intermitted aeration; two adjacent branch air pipelines of the second aeration zone and third aeration zone are alternated every two days, and thus, the method has the characteristic of intermitted aeration; and the method can save the electric power, enhances the anaerobic dephosphorization effect, reduces the investment, and has the advantages of land saving and low operating cost.

Description

A kind of ecological treatment method of municipal effluent
Technical field
The present invention relates to field of environment engineering, specifically a kind of ecological treatment method of municipal effluent.
Background technology
Along with environmental pollution is on the rise, more strict to the requirement of sewage discharge water quality, the process of current municipal effluent is mainly based on biological treatment.Due to the shortage of water resources, the development of recycling to city of municipal effluent has profound significance.Sewage treatment process conventional both at home and abroad at present has A 2/ O, oxidation ditch process, SBR method and WWRR method.A 2/ O (anoxic-anaerobic-aerobic) utilizes the biology propagation activity of active sludge in anaerobism, anoxic, aerobic processes, the while of organic in degradation of sewage, reach denitrification dephosphorization function, become sewage recycling and the important measures preventing body eutrophication at present.This technology is promoted rapidly abroad, and domestic have also been obtained uses quite widely.The oxidation ditch process of preposition anaerobic pond has the depth of water more shallow, and surface aerating machine oxygenation power consumption is large, and water temperature is scattered and disappeared fast shortcoming, and treatment scale is larger, and these shortcomings are more outstanding, the middle or small sewage treatment of main applicable south China.SBR method collects homogenizing, just heavy, biological degradation, the function such as heavy is in a pond eventually, and sewage intermittent type enters in pond, is purified under the effect of active sludge, and after precipitate and separate, supernatant liquor drains outside pond.This technique is mainly applicable to middle-size and small-size sewage treatment project, but this processing requirement automatization level is higher, and its lness ratio of plant is high, and installed capacity is larger; And this technique uses the multiple blower fan of multiple Ventilator Room to the oxygen supply of ecological wastewater processing pond, be not easy to operational management, power consumption in operational process can be made too high, and on aerator decoration form, in ecological wastewater processing pond, an aeration zone aerator number arranges that too much power consumption is high.
Existing Sewage treatment systems also exists that complicated operation, running cost are high, the problem of poor processing effect, and apparatus and process is complicated, and to the COD in water, the index removal effects such as BOD, SS are also undesirable.Current water treatment worker, in the urgent need to providing a kind of enhanced sewage treatment process and equipment to solve in sewage disposal, water quality situation instability, poor processing effect, complex process, the problem that running cost is high.
Summary of the invention
The object of the present invention is to provide the ecological treatment method of the municipal effluent that a kind of less investment, running cost are low, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the invention provides following technical scheme:
An ecological treatment method for municipal effluent, concrete steps are as follows:
(1) municipal effluent pre-treatment: when sewage is by grid, removes bulk foreign material, enters sediment by aeration grease removal tank, remove the sand in sewage and oil slick after water inlet pumping plant promotes;
(2) municipal effluent filtration treatment: pretreated sewage is extracted into reaction water tank, carry out dosing reaction 10-12h, according to water quality requirement, add medicament, medicine is mixed completely with sewage, by reacted sewage suction settling tank precipitation 20-24h, oettIed sewage flows in strumbox and filters, with vacuum primingpump suction filtration water below filtering layer, under suction function, forced filtration water filters through filtering layer;
(3) municipal effluent biological treatment: returned sluge and the sewage after filtering are fully mixed in the ecological treatment ponds of 4-6m in the degree of depth, and pollutent adsorbs by active sludge in 3-5min, polyP bacteria release phosphorus, carries out biological phosphate-eliminating;
(4) municipal effluent enters aeration tank: the sewage after biological phosphate-eliminating is promoted the bottom delivering to an aeration zone by submersible sewage pump, before entering an aeration zone, be provided with measuring apparatus measure the discharge of sewage, the end of sewage an aeration zone enters No. two aeration zones by rubber plate training wall overflow water outlet, then flows automatically to No. three aeration zones by No. two aeration zones;
