CN201321417Y - Multi-level biochemical domestic sewage treatment device - Google Patents
Multi-level biochemical domestic sewage treatment device Download PDFInfo
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- CN201321417Y CN201321417Y CNU2008201602658U CN200820160265U CN201321417Y CN 201321417 Y CN201321417 Y CN 201321417Y CN U2008201602658 U CNU2008201602658 U CN U2008201602658U CN 200820160265 U CN200820160265 U CN 200820160265U CN 201321417 Y CN201321417 Y CN 201321417Y
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- contact oxidation
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Abstract
The utility model discloses a multi-level biochemical domestic sewage treatment device, which is characterized in that a treatment device body is divided into a primary contact oxidation tank, a secondary contact oxidation tank and a settling tank, wherein the primary contact oxidation tank is communicated with the secondary contact oxidation tank, the secondary contact oxidation tank is communicated with the settling tank, the primary contact oxidation tank with a primary tank aeration pipe inside is connected with a sewage input pipe, a secondary tank aeration pipe and soft filling materials are arranged inside the secondary contact oxidation tank, and a settling tank foldback pipe is positioned inside the settling tank. Besides, a membrane bioreaction tank is separately arranged inside the treatment device body, and a membrane tank aeration pipe, both a membrane tank foldback pipe and a filter membrane group are mounted inside the membrane bioreaction tank. Further, the settling tank is communicated with the membrane bioreaction tank, and the filter membrane group is used for extracting clean water. The method for treating domestic sewage has the advantages of good quality of discharged water, less quantity of remained sludge, which is capable of meeting strict discharge requirements and widely applied to domestic sewage treatment systems on ships or on land.
Description
Technical field
The utility model relates to technical field of sewage, the treatment unit of particularly a kind of boats and ships or land sanitary sewage.
Background technology
Increase, quickening of urbanization process and socioeconomic fast development along with population, the quantity discharged of sanitary sewage is increasing, and sanitary sewage discharging has become the obstacle that serious obstruction Economic development and people's quality of life improve to environment damage and the shortage of water resources that therefore brings.For this reason, the also former effective way of being determined to make great efforts to seek sewage recycling that does not have of people, and by formulating various international conventioies, emission standard limits and improving the emission request of sanitary sewage.
With regard to the discharging of marine ships sanitary sewage; subordinate Marine Environmental Protection Committee of International Maritime Organizaton of United Nations; emission standard to promulgation on December 3rd, 1976: SS ≯ 50mg/l; BOD5 ≯ 50mg/l; coliform ≯ 250/100ml; chlorine residue is low as far as possible; indexs such as no quantitative criterion have carried out significantly adjusting; 13 days October in 2006 after 30 years is tighter one times with the emission standard of IMO MEPC.159 (55) resolution promulgation: SS ≯ 35mg/l; BOD5 ≯ 25mg/l; CODcr ≯ the 125mg/l of former no standard, coliform ≯ 100/100ml, chlorine residue ≯ 0.5mg/l.This emission standard shows human resolution to marine environmental protection once more, also makes to use traditional marine sewage treatment system will all can't adapt to the emission request of strictness like this.
Obviously, traditional sewage water treatment method can not satisfy the high request of modern pollution exhaust criteria fully.Especially for marine ships, restriction because of condition on its ship, the cabin space is narrow and small, wave, tilt, harsh environmental conditions such as vibration, particularly the design of treatment unit is given in the restriction of service clearance, and installation and maintenance have all brought inconvenience, traditional sewage treatment process and treatment unit, not thorough to sewage disposal, even BOD
5Can reach requirement, COD
CrStill can not reach requirement.Traditional sewage water treatment method not only can not satisfy the processing requirements of sanitary sewage on the ship, can not satisfy land sanitary sewage emission request well equally.
