CN106336079A - In-situ water purification system of polluted water source - Google Patents
In-situ water purification system of polluted water source Download PDFInfo
- Publication number
- CN106336079A CN106336079A CN201610856631.2A CN201610856631A CN106336079A CN 106336079 A CN106336079 A CN 106336079A CN 201610856631 A CN201610856631 A CN 201610856631A CN 106336079 A CN106336079 A CN 106336079A
- Authority
- CN
- China
- Prior art keywords
- box
- deodorization
- solid
- biological membrane
- pipeline
- 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.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 238000000746 purification Methods 0.000 title claims abstract description 25
- 238000011065 in-situ storage Methods 0.000 title claims abstract description 16
- 238000004332 deodorization Methods 0.000 claims abstract description 50
- 239000010865 sewage Substances 0.000 claims abstract description 49
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 48
- 239000007788 liquid Substances 0.000 claims abstract description 45
- 230000001954 sterilising effect Effects 0.000 claims abstract description 36
- 238000004659 sterilization and disinfection Methods 0.000 claims abstract description 36
- 239000012528 membrane Substances 0.000 claims abstract description 35
- 238000000926 separation method Methods 0.000 claims abstract description 30
- 238000001914 filtration Methods 0.000 claims abstract description 14
- 238000005192 partition Methods 0.000 claims description 39
- 239000007787 solid Substances 0.000 claims description 21
- 239000002245 particle Substances 0.000 claims description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 15
- 239000004519 grease Substances 0.000 claims description 10
- 239000006004 Quartz sand Substances 0.000 claims description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 9
- 239000000463 material Substances 0.000 claims description 9
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 claims description 8
- 239000003830 anthracite Substances 0.000 claims description 8
- 238000007664 blowing Methods 0.000 claims description 8
- 239000007921 spray Substances 0.000 claims description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 6
- 229910052760 oxygen Inorganic materials 0.000 claims description 6
- 239000001301 oxygen Substances 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 5
- 229910001256 stainless steel alloy Inorganic materials 0.000 claims description 4
- 230000000694 effects Effects 0.000 abstract description 5
- 230000009897 systematic effect Effects 0.000 abstract 1
- 238000003911 water pollution Methods 0.000 description 5
- 239000003673 groundwater Substances 0.000 description 4
- 230000000249 desinfective effect Effects 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 239000008187 granular material Substances 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- 239000013618 particulate matter Substances 0.000 description 3
- 239000002957 persistent organic pollutant Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011859 microparticle Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000000644 propagated effect Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/50—Treatment of water, waste water, or sewage by addition or application of a germicide or by oligodynamic treatment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The invention relates to an in-situ water purification system of a polluted water source. The in-situ water purification system comprises a solid-liquid separation tank (28), a rough filtration tank (22), a refined filtration tank (16), a biological membrane deodorization tank (10) and an ozone sterilization tank (3) that are communicated in sequence. The system is simple in structure and low in cost, can exert a higher sewage purification treatment effect and perform systematic purification, deodorization and sterilization, and is particularly applicable to in-situ sewage treatment in areas with lower purification requirements and small purification amount, such as a pond, a reservoir, a lake and a small river.
Description
Technical Field
The invention relates to sewage treatment equipment, belongs to the field of water treatment and environmental protection, and particularly relates to an in-situ purification system for polluted source water.
Background
Sewage treatment (sewage treatment, water treatment): the sewage is purified to reach the water quality requirement of draining a certain water body or reusing the water body. Sewage treatment is widely applied to various fields such as buildings, agriculture, traffic, energy, petrifaction, environmental protection, urban landscape, medical treatment, catering and the like, and is increasingly used in daily life of common people.
The topics about water pollution are continuously raised, particularly the problem of underground water pollution, farmers or enterprises in Hangzhou and Wenzhou Zhejiang pay for the environmental protection captivity to go to the river and swim, so that attention to the serious degree of water pollution is brought to people.
