CN112707603A

CN112707603A - Deep purification and recycling system and method for municipal sewage

Info

Publication number: CN112707603A
Application number: CN202110004241.3A
Authority: CN
Inventors: 罗依依
Original assignee: Individual
Current assignee: Individual
Priority date: 2021-01-04
Filing date: 2021-01-04
Publication date: 2021-04-27

Abstract

The invention discloses a municipal sewage deep purification and recycling system and a method thereof. According to the invention, after municipal sewage is purified by a primary treatment device, a physicochemical purification device, a catalytic electrolysis deep purification device and a biochemical purification device in sequence, the COD in the water body can be removed by 92%, so that the COD of the effluent is less than or equal to 20 mg/L; BOD is removed by 98 percent, so that BOD of effluent is less than or equal to 4 mg/L; removing 99% of total phosphorus, so that the total phosphorus of effluent is less than or equal to 0.1 mg/L; 99% of ammonia nitrogen is removed, the ammonia nitrogen content of the effluent is less than or equal to 1.0mg/L, the total nitrogen content of the effluent is 98.6.00% removed, the total nitrogen content of the effluent is less than or equal to 1.0mg/L, the chromaticity is less than 2, the dissolved oxygen in the water body is increased to more than 5mg/L, the purified water body reaches the III or IV class water quality standard of the surface water environmental quality standard (GB3838-2002), the municipal sewage is converted into water resources, and the method is particularly suitable for deep purification and regeneration utilization of the municipal sewage and expansion upgrading reconstruction of the existing sewage treatment plants.

Description

Deep purification and recycling system and method for municipal sewage

Technical Field

The invention relates to a municipal sewage deep purification and regeneration system and a method thereof, in particular to a municipal sewage purification and regeneration utilization system and a method integrating physicochemical purification, electrolytic purification, biochemical purification and the like, belonging to the field of environmental protection.

Background

Municipal sewage is a polluted water body produced in the living and production processes of people. Main pollutants of municipal sewage in China have the characteristic of high north and south, and the general physicochemical indexes are that COD is less than or equal to 700mg/L (mostly 200-500 mg/L, wherein the COD in the southern area is less than or equal to 500mg/L), BOD is less than or equal to 350mg/L (mostly 100-300 mg/L, and BOD in the southern area is less than or equal to 300mg/L), SS is less than or equal to 400mg/L, ammonia nitrogen is less than or equal to 50mg/L, total nitrogen is less than or equal to 70mg/L, and total phosphorus is less than or equal to 10mg/L, pH 7-9. At present, municipal sewage at home and abroad mainly adopts a biochemical method which comprises primary treatment, secondary treatment and advanced treatment. The main process of the first-stage treatment comprises sewage collection, coarse grid filtration and fine grid filtration to an aeration sand settling tank and a primary settling tank; the main process of the secondary treatment comprises the following steps: three major types of activated sludge treatment, biofilm process and Membrane Bioreactor (MBR) processes. The activated sludge treatment process applied to the urban sewage plant mainly comprises three series: (1) oxidation ditch series; (2) A/A/O series; (3) sequencing Batch Reactor (SBR) series. The biofilm process applied to the urban sewage treatment plant mainly comprises a Biological Aerated Filter (BAF) process and a Moving Bed Biofilm (MBBR) process. Membrane Bioreactors (MBR) are a new type of wastewater treatment process developed at the end of the 20 th century. The advanced treatment process applied at home and abroad mainly comprises a chemical dephosphorization and denitrification process. Since 1912 Clark's invention biochemical treatment process of sewage for more than 100 years, the sewage treatment process has hardly changed significantly. However, the existing sewage biochemical treatment process has five outstanding problems:

1. unstable low-temperature operation: in a sewage treatment plant constructed by adopting an activated sludge treatment process, a biofilm process and a Membrane Bioreactor (MBR) process, the activity of nitrifying bacteria is strongly inhibited and the nitrification effect is poor due to low temperature in winter or some severe cold areas and when the water temperature is lower than 15 ℃, most of ammonia nitrogen in effluent is greater than 10mg/L, and some of ammonia nitrogen in effluent is even greater than 20 mg/L. Because the nitrification effect is poor, the denitrification effect is not guaranteed, and the total nitrogen of effluent is mostly more than 20 mg/L. Therefore, in winter, the effluent of the northern sewage treatment plant can not meet the quasi IV-class water quality of the environmental quality standard for surface water (GB3838-2002), which is the primary A standard of the pollutant discharge standard for urban sewage treatment plant (GB 18918-2002).

2. The occupied area is large: when the sewage treatment plant is constructed by adopting an activated sludge treatment process, a biofilm process and a Membrane Bioreactor (MBR) process to treat sewage, the retention time of the sewage is more than 17 hours, the land area of the sewage treatment plant with more structures and ten thousand tons is 10-15 mu, the occupied land is large, and a large amount of land resources are wasted.

3. The effluent quality is not high: when the sewage treatment plant is constructed by adopting an activated sludge treatment process, a biofilm process and a Membrane Bioreactor (MBR) process to treat the sewage, the effluent quality is mostly quasi IV (mainly the total nitrogen can only reach about 10 mg/L) of pollutant discharge standard (GB 18918-.

4. Capacity expansion is achieved: due to the rapid economic development of the last forty years, most of the existing sewage treatment plants treat urban centers. When most sewage is planned and constructed, the social and economic development is not estimated sufficiently, and enough extension land is not reserved, so that when the current capacity expansion is needed, no construction land is reserved.

5. The main root cause of water eutrophication is as follows: the eutrophication of the water body is mainly caused by the fact that the nitrogen and phosphorus content in the water body accumulates day by day and continuously and seriously exceeds the standard, and one of the main reasons for the result is the sewage discharge of a municipal sewage treatment plant. At present, according to the discharge standard of pollutants for urban sewage treatment plants, most of ammonia nitrogen in effluent of a sewage treatment plant constructed by an activated sludge process is larger than 1mg/L, most of total nitrogen is larger than 10mg/L, most of total phosphorus is larger than 0.4mg/L, a large amount of nitrogen and phosphorus in the effluent are discharged into a water body, and the content of the nitrogen and phosphorus accumulates day by month and continuously, so that eutrophication of the water body is caused, and a large amount of algae is proliferated and water bloom is erupted repeatedly.

6. Difficulty of sludge dehydration and odor of taste: when the biochemical method is adopted for treatment, the sludge contains a large amount of microbial colonies, the microbial colonies contain a large amount of intercellular water, and the sewage can be dehydrated to the water content of below 60 percent by adopting high-pressure plate-and-frame filter pressing after high-temperature cooking or physicochemical conditioning. In addition, because the sewage contains a large amount of organic matters and anaerobic bacteria, in the process of collecting, dehydrating and transferring the sludge, the organic matters can release a large amount of stink difficult to smell under the action of the anaerobic bacteria, and the production environment of a sewage treatment plant and the living environment around the sewage treatment plant are influenced.

7. The odor disturbs people: when the biochemical method is adopted for treatment, a large amount of gas with odor is generated in the anaerobic process and the anoxic process, and in order to eradicate the odor which disturbs people, more capital needs to be invested, and an odor collecting and treating device is built.

8. The carbon source needs to be added: firstly, when the COD concentration of the inlet water is low and the carbon-nitrogen ratio is inconsistent, and secondly, when denitrification is needed to remove the total nitrogen, carbon sources are required to be added.

Therefore, the reduction of nitrogen and phosphorus emission of urban sewage treatment plants is the primary target of municipal sewage treatment at present and is also an important problem. Therefore, although the classical sewage treatment processes are applied for more than a hundred years, the quality of the effluent cannot meet the index requirements of social and economic development and the quality standard of surface water environment (GB3838-2002) so far, and therefore, a novel sewage treatment process which has the advantages of high effluent quality (meeting the requirement of water resource utilization), short sewage retention time, small land area, few structures, low operation cost and greatly shortened construction time is urgently needed.

Disclosure of Invention

In order to solve the technical problems, the invention aims to provide a system and a method for deeply purifying and recycling municipal sewage.

The invention designs a municipal sewage deep purification and recycling system and a method thereof, wherein the system comprises a primary treatment device, a physicochemical purification device, a catalytic electrolysis deep purification device, a reduction pool (water quality restoration) for reducing and eliminating sodium hypochlorite, a biochemical purification device and a sludge treatment device, wherein the primary treatment device, the physicochemical purification device, the catalytic electrolysis deep purification device, the reduction pool and the biochemical purification device are sequentially connected, and sludge of the primary treatment device and the physicochemical purification device can enter the sludge treatment device for sludge treatment, so that the municipal sewage deep purification is realized.

After the treatment by the system and the method, the prediction of the effect of removing main sewage in each step of water body purification is shown in the table 1.1:

TABLE 1.1 prediction of the effectiveness of removing major waste products in water purification steps

Processing unit	CODcr	BOD₅	SS	Ammonia nitrogen	Total phosphorus	Total nitrogen	Petroleum products
								The water inflow is less than or equal to	700	350	300	50	10	70	-
The first-stage treatment is less than or equal to	630(10％)	315(10％)	210(30％)	50(-)	10(-)	70(-)	-
								Physicochemical purification is less than or equal to	72(89％)	63(80％)	10(95％)	47.5(5％)	0.2(98％)	56(20％)	0.5(90％)
Electrolytic purification is less than or equal to	25.2(65％)	3.2(95％)	10(10％)	1.0(99％)	0.2(10％)	3.0(96％)	0.3(40％)
								Elimination of sodium hyporeduction	25.2(-)	3.2(-)	9(-)	1.0(-)	0.2(-)	3.0(-)	0.3(-)
Biochemical treatment	20.00	3	9	1.00	0.1	1.00	0.05
								Earth surface III standard	≤20	≤4	-	≤1.0	≤0.1	≤1.0	≤0.05

Description of the drawings: 1. physicochemical purification following COD and BOD₅The removal rate is increased due to the increase of the concentration, and the COD is higher than 500mg/L (chemical oxygen demand), BOD₅The removal rate of the municipal sewage higher than 250mg/L is up to more than 90 percent, and the COD is 200-500 mg/L, BOD₅COD and BOD of municipal sewage of 150-250 mg/L₅The removal rate is 75-90%, and the COD is lower than 200mg/L (chemical oxygen demand) and BOD₅COD and BOD of municipal sewage higher than 100mg/L₅The removal rate is 65-80%; the physicochemical purification has poor ammonia nitrogen removal effect, the total nitrogen removal rate is 5-30%, and the total phosphorus removal rate is up to 98%;

2. the removal rate of ammonia nitrogen in municipal sewage by catalytic electrolysis is up to 97-99%, and the removal rate of total nitrogen is up to 90-96%.