The treatment process of domestic sewage resource roughly has at present: sewage water treatment methods such as biochemical treatment process, physicochemical treatment method and electrochemical treatment method, because that biochemical processing method and treatment unit thereof have is simple in structure, good purification, dosing reach the low advantage of running cost less, and becomes the most generally sanitary sewage disposal approach of approval.This treatment process is to set up and keep the suitable growth condition of aerobic bacteria by oxygenation, utilize this microbial population to come organism in the digest and decompose sewage, make it to generate the carbonic acid gas and the water of environmental sound, purify waste water with this, and microorganism is also bred in this process.Its concrete technical process is: sewage enters into aerate cabinet through water inlet pipe, under the situation of continuous bubbling air, rely on dissolved oxygen to clear up organism, aerobic bacteria is at this digest and decompose organism, the carbon that is contained in the mud, oxygen, hydrogen, nitrogen is mostly changed into carbonic acid gas and water and generates new cell by aerobic bacteria, carbonic acid gas is overflowed by escape vents, mixed solution enters into the bio-contact oxidation cabinet after coarse strainer filters afterwards, the soft-filler of some amount is housed in this oxidation cabinet, utilize microbial bacteria own in the sewage, aeration through certain hour, cultivate and make it to breed into rapidly certain active aerobic bacteria, aerobic bacteria continues to absorb organism and the oxygen in the sewage, carry out bio-oxidation, decompose, a part generates carbonic acid gas, water and inorganics, another part then generates new certain active microbial film that has on filler, continue the organism in the degradation of sewage, enter the precipitation sterilizing-cabinet then, active sludge in the sanitary sewage is deposited in the bottom of sump tank, by the blank pipe that leads to the bottom with its lifting and return aerate cabinet, simultaneously the sanitary sewage clear liquid after purifying treatment flows into disinfection cavity, and is added by pump of constant delivery type and a certain amount ofly to contain the chlorine solution disinfection and discharge.
Correspondingly, adopt the treatment unit of above-mentioned domestic sewage processing method, include aerate cabinet, bio-contact oxidation cabinet and precipitation sterilizing-cabinet, be connected with the sewage input tube on the aerate cabinet, be communicated with macerator pump between aerate cabinet and the bio-contact oxidation cabinet, between bio-contact oxidation cabinet and the sump tank suction pump is housed, be communicated with delivery pipe and emptying pump on the precipitation sterilizing-cabinet, aerator pump leads to aerate cabinet and bio-contact oxidation cabinet respectively, so that in aerate cabinet and bio-contact oxidation cabinet, charge into air, and make the aerobic bacteria growth and breeding and clear up organism in the mud.
Existing such waste disposal plant, make the organism in the mud obtain clearing up to a certain degree, mud is subtracted appearance, decrement effectively, reduced the biomass that outwards discharges in the whole biological treatment system, improved the water quality of discharge water to a certain extent, reduced the pollution of sewage environment and water resources.But still there are many deficiencies in existing this treatment unit: at first, this treatment unit is not thorough to the processing of sewage, even satisfy the BOD in the sanitary sewage emission standard
5Requirement but can't reach COD
CrEmission request.The second, the sump tank outwards surplus sludge volume and the peculiar smell of discharging still can not reach desirable requirement, even will spend suitable expense excess sludge is carried out subsequent disposal, seems very uneconomical, does not also give full play to the maximum efficiency of sewage biochemical treatment process.The 3rd, in traditional continuous aeration process, make the thread fungus excessive multiplication, thereby cause the expansion of mud, and expansible mud will inevitably be taken out of with drainage water again, causes the repeated contamination of drainage water to exceed standard, particularly the ammonia nitrogen index exceeding standard is serious.
The utility model content
At the above-mentioned deficiency of existing in prior technology, technical problem to be solved in the utility model provides a kind of multi-stage biochemical domestic sewage treatment unit, it guarantees effectively that not only the discharging water quality after its purifying treatment is good, and surplus sludge volume is few, can satisfy strict emission control standards; And technical process is reasonable, and treatment effect is stable.
