CN101913735A - Self-oxygenation and self-stirring domestic sewage purification device - Google Patents

Self-oxygenation and self-stirring domestic sewage purification device Download PDF

Info

Publication number
CN101913735A
CN101913735A CN 201010253534 CN201010253534A CN101913735A CN 101913735 A CN101913735 A CN 101913735A CN 201010253534 CN201010253534 CN 201010253534 CN 201010253534 A CN201010253534 A CN 201010253534A CN 101913735 A CN101913735 A CN 101913735A
Authority
CN
China
Prior art keywords
anaerobic zone
pipe
anaerobic
zone
area
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
CN 201010253534
Other languages
Chinese (zh)
Other versions
CN101913735B (en
Inventor
郑平
陈小光
胡宝兰
季军远
张萌
陆慧锋
沈李东
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.)
Zhejiang University ZJU
Original Assignee
Zhejiang University ZJU
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 Zhejiang University ZJU filed Critical Zhejiang University ZJU
Priority to CN2010102535347A priority Critical patent/CN101913735B/en
Publication of CN101913735A publication Critical patent/CN101913735A/en
Application granted granted Critical
Publication of CN101913735B publication Critical patent/CN101913735B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

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

Abstract

本发明公开了一种自充氧自搅拌生活污水净化装置。该净化装置包括格栅集水区、第一弹性填料、细格栅、进水管、第一厌氧区气室、兼氧区,第一L型气压平衡管、第二厌氧区气室、第二L型气压平衡管、第三方形孔、第三厌氧区气室、进风口、兼氧区气室、第三L型气压平衡管、拔风管、第四方形孔、排水管、斜板、沉淀区、第三双向流通管、第三厌氧区、第三弹性填料、第二单向流通管、第二弹性填料、第二厌氧区、第二方形孔、第一单向流通管、第一厌氧区、第一方形孔。本发明结构紧凑,占地少;净化池中的兼氧区能实现自动浅层充氧,有助于生物脱氮;净化池厌氧区能实现自动搅拌,有助于防止泥水分层,提高净化效果。

Figure 201010253534

The invention discloses a self-oxygenating and self-stirring domestic sewage purification device. The purification device includes a grid water collection area, a first elastic packing, a fine grid, a water inlet pipe, an air chamber in the first anaerobic zone, a facultative oxygen zone, a first L-shaped air pressure balance pipe, an air chamber in the second anaerobic zone, The second L-shaped air pressure balance pipe, the third square hole, the third anaerobic zone air chamber, the air inlet, the facultative oxygen zone air chamber, the third L-shaped air pressure balance pipe, the air extraction pipe, the fourth square hole, the drain pipe, Inclined plate, settling area, third two-way flow pipe, third anaerobic area, third elastic packing, second one-way flow pipe, second elastic packing, second anaerobic area, second square hole, first one-way Flow tube, first anaerobic zone, first square hole. The invention has a compact structure and occupies less land; the facultative oxygen zone in the purification tank can realize automatic shallow oxygenation, which is helpful for biological denitrification; the anaerobic zone of the purification tank can realize automatic stirring, which is helpful to prevent muddy water stratification and improve Purifying effect.

Figure 201010253534

Description

自充氧自搅拌生活污水净化装置 Self-oxygenation and self-stirring domestic sewage purification device

技术领域technical field

本发明涉及一种自充氧自搅拌生活污水净化装置。The invention relates to a self-oxygenating and self-stirring domestic sewage purification device.

背景技术Background technique

目前,面源污染已成为我国重大的水环境问题,而农村生活污水是面源污染主要的来源之一。我国大多数农村住宅布局零乱,缺乏统一规划,没有完整的污水收集管网和污水处理设施;大部分已建户用三格式化粪池质量较差,易渗漏,污水净化效果不佳。以厌氧处理为主的农村生活污水净化池在我国各地已得到广泛应用,该技术COD去除效率高、运行稳定、管理方便。但仍存在脱氮效果差,长期运行易产生污泥沉积的问题。在现有污水净化池的基础上,采本发明,将兼氧池与厌氧池上下合建,既可节省占地,又增强脱氮效果,避免污泥沉积。At present, non-point source pollution has become a major water environment problem in my country, and rural domestic sewage is one of the main sources of non-point source pollution. The layout of most rural residential buildings in my country is messy, lack of unified planning, and there is no complete sewage collection pipe network and sewage treatment facilities; most of the three-format septic tanks that have been built for households are of poor quality, easy to leak, and the sewage purification effect is not good. Rural domestic sewage purification tanks based on anaerobic treatment have been widely used in various parts of my country. This technology has high COD removal efficiency, stable operation and convenient management. However, there are still problems of poor denitrification effect and easy sludge deposition in long-term operation. On the basis of the existing sewage purification tank, the present invention is adopted to build the facultative tank and the anaerobic tank together, which can not only save land occupation, but also enhance the denitrification effect and avoid sludge deposition.

