CN204607801U - The advanced sewage treatment system of a kind of cities and towns and industrial park - Google Patents
The advanced sewage treatment system of a kind of cities and towns and industrial park Download PDFInfo
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- CN204607801U CN204607801U CN201520137570.5U CN201520137570U CN204607801U CN 204607801 U CN204607801 U CN 204607801U CN 201520137570 U CN201520137570 U CN 201520137570U CN 204607801 U CN204607801 U CN 204607801U
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Abstract
The utility model discloses the advanced sewage treatment system of a kind of cities and towns and industrial park, comprise the ozone contact reaction device, the BAF that connect successively with structures connecting tube, denitrification deep-bed filter and disinfecting tank; Also have gas blower, backwash pump, carbon source throwing device, polymerize aluminum chloride throwing device and chlorine throwing device.In whole treatment process, ozone contact reaction device plays oxidation difficult degradation macromolecule organic, and becoming difficult degradation macromolecule organic is readily biodegradable low molecule organic matter, improves the effect of sewage B/C.BAF utilizes high density aerobic microbiological, BOD, COD in degradation of sewage, oxidation ammonia nitrogen.Denitrification deep-bed filter can maintain high density obligate denitrifying bacteria, carries out denitrification denitrogenation to effluent of aeration biological filter.Disinfecting tank can ensure that sewage effluent microbiological indicator is up to standard.This advanced sewage treatment system can wide scope be promoted on a large scale, and investment rationally, and running cost is low.
Description
Technical field
The utility model relates to a kind of advanced sewage treatment system, particularly relates to a kind of advanced sewage treatment system being applicable to cities and towns and industrial park.
Background technology
At present, the technique for advanced treatment of wastewater is a lot, but carries mark transformation and the sewage work containing Persistent organic pollutants for existing water treatment plant, lack a set of can large-scale promotion, technical feasibility, economical rationality carry mark reforming technology.Existing deep treatment method and technique are substantially as follows.
(1) membrane filtration technique, mainly contains ultrafiltration, micro-filtration, or two film (ultrafiltration, micro-filtration+reverse osmosis membrane) treatment process.Adopt membrane filtration process can ensure that membrane filtration water outlet reaches high standard emission request, be applicable to the water treatment occasion of reuse requirement.But propose mark transformation on a large scale for Sewage Plant, filter because this technique is just simple, the total amount of pollutant cannot be cut down, and membrane filtration produces dense water cannot reach requirement, therefore this technique is not suitable for carrying mark reforming technology as Sewage Plant.
(2) (be called for short: MBR), the method utilizes its effective crown_interception, can retain generation cycle longer microorganism, nitrification effect is obvious, provides possibility, can realize deep purification of waste water deep phosphorous removal denitrogenation for membrane bioreactor.For the industrial sewage containing Recalcitrant chemicals, MBR reactor cannot ensure that water outlet COD is up to standard; Because the expensive of membrane module and life-span are shorter, not only construction investment is high, and needs frequently to change membrane module, and running cost is high, and therefore, the method is at 100,000 m
3it is larger that/d and above sewage work apply difficulty.
(3) ozone-BAC process, this technique has good removal efficiency for Persistent organic pollutants, also can extensively promote, and running cost is low at large-scale wastewater treatment plant.But this technique requires lower to TN and TP clearance.
At present, national water-deficient area especially north water deficit area, in order to improve urban water-body environmental quality, proposes the emission standard of increasingly stringent to works liquor in region, and primary discharge water-quality guideline is close to surface water IV class, V class standard requirement.Therefore, need to find a set of technical feasibility, economical rationality, can large-scale promotion for advanced treatment of wastewater carry mark transformation system.
Utility model content
For the deficiency that prior art exists, the utility model provides the advanced sewage treatment system of a kind of cities and towns and industrial park, and can wide scope promote on a large scale, and investment rationally, running cost is low.