In order to solve the problems of the technologies described above, multi-stage biochemical domestic sewage treatment unit of the present utility model comprises the treatment unit body, divides in this treatment unit body to be separated with one-level catalytic oxidation cabinet, two-stage biological contact oxidation cabinet and sump tank; Described one-level catalytic oxidation cabinet is connected with the two-stage biological contact oxidation cabinet, and the two-stage biological contact oxidation cabinet is connected with sump tank; The one-level catalytic oxidation is connected with the sewage input tube cashier's office in a shop, and also is provided with one-level cabinet aeration tube in this one-level catalytic oxidation cabinet; Be provided with secondary cabinet aeration tube and soft-filler in the two-stage biological contact oxidation cabinet; Be provided with sump tank foldback pipe in the described sump tank; Also separate in the described treatment unit body and be provided with the membrane biological reaction cabinet, be provided with film cabinet aeration tube, film cabinet foldback pipe and filter membrane group in this membrane biological reaction cabinet, described sump tank is connected with this membrane biological reaction cabinet; Described filter membrane group extraction clear water output leads to vacuum pump.
Biochemical domestic sewage treatment unit of the present utility model makes this treatment unit have following significant advantage owing to adopted the aeration aerating in the one-level catalytic oxidation cabinet, the biomembrance process of two-stage biological contact oxidation cabinet, the mud-water separation of sump tank and the film of membrane biological reaction cabinet to hold back multistage sewage treatment structures such as processing:
At first, sanitary sewage enters into one-level catalytic oxidation cabinet, because bubbling air in this grade catalytic oxidation cabinet constantly, utilizing to exist in the cabinet relies on dissolved oxygen to clear up organic aerobic bacteria, common contained compositions such as carbon, oxygen, hydrogen and nitrogen are converted into carbonic acid gas and water in most of sewage and make, and generate new cell.Sanitary sewage is fed to again in the two-stage biological contact oxidation cabinet after being handled by aeration, and be provided with soft-filler in this oxidation cabinet, soft-filler is floating shape at the water surface, microorganism can be grown on the soft-filler and form microbial film, this microbial film further absorption is cleared up organism, and most of protozoon and metazoan in the sanitary sewage are lodged in the microbial film, and can breed rapidly becomes certain active aerobic bacteria, aerobic bacteria continues by absorbing organism and the oxygen in the sewage, carry out bio-oxidation, decompose, a part generates carbonic acid gas, water and inorganics, another part then generates new certain active microbial film that has on filler, continue the organism in the degradation of sewage.Sump tank carries out mud-water separation again.And the mud in the sump tank intermittently is returned in the one-level catalytic oxidation cabinet continues digest and decompose.In this process mud by multistage, clear up organism repeatedly, obtained comparatively fully degraded, organic removal rate is higher, technical process is reasonable, surplus sludge volume is few.
The second, in this treatment unit, especially adopted the film biologic treating technique of membrane biological reaction cabinet, this device can utilize the crown_interception of film to improve sludge concentration in the reaction cabinet dexterously, increase sludge retention time, help the growth of nitrobacteria in the system, improve the removal effect and the pollutants removal rate of ammonia nitrogen greatly.The crown_interception of film has also improved effluent quality greatly simultaneously, removes bacterium and virus significantly, makes the arrangement treatment system have extremely strong dirt processing power, has satisfied the BOD of strict emission standard fully
5And COD
CrRequirement.
The 3rd, also because in this treatment unit, can be implemented in the work of treatment process filter membrane group in the biological cabinet of film is carried out intermittent suction and continuous aeration, when stopping the film group aspirated, the caused current of continuous aeration stir and film are adhered to dirt generation shearing action, make the film surface deposits come off automatically, realized on-line cleaning to the film group, the working flux and the work effect that have not only kept film, and alleviating the workload that artificial rust cleans greatly, this intermittent suction has fundamentally solved impassable technology barrier in the film cleaning.
The 4th, owing to can adopt aeration aerating intermittently at two-stage biological contact oxidation cabinet and membrane biological reaction cabinet, formed aerobic-anoxybiotic treatment effect, not only overcome the thread fungus excessive multiplication in the traditional technology, caused sludge bulking is taken out of with water and is caused discharge water to exceed standard, and have the treatment effect of nitrification and denitrification, efficiently solve the denitrogenation dephosphorizing problem.
Five, because the film crown_interception in the membrane biological reaction cabinet, realized mud-water separation completely, thereby good effluent quality and higher sludge concentration have been guaranteed, and bigger organic loading and sludge concentration, the bio-reactor volume is diminished, the multiprocessing cabinet is arranged in the treatment unit body mutually separatedly in addition, makes the very reasonable compactness of one-piece construction.