The pollution of surface water is obvious, and the pollution of underground water is eye surprise. In 13 hundred million people in China, 70% of groundwater is drunk, and in more than 660 cities, more than 400 cities use groundwater as drinking water sources. But statistically 90% of municipal groundwater throughout the country has become contaminated, and another group of data also indicates that groundwater is facing a serious challenge. In 2011, 857 monitoring wells in the district are evaluated to have water quality of 2% of monitoring wells of type I and type II in 9 provinces such as Beijing, Shanghai and the like, while the monitoring wells of type IV and type V are up to 76.8%, and in nine provinces, the best water quality belongs to Hainan province and the type II is taken as the main reason; shanghai and Beijing are mostly III types; black Longjiang and Jiangsu are highest in proportion to IV-class water, but Jilin, Liaoning, Guangdong and Ningxia provinces generally only reach the level of V-class water. The water pollution condition is continuously intensified, so that the sewage treatment and regeneration industry is concerned unprecedentedly, the gross profit rate of each region is kept about 70% in recent two years, even some regions exceed 100%, and the industry development potential is very large.
Aiming at the areas such as a plurality of ponds, lakes, rivers or reservoirs, and the like, which are in the prior art, because the water source circulation is poor, the water source in the areas is very easy to be polluted, so that the water quality is smelly and green, and algae plants are excessively propagated, so that the utilization of the water in the areas is influenced.
Disclosure of Invention
Based on the technical problems, the invention provides a water in-situ purification system for a polluted water source, thereby solving the technical problems of high cost and complex structure of the conventional water in-situ water pollution purification.
In order to solve the technical problems, the technical scheme adopted by the invention is as follows:
an in-situ purification system for polluted source water, which comprises a solid-liquid separation box, a rough filter box, a fine filter box, a biomembrane deodorization box and an ozone sterilization box which are communicated in sequence,
wherein,
the bottom end in the solid-liquid separation box is provided with an air blowing device, the upper end of the air blowing device is provided with a water inlet pipe, the upper end of the solid-liquid separation box is also provided with a grease outlet and a suspended matter salvage net, the suspended matter salvage net is positioned on the inner side wall of the solid-liquid separation box and is connected with an external motor through a rotating shaft, and the external motor can drive the suspended matter salvage net to rotate circumferentially and rotate and then be discharged out of the solid;
a quartz sand filter material layer is arranged inside the coarse filter box, and the lower end of the coarse filter box is positioned at the lower end of the quartz sand filter material layer and is communicated with the inside of the solid-liquid separation box through a first pipeline;
the upper end of the fine filter box is provided with a liquid discharge port, the middle section in the fine filter box is provided with three partition plates with through holes, activated carbon particles and anthracite particles are sequentially filled among the three partition plates from bottom to top, the bottom surface of the fine filter box is provided with a conical inclined bottom surface, the upper end of the conical inclined bottom surface is also provided with a plurality of settling plates parallel to the conical inclined bottom surface, and the fine filter box is positioned at the lower end of each settling plate and is communicated with the upper part of the coarse filter box through a second pipeline;
the bottom of the biological membrane deodorization box is provided with an oxygen conveying pipe, the top of the biological membrane deodorization box is provided with an air outlet, a plurality of layers of biological membrane partition plates are arranged in the biological membrane deodorization box, one side of each biological membrane partition plate is sealed with the side wall of the biological membrane deodorization box, a gap is formed between the other side of each biological membrane partition plate and the side wall of the other end of the biological membrane deodorization box, the gaps formed by the adjacent partition plates and the side walls of the biological membrane deodorization boxes are staggered left and right to form a sewage deodorization channel, illuminating light plates are arranged on the side walls of the two sides of the biological membrane deodorization box, and the lower end of the right side of the biological membrane deodorization box is communicated with;
a plurality of layers of partition plates which are vertically arranged are arranged in the ozone sterilization box, one end of each partition plate is sealed with the ozone sterilization box, a gap is formed between the other end of each partition plate and the ozone sterilization box, the gaps formed between the adjacent partition plates and the ozone sterilization box are staggered up and down to form a sewage sterilization channel, a plurality of ozone spray heads are arranged between the partition plates at the bottom end in the ozone sterilization box and between the partition plates and the inner side wall of the ozone sterilization box, and the ozone spray heads are connected with an ozone generator through air supply pipelines; the lower end of the right side of the ozone sterilization box is communicated with the upper part of the biomembrane deodorization box through a fourth pipeline, and the left end of the ozone sterilization box is also provided with a water outlet and an ozone recovery port;
and the first pipeline, the second pipeline, the third pipeline and the fourth pipeline are all provided with water suction pumps.
