CN212640090U - Domestic sewage intelligent integrated treatment equipment - Google Patents
Domestic sewage intelligent integrated treatment equipment Download PDFInfo
- Publication number
- CN212640090U CN212640090U CN202021801907.5U CN202021801907U CN212640090U CN 212640090 U CN212640090 U CN 212640090U CN 202021801907 U CN202021801907 U CN 202021801907U CN 212640090 U CN212640090 U CN 212640090U
- Authority
- CN
- China
- Prior art keywords
- sludge
- treatment device
- top surface
- membrane
- domestic sewage
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- 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
Landscapes
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
本实用新型提供一种生活污水智能一体化处理设备及工艺，由PLC电控柜控制，包括高效除磷装置、厌氧处理装置、有氧处理装置和膜生物处理装置；高效除磷装置与厌氧处理装置之间的第一隔板顶面低于设备本体的顶面，厌氧处理装置与有氧处理装置之间的第二隔板顶面高于第一隔板顶面但低于设备本体的顶面；有氧处理装置与膜生物反应器之间设置有配水槽，配水槽与膜生物反应器之间设置有第四隔板，第四隔板的顶面低于设备本体的顶面，第三隔板和第四隔板的顶面之间设置有筛网。本实用新型的设备提高膜生物反应器对磷的去除率，解决传统膜生物反应器出水总磷超标的问题，出水稳定达到《城市污水处理厂污染物排放标准》（GB18918‑2002）一级A排放标准。
The utility model provides an intelligent integrated treatment equipment and process for domestic sewage, which is controlled by a PLC electric control cabinet, and includes a high-efficiency phosphorus removal device, an anaerobic treatment device, an aerobic treatment device and a membrane biological treatment device; The top surface of the first separator between the oxygen treatment devices is lower than the top surface of the equipment body, and the top surface of the second separator between the anaerobic treatment device and the aerobic treatment device is higher than the top surface of the first separator but lower than the equipment The top surface of the body; a water distribution tank is arranged between the aerobic treatment device and the membrane bioreactor, and a fourth partition is arranged between the water distribution tank and the membrane bioreactor, and the top surface of the fourth partition is lower than the top of the equipment body. A screen is arranged between the top surfaces of the third partition plate and the fourth partition plate. The device of the utility model improves the phosphorus removal rate of the membrane bioreactor, solves the problem that the total phosphorus in the effluent of the traditional membrane bioreactor exceeds the standard, and the effluent stably reaches the level A of the Pollutant Discharge Standard for Urban Sewage Treatment Plants (GB18918-2002). Emission Standards.
Description
Technical Field
The utility model relates to an urban domestic sewage treatment equipment technical field, concretely relates to domestic sewage intelligence integration treatment facility.
Background
In recent years, the country has paid high attention to rural environment improvement work. The construction of toilet sewer pipe networks and the treatment of rural sewage are well done according to local conditions, and the living quality of rural residents is continuously improved.
In 2015, 4 months, the State Council released ' Water Ten ', which required ' implementation of unified planning, unified construction and unified management of rural sewage treatment. By 2020, 13 ten thousand building villages for completing the comprehensive environmental remediation are newly added. The nineteen reports from the party suggest: the action of renovating the rural human settlements is carried out, and the Qingshan is the Jinshan Yinshan.
In 2016, 12 months, and the ' thirteen five ' ecological environment protection planning ' issued by the State Council indicates that in the ' thirteen five ' period, the comprehensive treatment of the environment of 13 ten thousand administrative villages is promoted, the demonstration project of agricultural waste resource utilization is implemented, the facilities for collecting, treating and utilizing sewage and garbage are built, and the treatment of rural domestic sewage is promoted in a gradient way.
In 2018, the work report of the government of two parties emphasizes again, the toilet revolution needs to be promoted, and the construction strength of sewage treatment facilities is increased.
The rural domestic sewage has the following characteristics:
1. high dispersity and difficult uniform collection. China is vast, and due to the influence of complex rural terrain and low economic development degree, sewage cannot be collected uniformly by using a municipal pipe network, and farmers generally directly discharge the sewage to an outdoor ditch or splash the sewage to the ground.
2. Small water volume and large water volume fluctuation. Due to the fact that rural areas are scattered, resident population is small, correspondingly generated domestic sewage is little, but the water consumption habits of residents are basically similar every day, water consumption peak periods are respectively arranged in the morning, the noon and the evening, water consumption is little at other times, and the daily change coefficient of the water consumption is generally 1.9-2.5. The season is obvious, and the discharge amount in summer is larger than that in winter.
3. The regional differences were significant. Different from the source of urban sewage, the domestic sewage of villages and towns not only comes from the domestic sewage of towns and towns, but also has the domestic sewage of villages and towns. Through investigation discovery, in the aspect of domestic sewage treatment in partial areas, the phenomenon that domestic sewage flows into farmlands carelessly due to untimely treatment is avoided, the influence on the yield of the farmlands in the season is caused, and meanwhile, the phenomenon of soil infiltration is caused under the condition that rainwater is flushed.
4. The biodegradability is strong. The domestic sewage contains elements such as COD, nitrogen, phosphorus and the like, does not contain harmful substances such as heavy metal elements and the like, has strong biodegradability and is beneficial to applying a biological treatment technology.