Description of drawings
Following structure the drawings and specific embodiments are described in further detail the utility model.
Fig. 1 is the structure general flow chart of a kind of embodiment of the utility model.
Fig. 2 is a schematic construction sectional view of realizing a kind of concrete treatment unit of flow process shown in Figure 1.
Fig. 3 is the structural representation of A-A section in the structure shown in Figure 2.
Fig. 4 is the structural representation of B-B section in the structure shown in Figure 2.
Fig. 5 is the structural representation of C-C section in the structure shown in Figure 2.
Fig. 6 is the structural representation of D-D section in the structure shown in Figure 2.
Embodiment
As shown in Figure 1, treatment unit body 2 is separated into level Four such as one-level catalytic oxidation cabinet 3, two-stage biological contact oxidation cabinet 8, sump tank 17 and membrane biological reaction cabinet 10 and handles cabinet.In one-level catalytic oxidation cabinet 3, be provided with one-level cabinet aeration tube 1.Be provided with secondary cabinet aeration tube 24 and soft-filler 5 in two-stage biological contact oxidation cabinet 8, this soft-filler 5 adopts common materials such as vinylon, nylon wire.In sump tank 17, be provided with sump tank foldback pipe 18, in membrane biological reaction cabinet 10, be provided with film cabinet aeration tube 22, film cabinet foldback pipe 21 and filter membrane group 13.Top position at one-level catalytic oxidation cabinet 3 is connected with sewage input tube 6, this one-level catalytic oxidation cabinet 3 is connected with two-stage biological contact oxidation cabinet 8 through macerator pump 25, between one-level catalytic oxidation cabinet 3 and two-stage biological contact oxidation cabinet 8, also be provided with filter screen 29 (as shown in Figure 3), diffuse in mud floating block in the two-stage biological contact oxidation cabinet 8 with elimination.Two-stage biological contact oxidation cabinet 8 is connected with sump tank 17 by supernatant liquor transfer lime 12, and 17 of sump tanks are connected with membrane biological reaction cabinet 10 by clear liquor transfer lime 14.The extraction water outlet of the filter membrane group 13 in the membrane biological reaction cabinet 10 is connected with vacuum pump 16, and vacuum pump 16 exits are communicated with sterilizer 26, and the water outlet of this sterilizer 26 connects to delivery pipe 28 through under meter 27.One-level cabinet aeration tube 1, secondary cabinet aeration tube 8 and film cabinet aeration tube 22 pipeline by separately respectively are connected with aerator pump 7, and this aerator pump 7 can be universal blower.Be communicated with dosing pump 9 in membrane biological reaction cabinet 10 top positions.Lifting air pump 11 is through each self-corresponding magnetic valve and sump tank promotes tracheae 15 and film cabinet lifting tracheae 20 leads in precipitation foldback pipe 18 and the film cabinet foldback pipe 21.
During work, sanitary sewage is imported in the one-level catalytic oxidation cabinet 3 through sewage input tube 6, the one-level cabinet aeration tube 1 that is arranged in this cabinet constantly charges into air to the cabinet sanitary sewage, in sewage, form various micro-bubbles, and cause the turbulent flow of water, thereby reach airborne oxygen is dissolved in purpose in the sewage, form aeration aerating, make activated sludge digestion decompose organism in the sewage sewage.Sanitary sewage in the one-level catalytic oxidation cabinet behind aeration is transported in the two-stage biological contact oxidation cabinet 8 by the pulverizing of macerator pump 25, secondary cabinet aeration tube 24 is the sanitary sewage aeration aerating in the secondary cabinet off and on, this intermittent process comprises entering of carrying out successively, aeration, precipitation, discharging and leisure, forms aerobic, anoxic effect; Meanwhile, form on the soft-filler 5 in two-stage biological contact oxidation cabinet 8 and have certain active microbial film, this has not only further strengthened itself and organic contact area, and makes it to suspend in water to sink.Supernatant liquor in the two-stage biological contact oxidation cabinet 8 is delivered to sump tank 17 through supernatant liquor transfer lime 12, be equipped with hard filler 30 in this sump tank 17, to quicken the precipitation and the mud-water separation of supernatant liquor, precipitating sludge in the sump tank 17 is off and on to one-level catalytic oxidation cabinet 3 foldbacks, and this foldback time at intermittence looks sewage load and treatment condition are set as the case may be.Clear liquor in the sump tank 17 is delivered in the membrane biological reaction cabinet 10 through clear liquor transfer lime 14, in this membrane biological reaction cabinet 10, preestablish low-water line, this low-water line should be positioned at the above certain altitude in filter membrane group 13 tops, the real work situation that this height should be looked treatment unit film group total height 1/6～1/3 between select, this moment best results.