发明内容Contents of the invention

本发明的目的是克服现有分散式生活污水净化池的不足,提供一种自充氧自搅拌的生活污水净化装置。The purpose of the present invention is to overcome the shortcomings of the existing distributed domestic sewage purification tanks and provide a self-oxygenating and self-stirring domestic sewage purification device.

自充氧自搅拌生活污水净化装置包括格栅集水区、第一弹性填料、细格栅、进水管、第一厌氧区气室、兼氧区,第一L型气压平衡管、第二厌氧区气室、第二L型气压平衡管、第三方形孔、第三厌氧区气室、进风口、兼氧区气室、第三L型气压平衡管、拔风管、第四方形孔、排水管、斜板、沉淀区、第三双向流通管、第三厌氧区、第三弹性填料、第二单向流通管、第二弹性填料、第二厌氧区、第二方形孔、第一单向流通管、第一厌氧区、第一方形孔;格栅集水区与第一厌氧区、第二厌氧区、第三厌氧区、兼氧区和沉淀区依次相连;格栅集水区内设有细格栅,格栅集水区上部侧壁设有进水管,格栅集水区下部通过第一方形孔与第一厌氧区相连,第一厌氧区内设有第一弹性填料、第一单向流通管、第一L型气压平衡管和第一厌氧区气室,第一厌氧区下部通过第二方形孔与第二厌氧区相连,第二厌氧区内设有第二弹性填料、第二单向流通管、第二L型气压平衡管和第二厌氧区气室,第二厌氧区上部通过第三方形孔与第三厌氧区相连,第三厌氧区内设有第三弹性填料、第三双向流通管、第三L型气压平衡管和第三厌氧区气室,第三厌氧区通过第三双向流通管与兼氧区相连,兼氧区在第一、二、三厌氧区的正上方,该区上部设有进风口、拔风管,兼氧区上部通过第四方形孔与沉淀区相连,沉淀区内设有斜板,沉淀区上部侧壁设有排水管;兼氧区与第一厌氧区通过第一单向流通管、第一L型气压平衡管相贯穿,兼氧区与第二厌氧区通过第二单向流通管、第二L型气压平衡管相贯穿,兼氧区与第三厌氧区通过第三双向流通管、第三L型气压平衡管相贯穿;净化装置顶覆土,可考虑绿化,进风口和拔风管从装置顶端接出。Self-oxygenation and self-stirring domestic sewage purification device includes grid catchment area, first elastic packing, fine grid, water inlet pipe, first anaerobic zone air chamber, facultative oxygen zone, first L-shaped air pressure balance pipe, second Anaerobic area air chamber, second L-shaped air pressure balance pipe, third rectangular hole, third anaerobic area air chamber, air inlet, facultative oxygen area air chamber, third L-shaped air pressure balance pipe, air extraction pipe, fourth Square hole, drainage pipe, inclined plate, sedimentation area, third two-way flow pipe, third anaerobic area, third elastic packing, second one-way flow pipe, second elastic packing, second anaerobic area, second square hole, first one-way flow pipe, first anaerobic zone, first square hole; grid catchment area with first anaerobic zone, second anaerobic zone, third anaerobic zone, facultative zone and sedimentation There are fine grids in the grid catchment area, water inlet pipes are arranged on the upper side wall of the grill catchment area, the lower part of the grid water collection area is connected with the first anaerobic zone through the first square hole, and the second An anaerobic zone is provided with a first elastic packing, a first one-way flow pipe, a first L-shaped air pressure balance tube and an air chamber in the first anaerobic zone, and the lower part of the first anaerobic zone is connected to the second anaerobic zone through the second square hole. The oxygen zone is connected, and the second anaerobic zone is provided with a second elastic packing, a second one-way flow pipe, a second L-shaped air pressure balance tube and an air chamber in the second anaerobic zone, and the upper part of the second anaerobic zone passes through a third square The hole is connected to the third anaerobic zone, and the third anaerobic zone is provided with a third elastic packing, a third two-way flow pipe, a third L-shaped air pressure balance tube and an air chamber of the third anaerobic zone, and the third anaerobic zone passes through The third two-way flow pipe is connected with the aerobic zone, and the aerobic zone is directly above the first, second, and third anaerobic zones. The upper part of the zone is provided with an air inlet and an air extraction pipe, and the upper part of the aerobic zone is connected with the fourth square hole. The sedimentation area is connected, with a sloping plate in the sedimentation area, and a drainage pipe on the upper side wall of the sedimentation area; the aerobic area and the first anaerobic area are connected through the first one-way flow pipe and the first L-shaped air pressure balance pipe, and the The oxygen zone and the second anaerobic zone are connected through the second one-way flow pipe and the second L-shaped air pressure balance pipe, and the facultative oxygen zone is connected with the third anaerobic zone through the third two-way flow pipe and the third L-shaped air pressure balance pipe. Penetration; the top of the purification device is covered with soil, greening can be considered, and the air inlet and exhaust pipe are connected from the top of the device.