In order to solve the problems of the technologies described above, a kind of cities and towns that the utility model proposes and the advanced sewage treatment system of industrial park, this system comprises the ozone contact reaction device, the BAF that connect successively with structures pipe connecting, denitrification deep-bed filter and disinfecting tank; Also include gas blower, backwash pump, carbon source throwing device, polymerize aluminum chloride throwing device and chlorine throwing device; The ozone pipeline that described ozone contact reaction device comprises ozone contact tank and is connected with ozonizer, described ozone contact tank is provided with water inlet pipe and water outlet, N road baffle is provided with successively to water outlet side from water inlet pipe side in order to described ozone contact tank is divided into N+1 section reaction tank in described ozone contact tank, the water port of N road baffle goes to upper and lower successively alternately arranges, thus in described ozone contact tank, define vertical folding streaming contact reacts route; Be provided with coil pipe turbulent flow reactor respectively in every section of reaction tank, described water inlet pipe is connected with the coil pipe turbulent flow reactor in first paragraph reaction tank, and described water outlet is arranged on N+1 section reaction tank; Be respectively equipped with a backflow water pipe in first paragraph to N section reaction tank, the top of described backflow water pipe extend in the section reaction tank of place, and described backflow water pipe is provided with a reflux pump respectively; The top of every section of reaction tank is provided with an ozone tail gas outlet respectively; Described water inlet pipe and the upper high speed water emitter being provided with a pair of inlet mouth in the junction with coil pipe turbulent flow reactor respectively of backflow water pipe, the high speed water emitter of described pair of inlet mouth comprises water-in, jetting orifice, ozone import and ozone tail gas import, the end of described backflow water pipe is connected with the water-in of the high speed water emitter of this Duan Houyi reaction tank, described ozone import is connected to described ozone pipeline, described ozone tail gas import is connected to ozone tail gas outlet, and the connection line that described ozone tail gas import and ozone tail gas export is provided with valve; Described BAF adopts the water flow mode of upper water distribution, lower water inlet, upper water-out, the parallel running of many lattice filter tank; Be provided with inlet passage successively from bottom to top in described BAF, water gallery is received in concrete filter, cobble supporting layer, granular carbon filter material layer, clear water zone and water outlet; The chemical feed pipe of described carbon source throwing device and polymerize aluminum chloride throwing device all leads to described water outlet receives water gallery; Described denitrification deep-bed filter adopts the water flow mode of upper water distribution, upper water inlet, lower water outlet, the parallel running of many lattice filter tank; Distributing flue, mixing zone, quartz sand filter media layer, cobble supporting layer, concrete filter and clear water zone is provided with from bottom to top successively in described denitrification deep-bed filter; Be respectively equipped with in described BAF and denitrification deep-bed filter and lead to airduct bottom pond from described gas blower; Be provided with multiple tracks traverse baffle in described disinfecting tank, the chemical feed pipe of described chlorine throwing device leads to described disinfecting tank; The water-in of described backwash pump is connected at the bottom of the pond of described disinfecting tank by pipeline, the water outlet of described backwash pump is connected at the bottom of the pond of described BAF and described denitrification deep-bed filter by pipeline in parallel; The water inlet pipe of described ozone contact reaction device is the water inlet pipe of system, and described disinfecting tank is provided with the rising pipe of whole system.
In the utility model, the concrete filter in described BAF and described denitrification deep-bed filter is furnished with short-handled filter head by perforation.
Compared with prior art, the beneficial effects of the utility model are:
In the utility model technical process, each technique objective monomer is clear and definite: ozone plays the effect of distortion Persistent organic pollutants; BAF plays the effect reducing readily biodegradable organism, nitration for removing ammonia nitrogen, plays adsorption for special hardly degraded organic substance and heavy metal simultaneously; Dark bed denitrification filter pool plays denitrification removing total nitrogen, filters the effect of dephosphorization, SS (suspended substance); Chlorine disinfecting tank can ensure microbiological indicator stably reaching standard.What the utility model both can be used as existing water treatment plant carries mark reforming technology, also can be used as the advanced treatment process containing Persistent organic pollutants sewage work.Recommend technology chain more than adopting, sewage effluent stably reaching standard can be ensured, and running cost is cheap, can large-scale promotion.
The utility model can be widely used in existing cities and towns and mark reforming technology is carried by industrial park sewage work, or the advanced treatment process of newly-merged university and industrial park sewage work.For the industrial enterprise's draining containing Persistent organic pollutants, when routine biochemistry treatment process cannot meet its drainage requirement or reuse technology requirement, native system is applicable equally.
Accompanying drawing explanation
Fig. 1 is the utility model advanced sewage treatment system artwork.