When the water level in the membrane biological reaction cabinet 10 when predetermined low-water line is above, 16 pairs of filter membrane groups 13 of vacuum pump are aspirated with gap, as aspirate 12min, stop to aspirate 2min, through a large amount of analysis of experiments, data contrast, suction time and the ratio that stops suction time selecting 4～12: between 1, and best results, also rationally appropriate to the cleaning of membrane module, film cabinet aeration tube 22 aeration aerating in cabinet continuously during this intermittent suction.When water intake velocity and suction rate of extraction make water level in the membrane biological reaction cabinet 10 be lower than predetermined low-water line, film cabinet aeration tube 22 stops to charge into air in cabinet, film cabinet foldback pipe 21 this moment foldback sewage in one-level catalytic oxidation cabinet 3 off and on, foldback sewage is further cleared up in one-level catalytic oxidation cabinet, as foldback 30min, stop foldback 2.5min, through analysis of experiments, data contrast, the foldback selection of time is between 20min～40min, and the ratio of the foldback time of foldback sewage and the foldback time that stops is 12～18: 1 the most effectively.
When whole Sewage treatment systems quit work, macerator pump 25 can be kept discontinuous operation, to keep the aerobic bacteria certain activity.When this waste disposal plant is stated from the boats and ships, and boats and ships navigate by water to high sea etc. when allowing direct discharge areas, or meet by land when allowing in line condition, can adopt sequence batch (to dispose of sewage, and the preface batch processing water in the sump tank is directly discharged.Membrane biological reaction cabinet 10 quits work at this moment, can prolong the work-ing life of permeable membrane level like this.
In order to prolong the working efficiency of membrane module in the membrane biological reaction cabinet, keep membrane flux, prevent that film from polluting, should regularly carry out matting to membrane module, during matting, at first make this film cabinet and other chamber isolated, add clean-out system by dosing pump 9 membrane module is carried out soaking and washing.This treatment unit adopts on-line cleaning mode, makes the automatic cleaning of film group become possibility, and not only cleaning performance is good, prolongs the work-ing life of film, and reduces the cleaning amount greatly, has use, advantage easy to maintenance.
The keying of various macerator pumps, emptying pump, vacuum pump, dosing pump and many magnetic valves in this treatment unit is by the PLC time variable control of routine or adopt corresponding electrical control cabinet control, and each transfer lime is also looked concrete service condition with serial connection mode adjunction transferpump.
As shown in Figure 2, treatment unit body 2 adopts horizontal cylindrical structure, elipse head is adopted at the two ends of this horizontal cylinder, this structure not only pressurized is reasonable, avoids the dead angle, and according to fluid mechanics principle, cylindrical structure helps reacting the interior good turbulent fluctuation of mixed solution, keep suspended state, reduce the mud granule that causes because of shearing and crack, and improve the rate of oxygenation of aerator.Treatment unit body 2 is separated into one-level catalytic oxidation cabinet 3, two-stage biological contact oxidation cabinet 8, membrane biological reaction cabinet 10 and sump tank 17 by one-level cabinet dividing plate 4, secondary cabinet dividing plate 23 and film cabinet dividing plate 19 successively with body.Sump tank 17 is arranged at the elipse head place of body end, helps forming the funnel type bottom of sump tank, with accelerate precipitation.Owing to consider locus in the cabinet, film cabinet foldback pipe 21 passes wallboard in the two-stage biological contact oxidation cabinet 8 and extend in the membrane biological reaction cabinet 10.The sump tank that is communicated with lifting air pump 11 promotes tracheae 15, its bottom bending up extend in the sump tank foldback pipe 18, when sump tank promoted tracheae 15 to sump tank foldback pipe 18 suction air, the lower end suction inlet of foldback pipe 18 produced negative pressure and draws throw out.Film cabinet foldback pipe 21 and film cabinet riser tube 20 have same principle and effect.