自充氧自搅拌生活污水净化方法是:生活污水经进水管进入格栅集水区,水力停留时间12h,去除污水中大颗粒污物后,经第一方形孔流入第一厌氧区,水力停留时间16h,经第二方形孔流入第二厌氧区,水力停留时间16h,经第三方形孔流入第三厌氧区,水力停留时间16h,经第三双向流通管流入兼氧区,水力停留时间24h,经第四方形孔流入沉淀区,水力停留时间12h,最后经排水管达标排放;第一厌氧区气室、第二厌氧区气室和第三厌氧区气室分别通过第一L型气压平衡管、第二L型气压平衡管和第三L型气压平衡管实现与兼氧区气室的气压平衡;第一厌氧区、第二厌氧区和第三厌氧区分别通过第一单向流通管、第二单向流通管和第三双向流通管实现自搅拌功能,可有效避免厌氧区内颗粒污泥沉积;兼氧区通过进风口和拔风管实现自充氧功能,自充氧能力可达150mgO2/(m2·d),脱氮效果可达0.1-0.2kgN/(m3·d);净化装置顶覆土0.5m,进风口盖高于覆土约0.06m,拔风管高于覆土约0.1m,进水管和出水管两者高度差约0.3-0.5m,可确保污水由进水管自流至出水管。Self-oxygenation and self-stirring domestic sewage purification method is: domestic sewage enters the grid catchment area through the water inlet pipe, and the hydraulic retention time is 12h. After removing large particles of dirt in the sewage, it flows into the first anaerobic area through the first square hole. With a hydraulic retention time of 16h, it flows into the second anaerobic zone through the second square hole, and with a hydraulic retention time of 16h, it flows into the third anaerobic zone through the third rectangular hole with a hydraulic retention time of 16h, and flows into the facultative zone through the third two-way flow pipe The hydraulic retention time is 24h, and it flows into the sedimentation area through the fourth square hole. The hydraulic retention time is 12h, and finally it is discharged through the drainage pipe up to the standard; Through the first L-type air pressure balance pipe, the second L-type air pressure balance pipe and the third L-type air pressure balance pipe to realize the air pressure balance with the gas chamber of the aerobic zone; the first anaerobic zone, the second anaerobic zone and the third anaerobic zone The oxygen zone realizes the self-stirring function through the first one-way flow pipe, the second one-way flow pipe and the third two-way flow pipe respectively, which can effectively avoid the deposition of granular sludge in the anaerobic zone; Realize the self-oxygenation function, the self-oxygenation capacity can reach 150mgO 2 /(m 2 ·d), the denitrification effect can reach 0.1-0.2kgN/(m 3 ·d); the top of the purification device is covered with soil 0.5m, and the air inlet cover is high The overburden is about 0.06m, the air pipe is about 0.1m higher than the overburden, and the height difference between the inlet pipe and the outlet pipe is about 0.3-0.5m, which can ensure that the sewage flows from the inlet pipe to the outlet pipe.

本发明的有益效果是:1)净化池采用地埋式一体化结构,兼氧区与厌氧区上下合建,净化池结构紧凑,占地面积少;2)净化池采用厌氧+兼氧工艺,脱氮除碳效果佳;3)净化池采用浅层充氧原理,强化兼氧区自充氧功能,改善脱氮效果;4)净化池设置L型气压平衡管和单双向流通管,可实现厌氧区自搅拌和反硝化脱氮。The beneficial effects of the present invention are as follows: 1) the purification pool adopts an underground integrated structure, and the anaerobic zone and the anaerobic zone are built together up and down, and the purification pool has a compact structure and occupies less area; 2) the purification pool adopts anaerobic + facultative oxygen 3) The purification pool adopts the principle of shallow oxygenation to strengthen the self-oxygenation function of the anaerobic zone and improve the denitrification effect; 4) The purification pool is equipped with L-shaped air pressure balance pipes and single- and two-way flow pipes. It can realize self-stirring and denitrification denitrification in anaerobic zone.

