AU2020100706A4 - A membrane bioreactor system for rural decentralized wastewater - Google Patents
A membrane bioreactor system for rural decentralized wastewater Download PDFInfo
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- AU2020100706A4 AU2020100706A4 AU2020100706A AU2020100706A AU2020100706A4 AU 2020100706 A4 AU2020100706 A4 AU 2020100706A4 AU 2020100706 A AU2020100706 A AU 2020100706A AU 2020100706 A AU2020100706 A AU 2020100706A AU 2020100706 A4 AU2020100706 A4 AU 2020100706A4
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/28—Anaerobic digestion processes
- C02F3/2853—Anaerobic digestion processes using anaerobic membrane bioreactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/145—Ultrafiltration
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1205—Particular type of activated sludge processes
- C02F3/121—Multistep treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1268—Membrane bioreactor systems
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/30—Aerobic and anaerobic processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/002—Grey water, e.g. from clothes washers, showers or dishwashers
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/005—Black water originating from toilets
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1236—Particular type of activated sludge installations
- C02F3/1242—Small compact installations for use in homes, apartment blocks, hotels or the like
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Microbiology (AREA)
- Chemical & Material Sciences (AREA)
- Biodiversity & Conservation Biology (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
With the development of rural economy and continuous improvement of
living standards, rural sewage pollution has gradually increased, and the
pollution area has gradually increased. The invention aims at the rural
decentralized domestic sewage, and develops a rural decentralized
integrated membrane bioreactor system. The invention is a hybrid of a
conventional biological treatment system and physical liquid-solid
separation using membrane filtration in one system, which not only
eliminates the need for secondary clarifiers, but also greatly improves the
solid-liquid separation efficiency and the biochemical reaction rate. The
invention combines a new type of ultrafiltration membrane technology
and biological simulation technology. According to the quality and
fluctuations of the water, using flate membrane, the membrane flux is
increased by more than 30%, and the contact angle is reduced to less than
70 degrees, which optimizes the energy consumption of the equipment
and reduces Remaining sludge. Recirculation is performed by air
stripping to convert the air energy into the kinetic energy of the reflux
liquid. The invention reduces the sludge return pump in the process, saves
30% energy consumption compared with the traditional process, and
reduces the equipment failure rate.
Domestic sewage
[Grille filtering
Adjust the pool
I Facultative
I reaction tank
MBR
treatment pool Aerationfan
Drainage
Figure 1
I2\
7 5
Figure 2
1
Description
Domestic sewage
[Grille filtering
Adjust the pool
I Facultative I reaction tank
MBR treatment pool Aerationfan
Drainage
Figure 1
I2\
7 5
Figure 2
A membrane bioreactor system for rural decentralized wastewater
treatment
This patent is in the field of sewage treatment in water treatment
technology, and particularly relates to a membrane organism reactor.
With the rapid improvement of urban sewage treatment rate, China has
established a relatively complete technical system and management
system for centralized sewage treatment, but there is still a large gap in
rural decentralized domestic sewage treatment. Foreign research on
decentralized rural sewage treatment has been carried out earlier.
Currently, 20% to 30% of the population in Europe and the United States
uses decentralized sewage treatment facilities, and 66% of the population
in Japan uses purification tank technology. Decentralized processing
technology has matured in these countries. However, China began to
explore and practice decentralized wastewater treatment technology in the
1980s. The constructed wetland, stabilization pond, trickling filter, and
Anaerobic-aerobic combination process has been studied and applied in
rural areas of China. With the introduction of "Action Plan for Prevention
and Control of Water Pollution" and "Three-year action plan for the improvement of rural human settlements", people are paying more and more attention to the decentralized sewage treatment in rural areas.
Carrying out the treatment of rural domestic sewage is to change the
current situation of disorderly discharge of rural domestic sewage and
improve the living conditions of farmers. It is an important task to
improve the living environment in rural areas, and it is also the key to
improving the water environment in river basins and regions.