As shown in Figure 3, the lower position in one-level catalytic oxidation cabinet 3 is provided with one-level cabinet aeration tube 1, and this one-level cabinet aeration tube 1 is connected with aerator pump 7 by tracheae, and this aerator pump 7 adopts general centrifugal blower, makes it to constitute the blast aeration structure.Upper position at one-level cabinet dividing plate 4 has manhole, is covered with filter screen 29 on this manhole.
As shown in Figure 4, be respectively equipped with secondary cabinet aeration tube 24 and soft-filler 5 in two-stage biological contact oxidation cabinet 8, this soft-filler 5 adopts materials such as vinylon or nylon wire, the certain distance in space between every string flexible material.Secondary cabinet aeration tube 24 also is communicated with aerator pump 7 by tracheae, constitutes the blast aeration structure.
As shown in Figure 5, be provided with film cabinet aeration tube 22 and filter membrane group 13 in the membrane biological reaction cabinet 10.Film cabinet aeration tube 22 connects to aerator pump 7 by tracheae and magnetic valve.The filter membrane of filter membrane group 13 adopts hollow-fibre membrane, can certainly be microfiltration membrane and ultra-filtration membranes such as tubular membrane, and the aperture of general film should be chosen between 0.1～0.4um.One-level cabinet aeration tube 1, secondary cabinet aeration tube 24 and film cabinet aeration tube 22 can also lead to aerator pump separately respectively, or also connect to an aerator pump in twos.
As shown in Figure 6, in sump tank 17, be provided with precipitation foldback pipe 18, be positioned at the water-in of sump tank and be provided with hard filler 30, this hard filler 30 helps the sedimentation of accelerate sludge particulate, and its material adopts general equipment such as PVC inclined tube, the epoxy paper wasp nest of cutting back, the material of making pottery.
Claims (10)
1, a kind of multi-stage biochemical domestic sewage treatment unit comprises treatment unit body (2), divides in this treatment unit body (2) to be separated with one-level catalytic oxidation cabinet (3), two-stage biological contact oxidation cabinet (8) and sump tank (17); Described one-level catalytic oxidation cabinet (3) is connected with two-stage biological contact oxidation cabinet (8), and two-stage biological contact oxidation cabinet (8) is connected with sump tank (17); Be connected with sewage input tube (6) on the one-level catalytic oxidation cabinet (3), and also be provided with one-level cabinet aeration tube (1) in this one-level catalytic oxidation cabinet (3); Be provided with secondary cabinet aeration tube (24) and soft-filler (5) in the two-stage biological contact oxidation cabinet (8); Be provided with sump tank foldback pipe (18) in the described sump tank (17); It is characterized in that: also separate in the described treatment unit body (2) and be provided with membrane biological reaction cabinet (10), be provided with film cabinet aeration tube (22), film cabinet foldback pipe (21) and filter membrane group (13) in this membrane biological reaction cabinet (10), described sump tank (17) is connected with this membrane biological reaction cabinet (10); Described filter membrane group (13) extraction clear water output leads to vacuum pump (16).
2, waste disposal plant according to claim 1, it is characterized in that: described one-level catalytic oxidation cabinet (3) is connected with two-stage biological contact oxidation cabinet (8) through macerator pump (25), also is provided with filter screen (29) between one-level catalytic oxidation cabinet (3) and two-stage biological contact oxidation cabinet (8).
3, waste disposal plant according to claim 1 is characterized in that: described one-level cabinet aeration tube (1), secondary cabinet aeration tube (8) and film cabinet aeration tube (22) are connected with aerator pump (7).
4,, waste disposal plant according to claim 1, it is characterized in that: be provided with hard filler (30) in the described sump tank (17).
5, waste disposal plant according to claim 1 is characterized in that: promote air pump (11) in each self-corresponding magnetic valve leads to sump tank foldback pipe (18) and film cabinet foldback pipe (21) respectively.