附图说明Description of drawings

附图是本发明的一种自充氧自搅拌生活污水净化装置示意图;Accompanying drawing is a kind of self-oxygenation self-stirring domestic sewage purifying device schematic diagram of the present invention;

图中:格栅集水区1、第一弹性填料2、细格栅3、进水管4、第一厌氧区气室5、兼氧区6,第一L型气压平衡管7、第二厌氧区气室8、第二L型气压平衡管9、第三方形孔10、第三厌氧区气室11、进风口12、兼氧区气室13、第三L型气压平衡管14、拔风管15、第四方形孔16、排水管17、斜板18、沉淀区19、第三双向流通管20、第三厌氧区21、第三弹性填料22、第二单向流通管23、第二弹性填料24、第二厌氧区25、第二方形孔26、第一单向流通管27、第一厌氧区28、第一方形孔29。In the figure: grid catchment area 1, first elastic filler 2, fine grid 3, water inlet pipe 4, first anaerobic zone air chamber 5, facultative oxygen zone 6, first L-shaped air pressure balance pipe 7, second Anaerobic area air chamber 8, second L-shaped air pressure balance pipe 9, third rectangular hole 10, third anaerobic area air chamber 11, air inlet 12, facultative oxygen area air chamber 13, third L-shaped air pressure balance pipe 14 , air extraction pipe 15, fourth square hole 16, drain pipe 17, inclined plate 18, sedimentation area 19, third two-way flow pipe 20, third anaerobic area 21, third elastic packing 22, second one-way flow pipe 23. The second elastic filler 24, the second anaerobic zone 25, the second square hole 26, the first one-way flow pipe 27, the first anaerobic zone 28, and the first square hole 29.

具体实施方式Detailed ways

如附图所示,自充氧自搅拌生活污水净化装置包括格栅集水区1、第一弹性填料2、细格栅3、进水管4、第一厌氧区气室5、兼氧区6,第一L型气压平衡管7、第二厌氧区气室8、第二L型气压平衡管9、第三方形孔10、第三厌氧区气室11、进风口12、兼氧区气室13、第三L型气压平衡管14、拔风管15、第四方形孔16、排水管17、斜板18、沉淀区19、第三双向流通管20、第三厌氧区21、第三弹性填料22、第二单向流通管23、第二弹性填料24、第二厌氧区25、第二方形孔26、第一单向流通管27、第一厌氧区28、第一方形孔29;格栅集水区1与第一厌氧区28、第二厌氧区25、第三厌氧区21、兼氧区6和沉淀区19依次相连;格栅集水区1内设有细格栅3,格栅集水区1上部侧壁设有进水管4,格栅集水区1下部通过第一方形孔29与第一厌氧区28相连,第一厌氧区28内设有第一弹性填料2、第一单向流通管27、第一L型气压平衡管7和第一厌氧区气室5,第一厌氧区28下部通过第二方形孔26与第二厌氧区25相连,第二厌氧区25内设有第二弹性填料24、第二单向流通管23、第二L型气压平衡管9和第二厌氧区气室8,第二厌氧区25上部通过第三方形孔10与第三厌氧区21相连,第三厌氧区21内设有第三弹性填料22、第三双向流通管20、第三L型气压平衡管14和第三厌氧区气室11,第三厌氧区21通过第三双向流通管20与兼氧区6相连,兼氧区6在第一、二、三厌氧区的正上方,该区上部设有进风口12、拔风管15,兼氧区6上部通过第四方形孔16与沉淀区19相连,沉淀区19内设有斜板18,沉淀区19上部侧壁设有排水管17;兼氧区6与第一厌氧区28通过第一单向流通管27、第一L型气压平衡管7相贯穿,兼氧区6与第二厌氧区25通过第二单向流通管23、第二L型气压平衡管9相贯穿,兼氧区6与第三厌氧区21通过第三双向流通管20、第三L型气压平衡管14相贯穿;净化装置顶覆土,可考虑绿化,进风口12和拔风管15从装置顶端接出。As shown in the attached figure, the self-oxygenation and self-stirring domestic sewage purification device includes a grid catchment area 1, a first elastic filler 2, a fine grid 3, a water inlet pipe 4, an anaerobic zone air chamber 5, and an aerobic zone 6. The first L-shaped air pressure balance tube 7, the second anaerobic zone air chamber 8, the second L-shaped air pressure balance tube 9, the third square hole 10, the third anaerobic zone air chamber 11, the air inlet 12, and the oxygen Zone air chamber 13, third L-shaped air pressure balance pipe 14, air extraction pipe 15, fourth square hole 16, drain pipe 17, inclined plate 18, sedimentation area 19, third two-way flow pipe 20, third anaerobic area 21 , the third elastic packing 22, the second one-way flow tube 23, the second elastic packing 24, the second anaerobic zone 25, the second square hole 26, the first one-way flow tube 27, the first anaerobic zone 28, the second A square hole 29; the grid catchment area 1 is connected successively with the first anaerobic area 28, the second anaerobic area 25, the third anaerobic area 21, the aerobic area 6 and the precipitation area 19; the grid water collection area 1 is provided with a fine grid 3, and the upper side wall of the grid water collection area 1 is provided with a water inlet pipe 4, and the lower part of the grid water collection area 1 is connected with the first anaerobic area 28 through the first square hole 29, and the first anaerobic area The first elastic packing 2, the first one-way flow pipe 27, the first L-shaped air pressure balance pipe 7 and the first anaerobic zone air chamber 5 are arranged in the oxygen zone 28, and the lower part of the first anaerobic zone 28 passes through the second square hole 26 is connected with the second anaerobic zone 25, and the second elastic packing 24, the second one-way flow pipe 23, the second L-shaped air pressure balance tube 9 and the second anaerobic zone air chamber 8 are arranged in the second anaerobic zone 25 , the upper part of the second anaerobic zone 25 is connected with the third anaerobic zone 21 through the third rectangular hole 10, the third anaerobic zone 21 is provided with a third elastic filler 22, a third two-way flow pipe 20, a third L-shaped air pressure The balance pipe 14 and the air chamber 11 of the third anaerobic zone, the third anaerobic zone 21 is connected to the aerobic zone 6 through the third two-way flow pipe 20, and the aerobic zone 6 is directly above the first, second and third anaerobic zones , the upper part of this area is provided with air inlet 12, air extraction pipe 15, and the upper part of the aerobic area 6 is connected with the sedimentation area 19 through the fourth square hole 16, and the inclined plate 18 is arranged in the sedimentation area 19, and the side wall of the upper part of the sedimentation area 19 is provided with Drain pipe 17; the aerobic zone 6 and the first anaerobic zone 28 are connected through the first one-way flow pipe 27 and the first L-shaped air pressure balance tube 7, and the aerobic zone 6 and the second anaerobic zone 25 are passed through the second single It runs through the flow pipe 23 and the second L-shaped air pressure balance pipe 9, and the anaerobic zone 6 and the third anaerobic zone 21 pass through the third two-way flow pipe 20 and the third L-shaped air pressure balance pipe 14; the purification device is covered with soil , greening can be considered, and the air inlet 12 and the exhaust pipe 15 are connected from the top of the device.