At present, there are dozens of forms of decentralized rural sewage
treatment technologies in China, such as constructed wetlands, aerobic
biological contact oxidation processes, trickling filters, anaerobic biogas
digester treatment technologies, small secondary sewage treatment
devices, and membrane bioreactors. Constructed wetlands are artificial
ecosystems modeled on natural wetlands, using the triple synergy of
physical, chemical, and biological in the natural ecosystem to achieve the
purification of sewage. In the aerobic biological contact oxidation
treatment process, sewage flows through the filler with microorganisms
attached. During the contact with the filler, the organic pollutants in the
sewage are removed through the metabolism of the aerobic
microorganisms to achieve sewage purification. The trickling filter is a
biological treatment structure composed of crushed stone or plastic
product filler. By imitating the principle of natural ecosystem, the synergy of microorganisms, artificial fillers and biofilms is used to purify sewage.
Anaerobic biogas digester treatment technology uses human and animal
manure or crop straws to convert organic matter into methane and carbon
dioxide by anaerobic and facultative microorganisms under the condition
of hypoxia in the biogas digester. The small secondary sewage treatment
device uses a combination of physical and biological methods for sewage
treatment. Sewage first enters biological treatment such as anaerobic,
facultative or aerobic after passing through the grille, primary
sedimentation tank, and finally discharged through sedimentation.
Membrane Bioreactor (MBR, Membrane Bioreactor) is an efficient and
new sewage treatment technology formed by combining membrane
separation technology and activated sludge system. There are various
forms of decentralized sewage treatment technology in rural areas.
Therefore, how to scientifically choose a sewage treatment process, and
at the same time, based on the rural conditions, fully consider the
construction and development of surrounding towns and industrial areas,
formulate a suitable planning scheme deserves our attention. For more
developed and land-stressed areas, the research and development of
miniaturized integrated membrane bioreactor technology is particularly
important.
Therefore, this patent has developed a set of rural decentralized integrated membrane bioreactor system, including anaerobic tank, membrane bioreactor, clean-water reservoir, aeration blower, suction pump and splitter plates, and applied this system to China Regions such as Jiangsu and Zhejiang. The system not only has the technological advantages of the original membrane bioreactor, but also is convenient to use. It can carry out the evolutionary treatment of sewage from scattered households, and improves the flexibility of sewage treatment. Therefore, this system has an important role and promotional value for improving the quality of rural water environment in China.
MBR technology is suspension culture biological treatment (activated
sludge process) and the combination of membrane separation technology,
membrane separation technique to replace the two pond, in the traditional
activated sludge process, plays the biological treatment technology rely
on microorganisms (mixture) separated from the culture medium, and
microbes to insourcing stay in biochemical reaction pool, at the same
time ensure that basically out of the water does not contain microbes and
other suspended matter. The membrane bioreactor can effectively
overcome the limitation related to the sludge settling performance and
replace the secondary sedimentation tank. MBR can maintain a high
biomass concentration, usually 8 ~ lOg/L for MLSS, up to 10 ~ 15g/L, and 3 ~ 5g/L for MLSS in conventional activated sludge aeration tank.
Therefore, the footprint of MBR process is only 1/2 ~ 1/3 of that of
conventional treatment.
The sewage in the invention is led to the sewage treatment equipment
through the sewage collection pipeline, and the sewage is first filtered
through the grille and then sent to the regulating tank by the lifting pump,
and then continuously sent to the integrated sewage purification
equipment by the lifting pump.In integrated sewage purification
equipment in the pool of oxygen and the biochemical degradation, and
degradation of organic pollutants, the bottom aeration device, microbial
needed oxygen provided by the equipment inside the blower, system
through the mixture flow, use of denitrifying bacteria degradation of
ammonia nitrogen, water entering the MBR membrane pool further
degradation of filtering, spate separation, discharge standard after
discharge.
Figure 1 is technical route description.
Figure 2 is the flow diagram of the MBR process.
Figure 3 is the schematics design of our invention.
Principle
The Figure 1 illustrates a type of membrane bioreactor which consists of
an anaerobic tank 1, a membrane bioreactor tank 2, a clearwater holding
tank 3, an aerator 8, a suction pump 9,and and an isolation plate. The
anaerobic tank 1 and the membrane bioreactor tank 2 are isolated by an
isolation plate, and the membrane bioreactor tank 2 and the clearwater
holding tank 3 are isolated by an isolation plate. The anaerobic tank 1 is
provided with an anaerobic tank aeration pipe 7 and a water inlet pipe 12.
An MBR membrane module 11 is arranged in the membrane bioreactor
tank 2, and a membrane module aeration pipe 5 is arranged at the bottom
of the MBR membrane module 11. A clearwater holding tank 3 is inserted
with an outlet pipe 13. The anaerobic tank aeration pipe 7 and the
membrane module aeration pipe 5 control aeration by an aerator 8, and
the water outlet pipe 13 performs water outlet through a suction pump 9.