(5) municipal effluent aerated reaction: in aeration tank, sewage enters in the anaerobic layer of an aeration zone by the bottom of ecological treatment ponds, anerobe eliminates dirty Organic substance in water, by the aerator aeration of an aeration zone, sewage is fully mixed with the active sludge above anaerobic layer, and carry out oxygenation, aerobic bacteria in mud decomposes and absorbs dirty Organic substance in water, base sludge is under anaerobic state, the metabolism with microorganism is cleared up through anerobe, progressively stabilization, water outlet again successively behind No. two aeration zones and the process of No. three aeration zones eventually through training wall overflow to exhalant region, add after disinfectant processes further in exhalant region and collect outlet sump by pipeline, in outlet sump, adding Dephosphorization reagent carrying out dephosphorization process further to reaching sewage drainage standard.
As the present invention's further scheme: described aeration tank is divided into an aeration zone, No. two aeration zones and No. three aeration zones, the aerator interval 4-6m of a described aeration zone, two groups of branch wind pipe track pitch 8-10m; The aerator interval 8-10m of No. two aeration zones, two groups of branch wind pipe track pitch 15-20m; The aerator interval 10-15m of No. three aeration zones, two groups of branch wind pipe track pitch 20-30m.
Compared with prior art, the invention has the beneficial effects as follows:
The present invention can realize intermittent aeration, and No. two aeration zones and the rotation in every two days of adjacent twice branch wind pipe road, No. three aeration zones once, have intermittent aeration feature, can saves energy, in turn enhance the effect of anaerobism dephosphorization, decrease investment, take up an area province, running cost is low.
Embodiment
Be described in more detail below in conjunction with the technical scheme of embodiment to this patent.
Embodiment 1
An ecological treatment method for municipal effluent, concrete steps are as follows:
(1) municipal effluent pre-treatment: when sewage is by grid, removes bulk foreign material, enters sediment by aeration grease removal tank, remove the sand in sewage and oil slick after water inlet pumping plant promotes;
(2) municipal effluent filtration treatment: pretreated sewage is extracted into reaction water tank, carry out dosing reaction 10h, according to water quality requirement, add medicament, medicine is mixed completely with sewage, by reacted sewage suction settling tank precipitation 20h, oettIed sewage flows in strumbox and filters, with vacuum primingpump suction filtration water below filtering layer, under suction function, forced filtration water filters through filtering layer;
(3) municipal effluent biological treatment: returned sluge and the sewage after filtering are fully mixed in the ecological treatment ponds of 4m in the degree of depth, and pollutent adsorbs by active sludge in 3min, polyP bacteria release phosphorus, carries out biological phosphate-eliminating;
(4) municipal effluent enters aeration tank: aeration tank is divided into an aeration zone, No. two aeration zones and No. three aeration zones, the aerator interval 4m of a described aeration zone, two groups of branch wind pipe track pitch 8m; The aerator interval 8m of No. two aeration zones, two groups of branch wind pipe track pitch 15m; The aerator interval 10m of No. three aeration zones, two groups of branch wind pipe track pitch 20m; Sewage after biological phosphate-eliminating is promoted the bottom delivering to an aeration zone by submersible sewage pump, before entering an aeration zone, be provided with measuring apparatus measure the discharge of sewage, the end of sewage an aeration zone enters No. two aeration zones by rubber plate training wall overflow water outlet, then flows automatically to No. three aeration zones by No. two aeration zones;
(5) municipal effluent aerated reaction: in aeration tank, sewage enters in the anaerobic layer of an aeration zone by the bottom of ecological treatment ponds, anerobe eliminates dirty Organic substance in water, by the aerator aeration of an aeration zone, sewage is fully mixed with the active sludge above anaerobic layer, and carry out oxygenation, aerobic bacteria in mud decomposes and absorbs dirty Organic substance in water, base sludge is under anaerobic state, the metabolism with microorganism is cleared up through anerobe, progressively stabilization, water outlet again successively behind No. two aeration zones and the process of No. three aeration zones eventually through training wall overflow to exhalant region, add after disinfectant processes further in exhalant region and collect outlet sump by pipeline, in outlet sump, adding Dephosphorization reagent carrying out dephosphorization process further to reaching sewage drainage standard.
Embodiment 2
An ecological treatment method for municipal effluent, concrete steps are as follows:
(1) municipal effluent pre-treatment: when sewage is by grid, removes bulk foreign material, enters sediment by aeration grease removal tank, remove the sand in sewage and oil slick after water inlet pumping plant promotes;
(2) municipal effluent filtration treatment: pretreated sewage is extracted into reaction water tank, carry out dosing reaction 11h, according to water quality requirement, add medicament, medicine is mixed completely with sewage, by reacted sewage suction settling tank precipitation 22h, oettIed sewage flows in strumbox and filters, with vacuum primingpump suction filtration water below filtering layer, under suction function, forced filtration water filters through filtering layer;
(3) municipal effluent biological treatment: returned sluge and the sewage after filtering are fully mixed in the ecological treatment ponds of 5m in the degree of depth, and pollutent adsorbs by active sludge in 4min, polyP bacteria release phosphorus, carries out biological phosphate-eliminating;