6, waste disposal plant according to claim 1 is characterized in that: described filter membrane group (13) assembly adopts hollow-fibre membrane or tubular membrane.
7, waste disposal plant according to claim 1 is characterized in that: be communicated with dosing pump (9) on the described membrane biological reaction cabinet (10).
8, waste disposal plant according to claim 1 is characterized in that: described vacuum pump (16) exit that is communicated with filter membrane group (13) is communicated with sterilizer (26), and the water outlet of this sterilizer (26) connects to delivery pipe (28) through under meter (27).
9, waste disposal plant according to claim 8 is characterized in that: described sterilizer (26) is ultraviolet disinfector, ozonateur or chlorine-containing disinfecting device.
10, according to each described waste disposal plant among the claim 1-9, it is characterized in that: described treatment unit body (2) adopts horizontal cylindrical structure, and elipse head is adopted at the two ends of this horizontal cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201602658U CN201321417Y (en) | 2008-10-07 | 2008-10-07 | Multi-level biochemical domestic sewage treatment device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2008201602658U CN201321417Y (en) | 2008-10-07 | 2008-10-07 | Multi-level biochemical domestic sewage treatment device |
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| CN201321417Y true CN201321417Y (en) | 2009-10-07 |
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| CNU2008201602658U Expired - Fee Related CN201321417Y (en) | 2008-10-07 | 2008-10-07 | Multi-level biochemical domestic sewage treatment device |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102101748A (en) * | 2011-04-08 | 2011-06-22 | 中国人民解放军后勤工程学院 | Integrated ship wastewater treatment device |
| CN102050545B (en) * | 2009-10-30 | 2012-06-20 | 武汉金鼎机电设备有限公司 | Ship domestic sewage treatment device with pre-separation tank |
| CN102603059A (en) * | 2012-03-29 | 2012-07-25 | 深圳清华大学研究院 | Extraction membrane bioreactor and sewage processing method thereof |
| CN103387312A (en) * | 2013-07-17 | 2013-11-13 | 滕新君 | Multilevel biological contact oxidation reactor sewage treatment device |
| CN103539323A (en) * | 2013-11-13 | 2014-01-29 | 东台市东方船舶装配有限公司 | Electric flocculation membrane bioreactor |
| CN105084676A (en) * | 2015-09-11 | 2015-11-25 | 苏州中晟环境修复有限公司 | Buried micropower domestic sewage treatment facility and technique |
-
2008
- 2008-10-07 CN CNU2008201602658U patent/CN201321417Y/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102050545B (en) * | 2009-10-30 | 2012-06-20 | 武汉金鼎机电设备有限公司 | Ship domestic sewage treatment device with pre-separation tank |
| CN102101748A (en) * | 2011-04-08 | 2011-06-22 | 中国人民解放军后勤工程学院 | Integrated ship wastewater treatment device |
| CN102101748B (en) * | 2011-04-08 | 2012-05-30 | 中国人民解放军后勤工程学院 | Integrated ship wastewater treatment device |
| CN102603059A (en) * | 2012-03-29 | 2012-07-25 | 深圳清华大学研究院 | Extraction membrane bioreactor and sewage processing method thereof |
| CN102603059B (en) * | 2012-03-29 | 2013-08-14 | 深圳清华大学研究院 | Extraction membrane bioreactor and sewage processing method thereof |
| CN103387312A (en) * | 2013-07-17 | 2013-11-13 | 滕新君 | Multilevel biological contact oxidation reactor sewage treatment device |
| CN103387312B (en) * | 2013-07-17 | 2015-08-05 | 滕新君 | Multi-stage biological contact oxidation reactor sewage disposal device |
| CN103539323A (en) * | 2013-11-13 | 2014-01-29 | 东台市东方船舶装配有限公司 | Electric flocculation membrane bioreactor |
| CN105084676A (en) * | 2015-09-11 | 2015-11-25 | 苏州中晟环境修复有限公司 | Buried micropower domestic sewage treatment facility and technique |
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| C14 | Grant of patent or utility model | ||
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| 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: 20091007 Termination date: 20171007 |