自充氧自搅拌生活污水净化方法是:生活污水经进水管4进入格栅集水区1,水力停留时间12h,去除污水中大颗粒污物后,经第一方形孔29流入第一厌氧区28,水力停留时间16h,经第二方形孔26流入第二厌氧区25,水力停留时间16h,经第三方形孔10流入第三厌氧区21,水力停留时间16h,经第三双向流通管20流入兼氧区6,水力停留时间24h,经第四方形孔流入沉淀区19,水力停留时间12h,最后经排水管17达标排放;第一厌氧区气室5、第二厌氧区气室8和第三厌氧区气室11分别通过第一L型气压平衡管7、第二L型气压平衡管9和第三L型气压平衡管14实现与兼氧区气室13的气压平衡;第一厌氧区28、第二厌氧区25和第三厌氧区21分别通过第一单向流通管27、第二单向流通管23和第三双向流通管20实现自搅拌功能,可有效避免厌氧区内颗粒污泥沉积;兼氧区6通过进风口12和拔风管15实现自充氧功能,自充氧能力可达150mg O2/(m2·d),脱氮效果可达0.1-0.2kgN/(m3·d);净化装置顶覆土0.5m,进风口12盖高于覆土约0.06m,拔风管15高于覆土约0.1m,进水管4和出水管17两者高度差约0.3-0.5m,可确保污水由进水管4自流至出水管17。The self-oxygenation and self-stirring domestic sewage purification method is: domestic sewage enters the grid catchment area 1 through the water inlet pipe 4, and the hydraulic retention time is 12 hours. After removing large particles of dirt in the sewage, it flows into the first drain through the first square hole 29 Oxygen zone 28, hydraulic retention time 16h, flows into the second anaerobic zone 25 through the second square hole 26, hydraulic retention time 16h, flows into the third anaerobic zone 21 through the third rectangular hole 10, hydraulic retention time 16h, passes through the third The two-way flow pipe 20 flows into the aerobic zone 6 with a hydraulic retention time of 24 hours, flows into the sedimentation zone 19 through the fourth square hole, and has a hydraulic retention time of 12 hours, and finally discharges up to the standard through the drain pipe 17; the first anaerobic zone air chamber 5, the second anaerobic zone The gas chamber 8 in the oxygen zone and the gas chamber 11 in the third anaerobic zone are respectively realized by the first L-shaped air pressure balance pipe 7, the second L-shaped air pressure balance pipe 9 and the third L-shaped air pressure balance pipe 14 and the gas chamber 13 in the oxygen zone. air pressure balance; the first anaerobic zone 28, the second anaerobic zone 25 and the third anaerobic zone 21 are realized by the first one-way flow pipe 27, the second one-way flow pipe 23 and the third two-way flow pipe 20 respectively The stirring function can effectively avoid the deposition of granular sludge in the anaerobic zone; the anaerobic zone 6 realizes the self-oxygenation function through the air inlet 12 and the exhaust pipe 15, and the self-oxygenation capacity can reach 150mg O 2 /(m 2 ·d) , the denitrification effect can reach 0.1-0.2kgN/(m 3 ·d); the top of the purification device is covered with soil 0.5m, the cover of the air inlet 12 is about 0.06m higher than the covering soil, the air extraction pipe 15 is about 0.1m higher than the covering soil, and the water inlet pipe 4 The height difference between the water outlet pipe 17 and the water outlet pipe 17 is about 0.3-0.5m, which can ensure that the sewage flows from the water inlet pipe 4 to the water outlet pipe 17.