(4) municipal effluent enters aeration tank: aeration tank is divided into an aeration zone, No. two aeration zones and No. three aeration zones, the aerator interval 5m of a described aeration zone, two groups of branch wind pipe track pitch 9m; The aerator interval 9m of No. two aeration zones, two groups of branch wind pipe track pitch 18m; The aerator interval 12m of No. three aeration zones, two groups of branch wind pipe track pitch 25m; Sewage after biological phosphate-eliminating is promoted the bottom delivering to an aeration zone by submersible sewage pump, before entering an aeration zone, be provided with measuring apparatus measure the discharge of sewage, the end of sewage an aeration zone enters No. two aeration zones by rubber plate training wall overflow water outlet, then flows automatically to No. three aeration zones by No. two aeration zones;
(5) municipal effluent aerated reaction: in aeration tank, sewage enters in the anaerobic layer of an aeration zone by the bottom of ecological treatment ponds, anerobe eliminates dirty Organic substance in water, by the aerator aeration of an aeration zone, sewage is fully mixed with the active sludge above anaerobic layer, and carry out oxygenation, aerobic bacteria in mud decomposes and absorbs dirty Organic substance in water, base sludge is under anaerobic state, the metabolism with microorganism is cleared up through anerobe, progressively stabilization, water outlet again successively behind No. two aeration zones and the process of No. three aeration zones eventually through training wall overflow to exhalant region, add after disinfectant processes further in exhalant region and collect outlet sump by pipeline, in outlet sump, adding Dephosphorization reagent carrying out dephosphorization process further to reaching sewage drainage standard.
Embodiment 3
An ecological treatment method for municipal effluent, concrete steps are as follows:
(1) municipal effluent pre-treatment: when sewage is by grid, removes bulk foreign material, enters sediment by aeration grease removal tank, remove the sand in sewage and oil slick after water inlet pumping plant promotes;
(2) municipal effluent filtration treatment: pretreated sewage is extracted into reaction water tank, carry out dosing reaction 12h, according to water quality requirement, add medicament, medicine is mixed completely with sewage, by reacted sewage suction settling tank precipitation 24h, oettIed sewage flows in strumbox and filters, with vacuum primingpump suction filtration water below filtering layer, under suction function, forced filtration water filters through filtering layer;
(3) municipal effluent biological treatment: returned sluge and the sewage after filtering are fully mixed in the ecological treatment ponds of 6m in the degree of depth, and pollutent adsorbs by active sludge in 5min, polyP bacteria release phosphorus, carries out biological phosphate-eliminating;
(4) municipal effluent enters aeration tank: aeration tank is divided into an aeration zone, No. two aeration zones and No. three aeration zones, the aerator interval 6m of a described aeration zone, two groups of branch wind pipe track pitch 10m; The aerator interval 10m of No. two aeration zones, two groups of branch wind pipe track pitch 20m; The aerator interval 15m of No. three aeration zones, two groups of branch wind pipe track pitch 30m; Sewage after biological phosphate-eliminating is promoted the bottom delivering to an aeration zone by submersible sewage pump, before entering an aeration zone, be provided with measuring apparatus measure the discharge of sewage, the end of sewage an aeration zone enters No. two aeration zones by rubber plate training wall overflow water outlet, then flows automatically to No. three aeration zones by No. two aeration zones;
(5) municipal effluent aerated reaction: in aeration tank, sewage enters in the anaerobic layer of an aeration zone by the bottom of ecological treatment ponds, anerobe eliminates dirty Organic substance in water, by the aerator aeration of an aeration zone, sewage is fully mixed with the active sludge above anaerobic layer, and carry out oxygenation, aerobic bacteria in mud decomposes and absorbs dirty Organic substance in water, base sludge is under anaerobic state, the metabolism with microorganism is cleared up through anerobe, progressively stabilization, water outlet again successively behind No. two aeration zones and the process of No. three aeration zones eventually through training wall overflow to exhalant region, add after disinfectant processes further in exhalant region and collect outlet sump by pipeline, in outlet sump, adding Dephosphorization reagent carrying out dephosphorization process further to reaching sewage drainage standard.
The present invention can realize intermittent aeration, and No. two aeration zones and the rotation in every two days of adjacent twice branch wind pipe road, No. three aeration zones once, have intermittent aeration feature, can saves energy, in turn enhance the effect of anaerobism dephosphorization, decrease investment, take up an area province, running cost is low.
Above the better embodiment of this patent is explained in detail, but this patent is not limited to above-mentioned embodiment, in the ken that one skilled in the relevant art possesses, various change can also be made under the prerequisite not departing from this patent aim.

Claims (2)

1. an ecological treatment method for municipal effluent, is characterized in that, concrete steps are as follows:
(1) municipal effluent pre-treatment: when sewage is by grid, removes bulk foreign material, enters sediment by aeration grease removal tank, remove the sand in sewage and oil slick after water inlet pumping plant promotes;
(2) municipal effluent filtration treatment: pretreated sewage is extracted into reaction water tank, carry out dosing reaction 10-12h, according to water quality requirement, add medicament, medicine is mixed completely with sewage, by reacted sewage suction settling tank precipitation 20-24h, oettIed sewage flows in strumbox and filters, with vacuum primingpump suction filtration water below filtering layer, under suction function, forced filtration water filters through filtering layer;
(3) municipal effluent biological treatment: returned sluge and the sewage after filtering are fully mixed in the ecological treatment ponds of 4-6m in the degree of depth, and pollutent adsorbs by active sludge in 3-5min, polyP bacteria release phosphorus, carries out biological phosphate-eliminating;
(4) municipal effluent enters aeration tank: the sewage after biological phosphate-eliminating is promoted the bottom delivering to an aeration zone by submersible sewage pump, before entering an aeration zone, be provided with measuring apparatus measure the discharge of sewage, the end of sewage an aeration zone enters No. two aeration zones by rubber plate training wall overflow water outlet, then flows automatically to No. three aeration zones by No. two aeration zones;
(5) municipal effluent aerated reaction: in aeration tank, sewage enters in the anaerobic layer of an aeration zone by the bottom of ecological treatment ponds, anerobe eliminates dirty Organic substance in water, by the aerator aeration of an aeration zone, sewage is fully mixed with the active sludge above anaerobic layer, and carry out oxygenation, aerobic bacteria in mud decomposes and absorbs dirty Organic substance in water, base sludge is under anaerobic state, the metabolism with microorganism is cleared up through anerobe, progressively stabilization, water outlet again successively behind No. two aeration zones and the process of No. three aeration zones eventually through training wall overflow to exhalant region, add after disinfectant processes further in exhalant region and collect outlet sump by pipeline, in outlet sump, adding Dephosphorization reagent carrying out dephosphorization process further to reaching sewage drainage standard.
2. the ecological treatment method of municipal effluent according to claim 1, it is characterized in that, described aeration tank is divided into an aeration zone, No. two aeration zones and No. three aeration zones, the aerator interval 4-6m of a described aeration zone, two groups of branch wind pipe track pitch 8-10m; The aerator interval 8-10m of No. two aeration zones, two groups of branch wind pipe track pitch 15-20m; The aerator interval 10-15m of No. three aeration zones, two groups of branch wind pipe track pitch 20-30m.
CN201510275447.4A 2015-05-27 2015-05-27 A kind of ecological treatment method of municipal sewage Expired - Fee Related CN104891738B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510275447.4A CN104891738B (en) 2015-05-27 2015-05-27 A kind of ecological treatment method of municipal sewage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510275447.4A CN104891738B (en) 2015-05-27 2015-05-27 A kind of ecological treatment method of municipal sewage

Publications (2)

Publication Number Publication Date
CN104891738A true CN104891738A (en) 2015-09-09
CN104891738B CN104891738B (en) 2016-09-28

Family

ID=54024774

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510275447.4A Expired - Fee Related CN104891738B (en) 2015-05-27 2015-05-27 A kind of ecological treatment method of municipal sewage

Country Status (1)

Country Link
CN (1) CN104891738B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112079520A (en) * 2020-08-20 2020-12-15 重庆尚泽源环保科技有限公司 Urban domestic sewage recycling system
CN112777861A (en) * 2020-12-31 2021-05-11 北京邦源环保科技股份有限公司 Natural ecological treatment process for domestic sewage
CN114804507A (en) * 2022-03-17 2022-07-29 国网河北省电力有限公司电力科学研究院 Biochemical combined treatment method for municipal sewage

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101108757A (en) * 2006-07-21 2008-01-23 厦门中联环环保工程有限公司 Activated sludge method processing technique at sewage continuous drainage interval
CN101318758A (en) * 2008-05-16 2008-12-10 北京工业大学 Air-float and bio-filter combined water treatment process
CN101602563A (en) * 2009-02-20 2009-12-16 李颖 The method of biology, ecological sectional purifying treatment sanitary sewage
CN101638285A (en) * 2009-05-27 2010-02-03 北京能拓高科技有限公司 Sewage purification processing system
CN101817621A (en) * 2010-04-23 2010-09-01 北京工业大学 Semi-denitrification-based wastewater treatment technology
US20140014577A1 (en) * 2011-03-30 2014-01-16 Kubota Corporation Wastewater Treatment Method and Wastewater Treatment System
CN104326620A (en) * 2014-10-15 2015-02-04 西安华陆环保设备有限公司 Tannery wastewater treatment method
CN104355504A (en) * 2014-11-24 2015-02-18 富阳鸿祥技术服务有限公司 Industrial wastewater treatment system
CN204237680U (en) * 2014-10-31 2015-04-01 苏州工业园区清源华衍水务有限公司 A kind of industrial sewage advanced treatment system

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101108757A (en) * 2006-07-21 2008-01-23 厦门中联环环保工程有限公司 Activated sludge method processing technique at sewage continuous drainage interval
CN101318758A (en) * 2008-05-16 2008-12-10 北京工业大学 Air-float and bio-filter combined water treatment process
CN101602563A (en) * 2009-02-20 2009-12-16 李颖 The method of biology, ecological sectional purifying treatment sanitary sewage
CN101638285A (en) * 2009-05-27 2010-02-03 北京能拓高科技有限公司 Sewage purification processing system
CN101817621A (en) * 2010-04-23 2010-09-01 北京工业大学 Semi-denitrification-based wastewater treatment technology
US20140014577A1 (en) * 2011-03-30 2014-01-16 Kubota Corporation Wastewater Treatment Method and Wastewater Treatment System
CN104326620A (en) * 2014-10-15 2015-02-04 西安华陆环保设备有限公司 Tannery wastewater treatment method
CN204237680U (en) * 2014-10-31 2015-04-01 苏州工业园区清源华衍水务有限公司 A kind of industrial sewage advanced treatment system
CN104355504A (en) * 2014-11-24 2015-02-18 富阳鸿祥技术服务有限公司 Industrial wastewater treatment system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112079520A (en) * 2020-08-20 2020-12-15 重庆尚泽源环保科技有限公司 Urban domestic sewage recycling system
CN112777861A (en) * 2020-12-31 2021-05-11 北京邦源环保科技股份有限公司 Natural ecological treatment process for domestic sewage
CN114804507A (en) * 2022-03-17 2022-07-29 国网河北省电力有限公司电力科学研究院 Biochemical combined treatment method for municipal sewage

Also Published As

Publication number Publication date
CN104891738B (en) 2016-09-28

Similar Documents

Publication Publication Date Title
CN203845918U (en) Energy-saving emission-reducing type town sewage treatment system
CN101698550A (en) Advanced treating method of landfill leachate
CN102336500B (en) Rural domestic sewage treatment system suitable for northern part of China and technology thereof
JP2022001368A (en) Organic nitrogen wastewater treatment system and method
CN109650645B (en) Integrated rural domestic sewage treatment equipment and sewage treatment method
CN103449684B (en) High-toxicity coking phenol-cyanogen waste water recycling system and method
CN103979750B (en) Reactor for sewage treatment and phosphorus recovery and method for recovering phosphorus by using same
CN103979681B (en) Nitrification/denitrification integrated rural domestic sewage treatment system
CN107162339A (en) Return flow technique
CN104591473A (en) Advanced nitrogen and phosphorus removal technology
CN108585351A (en) Xinjiang textile industry garden dyeing waste water dual treatment and promotion reclamation rate integrated technique
CN104445837A (en) Industrial combined wastewater bio-augmentation treatment system and method
CN103723884B (en) The sewage water treatment method of a kind of COD that degrades, BOD, SS, ammonia nitrogen
CN103435233A (en) Equipment and method for recycling chemical fiber continuous-spinning wastewater
CN105174642A (en) Efficient biological denitrification method for sewage
CN104891738B (en) A kind of ecological treatment method of municipal sewage
CN103951140B (en) The low concentration wastewater treatment process of a kind of anaerobic built-in zero-valent iron reactor coupling artificial swamp
CN203781915U (en) Nitrification and denitrification integrated rural domestic sewage treatment system
CN103539324B (en) Biological ceramsite device for deeply treating domestic wastewater as well as process thereof
CN201614333U (en) Decentralized sewage treatment device
CN203461924U (en) Grain and oil production sewage treatment system
CN203021377U (en) High-concentration liquid waste processing system
CN105601045A (en) Domestic sewage treatment system and method
WO2020000214A1 (en) Wastewater recycling treatment apparatus
CN103387311B (en) A kind of waste disposal plant and method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160928

Termination date: 20170527

CF01 Termination of patent right due to non-payment of annual fee