The residence time of each step after the above treatment is shown in Table 2.

Table 2 residence time units for the procedure: min

First stage treatment

Coagulating sedimentation

Electrolytic purification

Reduction of

Biochemical engineering

Disinfection

Total up to

5～10

15～20

20～60

20～30

180～300

25～30

265～450

After the municipal sewage purification system adopting the physicochemical purification and the electrolytic purification is treated by the steps, more than 92 percent of COD in the water body can be removed, the COD of the effluent is less than or equal to 20mg/L, 98 percent of BOD is removed, the BOD of the effluent is less than or equal to 4mg/L, 99 percent of total phosphorus is removed, the total phosphorus of the effluent is less than or equal to 0.1mg/L, 98 to 99.99 percent of ammonia nitrogen is removed, the ammonia nitrogen of the effluent is less than or equal to 1.0mg/L, more than or equal to 98 percent of total nitrogen is removed, the total nitrogen of the effluent is less than or equal to 1.0mg/L, 95 to 100 percent of chroma is removed, the chroma is less than or equal to 2, and. Is particularly suitable for the purification treatment of municipal sewage, and leads the water body to reach the water quality standard of more than III (including III) in the environmental quality standard of surface water (GB 3838-2002). The main indexes of inlet and outlet water of sewage after deep purification by catalytic electrolysis are shown in table 3.

TABLE 3 Main indices of inlet and outlet water for purifying sewage or water

The invention eliminates the defects of poor effluent quality, large investment, long purification period and large occupied area of the existing sewage treatment process of the sewage treatment plant, so that the effluent of the sewage treatment plant reaches the IV-class or even III water quality standard of the quality standard of surface water environment (GB3838-2002), becomes a water resource which can be recycled, and the purified water is discharged to a natural water system, so that the water quality of the water body is improved, the water ecological system is recovered, and the reconstruction and the healthy sustainable development of river and lake ecological systems are realized. Compared with the prior art, the invention has the following outstanding effects:

1. high water quality and changing sewage into recyclable water resource

After the municipal sewage is purified by adopting the system and the method for the catalytic electrolysis deep purification of the municipal sewage, all indexes reach the III and above standards of surface water environmental quality Standard (GB3838-2002), the content of dissolved oxygen is higher than 5mg/L, the sewage is converted into water resources which can be recycled, and the water resources are discharged into natural water bodies, so that the dissolved oxygen of the water bodies can be effectively improved, the growth of algae is effectively inhibited, the water quality is comprehensively improved and promoted, and meanwhile, the system and the method can be used as industrial and agricultural production and commercial water.

2. Eliminate nitrogen and phosphorus pollution from source

At present, the discharge standard of sewage is that total nitrogen is less than or equal to 15mg/L and total phosphorus is less than or equal to 0.5mg/L, and a large amount of nitrogen and phosphorus enter a water body along with the discharge water of the sewage treatment plant, so that nitrogen and phosphorus in the water body of rivers and lakes are greatly enriched, so that the discharge water of the sewage treatment plant is one of main sources of nitrogen and phosphorus in the water body of the rivers and lakes, and the nitrogen and phosphorus in the water body accumulate in the days and months, so that the nitrogen and phosphorus seriously exceed the standards, and the eutrophication of the water body of the rivers and lakes is caused, and the blue-green algae in the main lakes in China are erupted year after year. In order to radically treat blue algae, China invests a great deal of financial resources, manpower and material resources, but the yield is not high. After the municipal sewage deep purification system and the method thereof are adopted to purify the sewage, the total nitrogen of the water body is less than or equal to 1mg/L, and the total phosphorus is less than or equal to 0.1mg/L, which all reach the III-class water quality standard of the environmental quality standard of surface water (GB3838-2002), and the nitrogen and phosphorus pollution of the water body can be thoroughly eradicated from the source.

3. Simple process flow and simple operation

The sewage treatment by the method only comprises two main processes of physicochemical purification and catalytic electrolysis, and the production process flow is simpler than the existing sewage treatment production process flow, the number of building structures is less, and the operation is simpler.

4. Saving two thirds of land

At present, when sewage treatment plants constructed by an activated sludge method are adopted at home and abroad to treat sewage, most of the sewage stays for 16-20 hours, some of the sewage stays even for more than 20 hours, the land occupation of each ten thousand tons of sewage treatment facilities is 0.6-1 hectare, and the land occupation is large. When the municipal sewage deep purification system is used for treating municipal sewage, the retention time of a water body is only 6.0-7.0 hours, the occupied area of the device is only one third of that of a traditional device, the occupied area is small, land resources can be greatly saved, the municipal sewage deep purification system is particularly suitable for cities with short land resources, is more suitable for expansion transformation and upgrading transformation of the existing sewage treatment plants with short land resources, and is also suitable for transformation of the sewage treatment plants in the center of the city and with short land resources so as to make two thirds of the land.

5. Investment saving

At present, the investment for construction of ten thousand tons of fixed assets of urban sewage treatment plants per day of mainstream urban sewage treatment processes at home and abroad is about 3500-5000 ten thousand yuan, while the investment for construction of ten thousand tons of fixed assets of urban sewage treatment plants per day of deep water purification systems adopting the invention is about 4000-5000 ten thousand yuan, which is equivalent to the investment of the prior art, but the water quality is much higher, and the investment is relatively saved.

6. Low running cost

The operation cost of the municipal sewage deep purification system for deep purification treatment of sewage is lower than that of the existing urban sewage treatment plant, but the water quality is much higher, and the effluent is three types of water which can be recycled, so the operation cost is relatively lower.

7. Short construction period

The main equipment physicochemical purification device, the electrolysis device and the like of the municipal sewage deep purification system are all setting equipment, the main equipment is produced in factories, and when the sewage treatment plants are built by adopting the equipment, the setting equipment is assembled in the sewage treatment plants without building a large number of structures, so that the construction period of the sewage treatment plants is shortened by more than half compared with the construction period of the traditional sewage treatment plants, and the construction period is short.

In addition, the sludge of the sewage treatment plant constructed by the invention does not contain a large amount of microbial colonies, and the dehydration is relatively easy. Meanwhile, as the anaerobic treatment process is not adopted, no odor is generated in the running process of the sewage treatment facility, and the investment of a deodorization device is avoided.

Drawings

In order to more clearly illustrate the technical solution of the present invention, the drawings needed for the description of the embodiments or the prior art will be briefly described below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings without creative efforts.

FIG. 1 is a schematic connection diagram of the system for deep purification and recycling of municipal sewage according to the present invention.

FIG. 2 is a schematic structural diagram of a primary treatment apparatus according to the present invention.

FIG. 3 is a schematic structural diagram of the purification apparatus for materialization of the present invention (high efficiency precipitation).

FIG. 4 is a schematic view of the physical and chemical purification apparatus according to the present invention (air flotation).

FIG. 5 is a schematic structural view of the catalytic electrolysis deep purification apparatus of the present invention.

FIG. 6 is a schematic structural view of an aerobic purification apparatus according to the present invention.

FIG. 7 is a schematic view showing the construction of a biological aerated filter apparatus according to the present invention.

FIG. 8 is a schematic view of the structure of a sludge treatment apparatus of the present invention.

Detailed Description

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments of the present invention without any inventive step, are within the scope of the present invention.

Referring to fig. 1, a municipal sewage's deep purification regeneration system, includes primary treatment device (100), materialization purifier (200), catalytic electrolysis deep purification device (300), reduction pond (400) (quality of water is recovered) that reduces and eliminates sodium hypochlorite, biochemical purifier (500) and sludge treatment device (600), wherein:

primary treatment device (100): referring to fig. 2, the primary treatment apparatus (100) includes a coarse grill (110), a fine grill (120), a grit chamber (130), and a lift pump (140); an input port of the coarse grating (110) is communicated with a sewage pipe network, an output port of the coarse grating (110) is communicated with an inlet of the fine grating (120), an output end of the fine grating (120) is communicated with a water inlet of the grit chamber (130), and a water outlet of the grit chamber (130) is communicated with the lift pump (140); the primary treatment device (100) is used for removing large particles such as leaves, branches, fruit peels, waste plastics, paper and the like and mud and sand in the sewage; the grit chamber (130) is one of an aeration grit chamber or a cyclone grit chamber.