本发明运行方式是:生活污水经进水管4进入格栅集水池1,通过第一方形孔29流入第一厌氧区28,经第二方形孔26流入第二厌氧区25,经第三方形孔10流入第三厌氧区21,经第三双向流通管20流入兼氧区6,再经第四方形孔16流入沉淀区19,最后经排水管17达标排放;空气由进风口12流入兼氧区气室13,由拔风管15排出兼氧区气室13,通过与兼氧区6内污水接触,从而实现兼氧区6的自充氧功能;兼氧区6内污水通过第一L型气压平衡管7、第二L型气压平衡管9和第三L型气压平衡管14的气压平衡平衡作用,经第一单向流通管27、第二单向流通管23和第三双向流通管20,分别流入第一厌氧区28、第二厌氧区25和第三厌氧区21,对厌氧区内的沉积污泥产生激烈的冲击作用,从而实现各厌氧区的自搅拌功能。The operation mode of the present invention is: domestic sewage enters the grid sump 1 through the water inlet pipe 4, flows into the first anaerobic zone 28 through the first square hole 29, flows into the second anaerobic zone 25 through the second square hole 26, and flows into the second anaerobic zone 25 through the second square hole 26. The three square holes 10 flow into the third anaerobic zone 21, flow into the aerobic zone 6 through the third two-way flow pipe 20, flow into the sedimentation zone 19 through the fourth square hole 16, and finally discharge through the drain pipe 17 up to the standard; the air is discharged from the air inlet 12 It flows into the gas chamber 13 of the aerobic zone, and is discharged from the gas chamber 13 of the aerobic zone by the exhaust pipe 15. By contacting the sewage in the aerobic zone 6, the self-oxygenation function of the aerobic zone 6 is realized; the sewage in the aerobic zone 6 passes through The first L-type air pressure balance pipe 7, the second L-type air pressure balance pipe 9 and the third L-type air pressure balance pipe 14 balance the air pressure, through the first one-way flow pipe 27, the second one-way flow pipe 23 and the first one-way flow pipe. The three-way flow pipes 20 respectively flow into the first anaerobic zone 28, the second anaerobic zone 25 and the third anaerobic zone 21, which have a strong impact on the deposited sludge in the anaerobic zone, thereby realizing the self-stirring function.

Claims (2)