5. After the traditional domestic sewage treatment is adopted, the problem that total phosphorus is difficult to meet the first-class A standard of pollutant discharge standard of urban sewage treatment plants still exists, and the eutrophication of surrounding water bodies is caused.
The domestic sewage integrated equipment adopted in the market mostly adopts ' AO + MBR ' and ' A2The O + MBR combined technology is used for treating domestic sewage, and although the quality of effluent is greatly improved, the problem that total phosphorus cannot meet the first-level A standard of pollutant discharge Standard of municipal wastewater treatment plants still exists.
Disclosure of Invention
Aiming at the defects of the prior art, the utility model provides an intelligent integrated treatment device and a process for domestic sewage, which integrate the domestic sewage treatment device through an improved device, can run simultaneously, and has small occupied area, simple and efficient flow and low cost; the removal rate of the membrane bioreactor to phosphorus is improved, the problem that the total phosphorus of the effluent of the traditional membrane bioreactor exceeds the standard is solved, and the effluent stably reaches the first-class A emission standard of pollutant emission Standard of municipal Sewage treatment plant (GB 18918-2002).
In order to solve the technical problem, the utility model provides a following technical scheme:
on one hand, the utility model provides an intelligent integrated domestic sewage treatment device, which is controlled by a PLC electric control cabinet and comprises a device body, wherein the device body comprises a high-efficiency dephosphorization device, an anaerobic treatment device, an aerobic treatment device and a membrane biological treatment device;
the water inlet of the equipment body is connected with a sewage adjusting tank, the sewage adjusting tank is connected with a fence tank, and the fence tank is provided with a sewage discharge port;
a first path of water inlet pipe of the equipment body directly extends to the bottom of the efficient phosphorus removal device, and a second path of water inlet pipe directly extends to the bottom of the anaerobic treatment device;
the high-efficiency phosphorus removal device comprises a first sludge area and a first aeration pipe; phosphorus-accumulating bacteria are placed in the high-efficiency phosphorus removal device;
the top surface of a first clapboard between the efficient phosphorus removal device and the anaerobic treatment device is lower than the top surface of the equipment body, so that a pulse overflow channel between the efficient phosphorus removal device and the anaerobic treatment device is formed;
the anaerobic treatment device comprises a second sludge area, a submersible stirrer and a BOA type biological filler;
the top surface of a second partition plate between the anaerobic treatment device and the aerobic treatment device is higher than the top surface of the first partition plate but lower than the top surface of the equipment body;
the aerobic treatment device comprises a third sludge area and a second aeration pipe;
the air inlet ends of the first aeration pipe and the second aeration pipe extend out of the equipment body and are connected with a fan;
a water distribution tank is arranged between the aerobic treatment device and the membrane bioreactor, the top surface of a third partition plate between the aerobic treatment device and the water distribution tank is arranged on the top surface of the equipment body, a water passing groove is arranged between the bottom surface of the third partition plate and a third sludge area, a fourth partition plate is arranged between the water distribution tank and the membrane bioreactor, the top surface of the fourth partition plate is lower than the top surface of the equipment body, and a screen is arranged between the top surfaces of the third partition plate and the fourth partition plate;
a plate-type membrane assembly is arranged in the membrane bioreactor, the water outlet of the membrane bioreactor is connected with a self-priming pump,
the delivery port and the self-priming pump's of self priming pump delivery port are connected, self-cleaning device includes disinfecting equipment, disinfecting equipment is direct to be connected with the delivery pipe.
Furthermore, the PLC electric cabinet comprises a PLC control box and an electric cabinet, and is used for controlling all equipment needing power utilization in the equipment and adjusting the size of the valve.
Furthermore, stop valves are arranged on the first water inlet pipe and the second water inlet pipe, the water inlet proportion of the high-efficiency phosphorus removal device to the anaerobic treatment device is controlled, and the water inlet proportion is designed to be 1: 4.
Furthermore, the first sludge area is in an inverted frustum shape, a first sludge outlet is formed in the bottom of the first sludge area and connected with a sludge discharge pipe, and a first valve is arranged on the sludge discharge pipe.
Further, the first aeration pipe is arranged on the side surface of the high-efficiency phosphorus removal device;
further, high-efficient phosphorus removal device is connected with charge device, charge device is provided with adds medicine flow control valve, it stays a kind control valve and is connected with the automatically controlled cabinet electricity of PLC to add medicine.
Furthermore, the second sludge area is in an inverted frustum shape, a second sludge outlet is formed in the bottom of the second sludge area and connected with a sludge discharge pipe, and a second valve is arranged on the sludge discharge pipe.
Further, the submersible stirrer is connected with the PLC through a wire and is arranged at the bottom of the anaerobic treatment device.
Further, an overflow port is formed in the top surface of the anaerobic treatment device, and the liquid level of the anaerobic treatment device is lower than the lowest point of the overflow port.
Further, the BOA-type biological filler acts as a carrier for denitrifying bacteria/polyphosphate microorganisms.
Furthermore, the third sludge area is in an inverted frustum shape, a third sludge outlet is formed in the bottom of the third sludge area and connected with a sludge discharge pipe, and a third valve is arranged on the sludge discharge pipe.
Furthermore, the second aeration pipes are arranged at the bottom of the aerobic treatment device and are uniformly distributed in a U shape to form a pulse overflow channel between the aerobic treatment device and the anaerobic treatment device.
Furthermore, the aerobic treatment device contains nitrifying bacteria and phosphorus accumulating bacteria.
Further, the plate-type membrane module adopts an organic or inorganic microfiltration membrane.
Furthermore, a pressure gauge is arranged at the position of the pipeline between the self-priming pump and the water outlet of the membrane bioreactor.
Further, the fan is a Roots fan or a rotary fan.
Furthermore, a concentrated solution discharge pipe is arranged in a concentrated area of the plate-type membrane assembly and connected with a concentrated solution discharge pump, and the concentrated solution discharge pump directly discharges the concentrated solution to anaerobic treatment equipment or a high-efficiency phosphorus removal device through a pipeline.
Further, the sludge discharge pipe is provided with a sludge reflux pump, and the sludge reflux pump discharges sludge to the sewage adjusting tank through a pipeline.
Furthermore, the first valve, the second valve and the third valve are all electrically connected with the PLC electric control cabinet.
The intelligent integrated domestic sewage treatment process based on the equipment comprises the following steps:
firstly, domestic sewage and sludge of a system return part enter a high-efficiency dephosphorization device and an anaerobic treatment device in a segmented mode according to a proportion; the part entering the high-efficiency phosphorus removal device is subjected to phosphorus removal by phosphorus accumulating bacteria under the action of aeration, and then the supernatant enters an anaerobic treatment device;
secondly, the sewage after dephosphorization and the part which initially enters the anaerobic treatment device are fully contacted with BOA type biological filler under the action of a submersible stirrer to be directly denitrified; the denitrification treatment comprises denitrification of the heterotrophic bacteria, hydrolysis of suspended pollutants and soluble organic matters, phosphorus removal effect of the phosphorus-accumulating bacteria and the like;
thirdly, the sewage after anaerobic denitrification treatment enters an aerobic treatment device and is treated by nitrification of autotrophic bacteria, phosphorus accumulation and phosphorus removal and degradation and oxidation of heterotrophic bacteria under the action of sufficient oxygen provided by an aerator pipe;
fourthly, the sewage after nitrification of the aerobic treatment device flows into the membrane bioreactor after being subjected to stable retention and filtration separation of suspended fillers through the water distribution tank, and mud-water separation is completed through membrane filtration;
pumping out the water filtered in the membrane bioreactor by a self-priming pump, and discharging the water outwards through a pipeline after the water is disinfected by a disinfection device carried by the self-cleaning device; the concentrated solution filtered by the membrane bioreactor flows back to the high-efficiency dephosphorization device and the anaerobic treatment device through the concentrated solution discharge pump.
Advantageous effects
Compared with the prior art, the utility model, following beneficial effect has:
(1) the utility model has simple structure, easy operation and small occupied area; each pool is completed in the same shell, so that the management is convenient;
(2) the utility model improves the traditional A/O-MBR process, adds a high-efficiency phosphorus removal device, part of sludge flows back to the high-efficiency phosphorus removal device, and the inlet water enters the high-efficiency phosphorus removal device and the anoxic tank in a segmented manner according to the proportion, thereby greatly improving the sewage treatment effect;
(3) the utility model, by arranging the sewage level meter, the flowmeter and the automatic valve and realizing full-automatic control on the equipment by the full-automatic control cabinet, solves the problems of dispersion of highway service areas, difficult operation and management and the like;
(4) based on the utility model discloses the water treatment process of equipment is better to COD, TP and TN's treatment effect, and the COD that goes out water can reach below 50mg/L, and total phosphorus goes out below 0.5mg/L, goes out below the water ammonia nitrogen 5mg/L, and each item goes out water quality of water index and all reaches and is superior to "town sewage treatment plant pollutant emission standard" one-level A standard.
Note: when the water temperature is lower than 12 ℃ in winter, the ammonia nitrogen reaches below 8 mg/L.
Drawings
Fig. 1 is a schematic view of the structure of the apparatus provided by the present invention;
in the figure, the efficient phosphorus removal device 1, the anaerobic treatment device 2, the aerobic treatment device 3, the membrane bioreactor 4, the water distribution tank 5, the self-priming pump 6, the automatic cleaning device 7, the concentrated solution discharge pump 8, the fan 9, the sewage adjusting tank 10, the first aeration pipe 11, the first clapboard 12, the fence pool 20, the submersible stirrer 21, the BOA type biological filler 22, the second clapboard 23, the overflow port 24, the sludge reflux pump 30, the second aeration pipe 31, the third clapboard 32, the screen 33, the fourth clapboard 34 and the plate type membrane component 41 are arranged in the tank.
Detailed Description
The present invention will be described in further detail with reference to specific embodiments, but it should not be construed that the scope of the subject matter of the present invention is limited to the following examples.
The process equipment or devices not specifically noted in the following examples are conventional in the art; the related devices and the process mode which are not disclosed in the utility model belong to the conventional technology, and all reagents can be purchased from commercial sources.
Example 1
In order to better solve the problem that the total phosphorus in the domestic sewage exceeds the standard, the GRP phosphorus-accumulating membrane bioreactor is researched and developed based on A2the/O process integrates the high-efficiency dephosphorization device and the self-cleaning membrane bioreactor into a whole, improves the phosphorus absorption of aerobic bacteria in the membrane bioreactor, ensures that all indexes of effluent can reach the standard IV of the ground surface level, and can be directly reused in agriculture, landscaping and the like. The device can be suitable for small-scale sewage treatment occasions, and is suitable for treating domestic sewage generated by dispersed crowd living places such as residential areas, towns, expressway service areas, hotels, restaurants, hospitals, sanatoriums, schools, markets, ship docks, stations, airports, industrial and mining enterprises, tourist attractions, villa areas, scenic spots and the like or treating various industrial organic sewage similar to the domestic sewage and with small scale.
The equipment has the following characteristics:
the water quality of the produced water is good: all indexes can reach local standard/first grade A standard/ground surface level IV standard, and can be directly applied to irrigation, car washing and greening.
Operation and maintenance: the self-cleaning device carries out automatic forward/backward cleaning according to the operation condition of the membrane device, and has long service life and simple maintenance.
Modular design: can be freely combined according to the scale to meet different use occasions.
Low energy consumption: the intelligent self-input system can automatically judge the operation period according to cloud connection, automatically adjust the operation load and reduce the energy consumption by 30 percent.
Intelligent design: APP wisdom management, unmanned on duty, the real-time feedback equipment running state of mobile client and quality of water data have solved the difficult problem of long-term small-scale sewage treatment facility dispersion, operation management.
The specific contents are as follows:
an intelligent integrated domestic sewage treatment device is controlled by a PLC (programmable logic controller) electric control cabinet and comprises a device body, wherein the device body comprises a high-efficiency dephosphorization device 1, an anaerobic treatment device 2, an aerobic treatment device 3 and a membrane biological treatment device 4;
the water inlet of the equipment body is connected with a sewage adjusting tank 10, the sewage adjusting tank 10 is connected with a fence tank 20, and the fence tank 20 is provided with a sewage discharge port;
the PLC electric control cabinet comprises a PLC control box and an electric control box and is used for controlling all equipment needing power utilization in the equipment and adjusting the size of a valve;
a first water inlet pipe of the equipment body directly extends to the bottom of the efficient phosphorus removal device 1, and a second water inlet pipe directly extends to the bottom of the anaerobic treatment device 2; stop valves are arranged on the first water inlet pipe and the second water inlet pipe, so that the water inlet proportion of the high-efficiency phosphorus removal device 1 to the anaerobic treatment device 2 can be conveniently controlled, the water inlet proportion is designed to be 1:4, the distance between liquid levels in the equipment body is ensured, and the high-efficiency phosphorus removal device 1 comprises a first sludge area and a first aeration pipe 11; the first sludge area is in an inverted frustum shape, so that all sludge is discharged from a sludge discharge port at the bottom of the inverted frustum shape, the sludge discharge port is connected with a sludge discharge pipe, and a valve is arranged on the sludge discharge pipe, so that the residual sludge is discharged periodically; the sludge discharge pipe is provided with a sludge return pump 30, and the sludge return pump 30 discharges sludge to the sewage adjusting tank through a pipeline; the air inlet end of the first aeration pipe 11 extends out of the equipment body and is connected with a fan 9, and the first aeration pipe 11 is arranged on the side surface of the high-efficiency phosphorus removal device 1; phosphorus accumulating bacteria in the efficient phosphorus removal device 1 are mixed with sludge in wastewater, polyphosphate stored in bacteria is released, energy is released simultaneously, part of the energy is supplied for the obligate aerobic phosphorus accumulating bacteria to live in an anaerobic inhibition environment, and the other part of the energy is supplied for the phosphorus accumulating bacteria to actively absorb fermentation products in sewage like VFA and the like and is stored in the bacteria in a PHA form; and a phosphorus removal agent can be selectively added into the high-efficiency phosphorus removal device 1 according to the water quality of inlet and outlet water, and polyphosphate released by phosphorus-accumulating bacteria is gathered in sludge, so that the phosphorus removal efficiency is further improved.
Further, the efficient phosphorus removal device 1 is connected with a dosing device, and the dosing device is used for adding a phosphorus removal agent.
The top surface of a first clapboard 12 between the high-efficiency phosphorus removal device 1 and the anaerobic treatment device 2 is lower than the top surface of the equipment body, so that a pulsating overflow channel between the high-efficiency phosphorus removal device 1 and the anaerobic treatment device 2 is formed;
the anaerobic treatment device 2 comprises a second sludge area, a submersible stirrer 21 and a BOA type biological filler 22; the second sludge area is in an inverted frustum shape, and is beneficial to discharging all sludge from a sludge outlet at the bottom of the inverted frustum shape; the submersible stirrer 21 is connected with the PLC through a wire, the submersible stirrer 21 is arranged at the bottom of the anaerobic treatment device 2, and a spiral liquid flow is formed by stirring the wastewater and is fully contacted with the BOA type biological filler 22, so that the backflow sludge and the nitrified liquid are prevented from being unevenly distributed, a stirring effect can be achieved, and the device has an important significance in improving the wastewater treatment efficiency; an overflow port 24 is arranged on the top surface of the anaerobic treatment device 2, and the liquid level of the anaerobic treatment device 2 is lower than the lowest point of the overflow port 24; the BOA type biological filler 22 is used as a carrier of denitrifying bacteria/phosphorus accumulating bacteria microorganism, and the filler has good effect of removing nitrogen, phosphorus and sulfide, thereby achieving the purpose of removing nitrogen and phosphorus, enabling the microorganism to be in an anaerobic and anaerobic alternate environment, and being beneficial to anaerobic phosphorus release and anaerobic denitrification;
the top surface of the second clapboard 23 between the anaerobic treatment device 2 and the aerobic treatment device 3 is higher than the top surface of the first clapboard 12 but lower than the top surface of the equipment body, so that the wastewater which is not anaerobically treated can be prevented from directly entering the aerobic treatment device;
the aerobic treatment unit 3 comprises a third sludge zone and a second aeration pipe 31; the third sludge area is in an inverted frustum shape, and is beneficial to discharging all sludge from a sludge outlet at the bottom of the inverted frustum shape; the air inlet end of the second aeration pipe 31 extends out of the equipment body and is connected with a fan 9, the second aeration pipe 31 is arranged at the bottom of the aerobic treatment device 3 and is uniformly arranged in a U shape, and a pulse type overflow channel between the aerobic treatment device 3 and the anaerobic treatment device 2 is formed; the aerobic treatment device 3 contains nitrifying bacteria and phosphorus accumulating bacteria, so that the aerobic tank is fully and uniformly oxygenated; sufficient oxygen is provided for microbial degradation, so that the wastewater of the aerobic treatment device 3 generates turbulent pulsation, and the liquid level of the aerobic zone fluctuates up under the action of the turbulent pulsation, so as to be fully contacted with the microbial filler; the dissolved oxygen in the wastewater discharged by the aerobic treatment device is between 1.5mg/L and 2.0 mg/L.
A water distribution tank 5 is arranged between the aerobic treatment device 3 and the membrane bioreactor 4, the top surface of a third partition plate 32 between the aerobic treatment device 3 and the water distribution tank 5 is arranged on the top surface of the equipment body, a stream of sewage is arranged between the bottom surface of the third partition plate 32 and a third sludge area, and sewage enters the water distribution tank 5 through the stream of sewage;
a fourth clapboard 34 is arranged between the water distribution tank 5 and the membrane bioreactor 4, the top surface of the fourth clapboard 34 is lower than the top surface of the equipment body, and a screen 33 is arranged between the top surfaces of the third clapboard 32 and the fourth clapboard 34 and is used for filtering sludge with overlarge particles and blocking suspended fillers;
a plate-type membrane assembly 41 is arranged in the membrane bioreactor 4, and wastewater discharged from the water distribution tank 5 enters the membrane bioreactor 4 for membrane filtration; the water outlet of the membrane bioreactor 4 is connected with a self-priming pump 6, under the action of the self-priming pump 6, a plate-type membrane component 41 in the membrane bioreactor 4 can rapidly filter water under the action of negative pressure, the membrane component replaces a terminal secondary sedimentation tank of the traditional biological treatment technology, the concentration of high-activity sludge is kept in the bioreactor, the organic load of biological treatment is improved, the floor area of a sewage treatment facility is reduced, and the amount of residual sludge is reduced by keeping low sludge load. The concentration of activated sludge (MLSS) in the membrane bioreactor system can be increased to 8000-10000mg/L, even higher; the sludge age (SRT) can be prolonged to more than 30 days. The membrane bioreactor can retain microorganisms with longer generation period due to effective interception, can realize deep purification of sewage, simultaneously nitrifying bacteria can be fully propagated in the system, has obvious nitrification effect, and provides possibility for deep phosphorus and nitrogen removal.
Further, the plate-type membrane module 41 is immersed and placed by an organic or inorganic microfiltration membrane, and the membrane module is stably placed in the reaction tank; the membrane has low-pressure (suction or gravity) water outlet, the working pressure of the system is low, and the power consumption is low; the operation is stable for a long time; the membrane is not easy to pollute, the membrane cleaning frequency is low, and the cleaning operation is convenient; the membrane can be replaced by a single membrane, and the like. The membrane greatly improves the solid-liquid separation capability of the system, so that the effluent quality and the volume load of the system are greatly improved, and the stable standard discharge of the effluent is ensured.
Furthermore, a pressure gauge is arranged at the position of a pipeline between the self-priming pump 6 and the water outlet of the membrane bioreactor 4 and is used for monitoring the pressure in real time, observing the change of the membrane pressure difference and judging the membrane pollution condition;
the water outlet of the self-sucking pump 6 is connected with the automatic cleaning device 7, and the wastewater is disinfected by disinfection equipment arranged in the automatic cleaning device 7 and then discharged up to the standard; in addition, the automatic cleaning device 7 can also judge that the membrane is seriously polluted by detecting the pressure, and automatically perform forward/backward cleaning according to the operation condition of the membrane device, so that the operation and maintenance are simple, and the service life of the MBR membrane is greatly prolonged;
the fan 9 is a Roots fan or a rotary fan, and is connected with a first aeration pipe and a second aeration pipe in the aeration assembly;
further, a concentrated solution discharge pipe is arranged in a concentration area of the plate-type membrane assembly 41, the concentrated solution discharge pipe is connected with a concentrated solution discharge pump 8, and the concentrated solution discharge pump 8 directly discharges concentrated solution to the anaerobic treatment device 2 or the efficient phosphorus removal device 1 through a pipeline to form synchronous treatment of activated sludge; the concentrated solution contains nitrifying liquid and can be subjected to denitrification in the anaerobic treatment device 2.
The intelligent integrated domestic sewage treatment process based on the equipment comprises the following steps:
domestic sewage enters an efficient dephosphorization device and an anaerobic treatment device in a segmented mode according to the proportion, and the water inlet proportion is automatically adjusted according to the water quality of inlet and outlet water. Part of water enters the high-efficiency phosphorus removal device and is fully mixed with the sludge of the return part of the system, the phosphorus-accumulating bacteria release polyphosphate stored in the bacteria and release energy, wherein part of the energy is used for the obligate aerobic phosphorus-accumulating bacteria to live in an anaerobic inhibition environment, and the other part of the energy is used for the phosphorus-accumulating bacteria to actively absorb fermentation products in sewage like VFA and the like and store the fermentation products in the bacteria in a PHA form; part of carbon is removed in the anaerobic section; the supernatant fluid enters an anaerobic treatment device, and the sludge is discharged for disposal at regular intervals. And a phosphorus removal agent can be selectively added into the high-efficiency phosphorus removal device according to the water quality of inlet and outlet water, and polyphosphate released by phosphorus-accumulating bacteria is gathered in sludge, so that the phosphorus removal efficiency is further improved.
Secondly, the sewage after phosphorus release of the high-efficiency phosphorus removal device enters an anaerobic treatment device through a first partition plate, the anaerobic treatment device has the primary function of nitrogen removal, most of sludge containing nitrifying liquid flows back to the anaerobic treatment device through a concentrated liquid discharge pump, and NO is subjected to denitrification by anaerobic bacteria under the anoxic condition3 -Reduction of-N to molecular nitrogen (N)2) C, N, O, completing the circulation in the system, realizing the harmless treatment of the sewage; meanwhile, heterotrophic bacteria hydrolyze suspended pollutants such as starch, fiber, carbohydrate and the like in sewage and soluble organic matters into organic acid, so that macromolecular organic matters are decomposed into micromolecular organic matters, insoluble organic matters are converted into soluble organic matters, and pollutants such as protein, fat and the like are aminated (N on an organic chain or amino in amino acid) to free ammonia (NH)3、NH4 +) (ii) a Simultaneously water inlet and system return sludgeThe facultative anaerobic zymocyte converts biodegradable organic matters in the sewage into micromolecular fermentation products such as Volatile Fatty Acid (VFA) and the like, the phosphorus accumulating bacteria also release polyphosphate stored in the thallus and release energy at the same time, wherein part of the energy is supplied for the obligate aerobic phosphorus accumulating bacteria to live in an anaerobic inhibition environment, and the other part of the energy is supplied for the phosphorus accumulating bacteria to actively absorb the fermentation products in the sewage similar to the VFA and the like and store the fermentation products in the thallus in a PHA form; part of the carbon is removed.
And the sewage treated by the anaerobic treatment device enters the aerobic treatment device through the second clapboard. The aerobic treatment device is multifunctional, and under the condition of sufficient oxygen supply, the nitrification of autotrophic bacteria can be used for producing NH3-N(NH4 +) Oxidation to NO3 --N; the phosphorus accumulating bacteria absorb excessive phosphorus which is more than the physiological requirement of the phosphorus accumulating bacteria; the heterotrophic bacteria further oxidize the organic matter into carbon dioxide and water, removing BOD.
Sewage after nitrification of the aerobic treatment device flows into the membrane bioreactor through the water distribution tank, and after pollutants are further removed in the section of the sewage, mud and water separation is completed through membrane filtration, and the sewage is pumped out through a self-priming pump, sterilized by a self-cleaning device and then discharged outside through a pipeline; a concentrated solution discharge pump is arranged in the membrane bioreactor, and most sludge flows back to the anaerobic treatment device according to the backflow proportion of 100-300 percent; a small part of sludge flows back to the high-efficiency dephosphorization device according to the proportion of 50 to 100 percent; the Membrane Bioreactor (MBR) is a combination of a suspension culture biological treatment method (an activated sludge method) and a membrane separation technology, wherein the membrane separation technology replaces a secondary sedimentation tank in the traditional activated sludge method and plays a role in separating microorganisms depending on the biological treatment technology from a biological culture solution (mixed solution), so that the microorganisms can be reserved in a biochemical reaction tank, and the effluent is ensured to be basically free of microorganisms and other suspended matters; the COD of the organic matters in the wastewater is thoroughly degraded in the high-concentration activated sludge, and NH is generated3-N(NH4 +) Further oxidized to NO3 -And N, the phosphorus in the water is absorbed by the efficient phosphorus accumulating bacteria.
Sixthly, the self-cleaning device is arranged in the equipment body and is provided with a disinfection device, and the treated sewage is pumped out by a self-sucking pump and then enters the self-cleaning device to be disinfected and then is discharged after reaching the standard; the self-cleaning device carries out automatic forward/backward cleaning according to the operation condition of the membrane device, is simple to maintain and operate, and greatly prolongs the service life of the MBR membrane.
The efficient phosphorus removal device, the anaerobic treatment device, the aerobic treatment device and the membrane biological treatment device are internally provided with a liquid level meter, an oxygen dissolving instrument and a sludge concentration meter; a pressure gauge is arranged at the outlet of the fan, and the PLC electric control cabinet can carry out full-automatic control according to the liquid level and the flow of the sewage;
the self-cleaning device is provided with an automatic control system, and automatic forward/backward cleaning is carried out according to the operation condition of the membrane device; the two water pumps and the two fans operate alternately, and when one fan fails, the other fan is started to enable the equipment to operate continuously; when the sewage is cut off, the fan can automatically and intermittently operate to protect the normal growth of the biological membrane. The PLC electric control cabinet has the automatic protection function of faults such as overcurrent, open-phase, overvoltage and undervoltage, and does not need special management; this equipment passes through intelligent design, and APP wisdom platform realizes unmanned on duty, long-range centralized management.
The utility model has simple structure and easy operation, and the intelligent input system can judge the operation period according to the cloud connection and automatically adjust the operation load; remote centralized management can be performed through mobile phone apps, so that unattended operation is realized; the device has small occupied area, improves the nitrogen and phosphorus removal efficiency, and is suitable for treating domestic sewage generated by dispersed crowd living places such as residential areas, towns, expressway service areas, hotels, restaurants, hospitals, sanatoriums, schools, markets, ship docks, stations, airports, industrial and mining enterprises, tourist attractions, villa areas, scenic spots and the like or treating various industrial organic sewage which is similar to the domestic sewage and has smaller scale.
Specific examples are as follows:
zhang Jia nationality Wuling Yuan harmonizing rural domestic sewage CODcrThe highest concentration can reach about 250mg/L, the highest concentration of ammonia nitrogen can reach about 35mg/L, the highest concentration of total phosphorus can reach about 3.5mg/L, and after the treatment by adopting the process and the equipment of the utility model, the COD of the effluent watercrThe concentration is less than 50mg/L, the ammonia nitrogen concentration is less than 5mg/L, and the total phosphorus concentrationLess than 0.5mg/L, the water quality indexes of the effluent reach and are superior to the first-class A standard of pollutant discharge standard of urban sewage treatment plants, and the stability of the effluent effect can be kept; meanwhile, the device has a perfect automatic control function, and solves the problems of excessive total nitrogen and total phosphorus of effluent of small-scale sewage treatment facilities in villages and towns and difficulty in operation and management for many years.
It is to be understood that the above embodiments are merely exemplary embodiments that have been employed to illustrate the principles of the present invention, and that the present invention is not limited thereto. It will be apparent to those skilled in the art that various modifications and improvements can be made without departing from the spirit and substance of the invention, and these modifications and improvements are also considered to be included in the scope of the invention.
Claims (9)
1. The intelligent integrated domestic sewage treatment equipment is characterized by being controlled by a PLC (programmable logic controller) electric control cabinet and comprising an equipment body, wherein the equipment body comprises a high-efficiency dephosphorization device, an anaerobic treatment device, an aerobic treatment device and a membrane biological treatment device;
the water inlet of the equipment body is connected with a sewage adjusting tank, the sewage adjusting tank is connected with a fence tank, and the fence tank is provided with a sewage discharge port; a first path of water inlet pipe of the equipment body directly extends to the bottom of the efficient phosphorus removal device, and a second path of water inlet pipe directly extends to the bottom of the anaerobic treatment device; the high-efficiency phosphorus removal device comprises a first sludge area and a first aeration pipe; phosphorus-accumulating bacteria are placed in the high-efficiency phosphorus removal device; the top surface of a first clapboard between the efficient phosphorus removal device and the anaerobic treatment device is lower than the top surface of the equipment body, so that a pulse overflow channel between the efficient phosphorus removal device and the anaerobic treatment device is formed; the anaerobic treatment device comprises a second sludge area, a submersible stirrer and a BOA type biological filler; the top surface of a second partition plate between the anaerobic treatment device and the aerobic treatment device is higher than the top surface of the first partition plate but lower than the top surface of the equipment body; the aerobic treatment device comprises a third sludge area and a second aeration pipe; the air inlet ends of the first aeration pipe and the second aeration pipe extend out of the equipment body and are connected with a fan; a water distribution tank is arranged between the aerobic treatment device and the membrane bioreactor, the top surface of a third partition plate between the aerobic treatment device and the water distribution tank is arranged on the top surface of the equipment body, a water passing groove is arranged between the bottom surface of the third partition plate and a third sludge area, a fourth partition plate is arranged between the water distribution tank and the membrane bioreactor, the top surface of the fourth partition plate is lower than the top surface of the equipment body, and a screen is arranged between the top surfaces of the third partition plate and the fourth partition plate; the membrane bioreactor is internally provided with a plate-type membrane assembly, the water outlet of the membrane bioreactor is connected with a self-priming pump, the water outlet of the self-priming pump is connected with an automatic cleaning device, the automatic cleaning device comprises a disinfecting device, and the disinfecting device is directly connected with a discharge pipe.
2. The intelligent integrated domestic sewage treatment equipment according to claim 1, wherein the PLC electric cabinet comprises a PLC control box and an electric control box, and is used for controlling the size adjustment of all equipment needing power consumption in the equipment.
3. The intelligent integrated domestic sewage treatment equipment according to claim 1, wherein stop valves are arranged on both the first water inlet pipe and the second water inlet pipe to control the water inlet ratio of the high-efficiency phosphorus removal device to the anaerobic treatment device, and the designed water inlet ratio is 1: 4.
4. The intelligent integrated domestic sewage treatment equipment according to claim 1, wherein the first sludge zone is in an inverted frustum shape, a first sludge outlet is arranged at the bottom of the first sludge zone, the first sludge outlet is connected with a sludge discharge pipe, and a first valve is arranged on the sludge discharge pipe; the third sludge area is in an inverted frustum shape, a third sludge outlet is formed in the bottom of the third sludge area, the third sludge outlet is connected with a sludge discharge pipe, and a third valve is arranged on the sludge discharge pipe; the second sludge area is in an inverted frustum shape, a second sludge outlet is formed in the bottom of the second sludge area and connected with a sludge discharge pipe, and a second valve is arranged on the sludge discharge pipe; the sludge discharge pipe is provided with a sludge reflux pump, and the sludge reflux pump discharges sludge to the sewage adjusting tank through a pipeline; and the first valve, the second valve and the third valve are all electrically connected with the PLC electric control cabinet.
5. The intelligent integrated domestic sewage treatment apparatus according to claim 1, wherein the first aeration pipe is disposed at a side of the efficient phosphorus removal device.
6. The intelligent integrated domestic sewage treatment equipment according to claim 1, wherein the efficient phosphorus removal device is connected with a dosing device, the dosing device is provided with a dosing flow control valve, and the dosing sample retention control valve is electrically connected with the PLC electric control cabinet.
7. The intelligent integrated domestic sewage treatment equipment according to claim 1, wherein the submersible stirrer is connected with the PLC controller through a wire, and is arranged at the bottom of the anaerobic treatment device; the top surface of the anaerobic treatment device is provided with an overflow port, and the liquid level of the anaerobic treatment device is lower than the lowest point of the overflow port; the BOA type biological filler is used as a carrier of denitrifying bacteria/phosphorus accumulating bacteria microorganisms; the aerobic treatment device contains nitrifying bacteria and phosphorus accumulating bacteria.
8. The intelligent integrated domestic sewage treatment equipment according to claim 1, wherein the second aeration pipes are arranged at the bottom of the aerobic treatment device and are uniformly arranged in a U shape to form a pulsating overflow channel between the aerobic treatment device and the anaerobic treatment device.
9. The intelligent integrated domestic sewage treatment equipment according to claim 1, wherein the plate-type membrane module employs an organic or inorganic microfiltration membrane; a pressure gauge is arranged at the position of a pipeline between the self-priming pump and the water outlet of the membrane bioreactor; the fan is a Roots fan or a rotary fan; the concentrated zone of the plate-type membrane component is provided with a concentrated solution discharge pipe, the concentrated solution discharge pipe is connected with a concentrated solution discharge pump, and the concentrated solution discharge pump directly discharges concentrated solution into anaerobic treatment equipment or a high-efficiency phosphorus removal device through a pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021801907.5U CN212640090U (en) | 2020-08-25 | 2020-08-25 | Domestic sewage intelligent integrated treatment equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202021801907.5U CN212640090U (en) | 2020-08-25 | 2020-08-25 | Domestic sewage intelligent integrated treatment equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212640090U true CN212640090U (en) | 2021-03-02 |
Family
ID=74785932
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202021801907.5U Expired - Fee Related CN212640090U (en) | 2020-08-25 | 2020-08-25 | Domestic sewage intelligent integrated treatment equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212640090U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111875068A (en) * | 2020-08-25 | 2020-11-03 | 湖南湘牛环保实业有限公司 | Domestic sewage intelligent integrated treatment equipment and technology |
-
2020
- 2020-08-25 CN CN202021801907.5U patent/CN212640090U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111875068A (en) * | 2020-08-25 | 2020-11-03 | 湖南湘牛环保实业有限公司 | Domestic sewage intelligent integrated treatment equipment and technology |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204125300U (en) | A kind of purification tank for the treatment of dispersion type domestic wastewater | |
| CN103880244B (en) | A comprehensive treatment method for livestock and poultry manure and domestic sewage in rural areas | |
| CN102381814A (en) | Integrated rural sewage treatment plant | |
| CN101811804A (en) | Domestic sewage bioreaction treatment and recycling system | |
| CN204569669U (en) | Integrated small microkinetic sewage disposal device | |
| CN102976548A (en) | Zero emission district sewage resource treatment apparatus | |
| CN206266394U (en) | Integrated scattered domestic sewage treatment device | |
| CN205398371U (en) | Rural miniaturized integration sewage treatment unit | |
| CN107188379A (en) | A kind of domestic sewage of villages and small towns rural area landscape type total system | |
| CN205710300U (en) | A kind of sewage-treatment plant | |
| CN109879528A (en) | Treatment method and system for self-driven landscape ecologicalization of rural domestic sewage | |
| CN210764894U (en) | Temple sewage treatment and recycling system | |
| CN112093993A (en) | Ecological energy-saving rural sewage treatment equipment and system | |
| CN212640090U (en) | Domestic sewage intelligent integrated treatment equipment | |
| CN207047066U (en) | A kind of domestic sewage of villages and small towns rural area landscape type total system | |
| CN204022622U (en) | A kind of combined tank shape biochemical technology is processed domestic sewage apparatus | |
| CN111875068A (en) | Domestic sewage intelligent integrated treatment equipment and technology | |
| CN110171903A (en) | City micropolluted river water processing method and system | |
| CN104671408A (en) | Scattered small integrated sewage processing device for rural areas | |
| CN208414147U (en) | WSZ series of integral sewage disposal device | |
| CN208308624U (en) | Integrated intelligent sewage-treatment plant | |
| CN215403684U (en) | Side flow dephosphorization coupling efficient precipitation domestic sewage treatment integrated equipment | |
| CN206014597U (en) | A kind of sewage disposal system | |
| CN212451085U (en) | Rural sewage treatment system | |
| CN104030442A (en) | Integral domestic sewage treatment equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| 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: 20210302 |