Materialization purification apparatus (200): the materialized purification device (200) is one of an air flotation purification device or a coagulating sedimentation purification device; referring to fig. 4, the materialized purification device (200) is the air-floating purification device, and comprises a pH adjusting tank (210), a coagulation tank (220), a coagulation aiding tank (230), an air-floating tank (240) and a middle water tank (250); the water inlet of the pH adjusting tank (210) is connected with the water outlet of a lifting pump (140) behind the grit chamber (130), the water outlet of the pH adjusting tank (210) is connected with the water inlet of the coagulation tank (220), the water outlet of the coagulation tank (220) is connected with the water inlet of the coagulation aiding tank (230), the water outlet of the coagulation aiding tank (230) is connected with the water inlet of the air flotation tank (240), a scum outlet (241) is further arranged at the upper part of the air flotation tank (240), a clear water outlet (242) is arranged at the lower part of the air flotation tank (240), the clear water outlet (242) is connected with the water inlet of the middle water tank (250), and the scum outlet (241) is connected with a sludge pump (244). Referring to fig. 3, the materialized purifying device (200) is a coagulating sedimentation purifying device, which comprises a pH adjusting tank (210), a coagulating tank (220), a coagulation aiding tank (230), a settling tank (240') and an intermediate water tank (250); the water inlet of the pH adjusting tank (210) is connected with the water outlet of a lifting pump (140) behind the grit chamber (130), the water outlet of the pH adjusting tank (210) is connected with the water inlet of the coagulation tank (220), the water outlet of the coagulation tank (220) is connected with the water inlet of the coagulation aiding tank (230), the water outlet of the coagulation aiding tank (230) is connected with the water inlet of a sedimentation tank (240 '), the top of the sedimentation tank (240') is provided with a supernatant outlet (241 '), and the supernatant outlet (241') is connected with the water inlet of the intermediate water tank (250); the bottom of the sedimentation tank (240 ') is provided with a sludge outlet (242 '), and the sludge outlet (242 ') is connected with a sludge pump (244); the materialization purification device (200) removes SS, chroma, water insoluble COD and BOD in the sewage₅Petroleum based, anionic surfactant and total phosphorus.

The catalytic electrolysis deep purification device (300) is shown in figure 5 and comprises an electrolysis machine (310), a direct current power supply (320), a degassing tank (330), an electrolyte feeding device (340) and an electrode cleaning device (350), wherein a water inlet of the electrolysis machine (310) and the middle part of the electrolysis machine (310) are connected with each otherThe water outlet of the intermediate water pool (250) is connected, the water outlet of the electrolytic machine (310) is connected with the water inlet (331) of the degassing pool, the water outlet (333) of the degassing pool is connected with the water inlet pipe (410) of the reduction pool, the water outlet (430) of the reduction pool is communicated with the water outlet pipe, and a circulating water pump (345) is arranged between the water outlet of the reduction pool and the water inlet of the air flotation pool or the sedimentation pool (240 or 240') and is used for refluxing part of the effluent into the physicochemical purification device (200); the clean water after the deep purification by electrolysis firstly enters a water distributor (332) at the bottom of the degassing tank (330) through a water inlet (331) of the degassing tank, and then enters a water distributor (420) at the bottom of a reduction tank (400) through a water inlet pipe (410) of the reduction tank arranged at the upper part of the degassing tank (330); the electrolyte adding device (340) is composed of an electrolyte solution storage tank (341), an electrolyte solution delivery pump (342) and an electrolyte solution flowmeter, and the electrolyte adding device (340) is arranged on a pipeline from the lift pump to the electrolysis machine (310) and is mixed with sewage by adopting a pipeline mixer; the electrode cleaning device (350) is composed of a pickling solution storage tank (351) and a pickling solution delivery pump (352); the bottoms of the degassing tank (330) and the reduction tank are also provided with a drain outlet (334), and the drain outlet (334) is connected with a water inlet pipe of the materialization purification device (200); the catalytic electrolysis deep purification device (300) is used for removing ammonia nitrogen, total nitrogen and residual chroma, water-soluble COD and BOD after treatment by the physicochemical purification device (200)₅Petroleum, and anionic surfactants.

The reducing pool (400) comprises a water inlet pipe (410), a pipeline mixer arranged on the water inlet pipe, a water distributor (420), a reducing agent solution storage tank and a reducing agent solution metering and conveying pump; the water inlet pipe (410) is connected with a water outlet (333) at the top of a degassing tank (330) of the catalytic electrolysis deep purification device (300), and the middle part of the water inlet pipe (410) is provided with a pipeline mixer; the reducing agent solution storage tank is communicated with a water inlet pipe (410) through a reducing agent solution metering and conveying pump and is arranged in front of the pipeline mixer, and a water pipe connected with the middle water tank is also arranged on the water inlet pipe; the reduction pool (400) is used for removing the residual sodium hypochlorite treated by the catalytic electrolysis deep purification device (300), so that the water body property is restored, and the subsequent biochemical treatment is facilitated.

Biochemical purification device (500): the biochemical purification device (500) is one of an aerobic purification device or an aeration biological filter; referring to fig. 6, the biochemical purification device (500) is an aerobic purification device, which comprises an aerobic tank (510), an aeration pipe (511), an aeration fan (512), a sewage outlet (513), a sludge outlet (514), a secondary sedimentation tank (520) and a disinfection tank (530); the water inlet of the aerobic tank (510) is communicated with the water outlet of the reduction tank (400), the sewage outlet (513) of the aerobic tank (510) is communicated with the water inlet of the secondary sedimentation tank (520), and the water outlet of the secondary sedimentation tank (520) is communicated with the water inlet of the disinfection tank (530). Referring to fig. 7, the biochemical purification device (500) is an aeration biological filter, and is composed of a biological filter body (510'), an aeration pipe (520'), a support (530'), a filter material support layer (540'), a filter material (550'), a water collecting tank (560'), an aeration fan (570'), a backwashing water pipe (580'), a sewage outlet (511'), a sludge outlet (514') and a disinfection tank (590'), wherein the filter material is arranged above the filter material support layer, the support is arranged below the filter material support layer, and the aeration pipe is arranged below the filter material support layer; the water inlet of the biological aerated filter is communicated with the water outlet of the reduction tank (400), and the sewage outlet (511') of the biological aerated filter is communicated with the water inlet of the disinfection tank (590').

The sludge treatment device (600) is shown in fig. 8 and comprises a sludge pump (244), a sludge concentration tank (610), a physicochemical adjusting tank (620), a dehydrator (630) and a sludge tank (640); the inlet of the sludge pump (244) is connected with the sludge outlet or the scum outlet of the materialization purification device; an outlet of the sludge pump (244) is connected with an inlet of the sludge concentration tank (610), a supernatant outlet (611) is arranged at the upper part of the sludge concentration tank (610), and a concentrated sludge outlet (612) is arranged at the bottom of the sludge concentration tank (610); the supernatant water outlet (611) is connected with the water inlet of the physicochemical purification device (200), the concentrated sludge outlet (612) is connected with the inlet of the physicochemical adjusting tank (620), the outlet of the physicochemical adjusting tank (620) is connected with the dehydrator (630), the water outlet (631) of the dehydrator is connected with the water inlet of the physicochemical purification device (200), and the sludge outlet of the dehydrator (630) is connected with the sludge tank (640).

The air-flotation purification of the materialized purification device (200) is one of dissolved air flotation or shallow layer air flotation.

The coagulating sedimentation device (200) is one of a high-efficiency sedimentation device, a magnetic coagulation device and a supermagnetic coagulating sedimentation device.

The coagulation tank (220) also comprises a coagulant dosing device and a stirrer; ferric sulfate, ferric trichloride solution or polyaluminium chloride solution with the mass ratio of 1-20% is stored in the coagulant dosing device (211); the coagulant aid tank (230) also comprises a coagulant aid dosing device and a stirrer; PAM solution with the mass ratio of 1-2 per mill is stored in the coagulant aid dosing device.

The working voltage of the electrolysis machine (310) can be 5-300V, and the current density can be 10-150 mA/cm²。

The catalytic electrolysis deep purification device (300) further comprises an electrolyte adding device (340) of an electrolysis machine, wherein the electrolyte adding device comprises an electrolyte solution storage tank (341) and an electrolyte solution delivery pump (342).

More specifically, the electrolyte adding device (340) is used for adding 8-12% of sodium hypochlorite solution or 2-6% of sodium chloride solution into the catalytic electrolysis deep purification device (300).

Preferably, during catalytic electrolysis, an electrolyte adding device (340) is adopted to add 10-12% of sodium hypochlorite solution into the catalytic electrolysis deep purification device according to the concentration of ammonia nitrogen in the water body, and the adding amount is three-ten-thousandth to one-thousandth (volume ratio);

optimally, adding 10-12% of sodium hypochlorite solution into the catalytic electrolysis deep purification device in an amount of three to six ten-thousandths (volume ratio);

specifically, the catalytic electrolysis deep purification device also comprises an electrode cleaning device (350) of the electrolysis main machine (310), which is composed of a pickling solution distribution tank (351) and a pickling solution delivery pump (352). The acid washing solution adopts 2 to 3 percent hydrochloric acid solution or 4 to 5 percent citric acid solution. When the electrodes of the catalytic electrolysis deep purification device are polluted and scaled and the electrolysis efficiency is reduced, the catalytic electrolysis device stops working, and the electrode cleaning device (350) is started to remove the scale deposited on the surfaces of the electrodes.

Furthermore, the wastewater of the electrode cleaning device (350) enters a materialization purification device (200) for treatment.

Furthermore, a water inlet (331) of a degassing tank (330) of the catalytic electrolysis deep purification device (300) is connected with a water distributor (332) at the bottom of the degassing tank (330), a water outlet (333) at the upper part of the degassing tank is connected with a water inlet pipe (410) of a reduction tank (400), and the top of the degassing tank (330) is also provided with a slag scraper and a scum collecting tank for removing and collecting bubbles and scum generated by a large amount of nitrogen and carbon dioxide released during electrolysis deep purification; the slag scraper is a reciprocating type or a rotary type slag scraper.

Specifically, the reduction pool (400) is sleeved in the degassing pool (330), a water inlet pipe of the reduction pool is connected with a water outlet of the degassing pool (330), the water inlet pipe is connected with a water distributor (420) at the bottom of the reduction pool (400) from top to bottom, and the water outlet of the reduction pool (400) is connected with a water outlet pipe; the reduction pool (400) is also provided with a reducing agent solution storage tank, a reducing agent solution feeding metering pump and a stirrer; the bottom of the degassing tank (330) and the bottom of the reduction tank (400) are provided with drain outlets (334), and the drain outlets (334) are connected with water inlets of the air floatation or coagulation sedimentation device (200).