1. self-oxygenate self-stirring domestic sewage purification device, it is characterized in that comprising grid catchment area (1), first elastic filler (2), fine fack (3), water inlet pipe (4), the first anaerobic zone air chamber (5), aerobic area (6), a L type barometric pipe (7), the second anaerobic zone air chamber (8), the 2nd L type barometric pipe (9), third square hole (10), the 3rd anaerobic zone air chamber (11), blast inlet (12), aerobic area air chamber (13), the 3rd L type barometric pipe (14), pull out airduct (15), fourth square hole (16), water shoot (17), swash plate (18), settling region (19), the 3rd bidirectional flow siphunculus (20), the 3rd anaerobic zone (21), the 3rd elastic filler (22), second one-way flow control (23), second elastic filler (24), second anaerobic zone (25), second square opening (26), first one-way flow control (27), first anaerobic zone (28), first square opening (29); Grid catchment area (1) links to each other with settling region (19) successively with first anaerobic zone (28), second anaerobic zone (25), the 3rd anaerobic zone (21), aerobic area (6); Be provided with fine fack (3) in the grid catchment area (1), grid catchment area (1) upper portion side wall is provided with water inlet pipe (4), bottom, grid catchment area (1) links to each other with first anaerobic zone (28) by first square opening (29), be provided with first elastic filler (2) in first anaerobic zone (28), first one-way flow control (27), the one L type barometric pipe (7) and the first anaerobic zone air chamber (5), first anaerobic zone (28) bottom links to each other with second anaerobic zone (25) by second square opening (26), be provided with second elastic filler (24) in second anaerobic zone (25), second one-way flow control (23), the 2nd L type barometric pipe (9) and the second anaerobic zone air chamber (8), second anaerobic zone (25) top links to each other with the 3rd anaerobic zone (21) by third square hole (10), be provided with the 3rd elastic filler (22) in the 3rd anaerobic zone (21), the 3rd bidirectional flow siphunculus (20), the 3rd L type barometric pipe (14) and the 3rd anaerobic zone air chamber (11), the 3rd anaerobic zone (21) links to each other with aerobic area (6) by the 3rd bidirectional flow siphunculus (20), aerobic area (6) is first, two, directly over three anaerobic zones, this top, district is provided with blast inlet (12), pull out airduct (15), aerobic area (6) top links to each other with settling region (19) by fourth square hole (16), be provided with swash plate (18) in the settling region (19), settling region (19) upper portion side wall is provided with water shoot (17); Aerobic area (6) runs through by first one-way flow control (27), a L type barometric pipe (7) mutually with first anaerobic zone (28), aerobic area (6) runs through by second one-way flow control (23), the 2nd L type barometric pipe (9) mutually with second anaerobic zone (25), and aerobic area (6) runs through by the 3rd bidirectional flow siphunculus (20), the 3rd L type barometric pipe (14) mutually with the 3rd anaerobic zone (21); Refining plant top earthing can be considered greening, blast inlet (12) and pull out airduct (15) and pick out from installing the top.
2. self-oxygenate self-stirring domestic sewage purifying method that use is installed according to claim 1, it is characterized in that sanitary sewage enters grid catchment area 1 through water inlet pipe (4), hydraulic detention time 12h, remove in the sewage behind the macrobead dirt, flow into first anaerobic zone (28) through first square opening (29), hydraulic detention time 16h, flow into second anaerobic zone (25) through second square opening (26), hydraulic detention time 16h, flow into the 3rd anaerobic zone (21) through third square hole (10), hydraulic detention time 16h, flow into aerobic area (6) through the 3rd bidirectional flow siphunculus (20), hydraulic detention time 24h flows into settling region (19) through fourth square hole, hydraulic detention time 12h is after water shoot (17) qualified discharge; The first anaerobic zone air chamber (5), the second anaerobic zone air chamber (8) and the 3rd anaerobic zone air chamber (11) are respectively by a L type barometric pipe (7), the 2nd L type barometric pipe (9) and the realization of the 3rd L type barometric pipe (14) air pressure balance with aerobic area air chamber (13); First anaerobic zone (28), second anaerobic zone (25) and the 3rd anaerobic zone (21) are realized can effectively avoiding the sludgd deposition of anaerobic zone endoparticle from agitating function by first one-way flow control (27), second one-way flow control (23) and the 3rd bidirectional flow siphunculus (20) respectively; Aerobic area (6) is by blast inlet (12) and pull out airduct (15) realization from the oxygenation function, can reach 150mgO from oxygenation capacity 2/ (m 2D), denitrification effect can reach 0.1-0.2kgN/ (m 3D); Refining plant top earthing 0.5m, blast inlet (12) lid is higher than the about 0.06m of earthing, pulls out airduct (15) and is higher than the about 0.1m of earthing, and water inlet pipe (4) and the about 0.3-0.5m of both difference of altitude of rising pipe (17) can guarantee that sewage flow to rising pipe (17) certainly by water inlet pipe (4).
CN2010102535347A 2010-08-13 2010-08-13 Self-oxygenation and self-stirring domestic sewage purification device Expired - Fee Related CN101913735B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2010102535347A CN101913735B (en) 2010-08-13 2010-08-13 Self-oxygenation and self-stirring domestic sewage purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2010102535347A CN101913735B (en) 2010-08-13 2010-08-13 Self-oxygenation and self-stirring domestic sewage purification device

Publications (2)

Publication Number Publication Date
CN101913735A true CN101913735A (en) 2010-12-15
CN101913735B CN101913735B (en) 2012-05-30

Family

ID=43321418

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2010102535347A Expired - Fee Related CN101913735B (en) 2010-08-13 2010-08-13 Self-oxygenation and self-stirring domestic sewage purification device

Country Status (1)

Country Link
CN (1) CN101913735B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102765808A (en) * 2012-07-12 2012-11-07 中国矿业大学 Mid-position aeration sequencing batch type biological dephosphorization and denitrifying process
CN104245596A (en) * 2012-04-04 2014-12-24 威立雅水务解决方案与技术支持公司 Compact water treatment unit
CN107814439A (en) * 2017-12-14 2018-03-20 凌志环保股份有限公司 A kind of new rural village domestic sewage denitrifying-dephosphorizing purifies wet land system
CN107814468A (en) * 2017-12-14 2018-03-20 凌志环保股份有限公司 A kind of domestic sewage in rural areas purifies wet land system
CN107814467A (en) * 2017-12-14 2018-03-20 凌志环保股份有限公司 A kind of simple domestic sewage in rural areas wet land treating system