A sedimentation tank 4 is set on the other end of the water inlet pipe 12.
A feed pump 10 is set on the water inlet pipe 12.
An overflow port 6 is set near the top of the isolation plate between the
anaerobic tank 1 and the membrane biological reaction tank 2.
In the process of use, the membrane bioreactor is installed in a container and placed in the decentralized residence. The sewage is introduced into the sedimentation tank 4 through a pipeline for sedimentation, and then the precipitated sewage is sent to the anaerobic tank 1 for aeration through a water inlet pipe 12 by a feed pump 10, and then the aerated wastewater in the anaerobic tank 1 flows into the membrane bioreactor tank 2 through the overflow port 6, and the MBR membrane module 11 performs sewage purification treatment, and finally The treated sewage is pumped out by the suction pump 9 and sent to the clearwater holding tank 3 by the outlet pipe.
The anaerobic tank aeration pipe 7 is set to provide sufficient oxygen for
the anaerobic tank 1 . The setting of the membrane module aeration pipe
5 can facilitate the scouring of the fouling on the MBR membrane module
11, so that the MBR membrane module 11 can maintain stable and
effective sewage purification.
Procedure
The procedure of this invention is implemented as follows:
(1) The feed pump starts to feed water, and then the activated sludge,
which is taken from the nearby sewage treatment plant, is added to the
aerobic tank. The aeration period is 3 days, and the carbon source is
added at the same time.
(2) Observe the growth of activated sludge. When the concentration of
sludge in the aerobic tank reaches 2000-3000mg -L-1, the water will flow
out, and a certain amount of denitrifying bacteria will be added to the
anoxic tank to improve the nitrification reaction capacity of the system;
(3) The equipment enters and exits the water, replenishes the bacteria
at any time. When SV be maintained at about 30%, the installation
operates normally.
Results and discussion
Table 1 Characterization of the wastewater before and after treatment.
sample CODcr(mg-L-1) NH4 -N(mg-L- 1) TP(mg-L- 1) SS(mg-L- 1
) 1 Feed 813 57.9 11.3 120 Effluent 21 0.512 0.820 16 Removal efficiency% 97.4 99.1 92.7 86.7 2 Feed 243 60.1 10.4 108 Effluent 20 0.616 0.792 11 Removal efficiency% 91.8 99.0 92.4 89.8 3 Feed 481 136 21.7 142 Effluent 21 5.840 0.784 10 Removal efficiency% 95.6 95.7 96.4 93.0 4 Feed 142 42.4 6.54 67 Effluent 5 0.484 0.416 6 Removal efficiency% 96.5 98.9 93.6 91.0 Feed 465 91.2 16.7 85 Effluent 10 0.892 0.908 12 Removal efficiency% 97.8 99.0 94.6 85.9 6 Feed 129 52.6 5.23 63 Effluent 24 3.030 0.780 10 Removal efficiency% 81.4 94.2 85.1 84.1 Discharge standard(1B) 60 8(15) 1 20
Analysis
The process achieved good removal efficiency of 81.4%- 9 7 .8 % of CODcr,
94.2%-99.1% of NH 4 +-N, 85.1%-96.4% of TP, and 84.1%-93.0% of SS,
which allowed the effluent quality to meet the 1B standard (GB
18918-2002) (e.g., COD, NH4+-N, TP and SS no higher than 60, 8, 1, 20
mg-L-', respectively)
The study examined the performances of the integrated MBR for rural
wastewater reclamation. It was found that in the system 81.4%-97.8% of
CODcr, 94.2%-99.1% of NH 4+-N, 85.1%-96.4% of TP, and 84.1%-93.0%
of SS could be removed, and the treated water quality succeeded to meet
the 1B standard of Discharge standard of pollutants for municipal
wastewater treatment plant(GB 18918-2002). The MBR treatment
process provides stable and high quality product water and has low
emission amount of sludge. This integrated sewage purification
installation has its distinct advantages of high treatment efficiency, ease
of construction, and small footprint, thus saving land use and construction
costs, which is extremely important for rural areas where limited footprint
and financial issues exist. So this novel type of MBR is promising in the
foreseeable future.