Preferably, the suspension fishing net is a stainless steel alloy net.
Preferably, this clean system is still including salvage collecting box, and salvage collecting box is located the outside that solid-liquid separation case set up the lateral wall that the suspended solid salvaged the net, salvage collecting box is including the separable solid collecting box and the liquid collecting box that set up from top to bottom, solid collecting box bottom is provided with the hole that leaks.
Preferably, the liquid collecting tank is further provided with a water outlet and rollers.
Preferably, the bottom of the solid-liquid separation box, the rough filtering box, the fine filtering box and the biomembrane deodorization box is provided with a drain pipe.
In summary, the invention adopts the above technical scheme, and has the following beneficial effects: the invention has simple structure and low cost, can play a role in higher sewage purification treatment effect, can systematically purify, deodorize and sterilize, and is particularly suitable for the in-situ sewage treatment of water in ponds, reservoirs, lakes, small rivers and other areas with lower purification requirements and small purification amount.
Drawings
FIG. 1 is a schematic structural view of the present invention;
the reference numerals in the drawings denote: 1. a water outlet; 2. an ozone recovery port; 3. an ozone sterilization box; 4. a partition plate; 5. an ozone spray head; 6. an air supply duct; 7. an ozone generator; 8. a fourth conduit; 9. an air outlet; 10. a biofilm deodorization box; 11. a biofilm barrier; 12. an oxygen delivery pipe; 13. a lighting board; 14. a third pipeline; 15. a liquid discharge port; 16. a fine filter box; 17. a settlement plate; 18. a partition plate; 19. anthracite coal particles; 20. activated carbon particles; 21. a second conduit; 22. a coarse filter box; 23. a quartz sand filter material layer; 24. a first conduit; 25. a grease outlet; 26. an air blowing device; 27. a water inlet pipe; 28. a solid-liquid separation tank; 29. an external motor; 30. a suspended matter salvage net; 31. a solid matter collecting box; 32. a water leakage hole; 33. a liquid collection tank.
Detailed Description
The invention will be further described with reference to the accompanying drawings. Embodiments of the present invention include, but are not limited to, the following examples.