In figure:
1-ozone contact tank 2-BAF 3-denitrification deep-bed filter 4 disinfecting tank
5-ozonizer 6-backflow water pump 7-gas blower 8-backwash pump
9 carbon source throwing device 10-polymerize aluminum chloride throwing device 11 chlorine throwing device 12-water inlet pipes
13-rising pipe 14-rising pipe 15-ozone pipeline 16-airduct
17-chemical feed pipe 18-coil pipe turbulent flow reactor 20-high speed water emitter 21-valve
22-structures connecting tube
Embodiment
Be described in further detail technical solutions of the utility model below in conjunction with the drawings and specific embodiments, described specific embodiment only explains the utility model, not in order to limit the utility model.
As shown in Figure 1, the advanced sewage treatment system of a kind of cities and towns of the utility model and industrial park, comprises the ozone contact reaction device 1, the BAF 2 that connect successively with structures connecting tube 22, denitrification deep-bed filter 3 and disinfecting tank 4; Also include gas blower 7, backwash pump 8, carbon source throwing device 9, polymerize aluminum chloride throwing device 10 and chlorine throwing device 11.The water-in of described backwash pump 8 is connected at the bottom of the pond of described disinfecting tank 4 by pipeline, the water outlet of described backwash pump 8 is connected at the bottom of the pond of described BAF 2 and described denitrification deep-bed filter 3 by pipeline in parallel.
The ozone pipeline 15 that described ozone contact reaction device 1 comprises ozone contact tank 1 and is connected with ozonizer 5, described ozone contact tank 1 is provided with water inlet pipe 12 and rising pipe 13, be provided with N road baffle in described ozone contact tank 1 successively to rising pipe 13 side from water inlet pipe 12 side in order to described ozone contact tank 1 is divided into N+1 section reaction tank, described N road baffle is at least twice baffle.The water port of N road baffle goes to upper and lower successively alternately arranges, thus in described ozone contact tank 1, define vertical folding streaming contact reacts route; Be provided with coil pipe turbulent flow reactor 18 respectively in every section of reaction tank, described water inlet pipe 12 is connected with the coil pipe turbulent flow reactor 18 in first paragraph reaction tank, and described rising pipe 13 is arranged on N+1 section reaction tank; Be respectively equipped with a backflow water pipe 19 in first paragraph to N section reaction tank, the top of described backflow water pipe 19 extend in the section reaction tank of place, described backflow water pipe 19 is provided with respectively a reflux pump 6; The top of every section of reaction tank is provided with an ozone tail gas outlet respectively; Described water inlet pipe 12 and backflow water pipe 19 are positioned at the high speed water emitter 20 being provided with a pair of inlet mouth with the junction of coil pipe turbulent flow reactor 18 respectively, and the high speed water emitter 20 of described pair of inlet mouth is arranged on the pipeline section of close coil pipe turbulent flow reactor 18 on described water inlet pipe 12 or backflow water pipe 19.The high speed water emitter 20 of described pair of inlet mouth comprises water-in, jetting orifice, ozone import and ozone tail gas import; In the high speed water emitter 20 of described pair of inlet mouth, the bore of water-in is D
1, the bore of jetting orifice is D
2, the bore of ozone import is D
3, the bore of ozone tail gas import is D
4; Wherein, D
4≤ D
3< D
2< D
1.The end of described backflow water pipe 19 is connected with the water-in of the high speed water emitter 4 of this Duan Houyi reaction tank, described ozone import is connected to described ozone pipeline 15, described ozone tail gas import is connected to the ozone tail gas outlet of ozone contact tank top, and the connection line that described ozone tail gas import and ozone tail gas export is provided with valve 21.
Described BAF 2 adopts the water flow mode of upper water distribution, lower water inlet, upper water-out, the parallel running of many lattice filter tank; Be provided with inlet passage successively from bottom to top in described BAF 2, water gallery is received in concrete filter, cobble supporting layer, granular carbon filter material layer, clear water zone and water outlet; The chemical feed pipe of described carbon source throwing device 9 and polymerize aluminum chloride throwing device 10 all leads to described water outlet receives water gallery.
Described denitrification deep-bed filter 3 adopts the water flow mode of upper water distribution, upper water inlet, lower water outlet, the parallel running of many lattice filter tank; Distributing flue, mixing zone, quartz sand filter media layer, cobble supporting layer, concrete filter and clear water zone is provided with from bottom to top successively in described denitrification deep-bed filter 3.
Concrete filter in described BAF 2 and described denitrification deep-bed filter 3 is furnished with short-handled filter head by perforation.Be respectively equipped with in described BAF 2 and denitrification deep-bed filter 3 and lead to airduct 16 bottom pond from described gas blower 7.