Table 2 below shows the main parameters of this MBR Table 2 The main parameters of the installation:
Serial item factor remark
number
Integrated sewage Capacity:5-200ton-d-' ; Full- automatic PCL control, purification water pump and water level linkage control; Intelligent
installation alarm; No personnel required.
1 Integrated sewage The box material can be divided into carbon steel and
tank glass steel; Carbon steel needs to be anticorrosive paint:
epoxy coal asphalt paint. 2 MBR membrane Flat sheet membrane, membrane pore size: 0.1pm;
module Membrane material: polyvinylidene fluoride (PVDF);
water production: 400 -600L-p-'-d-'.
3 Centrifugal pump Self-priming centrifugal pump is selected according to the water production.
4 Vortex air pump The high-pressure vortex air pump is selected according to the required aeration of the membrane module.
Level controller Controlling the water level of the membrane pool and
the water level of the clearwater holding tank
6 Electronic control Full- automatic PCL control; Telemonitoring.
system
Claims (3)
1. A membrane bioreactor system for rural decentralized wastewater
treatment, characterized in that: the equipment has the characteristics of
miniaturization and integration, suitable for decentralized treatment of
rural sewage, and the quality of the effluent water is high, which can be
reused.
2. According to system of claim 1, wherein integrate new ultrafiltration
membrane technology and biological simulation technology; according to
the quality and fluctuations of the water, the use of flat membranes has
improved the membrane flux by more than 30%, and the contact angle
has been reduced to below 70 degrees, optimizing the energy
consumption of the equipment and the remaining pollution; very little
mud.
3. According to system of claim 1, wherein backflow can be carried out
by air stripping, which converts air energy into reflux liquid kinetic
energy, which reduces the sludge return pump in the process; this
technology saves 30% energy consumption compared with traditional
processes, and reduces equipment failure rate.
Figure 2 Figure 1
Figure 3
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU2020100706A AU2020100706A4 (en) | 2020-05-05 | 2020-05-05 | A membrane bioreactor system for rural decentralized wastewater |
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| Publication Number | Publication Date |
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| AU2020100706A4 true AU2020100706A4 (en) | 2020-06-18 |
Family
ID=71079457
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Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113307368A (en) * | 2021-05-27 | 2021-08-27 | 公安县佳源水务有限公司 | Backflow device used in oxidation ditch |
| CN113666576A (en) * | 2021-08-23 | 2021-11-19 | 武汉亦非凡建筑工程有限公司 | Ecological reconstruction method for rural domestic sewage discharge port |
| CN114163072A (en) * | 2021-11-26 | 2022-03-11 | 上海应用技术大学 | Reclaimed water recycling system capable of being switched to adapt to different recycling requirements and process flow thereof |
| CN114291891A (en) * | 2021-12-27 | 2022-04-08 | 图方便(苏州)环保科技有限公司 | Sewage treatment method based on MBR (membrane bioreactor) |
| CN114349163A (en) * | 2021-12-31 | 2022-04-15 | 山西省交通新技术发展有限公司 | Starting method for treating domestic sewage based on A/O (anaerobic/anoxic/oxic) biomembrane-MBR (membrane bioreactor) process |
| CN115340188A (en) * | 2022-09-07 | 2022-11-15 | 安徽拓水环境工程科技有限公司 | High-temperature-resistant, low-temperature-resistant and high-altitude sewage treatment equipment |
| CN115367865A (en) * | 2022-08-24 | 2022-11-22 | 北京国环莱茵环保科技股份有限公司 | Rural domestic sewage treatment system and treatment method |
| CN115367972A (en) * | 2022-09-22 | 2022-11-22 | 浙江开创环保科技股份有限公司 | Small-sized integrated MBR sewage treatment equipment and process suitable for inflow fluctuation |
| CN115583677A (en) * | 2022-10-31 | 2023-01-10 | 江苏创健健康科技有限公司 | A sewage intelligent classification method, device, computer equipment and storage medium |