Specifically, the coagulation tank (220) comprises a coagulant dosing device and a stirrer, wherein one of a PAC (poly aluminum chloride) solution, a ferric sulfate solution and a ferric trichloride solution with the mass ratio of 1-10% is placed in the coagulant dosing device; the coagulant aid tank (230) comprises a tank body, a coagulant aid dosing device and a stirrer, wherein a PAM solution with the mass ratio of 1-2 per mill is stored in the coagulant aid dosing device.

Further, the coagulation device also comprises a sludge return pump (243) which is used for returning part of sludge in the sedimentation tank to the coagulation aiding tank (230), wherein the input port of the sludge return pump (243) is communicated with the sludge outlet, and the output port of the sludge return pump (243) is communicated with the coagulation aiding tank (230).

Specifically, sludge dewatering device (600), including sludge pump (244), sludge concentration tank (610), physics and chemistry equalizing basin (620) and hydroextractor (630), sludge concentration tank is gravity concentration tank, the export of sludge mouth, mud export and dross collecting vat respectively with the input port intercommunication of sludge pump (244), the delivery outlet of sludge pump (244) with gravity concentration tank's entry intercommunication, including the sludge concentration district of the clear liquid district on upper strata and the sludge concentration district of lower floor from top to bottom in gravity concentration tank (610), the delivery port of upper strata district is used for the inlet tube of intercommunication air supporting or coagulating sedimentation purifier (200), the mud outlet of lower strata district with the import intercommunication of hydroextractor (630), gravity concentration tank (610), physics and chemistry equalizing basin (620) and hydroextractor (630) communicate in proper order.

Specifically, the municipal sewage deep purification and recycling system can adopt one of an underground type, a semi-underground type or an above-ground type.

The deep purification and regeneration utilization method of the municipal sewage comprises the following steps:

(1) primary treatment: the municipal sewage is filtered by the coarse grating (110) and the fine grating (120) in sequence to remove large granular solids, then is output and flows into the grit chamber (130) to remove silt;

(2) physicochemical purification: inputting the effluent water obtained in the step (1) into a pH adjusting tank (210), and adding 3-10 g/m³Continuously stirring the sodium hydroxide or sodium carbonate solution at the stirring speed of 80-200 r/min for 5-10 min, and adjusting the pH of the sewage to 9-9.5; feeding the sewage with the pH value adjusted to 9-9.5 into a coagulation tank (220), and adding 6-20 g/m of the sewage through a coagulant adding device³Continuously stirring the coagulant solution at the stirring speed of 100-200 r/min for 3-6 min; the effluent after coagulant addition is input into a coagulation aiding tank (230), PAM is added through a coagulant aid dosing device, and the relation between the weight of the added PAM and the volume of the sewage is 0.1-1 g/m³Stirring and reacting for 3-10 min at a stirring speed of 20-80 r/min; the effluent of the coagulation tank is input into an air flotation tank or a sedimentation tank (240) for solid-liquid separation, clear liquid is concentrated at the bottom of the air flotation tank (240) or the upper layer of the sedimentation tank (240 '), scum or solid substances are collected at the upper part of the air flotation tank (240) or the bottom of the sedimentation tank (240 '), and a solid-liquid separation middle area is formed in the middle of the air flotation tank or the sedimentation tank (240 or 240 '); judging whether the sediment amount formed in the coagulation aiding tank (230) in the steps is sufficient or not, if not, starting a sludge return pump (243), and returning partial sludge from the sedimentation tank (240) into the coagulation aiding tank (230) to promote generation of flocculent sediment; the clear liquid of the sewage obtained by physicochemical purification is input into an intermediate water tank(250) Performing the following steps; the main water quality of the effluent of the municipal sewage after physicochemical purification treatment is that the pH is 6-9, the chroma is less than 10, the COD (chemical oxygen demand) is less than or equal to 80mg/L, the total phosphorus (counted by P) is less than or equal to 0.3mg/L, the anionic surfactant is less than or equal to 0.5mg/L, and the petroleum is less than or equal to 0.5 mg/L;

(3) deep purification by catalytic electrolysis: conveying the purified clean water in the step (2) to an electrolytic machine (310) of a catalytic electrolysis deep purification device (300) through a lifting pump, and carrying out electrolytic denitrification deep purification on the clean water, wherein the sewage stays in the electrolytic machine (310) for 30-300 s; when sewage enters an electrolysis machine, adding 10-12% of sodium hypochlorite according to the proportion of 0.3-1 per mill (volume ratio), uniformly mixing by a pipeline mixer, and conveying the mixture to the electrolysis machine (310) for electrolytic denitrification; hypochlorous acid generated by the electrolysis machine (310) reacts with ammonia nitrogen in the sewage to be converted into nitrogen; the working voltage of the electrolysis machine (310) is 5-300V, and the current density is 10-150 mA/cm²(ii) a Delivering the effluent obtained by electrolysis to a degassing tank (330), wherein the retention time is 10-60 min, and sodium hypochlorite generated by an electrolysis machine (310) reacts with COD in the water body to further remove COD and BOD in the water₅(ii) a Meanwhile, the oxygen of the new ecology generated by the electrolysis machine (310) reacts with the organic matters to remove COD and BOD in the sewage; a large amount of gases such as nitrogen, carbon dioxide and the like generated by electrolytic denitrification are released in a degassing pool (330) to generate a large amount of bubbles, and scum is collected in a scum collecting tank by a scum scraper; the clean water after the electrolytic denitrification and the deep purification is injected into a reduction tank (400); the catalytic electrolysis deep purification device (300) is used for removing ammonia nitrogen, total nitrogen and residual chroma, water-soluble COD and BOD after treatment by the physicochemical purification device (200)₅Petroleum, anionic surfactant, the main indexes of effluent water are as follows: the pH value is 6-9, the chroma is less than 4, and the COD (chemical oxygen demand) is less than or equal to 30mg/L, BOD₅(five-day biochemical oxygen demand) is less than or equal to 6mg/L, NH3-N (ammonia nitrogen) is less than or equal to 1.5mg/L, total nitrogen is less than or equal to 3.0mg/L, total phosphorus (counted by P) is less than or equal to 0.3mg/L, anionic surfactant is less than or equal to 0.3mg/L, petroleum is less than or equal to 0.5mg/L, faecal coliform is less than or equal to 10 (ammonia nitrogen/nitrogen), and dissolved oxygen is more than or equal to 3 mg/L;

(4) reducing and eliminating sodium hypochlorite: quantitatively adding a 5-20% sodium sulfite solution into a reduction tank (400) or pumping one fifth to one third of coagulating sedimentation supernatant from an intermediate water tank (250) of a physicochemical purification system to mix with electrolytic water in the reduction tank to eliminate excessive sodium hypochlorite in the clear water and recover the water body;

(5) biochemical purification: carry the water after removing sodium hypochlorite through the reduction to the cell body of biochemical purifier (500), carry out biochemical treatment, the dwell time of polluted water in biochemical pond is 180 ~ 300min for detach remaining COD, BOD5, total phosphorus and total nitrogen, main index after biochemical treatment is: the pH value is 6-9, the chroma is less than 2, the COD (chemical oxygen demand) is less than or equal to 20mg/L, BOD5 (five-day biochemical oxygen demand) is less than or equal to 4mg/L, NH3-N (ammonia nitrogen) is less than or equal to 1.0mg/L, the total nitrogen is less than or equal to 1.0mg/L, the total phosphorus (calculated by P) is less than or equal to 0.1mg/L, the fluoride (calculated by F-) is less than or equal to 1.0mg/L, the copper is less than or equal to 1.0mg/L, the zinc is less than or equal to 1.0mg/L, the selenium is less than or equal to 0.01mg/L, the arsenic is less than or equal to 0.05mg/L, the anionic surfactant is less than or equal to 0.2mg/L, the petroleum is less than or equal to 0.05mg/L, the faecal coliform group is less than or equal; for example, the biochemical purification device is an aerobic purification device, the water body treated by the aerobic tank is sent to a secondary sedimentation tank of a biochemical system, solid-liquid separation is carried out in the secondary sedimentation tank, the supernatant is disinfected and reaches the III or IV class water quality standard of surface water environmental quality standard (GB3838-2002), and the bottom sludge is sent to a sludge treatment device (600) through a sludge pump for sludge dehydration treatment.

(6) Sludge dewatering: respectively conveying sludge generated by the primary treatment (100) and the physicochemical purification (200) and scum or sediment obtained by catalytic electrolysis deep purification into a sludge concentration tank (610), and performing gravity concentration to form supernatant on the upper part and sludge on the bottom part; conveying the supernatant in the supernatant layer to a water inlet pipe of an air floatation or coagulating sedimentation purifying device (200), and inputting bottom sludge into a physicochemical adjusting tank (620); adding a physical and chemical conditioner into the physical and chemical regulating pool (620), conveying the physical and chemical conditioner into a dehydrator (630), processing the physical and chemical conditioner into organic mud blocks, and collecting the organic mud blocks, wherein the physical and chemical conditioner comprises lime, ferric trichloride and polyaluminium chloride.

In the processes of coagulation, coagulation aiding and precipitation, phosphate radicals and hydrogen phosphate radicals in the sewage react with trivalent aluminum ions or trivalent iron ions to generate iron phosphate precipitates, so that total phosphorus in the sewage is removed;

3Al³⁺+2PO₄ ^3-＝Al₃(PO₄)₂↓

in addition, as a large amount of generated floc precipitates have huge specific surface area and are charged, organic matters in the sewage can be adsorbed, and the chromaticity and COD in the sewage can be removed simultaneously;

after physicochemical purification treatment, 80-95% of SS in the water body is removed, so that the SS in the water body is less than or equal to 50mg/L, 90-95% of total phosphorus in the water body is removed, so that the total phosphorus in the water body is less than or equal to 0.2mg/L, and 85-95% of COD in the water body is removed together, so that the COD in the sewage is less than or equal to 80 mg/L;

in step 3), the specific steps of the catalytic electrolysis deep purification can be as follows:

catalytic electrolysis: conveying the sewage subjected to physicochemical purification to an electrolysis machine (310) through an intermediate water tank (250) and a lifting pump for electrolysis for 30-300 s; during electrolysis, 10-12% of sodium hypochlorite solution or 2-6% of sodium chloride solution is added through an electrolyte adding system;

during the catalytic electrolysis deep purification, in the electrolysis equipment, the sodium hypochlorite generated by electrolysis reacts with ammonia nitrogen to generate nitrogen and sodium chloride, and the sodium chloride is electrolyzed to generate sodium hypochlorite.

NaOCl+H₂O→HOCl+NaOH

NH₃+HOCl→NH₂Cl+H₂O (monochloramine)

NH₂Cl+HOCl→NHCl₂+H₂O (dichloramine)

2NHCl₂+NaOCl→N₂↑+3NaCl+H₂O (denitrogenation main reaction one)

The main reaction formula is as follows:

2NH₃+3NaOCl→N₂↑+3NaCl+3H₂O

the generated sodium chloride is electrolyzed to generate sodium hypochlorite for repeated use, and the sodium hypochlorite plays a role as a catalyst.

Principle of deammoniation (side reaction)

At the same time, the radical O.produced by electrolysis reacts with ammonia to produce nitrate radical.

2NH⁴⁺+5O₂→2NO₃ ^-+4H₂O

In addition, hydrogen generated by electrolysis reacts with nitrate and nitrite in the water body under the action of the catalyst to generate nitrogen, so that nitrate nitrogen in the water body is removed.

NO₃ ^-+H₂—→NO₂ ^-+H₂O

2NO₂ ^-+2H₂—→N₂↑+2H₂O (total nitrogen removal reaction)

Clear water after catalytic electrolysis deep purification flows into the water distributor at the bottom of the reduction tank through the top of the degassing tank, the clear water flows from bottom to top, and the content of sodium hypochlorite in the produced excessive sodium hypochlorite reduced effluent by 5-20% of sodium sulfite is less than or equal to 0.1 mg/L.

Specific examples are given below.

Example 1

The municipal sewage treatment plant constructed by the production process comprises primary treatment, physicochemical purification, catalytic electrolysis deep purification, sodium sulfite solution reduction, biochemical treatment and sludge dehydration, wherein the production process comprises the following steps: the primary treatment adopts a process of a coarse grating, a fine grating and an aeration desilting tank; the physicochemical purification adopts a coagulating sedimentation (high density sedimentation) process, and the biochemical treatment is an aerobic treatment process.

TABLE 1 Water quality index of Water inlet and outlet designed for certain Sewage treatment plant

And the municipal domestic sewage enters the municipal sewage deep purification and recycling system. The municipal sewage deep purification and recycling system comprises a primary treatment device (100), a materialization purification device (200), a catalytic electrolysis deep purification device (300), a reduction tank (400), an aerobic purification device (500) and a sludge treatment device (600).

The materialized purification device (200) is a coagulating sedimentation purification device.

The sewage enters a primary treatment device (100), a coagulating sedimentation device (200), a catalytic electrolysis deep purification device (300), a reduction tank (400) and an aerobic purification device in sequence.

Adding 20% sodium hydroxide solution into sewage to adjust the pH to 9, adding 10% polyaluminium chloride (PAC) solution coagulant with the addition amount of 12mg/L (calculated by PAC), carrying out coagulation reaction at the rotating speed of 100 revolutions per minute, adding 1mg/L coagulant aid PAM, reacting at the rotating speed of 20 revolutions per minute, and separating in a sedimentation tank, wherein the water quality of the coagulating sedimentation effluent is shown in Table 2.

TABLE 2 Water quality index after efficient precipitation treatment of certain municipal wastewater treatment plant at certain day

Serial number	Item	Sewage plant influent (mg/L)	High density water (mg/L)	Removal Rate (%)
					1	COD	481.5	72.05	85.04
2	BOD	206	66.51	67.71
					3	SS	200	15	92.50
4	Animal and vegetable oil	-	0.5
					5	Petroleum products	-	0.3
6	Total nitrogen (in N)	47.2	45.31	4.00
					7	Ammonia nitrogen (in N)	42.7	40.09	6.11
8	Total phosphorus(in P)	8	0.26	88.13
					9	Dissolved oxygen	-	2.5	-
10	Chroma (dilution multiple)	80	20	75.00
					11	pH	6～9	6-9	-

As can be seen from Table 2, the physicochemical purification device (200) (coagulating sedimentation) has good removal effects on SS, COD, BOD, total phosphorus, animal and plant oil, petroleum and chromaticity, but has poor removal effects on ammonia nitrogen and total nitrogen. The sewage after coagulating sedimentation enters a catalytic electrolysis deep purification device (300) for treatment, the treated water body enters a reduction pool (400) to eliminate sodium hypochlorite, so that the water quality is reduced, and the effluent indexes are shown in table 3. The working voltage of the electrolytic machine (310) for catalytic electrolysis is 36.5V, and the current density is 11mA/cm². When the electrolysis host machine works, a 12% sodium hypochlorite solution is added according to four ten-thousandth of the volume ratio and is uniformly mixed into the sewage through a pipeline mixer.

TABLE 3 Water quality index of a certain sewage after coagulating sedimentation and electrolytic purification

Serial number	Item	Coagulation water (mg/L)	Purified water (mg/L)	Removal Rate (%)
					1	COD	72.05	36.40	49.48
2	BOD	66.51	Not detected out	-
					3	SS	15	6	60.00
4	Animal and vegetable oil	0.5	0.4	20
					5	Petroleum products	0.3	0.2	33.33
6	Total nitrogen (in N)	45.31	2.63	94.20
					7	Ammonia nitrogen (in N)	40.09	0.72	97.21
8	Total phosphorus (in terms of P)	0.26	0.21	19.23
					9	Dissolved oxygen	2.5	8.91	-
10	Chroma (dilution multiple)	20	2	-
					11	pH	6～9	6～9	-

The clean water after the electrolytic purification treatment enters a reduction tank (400) to reduce and eliminate excessive sodium hypochlorite generated during the electrolytic purification, and then enters an aerobic purification device for further purification treatment, and the purified water quality is shown in the table 5.

TABLE 5 effluent quality index of clean water after electrolysis and purification and after aerobic further purification

The water quality of the sewage treatment plant operating continuously for 7 days is shown in Table 6.

Table 6 water quality index recording table unit for continuous one-week operation of a certain sewage treatment plant: (mg/L)

From table 5, it can be seen that the effluent indexes of the sewage after passing through the advanced purification and recycling device for municipal sewage completely meet the quality standards for surface water environment (GB3838-2002 III water quality standards), and from table 6, the effluent purified by the advanced purification and recycling system for municipal sewage completely meets the quality standards for surface water environment (GB3838-2002 III water quality standards, and the effluent quality is stable, although the fluctuation of the quality of the influent water is large.

Example 2

The municipal sewage treatment plant of 20000 tons/day constructed by the production process mainly comprises a primary treatment device (100), a physicochemical purification device (200), a catalytic electrolysis deep purification device (300), a sodium hypochlorite reduction and elimination device (400), a biological aerated filter (500) and a sludge treatment device (600). Wherein: the primary treatment device (100) adopts a process of a coarse grating, a fine grating and a rotational flow desilting tank; the physicochemical purification adopts a super-magnetic precipitation separation process; the sludge dewatering adopts a centrifugal dewatering process. The sewage treatment plant is characterized by smaller treatment scale, lower COD (chemical oxygen demand) of inlet water, higher ammonia nitrogen and total nitrogen and unbalanced nutrition, if the traditional AAO sewage treatment process is adopted, a carbon source must be continuously added during operation, the operation cost is high, the total nitrogen of outlet water is higher, the technical requirement that the total nitrogen of the outlet water is less than or equal to 1mg/L cannot be met, and in addition, the project is positioned in the center of a city and has very short land use.

TABLE 7 designed Water in and out index of certain Sewage plant

Serial number	Item	Inflow (mg/L)	Water outlet (mg/L)	Removal Rate (%)
					1	COD	300	30	90.00
2	BOD	130	6	95.38
					3	SS	100	10	90.00
4	Total nitrogen (in N)	50	3	94.00
					5	Ammonia nitrogen (in N)	35	1.5	95.71
6	Total phosphorus (in terms of P)	3	0.3	90.00
					7	Chroma (dilution multiple)	100	5	95.00
8	pH	6～9	6～9	-
					9	Dissolved oxygen	-	6.5	-

And the sewage enters the municipal sewage deep purification and recycling system. The system comprises a primary treatment device (100), a materialization purification device (200), a catalytic electrolysis deep purification device (300), a reduction pool (400) for reducing and eliminating sodium hypochlorite, a biochemical purification device (500) and a sludge treatment device (600); the primary treatment device (100) is a coarse grating, a fine grating and a rotational flow desilting tank; the materialized purification device (200) is a super-magnetic precipitation separation device, and the biochemical purification device is an aeration biological filter.

The water body enters a primary treatment device (100), a physicochemical purification device (200), a catalytic electrolysis purification device (300), a reduction tank (400) for reducing and eliminating sodium hypochlorite by sodium sulfite and an aeration biological filter in sequence.

Adding 10% sodium hydroxide solution into sewage to adjust the pH value to 9, adding 20% PAC solution into the sewage in the coagulating sedimentation device (200), wherein the adding amount is 8mg/L, after coagulating reaction at the rotating speed of 100 revolutions, adding 1mg/L coagulant aid PAM, reacting at the rotating speed of 20 revolutions, and then entering a sedimentation tank for separation, wherein the water quality of the coagulating sedimentation water is shown in the table 8.

TABLE 8 Water quality index of certain sewage after ultramagnetic treatment

The water body after the supermagnetic precipitation treatment enters a catalytic electrolysis deep purification device (300) for treatment, the treated water body enters a reduction pool (400) for reduction, sodium hypochlorite in the water body is eliminated, and the effluent indexes are as shown in table 9. The working voltage of the electrolysis main machine (310) is 5V, and the current density is 150mA/cm². When the electrolysis main machine works, 12% of sodium hypochlorite solution is added into the sewage according to six ten-thousandth of the volume ratio and is uniformly mixed through a pipeline mixer.

TABLE 9 Water quality index of municipal sewage after advanced purification by supermagnetism and catalytic electrolysis

Serial number	Item	Coagulation water (mg/L)	Electrolyzed outlet water (mg/L)	Removal Rate (%)
					1	COD	80.00	30.00	62.50
2	BOD	65.00	6	90.77
					3	SS	10	10	0.00
4	Animal and vegetable oil	0.3	0.3	0.00
					5	Petroleum products	0.2	0.2	0.00
6	Total nitrogen (in N)	45.01	3.00	93.33
					7	Ammonia nitrogen (in N)	34.29	1.00	97.08
8	Total phosphorus (in terms of P)	0.3	0.20	33.33
					9	Dissolved oxygen	2.5	6.50	-
10	Chroma (dilution multiple)	30	5	83.33
					11	pH	7～9	7～9	-

The water after the electrolytic purification treatment is purified by the biological aerated filter, and the water quality of the purified effluent is shown in the table 9.

TABLE 9.1 effluent quality index after biological aerated filter purification

As can be seen from Table 9.1, the effluent index after biochemical purification reaches the environmental quality Standard for surface Water (GB3838-2002 III class water quality Standard).

The water quality of the sewage treatment plant which was continuously operated for one week is shown in Table 10.

Table 10 water quality index units for one week of continuous operation of a municipal sewage plant: mg/L

From table 9.1, it can be seen that the effluent indexes of the sewage after the sewage is treated by the municipal sewage deep purification and recycling system (primary treatment + ultra-magnetic purification + catalytic electrolysis deep purification + sodium sulfite reduction + biological aerated filter) completely meet the surface water environment quality standard (GB3838-2002 III type water quality standard, from table 10, the municipal sewage deep purification and recycling system is stable in operation, and the effluent water quality indexes completely meet the surface water environment quality standard (GB3838-2002 III type water quality standard).

Example 3

The municipal sewage treatment plant constructed by the production process comprises primary treatment, physicochemical purification, catalytic electrolysis deep purification, sodium sulfite solution reduction, biochemical purification and sludge dehydration, wherein the production process comprises the following steps: the primary treatment adopts a process of a coarse grating, a fine grating and an aeration desilting tank; the physicochemical purification adopts a magnetic coagulation process; the biochemical purification adopts aerobic tank treatment.

TABLE 11 Water quality index of the design of municipal sewage plants in certain North

Sewage gets into municipal administration sewage's catalytic electrolysis deep purification system, purification system include primary treatment device (100), materialization purifier (200), catalytic electrolysis purifier (300), sodium sulfite reduction pond (400), good oxygen purifier (500) and sludge treatment device (600).

The sewage enters a primary treatment device (100), a materialization purification device (200), a catalytic electrolysis purification device (300), a sodium sulfite reduction pool (400) and an aerobic purification device (500) in sequence.

Adding 15% of sodium hydroxide solution into the magnetic coagulation device to adjust the pH value of the sewage to 9, adding 15% of ferric sulfate coagulant with the addition amount of 30mg/L, carrying out coagulation reaction at the rotation speed of 100 revolutions, adding 1mg/L of coagulant aid PAM, reacting at the rotation speed of 30 revolutions, and then separating in a sedimentation tank, wherein the water quality of the magnetic coagulation effluent is as shown in Table 12.

TABLE 12 Water quality index after magnetic coagulation treatment in actual operation of certain sewage plant

Serial number	Item	Inflow (mg/L)	Magnetic coagulation water (mg/L)	Removal Rate (%)
					1	COD	723	73.5	89.83
2	BOD	305	61.3	79.90
					3	SS	183	9	95.08
4	Animal and vegetable oil	-	0.3	-
					5	Petroleum products	-	0.2	-
6	Total nitrogen (in N)	73.2	65.5	10.52
					7	Ammonia nitrogen (in N)	55.5	54.1	2.52
8	Total phosphorus (in terms of P)	6.8	0.23	96.62
					9	Dissolved oxygen	-	1.3	-
10	Chroma (dilution multiple)	80	5	93.75
					11	pH	7	7	-

As can be seen from Table 12, the magnetic coagulation showed high COD and BOD₅(COD is higher than 500mg/L, BOD is higher than 250mg/L) municipal sewage has fine removal effect, and it gets into catalytic electrolysis deep purification device (300) purification treatment to the sewage after magnetic coagulation handles, and the water gets into sodium sulfite reduction pond (400) and takes off sodium hypochlorite reaction after handling, and the index of going out water is as table 13. The working voltage of the electrolysis main machine (310) is 39V, and the current density is 10mA/cm². When the electrolysis host machine works, a sodium hypochlorite solution with the concentration of 12 percent is added into the electrolysis host machine according to one thousandth of the volume ratio and is uniformly mixed into sewage through a pipeline mixer.

TABLE 13 Water quality index of municipal sewage after catalytic electrolysis purification

Serial number	Basic control items	Magnetic coagulation water (mg/L)	Electrolyzed outlet water (mg/L)	Removal Rate (%)
					1	COD	73.5	21.3	71.0
2	BOD	61.3	1.1	60.2
					3	SS	9	8	11.1
4	Animal and vegetable oil	0.3	0.2	33.3
					5	Petroleum products	0.2	0.2	0
6	Total nitrogen (in N)	65.5	2.8	95.7
					7	Ammonia nitrogen (in N)	54.1	1.1	98.0
8	Total phosphorus (in terms of P)	0.23	0.19	17.4
					9	Dissolved oxygen	1.3	7.8	-
10	Chroma (dilution multiple)	5	2	60.0
					11	pH	7	7	-

The effluent after the electrolytic purification is biochemically purified, and the effluent is shown in a table 14

TABLE 14 quality of electrolyzed effluent after biochemical purification

Serial number	Basic control items	Electrolyzed outlet water (mg/L)	Biochemical effluent (mg/L)	Removal Rate (%)
					1	COD	21.3	8.96	57.93
2	BOD	1.1	0.23	79.09
					3	SS	8	7	12.5
4	Animal and vegetable oil	0.2	0.01	95.00
					5	Petroleum products	0.2	0.02	90.00
6	Total nitrogen (in N)	2.8	0.89	68.21
					7	Ammonia nitrogen (in N)	1.1	0.31	71.82
8	Total phosphorus (in terms of P)	0.19	0.08	57.89
					9	Dissolved oxygen	7.8	6.3	-
10	Chroma (dilution multiple)	2	2	-
					11	pH	7	7.1	-

The water quality of the sewage treatment plant which was continuously operated for one week is shown in Table 15.

Table 15 operation recording table of advanced purification and regeneration process for municipal sewage used in certain factory

From table 14, it can be seen that the effluent indexes of the sewage after the sewage is subjected to the advanced purification and recycling system (primary treatment, magnetic coagulation purification, catalytic electrolysis advanced purification, sodium sulfite reduction and aerobic) of the municipal sewage completely meet the surface water environment quality standard (GB3838-2002 III type water quality standard, from table 15, the advanced purification and recycling system adopting the municipal sewage operates stably, and the effluent quality meets the surface water environment quality standard (GB3838-2002 III type water quality standard).

Example 4

The production process of the invention is adopted for construction of a certain municipal sewage plant, and comprises primary treatment, physicochemical purification, catalytic electrolysis deep purification, sodium sulfite solution reduction, biochemical purification and sludge dehydration, wherein: the primary treatment (100) comprises: a coarse grating, a fine grating and an aeration desilting tank; shallow air flotation is adopted in the physicochemical purification (200); the biochemical purification adopts an aeration biological filter.

Municipal sewage enters a primary treatment device (100) for treatment and then enters a shallow air flotation purification device (200) for purification, effluent is subjected to deep purification through a catalytic electrolysis machine (310), effluent treated by an electrolysis host enters a degassing tank (330) for degassing, effluent from the degassing tank (330) flows through a secondary reduction tank (400) to remove residual sodium hypochlorite, and water is recovered and then purified through an aeration biological filter to obtain deep purified water. The design water inlet and outlet indexes of the process are shown in the table 16.

TABLE 16 Water quality index for municipal wastewater treatment plant

Serial number	Item	Inflow (mg/L)	Water outlet (mg/L)	Removal Rate (%)
					1	COD	300	20	93.33
2	BOD	150	6	96.00
					3	SS	200	10	95.00
4	Total nitrogen (in N)	50	1.0	98.00
					5	Ammonia nitrogen (in N)	35	1.0	97.14
6	Total phosphorus (in terms of P)	5	0.1	98.00
					7	Chroma (dilution multiple)	100	5	95.00
8	pH	6～9	6～9

The municipal sewage enters a primary treatment device of a catalytic electrolysis deep purification system of the sewage for treatment and then enters a shallow air flotation purification device (200) for purification to remove SS, COD and BOD₅And the water quality of the effluent is shown in the table 17 after pollutants such as total phosphorus, animal and plant oil, petroleum and the like.