Be provided with multiple tracks traverse baffle in described disinfecting tank 4, described multiple tracks baffle is at least twice baffle, and the chemical feed pipe of described chlorine throwing device 11 leads to described disinfecting tank 4.The water inlet pipe 12 of described ozone contact reaction device 1 is the water inlet pipe of system, and described disinfecting tank 4 is provided with the rising pipe 14 of whole system.
The utility model aims to provide a kind of technical feasibility, economical rationality, the sewerage advanced treatment process that can extensively promote, not only can be used as the advanced treatment of newly-merged university and industrial park sewage work, and be applicable to existing cities and towns and industrial park sewage work and propose mark transformation.
Ozone contact reaction device in the utility model mainly plays oxidation difficult degradation macromolecule organic in treatment process chain, and becoming difficult degradation macromolecule organic is readily biodegradable low molecule organic matter, improves the effect of sewage B/C ratio.Ozone contact tank wherein adopts the water flow mode of upper and lower baffling, design upper water-out.Ozone adds and adopts two inlet mouth water sprayer and coil pipe turbulent flow reactor, and multi-point adding, to improve the mass-transfer efficiency of ozone; Carry out recovery to tail gas to add simultaneously, ozone tail gas breaking plant can be omitted, make the utilization ratio of ozone reach 100%; Be combined with backflow water pump, multiple spot backflow sewage, accelerates the speed of reaction of ozone.The technological process of its ozone contact reaction is: ozone pipeline 15 is connected to ozonizer 5, and water inlet pipe 12 is connected to pending water source; The useful volume of described ozone contact tank 1 meets the minimal-contact time, division hop count N+1 >=3 of described ozone contact tank 1, in described ozone contact tank 1, ozone dosage is adjustable, and minimal-contact time and ozone dosage are determined according to the test of the pollutant emission standard of the rear water outlet of pollutant level in pending water source and process; During process, ozone gas is introduced into the coil pipe turbulent flow reactor 18 be arranged in ozone contact tank 1 in first paragraph reaction tank after being mixed with water inlet by multiple high speed water emitter 20 to carry out moisture and fully mixes, mixed water outlet continues to carry out contact at this section of reaction tank and mixes, then successively by second segment to N+1 section reaction tank; The reflux pump 6 of the reacted water of part by refluxing in this section of reaction tank on water pipe 19 in first paragraph to N section reaction tank, be back to the high speed water emitter 20 be connected with this backflow water pipe 19, and again carry out after moisture fully mixes, entering in the coil pipe turbulent flow reactor 18 in rear one section of reaction tank respectively by high speed water emitter 20 with the ozone gas entered from ozonizer 15, the sufficient ozone tail gas of unreacted of discharging from ozone contact tank 1 top; Till the chemical oxygen demand COD index of water outlet reaches set(ting)value, chemical oxygen demand COD emission standard at least will meet GB8978-1996 " integrated wastewater discharge standard ".
In the utility model, BAF mainly utilizes the aerobic oxidation effect of high-concentration biological in treatment process chain, BOD, COD in degradation of sewage, and oxidation ammonia nitrogen is nitric nitrogen.Wherein, granular carbon filtrate is adopted to replace haydite, the quartz sand filter media of traditional BAF, not only there is the bio-oxidation of traditional BAF and retain the effect of suspended solids, and for special hardly degraded organic substance and heavy metal, there is good adsorption.The design of this BAF adopts upper water distribution, lower water inlet, the water flow mode of upper water-out, the parallel running of many lattice filter tank.BAF body is followed successively by from bottom to top: inlet passage, concrete filter (on filter plate, short-handled filter head is arranged in perforation), the cobble supporting layer (supporting layer bottom even arranges boring aeration pipe) of thick 0.25m, particle diameter 2 ~ 16mm, the activated-carbon filter bed of material of thick 1.0m, particle diameter 2 ~ 4mm, clear water zone, water gallery is received in water outlet.During normal filtration, the remaining oxygen oxygen supply in ozone contact tank water outlet can be utilized; When oxygen amount is not enough, adopt gas blower by airduct to BAF oxygen supply, utilization is distributed in supporting layer bottom perforated aeration tube gas distribution.When certain lattice filter tank filtering velocity does not wherein meet the minimum filtering velocity of design, this single pond stops water inlet, and backwash pump 8 and gas blower 7 are combined and carried out back flushing to system, adopt short-handled filter head on concrete filter to carry out water distribution, gas distribution.