| CN115611467A (en) * | 2022-10-26 | 2023-01-17 | 东南大学 | Rural domestic sewage treatment device with photovoltaic drive combined with solar heating control |
| CN116573753A (en) * | 2023-05-29 | 2023-08-11 | 宁波碧城生态科技有限公司 | Integrated rural domestic sewage MBR membrane treatment system |
| US20240002267A1 (en) * | 2020-12-31 | 2024-01-04 | Shanghai Yingshan Environmental Protection Technology Co., Ltd. | Chemical sewage treatment and reuse system |
| CN118724283A (en) * | 2024-09-02 | 2024-10-01 | 中国农业科学院农业环境与可持续发展研究所 | A denitrification equipment for rural domestic sewage |
| CN118993338A (en) * | 2023-05-22 | 2024-11-22 | 北京科泰兴达高新技术有限公司 | Standard upgrading and expanding method for standard IV water of standard surface of urban sewage plant without newly increasing occupied area |
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2020
- 2020-05-05 AU AU2020100706A patent/AU2020100706A4/en not_active Ceased
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| US20240002267A1 (en) * | 2020-12-31 | 2024-01-04 | Shanghai Yingshan Environmental Protection Technology Co., Ltd. | Chemical sewage treatment and reuse system |
| US12509377B2 (en) * | 2020-12-31 | 2025-12-30 | Shanghai Yingshan Environmental Protection Technology Co., Ltd. | Chemical sewage treatment and reuse system |
| CN113307368A (en) * | 2021-05-27 | 2021-08-27 | 公安县佳源水务有限公司 | Backflow device used in oxidation ditch |
| CN113666576A (en) * | 2021-08-23 | 2021-11-19 | 武汉亦非凡建筑工程有限公司 | Ecological reconstruction method for rural domestic sewage discharge port |
| CN114163072A (en) * | 2021-11-26 | 2022-03-11 | 上海应用技术大学 | Reclaimed water recycling system capable of being switched to adapt to different recycling requirements and process flow thereof |
| CN114163072B (en) * | 2021-11-26 | 2024-01-30 | 上海应用技术大学 | Reclaimed water recycling system capable of being switched to adapt to different recycling requirements and process flow thereof |
| CN114291891A (en) * | 2021-12-27 | 2022-04-08 | 图方便(苏州)环保科技有限公司 | Sewage treatment method based on MBR (membrane bioreactor) |
| CN114349163A (en) * | 2021-12-31 | 2022-04-15 | 山西省交通新技术发展有限公司 | Starting method for treating domestic sewage based on A/O (anaerobic/anoxic/oxic) biomembrane-MBR (membrane bioreactor) process |
| CN114349163B (en) * | 2021-12-31 | 2023-07-25 | 山西省交通新技术发展有限公司 | Starting method for treating domestic sewage based on A/O biological membrane-MBR process |
| CN115367865A (en) * | 2022-08-24 | 2022-11-22 | 北京国环莱茵环保科技股份有限公司 | Rural domestic sewage treatment system and treatment method |
| CN115367865B (en) * | 2022-08-24 | 2024-02-09 | 北京国环莱茵环保科技股份有限公司 | Rural domestic sewage treatment system and treatment method |
| CN115340188A (en) * | 2022-09-07 | 2022-11-15 | 安徽拓水环境工程科技有限公司 | High-temperature-resistant, low-temperature-resistant and high-altitude sewage treatment equipment |
| CN115367972A (en) * | 2022-09-22 | 2022-11-22 | 浙江开创环保科技股份有限公司 | Small-sized integrated MBR sewage treatment equipment and process suitable for inflow fluctuation |
| CN115611467A (en) * | 2022-10-26 | 2023-01-17 | 东南大学 | Rural domestic sewage treatment device with photovoltaic drive combined with solar heating control |
| CN115583677A (en) * | 2022-10-31 | 2023-01-10 | 江苏创健健康科技有限公司 | A sewage intelligent classification method, device, computer equipment and storage medium |
| CN118993338A (en) * | 2023-05-22 | 2024-11-22 | 北京科泰兴达高新技术有限公司 | Standard upgrading and expanding method for standard IV water of standard surface of urban sewage plant without newly increasing occupied area |
| CN116573753A (en) * | 2023-05-29 | 2023-08-11 | 宁波碧城生态科技有限公司 | Integrated rural domestic sewage MBR membrane treatment system |
| CN118724283A (en) * | 2024-09-02 | 2024-10-01 | 中国农业科学院农业环境与可持续发展研究所 | A denitrification equipment for rural domestic sewage |
| CN118724283B (en) * | 2024-09-02 | 2024-11-12 | 中国农业科学院农业环境与可持续发展研究所 | A denitrification equipment for rural domestic sewage |
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