Example 1
As shown in figure 1, the in-situ purification system for the polluted source water comprises a solid-liquid separation box 28, a coarse filtration box 22, a fine filtration box 16, a biomembrane deodorization box 10 and an ozone sterilization box 3 which are communicated in sequence,
wherein,
an air blowing device 26 is arranged at the bottom end inside the solid-liquid separation box 28, a water inlet pipe 27 is arranged at the upper end of the air blowing device 26, a grease outlet 25 and a suspended matter salvage net 30 are further arranged at the upper end of the solid-liquid separation box 28, the suspended matter salvage net 30 is located on the inner side wall of the solid-liquid separation box 28 and is connected with an external motor 29 through a rotating shaft, and the external motor 29 can drive the suspended matter salvage net 30 to rotate circumferentially and rotate out of the solid-liquid separation box 28;
a quartz sand filter material layer 23 is arranged inside the coarse filter box 22, and the lower end of the coarse filter box 22, which is positioned at the quartz sand filter material layer 23, is communicated with the middle part of the solid-liquid separation box 28 through a first pipeline 24;
a liquid discharge port 15 is formed in the upper end of the fine filter box 16, three partition plates 18 with through holes are arranged in the middle section of the interior of the fine filter box 16, activated carbon particles 20 and anthracite particles 19 are sequentially filled among the three partition plates 18 from bottom to top, the bottom surface of the fine filter box 16 is provided with a conical inclined bottom surface, a plurality of settling plates 17 parallel to the conical inclined bottom surface are further arranged at the upper end of the conical inclined bottom surface, and the fine filter box 16 is positioned at the lower end of the settling plates 17 and is communicated with the upper part of the coarse filter box 22 through a second pipeline 21;
an oxygen conveying pipe 12 is arranged at the bottom of the biological membrane deodorization box 10, an air outlet 9 is arranged at the top of the biological membrane deodorization box 10, a plurality of layers of biological membrane partition plates 11 are arranged in the biological membrane deodorization box 10, one side of each biological membrane partition plate 11 is sealed with the side wall of the biological membrane deodorization box 10, a gap is formed between the other side of each biological membrane partition plate and the side wall of the other end of the biological membrane deodorization box 10, the gaps formed between the adjacent partition plates 11 and the side walls of the biological membrane deodorization box 10 are staggered left and right to form a sewage deodorization channel, illuminating light plates 13 are arranged outside the side walls of the two sides of the biological membrane deodorization box 10, and the lower end of the right side of the biological membrane deodorization box 10 is communicated;
a plurality of layers of partition plates 4 which are vertically arranged are arranged in the ozone sterilization box 3, one end of each partition plate 4 is sealed with the ozone sterilization box 3, a gap is formed between the other end of each partition plate 4 and the ozone sterilization box 3, the gaps formed by the adjacent partition plates 4 and the ozone sterilization boxes 3 are vertically staggered to form a sewage sterilization channel, a plurality of ozone spray heads 5 are arranged at the bottom end in the ozone sterilization box 3 between the partition plates 4 and the inner side wall of the ozone sterilization box 3, and the ozone spray heads 5 are connected with an ozone generator 7 through an air supply pipeline 6; the lower end of the right side of the ozone sterilization box 3 is communicated with the upper part of the biomembrane deodorization box 10 through a fourth pipeline 8, and the left end of the ozone sterilization box 3 is also provided with a water outlet 1 and an ozone recovery port 2;
the first pipeline 24, the second pipeline 21, the third pipeline 14 and the fourth pipeline 8 are all provided with water suction pumps.
The working principle of the embodiment is as follows: the sewage firstly enters a solid-liquid separation box 26 through a water inlet pipe 27, the sewage is precipitated through the solid-liquid separation box 26 and is fixedly precipitated in the sewage, suspended matters and grease float on the upper end surface of the sewage in a layered mode, the grease is discharged through a grease outlet 25, meanwhile, a suspended matter fishing net 30 salvages and discharges the suspended matters, then, after partial particles and suspended matters are treated by the precipitated sewage, the sewage enters a rough filtration box 22 through a first pipeline 24, the sewage filters most large and medium-sized particles through a quartz sand filter material layer 23, then, the rough-filtered sewage enters a fine filtration box 16 through a second pipeline 21, the sewage sequentially passes through activated carbon particles 20 and anthracite particles 19 through a partition plate 18, the small and micro particles of the sewage are filtered through the activated carbon particles 20 and the anthracite particles 19, so that the finely-filtered sewage is obtained, and the finely-filtered sewage enters a biological membrane deodorization box 10 through a liquid outlet 15 and a third pipeline 14, when sewage passes through the biomembrane partition 11, the biomembrane on the surface of the biomembrane partition 11 adsorbs, decomposes and deodorizes organic pollutants in the sewage, the deodorized sewage is introduced into the ozone sterilization box 3 through the fourth pipeline 8, and the ozone generated by the ozone generator 7 in the ozone sterilization box 3 sterilizes the sewage, thereby completing the whole sewage treatment operation.
The invention has simple structure and low cost, can play a role in higher sewage purification treatment effect, can systematically purify, deodorize and sterilize, and is particularly suitable for the in-situ sewage treatment of water in ponds, reservoirs, lakes, small rivers and other areas with lower purification requirements and small purification amount.
Grease export 25 and suspended solid salvage net 30 of this embodiment can be with grease and suspended solid layering discharge in the sewage, the categorised collection of the grease of being convenient for or suspended solid, processing or reutilization, also convenient material's when purifying sewage recovery is recycled, simultaneously quartz sand filter bed 23, activated carbon particle 20 and anthracite particle 19 can the layering with big in the sewage, in, little and miniature particle filtration, thereby reach the suspended solid granule index in guaranteeing the sewage, and it is good to set up the filter effect through the above, and difficult jam, can use for a long time and need not to change or wash.
The bottom surface of the fine filtration box 16 of this embodiment is provided with the inclined bottom surface of toper, and the inclined bottom surface of toper upper end still sets up a plurality of settlement plates 17 parallel with the inclined bottom surface of toper to can reduce the come-up of particulate matter through settlement plate 17, reduce the particulate matter filter capacity of active carbon granule 20 and anthracite granule 19, the inclined bottom surface of toper is convenient for the deposit and the discharge of particulate matter moreover.
The lateral wall that the biomembrane deodorization case 10 bottom of this embodiment set up oxygen delivery pipe 12, biomembrane deodorization case 10 both sides all is provided with light board 13 outward to can guarantee its normal reproduction for sufficient oxygen and light source are provided to the biomembrane, and improve its organic pollutant decomposition speed to in the sewage, guarantee the deodorization effect.
The sewage deodorization channel structure that the biomembrane baffle 11 of this embodiment formed and the sewage sterilization channel structure that baffle 4 formed can prolong the distance of deodorization or disinfecting, increase the area of action of deodorization or disinfecting for deodorization or disinfecting more thoroughly, even, improved deodorization or bactericidal effect.
The air blowing device of the embodiment is composed of an air pump, a connecting pipeline and a bubble distributing device. Thus, bubbles are formed at the bottom of the solid-liquid separation tank 28, and the bubbles adhere to the surface of the fat to float the fat, and flow out through the fat outlet 25.
Example 2
This embodiment is optimized based on the technical solution of embodiment 1: the suspension salvaging net 30 is a stainless steel alloy net. The suspended matter salvage net 30 is often located in the solid-liquid separation box 28, and the suspended matter salvage net 30 is extremely easy to damage due to the fact that the sewage contains some corrosive substances, so that the stainless steel alloy net is not prone to corrosion and can be used for a long time.
Example 3
The embodiment adds the following structure on the basis of the technical scheme of the embodiment 1 or the embodiment 2: the purification system further comprises a salvage collecting box, the salvage collecting box is located outside the side wall, provided with the suspended matter salvage net 30, of the solid-liquid separation box 28, the salvage collecting box comprises a solid collecting box 31 and a liquid collecting box 33 which are arranged in a vertically separable mode, and a water leakage hole 32 is formed in the bottom of the solid collecting box 31.
In order to collect the suspended solid salvaged by the suspended solid salvage net 30, the salvage collecting box is arranged outside the side wall of the suspended solid salvage net 30, so that the suspended solid salvage net 30 can directly fall into the solid collecting box 31 after fishing the suspended solid, the solid separating box 28 and the solid collecting box 31 rotate, the sewage brought out enters the liquid collecting box 33 through the water leakage hole 32, and the salvage is collected and dried.
Preferably, the liquid collection tank is also provided with a drain 34 and rollers 35. The drain port 34 allows the sewage entering the liquid collection tank 33 to be drained, and the rollers 35 are added to facilitate the removal of the salvage collection tank in order to facilitate the carrying of the salvage collection tank.
Example 4
The embodiment is further improved on the basis of the technical scheme of any one of the embodiments, and specifically comprises the following steps: and the bottom parts of the solid-liquid separation box 28, the rough filtering box 22, the fine filtering box 16 and the biomembrane deodorization box 10 are all provided with a sewage discharge pipe. The sewage discharge pipe can discharge the particles deposited in the solid-liquid separation box 28, the rough filter box 22, the fine filter box 16 and the biomembrane deodorization box 10, and is convenient to clean and discharge the sewage.
The above description is an embodiment of the present invention. The specific parameters in the above embodiments and examples are only for the purpose of clearly illustrating the invention verification process of the inventor and are not intended to limit the scope of the invention, which is defined by the claims, and all equivalent structural changes made by using the contents of the specification and the drawings of the present invention should be covered by the scope of the present invention.
Claims (5)
1. The utility model provides a contaminated water source water normal position clean system which characterized in that: comprises a solid-liquid separation box (28), a coarse filter box (22), a fine filter box (16), a biomembrane deodorization box (10) and an ozone sterilization box (3) which are communicated in sequence,
wherein,
an air blowing device (26) is arranged at the bottom end inside the solid-liquid separation box (28), a water inlet pipe (27) is arranged at the upper end of the air blowing device (26), a grease outlet (25) and a suspended matter salvage net (30) are further arranged at the upper end of the solid-liquid separation box (28), the suspended matter salvage net (30) is located on the inner side wall of the solid-liquid separation box (28) and is connected with an external motor (29) through a rotating shaft, and the external motor (29) can drive the suspended matter salvage net (30) to rotate circumferentially and rotate out of the solid-liquid separation box (28;
a quartz sand filter material layer (23) is arranged inside the coarse filter box (22), and the coarse filter box (22) is positioned at the lower end of the quartz sand filter material layer (23) and is communicated with the middle part of the solid-liquid separation box (28) through a first pipeline (24);
a liquid discharge port (15) is formed in the upper end of the fine filter box (16), three partition plates (18) with through holes are arranged in the middle section of the interior of the fine filter box (16), activated carbon particles (20) and anthracite particles (19) are sequentially filled among the three partition plates (18) from bottom to top, the bottom surface of the fine filter box (16) is provided with a conical inclined bottom surface, a plurality of settling plates (17) parallel to the conical inclined bottom surface are further arranged at the upper end of the conical inclined bottom surface, and the fine filter box (16) is positioned at the lower end of each settling plate (17) and is communicated with the upper part of the rough filter box (22) through a second pipeline (21);
an oxygen conveying pipe (12) is arranged at the bottom of the biological membrane deodorization box (10), an air outlet (9) is arranged at the top of the biological membrane deodorization box, a plurality of layers of biological membrane partition plates (11) are arranged in the biological membrane deodorization box (10), one side of each biological membrane partition plate (11) is sealed with the side wall of the biological membrane deodorization box (10), a gap is formed between the other side of each biological membrane deodorization box and the side wall of the other end of each biological membrane deodorization box (10), the gaps formed by the adjacent partition plates (11) and the side walls of the biological membrane deodorization boxes (10) are staggered left and right to form a sewage deodorization channel, light plates (13) are arranged outside the side walls of the two sides of each biological membrane deodorization box (10), and the lower end of the right side of each biological membrane deodorization box (10) is communicated with a liquid discharge port (15) at;
a plurality of layers of vertically arranged partition plates (4) are arranged in the ozone sterilization box (3), one end of each partition plate (4) is closed with the ozone sterilization box (3), a gap is formed between the other end of each partition plate and the ozone sterilization box (3), the gaps formed by the adjacent partition plates (4) and the ozone sterilization boxes (3) are vertically staggered to form a sewage sterilization channel, the bottom end in the ozone sterilization box (3) is positioned between the partition plates (4), a plurality of ozone spray heads (5) are arranged between the partition plates (4) and the inner side wall of the ozone sterilization box (3), and the ozone spray heads (5) are connected with an ozone generator (7) through an air supply pipeline (6); the lower end of the right side of the ozone sterilization box (3) is communicated with the upper part of the biomembrane deodorization box (10) through a fourth pipeline (8), and the left end of the ozone sterilization box (3) is also provided with a water outlet (1) and an ozone recovery port (2);
and the first pipeline (24), the second pipeline (21), the third pipeline (14) and the fourth pipeline (8) are all provided with water suction pumps.
2. The in-situ purification system for polluted source water according to claim 1, wherein: the suspended matter salvage net (30) is a stainless steel alloy net.
3. The in-situ purification system for polluted source water according to claim 1, wherein: the purification system further comprises a salvage collecting box, the salvage collecting box is located outside the side wall, provided with the suspended matter salvage net (30), of the solid-liquid separation box (28), the salvage collecting box comprises a solid collecting box (31) and a liquid collecting box (33) which are arranged in a vertical separable mode, and a water leakage hole (32) is formed in the bottom of the solid collecting box (31).
4. The in-situ purification system for polluted source water according to claim 3, wherein: the liquid collecting tank (33) is also provided with a water outlet (34) and a roller (35).
5. The in situ purification system for contaminated source water according to any of claims 1-4, wherein: and the bottom parts of the solid-liquid separation box (28), the rough filtering box (22), the fine filtering box (16) and the biomembrane deodorization box (10) are all provided with sewage discharge pipes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610856631.2A CN106336079A (en) | 2016-09-28 | 2016-09-28 | In-situ water purification system of polluted water source |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610856631.2A CN106336079A (en) | 2016-09-28 | 2016-09-28 | In-situ water purification system of polluted water source |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106336079A true CN106336079A (en) | 2017-01-18 |
Family
ID=57840282
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610856631.2A Pending CN106336079A (en) | 2016-09-28 | 2016-09-28 | In-situ water purification system of polluted water source |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106336079A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107381858A (en) * | 2017-09-12 | 2017-11-24 | 张莲莲 | A marine oily sewage cleaning device |
| CN107935159A (en) * | 2017-11-07 | 2018-04-20 | 桐乡市锦格家纺有限公司 | A kind of sewage treatment filtering tank based on lattice wall material-bearing water-distribution method |
| CN110627274A (en) * | 2019-09-24 | 2019-12-31 | 舟山市海大科学技术研究院有限责任公司 | Aquaculture wastewater treatment device and treatment method |
| CN116874137A (en) * | 2023-08-25 | 2023-10-13 | 中船绿洲环保(南京)有限公司 | A comprehensive oil pollution control system for fishing ports |
| CN116878189A (en) * | 2023-07-27 | 2023-10-13 | 山东纳鑫新能源有限公司 | Low-temperature unclean water source online cleaning waste heat recovery unit and waste heat recovery method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101591097A (en) * | 2008-05-26 | 2009-12-02 | 北京锦奥华荣科技有限公司 | Medical waste water purification and recovery treatment system based on aerobic biological film method |
| CN203048748U (en) * | 2013-02-03 | 2013-07-10 | 成都源创环保工程有限公司 | Depth treatment device for drinking water from slightly polluted water source |
| CN204918272U (en) * | 2015-08-17 | 2015-12-30 | 深圳市明鑫高分子技术有限公司 | Water purifying appts |
| CN205528316U (en) * | 2016-04-25 | 2016-08-31 | 自贡市华尔美科技有限公司 | Domestic sewage purification regenerating unit |
-
2016
- 2016-09-28 CN CN201610856631.2A patent/CN106336079A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101591097A (en) * | 2008-05-26 | 2009-12-02 | 北京锦奥华荣科技有限公司 | Medical waste water purification and recovery treatment system based on aerobic biological film method |
| CN203048748U (en) * | 2013-02-03 | 2013-07-10 | 成都源创环保工程有限公司 | Depth treatment device for drinking water from slightly polluted water source |
| CN204918272U (en) * | 2015-08-17 | 2015-12-30 | 深圳市明鑫高分子技术有限公司 | Water purifying appts |
| CN205528316U (en) * | 2016-04-25 | 2016-08-31 | 自贡市华尔美科技有限公司 | Domestic sewage purification regenerating unit |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107381858A (en) * | 2017-09-12 | 2017-11-24 | 张莲莲 | A marine oily sewage cleaning device |
| CN107935159A (en) * | 2017-11-07 | 2018-04-20 | 桐乡市锦格家纺有限公司 | A kind of sewage treatment filtering tank based on lattice wall material-bearing water-distribution method |
| CN110627274A (en) * | 2019-09-24 | 2019-12-31 | 舟山市海大科学技术研究院有限责任公司 | Aquaculture wastewater treatment device and treatment method |
| CN110627274B (en) * | 2019-09-24 | 2021-09-28 | 舟山市海大科学技术研究院有限责任公司 | Aquaculture wastewater treatment device and treatment method |
| CN116878189A (en) * | 2023-07-27 | 2023-10-13 | 山东纳鑫新能源有限公司 | Low-temperature unclean water source online cleaning waste heat recovery unit and waste heat recovery method |
| CN116878189B (en) * | 2023-07-27 | 2023-12-22 | 山东纳鑫新能源有限公司 | Low-temperature unclean water source online cleaning waste heat recovery unit and waste heat recovery method |
| CN116874137A (en) * | 2023-08-25 | 2023-10-13 | 中船绿洲环保(南京)有限公司 | A comprehensive oil pollution control system for fishing ports |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101205109B (en) | Apparatus for treating chemical fiber waste water by anaerobic method | |
| CN102870708A (en) | Factory circulating water aquiculture system | |
| CN106336079A (en) | In-situ water purification system of polluted water source | |
| CN105502729A (en) | Water treatment equipment | |
| CN209210593U (en) | A kind of town sewage treatment system | |
| CN209428266U (en) | A sewage treatment and purification equipment | |
| CN215667605U (en) | Domestic sewage treatment detection device | |
| CN208029987U (en) | A kind of low-carbon zero-emission industrial circulating water cultivating system based on anaerobic denitrifying | |
| CN205076946U (en) | Water body remediation composite set based on magnetic separation and constructed wetland | |
| CN201154935Y (en) | Chemical fabrics waste water treatment plant | |
| CN207608462U (en) | A kind of Reed Bed effluent treatment plant | |
| CN103359846B (en) | Oily wastewater treatment system and process for treating oily wastewater by using same | |
| CN207130116U (en) | A kind of mechanical cleaning wastewater treatment equipment | |
| CN206940624U (en) | A kind of sewage-treatment plant | |
| CN206142929U (en) | A tertiary filtration purification device for sewage purification | |
| CN106348477A (en) | Multi-stage sewage water quality purification treatment equipment | |
| CN203382609U (en) | Food wastewater treatment system | |
| CN211198850U (en) | Novel integral type view water treatment device | |
| CN107739112B (en) | The vertical sleeping integral type sewage processing system of one kind | |
| CN207862039U (en) | A kind of oil-containing industrial water processing system | |
| CN208917004U (en) | A kind of sewage disposal device | |
| CN208414166U (en) | A kind of aquaculture ecological purified water system | |
| CN208378665U (en) | A kind of sewage quality processing unit after dyeing | |
| CN206279057U (en) | A kind of reservoir aquaculture wastewater processing unit | |
| CN206915952U (en) | A kind of unpowered biological purification tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170118 |