The filter bed of to be thickness the be 2.4m of the denitrification deep-bed filter in the utility model, anaerobic environment can be formed, grow denitrifying bacteria, in treatment process chain, utilize this denitrification deep-bed filter can maintain the characteristic of high density obligate denitrifying bacteria, denitrification denitrogenation is carried out to the nitric nitrogen of effluent of aeration biological filter; For improving the denitrification denitrogenation effect of system, often need to add carbon source; Meanwhile, when total phosphorus concentration of intaking is higher, by adding PB1 gene, utilizes the physics and chemistry filteration of denitrification deep-bed filter, carrying out chemical dephosphorization, and further removal system SS (suspended substance) concentration.The design of this denitrification deep-bed filter adopts upper water distribution, upper water inlet, the water flow mode of lower water outlet, the parallel running of many lattice filter tank.Pond body is followed successively by from top to bottom: distributing flue, mixing zone, the quartz sand filter media layer of thick 2.4m, particle diameter 2 ~ 8mm, the cobble supporting layer of thick 0.25m, particle diameter 4 ~ 16mm, concrete filter (on filter plate, short-handled filter head is arranged in perforation), clear water zone.When denitrification deep-bed filter normally runs, do not need aeration.When certain lattice filter tank filtering velocity does not wherein meet the minimum filtering velocity of design, this single pond stops water inlet, and backwash pump and gas blower are combined and carried out back flushing to system, adopt short-handled filter head on filter plate to carry out water distribution, gas distribution.
Disinfecting tank in the utility model plays the effect ensureing that sewage effluent microbiological indicator is up to standard in treatment process chain, recommends to adopt chlorine disinfectant, can add clorox, dioxide peroxide etc. in the utility model.
Although be described the utility model by reference to the accompanying drawings above; but the utility model is not limited to above-mentioned embodiment; above-mentioned embodiment is only schematic; instead of it is restrictive; those of ordinary skill in the art is under enlightenment of the present utility model; when not departing from the utility model aim, can also make a lot of distortion, these all belong within protection of the present utility model.
Claims (2)
1. the advanced sewage treatment system of cities and towns and industrial park, it is characterized in that: comprise the ozone contact reaction device, the BAF (2) that connect successively with structures connecting tube (22), denitrification deep-bed filter (3) and disinfecting tank (4); Also include gas blower (7), backwash pump (8), carbon source throwing device (9), polymerize aluminum chloride throwing device (10) and chlorine throwing device (11); The water-in of described backwash pump (8) is connected at the bottom of the pond of described disinfecting tank (4) by pipeline, the water outlet of described backwash pump (8) is connected at the bottom of the pond of described BAF (2) and described denitrification deep-bed filter (3) by pipeline in parallel;
The ozone pipeline (15) that described ozone contact reaction device (1) comprises ozone contact tank (1) and is connected with ozonizer (5), described ozone contact tank (1) is provided with water inlet pipe (12) and water outlet (13), N road baffle is provided with successively to water outlet (13) side from water inlet pipe (12) side in order to described ozone contact tank (1) is divided into N+1 section reaction tank in described ozone contact tank (1), the water port of N road baffle is presented successively, lower alternately layout, thus in described ozone contact tank (1), define vertical folding streaming contact reacts route, coil pipe turbulent flow reactor (18) is provided with respectively in every section of reaction tank, described water inlet pipe (12) is connected with the coil pipe turbulent flow reactor (18) in first paragraph reaction tank, and described water outlet (13) is arranged on N+1 section reaction tank, a backflow water pipe (19) is respectively equipped with in first paragraph to N section reaction tank, the top of described backflow water pipe (19) extend in the section reaction tank of place, and described backflow water pipe (19) is provided with a reflux pump (6) respectively, the top of every section of reaction tank is provided with an ozone tail gas outlet respectively, described water inlet pipe (12) and backflow water pipe (19) are positioned at the high speed water emitter (20) being provided with a pair of inlet mouth with the junction of coil pipe turbulent flow reactor (18) respectively, the high speed water emitter (20) of described pair of inlet mouth comprises water-in, jetting orifice, ozone import and ozone tail gas import, the end of described backflow water pipe (19) is connected with the water-in of the high speed water emitter (4) of this Duan Houyi reaction tank, described ozone import is connected to described ozone pipeline (15), described ozone tail gas import is connected to ozone tail gas outlet, the connection line that described ozone tail gas import and ozone tail gas export is provided with valve (21),