TABLE 17 Water quality index of municipal wastewater after passing through shallow air flotation device

Serial number	Item	Sewage plant influent (mg/L)	Air-float water outlet (mg/L)	Removal Rate (%)
					1	COD	232.80	53.40	77.05
2	BOD	113.56	41.00	63.90
					3	SS	180	9	95.00
4	Animal and vegetable oil	1.2	0.3	75.00
					5	Petroleum products	0.7	0.2	71.43
6	Total nitrogen (in N)	47.70	43.68	8.43
					7	Ammonia nitrogen (in N)	42.52	42.63	-0.2
8	Total phosphorus (in terms of P)	3.5	0.17	95.14
					9	Dissolved oxygen	2.6	4.8	-
10	Chroma (dilution multiple)	100	20	80.00
					11	pH	7	7.2	-

As can be seen from Table 17, when the municipal wastewater concentration is low, the removal rate of pollutants such as COD by the physicochemical purification device is reduced. The shallow air floating purification device (200) has better removal effect on SS, COD, BOD, total phosphorus, animal and plant oil, petroleum and chromaticity, but has poor removal effect on ammonia nitrogen and total nitrogen. The water purified by the shallow air-floating purification device (200) is subjected to deep purification by an electrolysis machine (310), the water purified by the electrolysis machine (310) enters a degassing tank (330) for degassing to remove nitrogen, carbon dioxide and foams generated by degassing, the water discharged from the degassing tank (330) flows through a sodium hypochlorite reduction tank (400) to remove residual sodium hypochlorite, so that the sewage is subjected to deep purification, and the water quality of the discharged water is as shown in Table 18.

TABLE 18 Water quality index of shallow air-floated effluent from certain sewage plant after deep electrolytic purification

Serial number	Item	Air-float water outlet (mg/L)	Electrolyzed outlet water (mg/L)	Removal Rate (%)
					1	COD	53.40	24.30	54.49
2	BOD	41.00	0.76	98.15
					3	SS	9	8	11.11
4	Animal and vegetable oil	0.3	0.2	33.33
					5	Petroleum products	0.2	0.2	0
6	Total nitrogen (in N)	43.68	2.93	93.29
					7	Ammonia nitrogen (in N)	42.63	0.18	99.58
8	Total phosphorus (in terms of P)	0.17	0.15	11.76
					9	Dissolved oxygen	4.8	7.93	-
10	Chroma (dilution multiple)	20	2	90.0
					11	pH	7.2	7.5	-

The effect of the whole process of electrolytic purification of municipal sewage on the removal of main pollutants of sewage is shown in Table 19.

TABLE 19 Effect of electrolytic deep purification on removal of major contaminants of municipal wastewater

The municipal sewage is reduced and biochemically purified (biological aerated filter purification) after electrolysis, and the water quality of the effluent is as shown in the table 20.

Serial number	Item	Raw Water quality (mg/L)	Effluent of biological filter (mg/L)	Removal Rate (%)
					1	COD	232.80	8.28	96.48
2	BOD	113.56	0.45	99.60
					3	SS	180	4	97.78
4	Animal and vegetable oil	1.2	0.02	98.33
					5	Petroleum products	0.7	0.02	97.14
6	Total nitrogen (in N)	47.70	0.86	98.20
					7	Ammonia nitrogen (in N)	42.52	0.21	99.46
8	Total phosphorus (in terms of P)	3.5	0.08	99.51
					9	Dissolved oxygen	2.6	6.07
10	Chroma (dilution multiple)	100	2	98.00
					11	pH	7	7.5	-

The water quality of the wastewater treatment plant operating continuously for one week is shown in Table 21.

TABLE 21 operation record chart of catalytic electrolysis deep purification process for municipal sewage adopted by certain factory

From table 20, it can be seen that the effluent indexes of the sewage purified by the municipal sewage catalytic electrolysis deep purification system (primary treatment, shallow air flotation purification, catalytic electrolysis deep purification, sodium sulfite reduction and biological aerated filter) completely meet the surface water environment quality standard (GB3838-2002 III type water quality standard, from table 21, the municipal sewage catalytic electrolysis deep purification system is stable in operation, and the effluent quality meets the surface water environment quality standard (GB3838-2002 III type water quality standard which meets the design requirements, however, when the COD concentration of the sewage is between 150-300 mg/L, the removal rate of the COD is correspondingly reduced, and is between 90-97%, and the average is 93%.

Example 5

The production process of the invention is adopted for construction of a certain municipal sewage plant, and comprises primary treatment, physicochemical purification, catalytic electrolysis deep purification, sodium sulfite solution reduction, biochemical purification and sludge dehydration, wherein: the primary treatment (100) comprises: a coarse grating, a fine grating and an aeration desilting tank; the physicochemical purification (200) adopts dissolved air flotation; the biochemical purification adopts aerobic.

Municipal sewage enters a primary treatment device (100) for treatment and then enters a dissolved air flotation purification device (200) for purification, effluent is subjected to deep purification through a catalytic electrolysis machine (310), effluent treated by the electrolysis machine enters a degassing tank (330) for degassing, effluent from the degassing tank (330) flows through a sodium hypochlorite reduction tank (400) to remove residual sodium hypochlorite, and clear water after water body restoration enters an aerobic device for purification to obtain deep purified water. The design water inlet and outlet indexes adopting the process are shown in a table 22.

TABLE 22 Water quality index for municipal wastewater treatment plant

The municipal sewage enters a primary treatment device of a catalytic electrolysis deep purification system for sewage treatment, and then enters dissolved air flotation purification (200) for purification to remove SS, COD and BOD₅And the water quality of the effluent is shown in the table 23 after pollutants such as total phosphorus, animal and plant oil, petroleum and the like.

TABLE 23 Water quality index of effluent after dissolved air flotation purification of certain sewage plant

Serial number	Item	Sewage plant influent (mg/L)	Air-float water outlet (mg/L)	Removal Rate (%)
					1	COD	217.80	44.40	79.61
2	BOD	100.59	39.00	61.23
					3	SS	165	8	95.15
4	Animal and vegetable oil	-	0.2	-
					5	Petroleum products	-	0.3	-
6	Total nitrogen (in N)	46.48	39.62	14.76
					7	Ammonia nitrogen (in N)	41.31	42.63	-3.2
8	Total phosphorus (in terms of P)	3.9	0.18	95.38
					9	Dissolved oxygen	2.2	4.2	-
10	Chroma (dilution multiple)	90	5	94.44
					11	pH	7	7.5	-

The purified water of the dissolved air flotation purification (200) is deeply purified by a catalytic electrolysis machine (310), the purified water of the electrolysis machine (310) enters a degassing tank (330) for degassing to remove nitrogen, carbon dioxide and foam generated by degassing, the water of the degassing tank (330) flows through a sodium hypochlorite reduction tank (400) to remove residual sodium hypochlorite, so that the sewage is deeply purified, and the water quality of the discharged water is as shown in Table 24.

TABLE 24 Water quality index of dissolved air flotation effluent from certain sewage plant after electrolytic purification

The effect of the overall process of the depth of catalytic electrolysis of municipal wastewater on the removal of the main pollutants from wastewater is shown in Table 25.

TABLE 25 removal effect of catalytic electrolytic purification on municipal wastewater major pollutants

Serial number	Item	Inflow (mg/L)	Electrolyzed outlet water (mg/L)	Removal Rate (%)
					1	COD	217.80	17.70	91.87
2	BOD	100.59	Not detected out	100
					3	SS	165	7	95.76
4	Animal and vegetable oil	-	0.2	-
					5	Petroleum products	-	0.2	-
6	Total nitrogen (in N)	46.48	2.46	94.71
					7	Ammonia nitrogen (in N)	41.31	1.28	96.90
8	Total phosphorus (in terms of P)	3.9	0.15	96.15
					9	Dissolved oxygen	2.2	8.5	-
10	Chroma (dilution multiple)	90	2	97.78
					11	pH	7	7.5	-

As can be seen from Table 25, the effluent indexes of the municipal sewage after the sewage is subjected to the advanced purification and regeneration system (primary treatment, dissolved air flotation purification, catalytic electrolysis advanced purification and sodium sulfite reduction) of the municipal sewage completely meet the water quality standards of class VI of the Water environmental quality Standard (GB3838-2002) except for the total nitrogen.

The water body which is reduced to eliminate the sodium hypochlorite is purified by an aerobic device, and the water quality of the effluent is shown in a table 26.

TABLE 26 quality of effluent after aerobic purification of electrolyzed effluent from certain sewage plant

Serial number	Item	Inflow (mg/L)	Aerobic effluent (mg/L)	Removal Rate (%)
					1	COD	217.80	6.83	96.86
2	BOD	100.59	1.21	98.80
					3	SS	165	7	95.76
4	Animal and vegetable oil	-	0.01
					5	Petroleum products	-	0.02
6	Total nitrogen (in N)	46.48	0.84	98.19
					7	Ammonia nitrogen (in N)	41.31	0.29	99.30
8	Total phosphorus (in terms of P)	3.9	0.05	98.72
					9	Dissolved oxygen	2.2	6.7	-
10	Chroma (dilution multiple)	90	2	97.78
					11	pH	7	7.4	-

As can be seen from Table 26, the effluent indexes of the sewage treated by the advanced purification and regeneration system of municipal sewage completely meet the quality standards of surface water environment (GB3838-2002 III class water quality standards).

While the foregoing description shows and describes the preferred embodiments of the present invention, it is to be understood that the invention is not limited to the forms disclosed herein, but is not to be construed as excluding other embodiments and is capable of use in various other combinations, modifications, and environments and is capable of changes within the scope of the inventive concept as described herein, commensurate with the above teachings, or the skill or knowledge of the relevant art. And that modifications and variations may be effected by those skilled in the art without departing from the spirit and scope of the invention as defined by the appended claims.

Claims

1. A municipal sewage deep purification and recycling system is characterized by comprising a primary treatment device, a physicochemical purification device, a catalytic electrolysis deep purification device, a reduction pool and a biochemical purification device, wherein,

the primary treatment device comprises a coarse grating, a fine grating, a grit chamber and a lift pump which are connected in sequence, wherein the grit chamber is an aeration grit chamber or a rotational flow grit chamber, an input port of the coarse grating is communicated with a water inlet pipeline of a polluted water body, a water inlet of the lift pump is communicated with the grit chamber, and a water outlet of the lift pump is communicated with the physicochemical purification device;

the materialized purification device is one of an air flotation purification device or a coagulating sedimentation purification device, the air flotation purification device comprises a pH adjusting tank, a coagulating tank, a coagulation assisting tank, an air flotation tank and a middle water tank which are sequentially connected, a water inlet of the pH adjusting tank is connected with a water outlet of the lift pump, a scum outlet is further formed in the upper part of the air flotation tank, a clear water outlet is formed in the lower part of the air flotation tank, the clear water outlet is connected with a water inlet of the middle water tank, and the scum outlet is connected with a sludge pump; or the coagulating sedimentation purification device comprises a pH adjusting tank, a coagulating basin, a coagulation assisting tank, a sedimentation basin and an intermediate water tank which are connected in sequence, wherein a supernatant outlet is arranged at the top of the sedimentation basin and is connected with a water inlet of the intermediate water tank, a sludge outlet is arranged at the bottom of the sedimentation basin and is connected with a sludge pump;

the catalytic electrolysis deep purification device comprises an electrolytic machine, a degassing tank, an electrolyte feeding device and an electrode cleaning device, wherein a water inlet of the electrolytic machine is connected with a water outlet of the middle water tank, a water outlet of the degassing tank is connected with a water inlet pipe of a reduction tank, a water outlet of the reduction tank is communicated with a water discharge pipe, a circulating water pump is arranged between the water outlet of the reduction tank and the water inlet of the flotation tank or the sedimentation tank, the electrolyte feeding device is arranged on a pipeline between the lifting pump and the electrolytic machine and is mixed with sewage by adopting a pipeline mixer, the electrode cleaning device comprises an acid cleaning solution storage tank and an acid cleaning solution delivery pump, and the acid cleaning solution adopts 2-3% hydrochloric acid solution or 4-5% citric acid solution;

the reducing tank comprises a water inlet pipe, a pipeline mixer arranged on the water inlet pipe, a water distributor, a reducing agent solution storage tank and a reducing agent solution metering and conveying pump, the reducing tank is sleeved in the degassing tank, the water inlet pipe is connected with a water outlet of the degassing tank, the water inlet pipe is connected with the water distributor arranged at the bottom of the reducing tank from top to bottom, the reducing agent solution storage tank is communicated with the water inlet pipe through the reducing agent solution metering and conveying pump, the reducing agent solution storage tank is arranged in front of the pipeline mixer, and a water pipe connected with a middle water tank is also arranged on the water inlet pipe;

the biochemical purification device is one of an aerobic purification device or an aeration biological filter, and a water inlet of the biochemical purification device is communicated with a water outlet of the reduction tank.

2. The system of claim 1, wherein the biochemical purification device is an aerobic purification device, and the aerobic purification device comprises an aerobic tank, an aeration pipe, an aeration fan, a sewage outlet, a sludge outlet, a secondary sedimentation tank and a disinfection tank; the water inlet of the aerobic tank is communicated with the water outlet of the reduction tank, the sewage outlet is communicated with the water inlet of the secondary sedimentation tank, and the water outlet of the secondary sedimentation tank is communicated with the water inlet of the disinfection tank.

3. The municipal sewage deep purification and recycling system according to claim 1, wherein the biochemical purification device is a biological aerated filter, the biological aerated filter comprises a biological aerated filter body, an aeration pipe, a support, a filter material support layer, a filter material, a water collection tank, an aeration fan, a backwash water pipe, a sewage outlet, a sludge outlet and a disinfection tank, the water inlet of the biological aerated filter is communicated with the water outlet of the reduction tank, and the sewage outlet is communicated with the water inlet of the disinfection tank.

4. The advanced purification and recycling system for municipal sewage according to claim 1, further comprising a sludge treatment device, wherein the sludge treatment device comprises a sludge pump, a sludge concentration tank, a physicochemical adjustment tank, a dehydrator and a sludge tank; the inlet of the sludge pump is connected with the sludge outlet or the scum outlet of the materialized purification device; the outlet of the sludge pump is connected with the inlet of the sludge concentration tank, the upper part of the sludge concentration tank is provided with a supernatant outlet, and the bottom of the sludge concentration tank is provided with a concentrated sludge outlet; the supernatant outlet is connected with the water inlet of the physicochemical purification device, the concentrated sludge outlet is connected with the inlet of the physicochemical adjusting tank, the outlet of the physicochemical adjusting tank is connected with the dehydrator, the water outlet of the dehydrator is connected with the water inlet of the physicochemical purification device, and the sludge outlet of the dehydrator is connected with the sludge tank.

5. The deep purification and recycling system for municipal sewage according to claim 1, wherein the degassing tank and the reduction tank are provided with drain outlets at the bottoms, and the drain outlets are connected with the water inlet of the physicochemical purification device.

6. The system of claim 1, wherein the coagulating sedimentation purifier is one of a high efficiency sedimentation device, a magnetic coagulation device and a supermagnetic coagulation sedimentation device.

7. The deep purification and recycling system for municipal sewage according to claim 1, wherein the coagulation tank further comprises a coagulant dosing device and a stirrer, and ferric sulfate, ferric trichloride solution or polyaluminium chloride solution is stored in the coagulant dosing device at a mass ratio of 1-20%; the coagulant aid tank further comprises a coagulant aid dosing device and a stirrer, and a PAM solution with the mass ratio of 1-2 per mill is stored in the coagulant aid dosing device.

8. The system of claim 1, wherein the electrolyte adding device comprises an electrolyte solution storage tank and an electrolyte solution delivery pump, and the electrolyte solution storage tank stores 8% -12% sodium hypochlorite solution or 2% -6% sodium chloride solution.

9. The method for deeply purifying the municipal sewage is characterized by comprising the following steps of:

(1) primary treatment: filtering the municipal sewage through a coarse grating and a fine grating in sequence to remove large-particle solid matters, outputting the municipal sewage and flowing into a grit chamber to remove silt;

(2) physicochemical purification: inputting the effluent water obtained in the step (1) into a pH adjusting tank, and adding 3-10 g/m³Continuously stirring sodium hydroxide or sodium carbonate solution at the stirring speed of 80-200 r/min for 5-10 min, adjusting the pH of the sewage to 9-9.5, then sending the adjusted sewage into a coagulation tank, and adding 6-20 g/m of the sewage into the coagulation tank through a coagulation medicine adding device³Continuously stirring the coagulant solution at the stirring speed of 100-200 r/min for 3-6 min; the effluent after the coagulant is added is input into a coagulation-aiding tank, PAM is added through a coagulation-aiding dosing device, and the relation between the weight of the added PAM and the volume of the sewage is 0.1-1 g/m³Stirring and reacting for 3-10 min at the stirring speed of 20-80 r/min, inputting the effluent of the coagulation aiding tank into an air floatation tank or a sedimentation tank for solid-liquid separation, and inputting the sewage clear liquid obtained by physicochemical purification into an intermediate water tank;

(3) deep purification by catalytic electrolysis: conveying the clean water which is subjected to physicochemical purification in the step (2) and is input into the middle water tank to an electrolysis machine for electrolysis and deep purification by a lifting pump, and allowing the sewage to stay in the electrolysis machine for 30-300 s; when sewage enters the electrolysis machine, 10-12% of sodium hypochlorite is added according to the volume ratio of 0.3-1 per mill, the sodium hypochlorite is uniformly mixed through a pipeline mixer, the mixture is conveyed to the electrolysis machine together for electrolysis and deep purification, the working voltage of the electrolysis machine is 5-300V, and the current density is 10-150 mA/cm²(ii) a Conveying the effluent obtained by electrolysis to a degassing tank, wherein the residence time is 10-60 min, and then injecting the effluent in the degassing tank into a reduction tank which is sleeved in the degassing tank;

(4) reduction: quantitatively adding a 5-20% sodium sulfite solution into the reduction pool or pumping one fifth to one third of coagulating sedimentation from a middle water pool to recover the water body;

(5) biochemical purification: conveying the water body subjected to reduction and sodium hypochlorite removal to a pool body of a biochemical purification device for biochemical treatment, wherein the retention time of the water body in the biochemical purification device is 180-300 min;

(6) sludge dewatering: conveying sludge or scum generated after primary treatment and physicochemical purification in the step (1) and the step (2) into a sludge concentration tank for gravity concentration to form an upper clear liquid area and a lower sludge concentration area from top to bottom; conveying the liquid in the upper clear liquid area to a physical and chemical purification device, and conveying the sludge in the lower sludge concentration area to a physical and chemical regulation pool; and adding a physical and chemical conditioner into the physical and chemical conditioning tank, and conveying the physical and chemical conditioner into a dewatering machine for dewatering, wherein the physical and chemical conditioner comprises lime, ferric trichloride and polyaluminium chloride.

10. The method for deeply purifying the municipal sewage according to claim 9, wherein the effluent treated in the steps (1) to (5): the pH value is 6-9, the chroma is less than 2, the COD (chemical oxygen demand) is less than or equal to 20mg/L, BOD5 (five-day biochemical oxygen demand) is less than or equal to 4mg/L, NH3-N (ammonia nitrogen) is less than or equal to 1.0mg/L, the total nitrogen is less than or equal to 1.0mg/L, the total phosphorus (calculated by P) is less than or equal to 0.1mg/L, the fluoride (calculated by F-) is less than or equal to 1.0mg/L, the copper is less than or equal to 1.0mg/L, the zinc is less than or equal to 1.0mg/L, the selenium is less than or equal to 0.01mg/L, the arsenic is less than or equal to 0.05mg/L, the anionic surfactant is less than or equal to 0.2mg/L, the petroleum is less than or equal to 0.05mg/L, the faecal coliform group is less than or equal.