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1084831A (en) * 1992-09-28 1994-04-06 大连理工大学 Vtbr
CN1935708A (en) * 2006-10-19 2007-03-28 北京科技大学 Treatment device with bio-sludge degrading and denitrogenation, and its operating method
CN101481194A (en) * 2008-04-26 2009-07-15 张政权 Town domestic sewage treatment process
CN201284266Y (en) * 2008-09-01 2009-08-05 海南大学 Unpowered bio-filter with oxygenation and backwash functions
CN201825820U (en) * 2010-08-13 2011-05-11 浙江大学 Self oxygenating and stirring purification device for domestic sewage

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1084831A (en) * 1992-09-28 1994-04-06 大连理工大学 Vtbr
CN1935708A (en) * 2006-10-19 2007-03-28 北京科技大学 Treatment device with bio-sludge degrading and denitrogenation, and its operating method
CN101481194A (en) * 2008-04-26 2009-07-15 张政权 Town domestic sewage treatment process
CN201284266Y (en) * 2008-09-01 2009-08-05 海南大学 Unpowered bio-filter with oxygenation and backwash functions
CN201825820U (en) * 2010-08-13 2011-05-11 浙江大学 Self oxygenating and stirring purification device for domestic sewage

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104245596A (en) * 2012-04-04 2014-12-24 威立雅水务解决方案与技术支持公司 Compact water treatment unit
CN104245596B (en) * 2012-04-04 2017-05-10 威立雅水务解决方案与技术支持公司 Compact water treatment unit
CN102765808A (en) * 2012-07-12 2012-11-07 中国矿业大学 Mid-position aeration sequencing batch type biological dephosphorization and denitrifying process
CN107814439A (en) * 2017-12-14 2018-03-20 凌志环保股份有限公司 A kind of new rural village domestic sewage denitrifying-dephosphorizing purifies wet land system
CN107814468A (en) * 2017-12-14 2018-03-20 凌志环保股份有限公司 A kind of domestic sewage in rural areas purifies wet land system
CN107814467A (en) * 2017-12-14 2018-03-20 凌志环保股份有限公司 A kind of simple domestic sewage in rural areas wet land treating system
CN107814439B (en) * 2017-12-14 2023-09-05 凌志环保股份有限公司 A new rural domestic sewage denitrification and phosphorus removal wetland purification system
CN107814468B (en) * 2017-12-14 2023-09-08 凌志环保股份有限公司 A rural domestic sewage purification wetland system
CN107814467B (en) * 2017-12-14 2023-09-08 凌志环保股份有限公司 A simple rural domestic sewage wetland treatment system

Also Published As

Publication number Publication date
CN101913735B (en) 2012-05-30

Similar Documents

Publication Publication Date Title
CN205222815U (en) Integrated sewage treatment device
WO2021174722A1 (en) Regulation, storage, and purification system and method for controlling rain and sewage confluence and overflow pollution
CN102001756B (en) Stable surface flow wetland for preventing silting and sewage treatment method
CN202594918U (en) Domestic garbage and sewage processing system
CN104692597A (en) Integrated device for ecological purification of domestic wastewater of small scattered river suspended sewage outlet
CN104445831B (en) A kind of family formula rural domestic sewage treatment, reusing integral system
CN101913735B (en) Self-oxygenation and self-stirring domestic sewage purification device
CN205382060U (en) Villages and small towns domestic sewage ecologization oligodynamic treatment system
CN102392475B (en) Water recycling system in high-rise buildings
CN105601043A (en) Ecological micro-power treatment system for domestic sewage of villages and towns
CN201825820U (en) Self oxygenating and stirring purification device for domestic sewage
CN111777261A (en) High drop environment unpowered sewage treatment system
CN101618926A (en) Urban environment comprehensive treatment scheme
CN105481171B (en) Unit equipment associated with a kind of more family sanitary sewage hydrolytic tanks and more processing units
CN201678520U (en) Improved Unpowered Sewage Biological Purification Device
CN205528274U (en) Rural sewage treatment system
CN205420076U (en) Many families domestic sewage hydrolysis groove with purify bank of cells and close treatment facility
CN205347109U (en) Many families domestic sewage hydrolysis groove and many processing apparatus series -parallel connection combination devices
CN215102725U (en) Rural household grey water treatment system
CN207748996U (en) A kind of residents sewage-treatment plant
CN223991017U (en) Domestic sewage treatment and resource utilization system for farmers
CN213625906U (en) Sewage drainage comprehensive utilization system for residential community
CN205575779U (en) Prevent wetland structure of stifled denitrogenation
CN203866096U (en) Sewage treatment unit and sewage treatment device
CN202492441U (en) Novel hydraulic enhanced biological septic tank

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

Granted publication date: 20120530

Termination date: 20180813