The water flow mode of water distribution in described BAF (2) employing, lower water inlet, upper water-out, the parallel running of many lattice filter tank; Described BAF is provided with inlet passage from bottom to top in (2) successively, and water gallery is received in concrete filter, cobble supporting layer, granular carbon filter material layer, clear water zone and water outlet; The chemical feed pipe of described carbon source throwing device (9) and polymerize aluminum chloride throwing device (10) all leads to described water outlet receives water gallery;
The water flow mode of water distribution in the employing of described denitrification deep-bed filter (3), upper water inlet, lower water outlet, the parallel running of many lattice filter tank; Distributing flue, mixing zone, quartz sand filter media layer, cobble supporting layer, concrete filter and clear water zone is provided with from bottom to top successively in described denitrification deep-bed filter (3);
Be respectively equipped with in described BAF (2) and denitrification deep-bed filter (3) and lead to airduct (16) bottom pond from described gas blower (7);
Described disinfecting tank is provided with multiple tracks traverse baffle in (4), and the chemical feed pipe of described chlorine throwing device (11) leads to described disinfecting tank (4);
The water inlet pipe that the water inlet pipe (12) of described ozone contact reaction device (1) is system, described disinfecting tank (4) is provided with the rising pipe (14) of whole system.
2. the advanced sewage treatment system of cities and towns and industrial park according to claim 1, it is characterized in that, the concrete filter in described BAF (2) and described denitrification deep-bed filter (3) is furnished with short-handled filter head by perforation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520137570.5U CN204607801U (en) | 2015-03-11 | 2015-03-11 | The advanced sewage treatment system of a kind of cities and towns and industrial park |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520137570.5U CN204607801U (en) | 2015-03-11 | 2015-03-11 | The advanced sewage treatment system of a kind of cities and towns and industrial park |
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| Publication Number | Publication Date |
|---|---|
| CN204607801U true CN204607801U (en) | 2015-09-02 |
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ID=53960372
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| CN201520137570.5U Withdrawn - After Issue CN204607801U (en) | 2015-03-11 | 2015-03-11 | The advanced sewage treatment system of a kind of cities and towns and industrial park |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104671616A (en) * | 2015-03-11 | 2015-06-03 | 天津市联合环保工程设计有限公司 | Advanced wastewater treatment system for cities and towns as well as industrial parks |
| CN105174623A (en) * | 2015-09-16 | 2015-12-23 | 潍坊沃华水处理设备有限公司 | MBR (membrane bioreactor) sewage treatment machine |
| CN105271616A (en) * | 2015-10-29 | 2016-01-27 | 广州乾峰环境治理工程有限公司 | System for deeply treating industrial wastewater through ozone combined aeration biological treatment |
| CN111977784A (en) * | 2020-08-21 | 2020-11-24 | 惠州市玮蓝环保科技有限公司 | Plug flow type aerobic biofilter and sewage treatment method |
| CN111977788A (en) * | 2020-08-21 | 2020-11-24 | 惠州市玮蓝环保科技有限公司 | Plug flow type anaerobic biological filter and use method thereof |
-
2015
- 2015-03-11 CN CN201520137570.5U patent/CN204607801U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104671616A (en) * | 2015-03-11 | 2015-06-03 | 天津市联合环保工程设计有限公司 | Advanced wastewater treatment system for cities and towns as well as industrial parks |
| CN105174623A (en) * | 2015-09-16 | 2015-12-23 | 潍坊沃华水处理设备有限公司 | MBR (membrane bioreactor) sewage treatment machine |
| CN105271616A (en) * | 2015-10-29 | 2016-01-27 | 广州乾峰环境治理工程有限公司 | System for deeply treating industrial wastewater through ozone combined aeration biological treatment |
| CN111977784A (en) * | 2020-08-21 | 2020-11-24 | 惠州市玮蓝环保科技有限公司 | Plug flow type aerobic biofilter and sewage treatment method |
| CN111977788A (en) * | 2020-08-21 | 2020-11-24 | 惠州市玮蓝环保科技有限公司 | Plug flow type anaerobic biological filter and use method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150902 Effective date of abandoning: 20160921 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |