CN110902904A - Sewage purification, filtration and sterilization device - Google Patents
Sewage purification, filtration and sterilization device Download PDFInfo
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- CN110902904A CN110902904A CN201911200195.3A CN201911200195A CN110902904A CN 110902904 A CN110902904 A CN 110902904A CN 201911200195 A CN201911200195 A CN 201911200195A CN 110902904 A CN110902904 A CN 110902904A
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- 239000010865 sewage Substances 0.000 title claims abstract description 95
- 238000000746 purification Methods 0.000 title claims abstract description 41
- 230000001954 sterilising effect Effects 0.000 title claims abstract description 31
- 238000001914 filtration Methods 0.000 title claims abstract description 23
- 238000004659 sterilization and disinfection Methods 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 109
- 239000002002 slurry Substances 0.000 claims abstract description 51
- 210000000078 claw Anatomy 0.000 claims abstract description 21
- 238000004062 sedimentation Methods 0.000 claims abstract description 19
- 238000003756 stirring Methods 0.000 claims description 45
- 239000000126 substance Substances 0.000 claims description 19
- 230000005540 biological transmission Effects 0.000 claims description 15
- 239000000654 additive Substances 0.000 claims description 10
- 230000000996 additive effect Effects 0.000 claims description 10
- 238000007667 floating Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- 241000883966 Astrophytum capricorne Species 0.000 claims 1
- 239000007921 spray Substances 0.000 claims 1
- 238000001556 precipitation Methods 0.000 abstract description 11
- 238000000034 method Methods 0.000 abstract description 5
- 230000008569 process Effects 0.000 abstract description 5
- 239000010410 layer Substances 0.000 description 39
- 239000010802 sludge Substances 0.000 description 18
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 9
- 239000003814 drug Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 9
- 229910052760 oxygen Inorganic materials 0.000 description 9
- 239000001301 oxygen Substances 0.000 description 9
- 230000000630 rising effect Effects 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 4
- 241000594310 Randia aculeata Species 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 229940037003 alum Drugs 0.000 description 2
- 238000005345 coagulation Methods 0.000 description 2
- 230000015271 coagulation Effects 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 238000005202 decontamination Methods 0.000 description 2
- 230000003588 decontaminative effect Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000007599 discharging Methods 0.000 description 2
- 229940079593 drug Drugs 0.000 description 2
- 230000002349 favourable effect Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 241000283707 Capra Species 0.000 description 1
- 241001494479 Pecora Species 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000000693 micelle Substances 0.000 description 1
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- 239000007800 oxidant agent Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- 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
- C02F11/00—Treatment of sludge; Devices therefor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
- C02F11/127—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
-
- 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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
-
- 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
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5281—Installations for water purification using chemical agents
-
- 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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F2001/007—Processes including a sedimentation step
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/20—Prevention of biofouling
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- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- Physical Water Treatments (AREA)
Abstract
The invention discloses a sewage purification, filtration and sterilization device, which comprises a sewage sedimentation tank, wherein the upper end of the sewage sedimentation tank is provided with a sewage inlet, the lower end of the sewage inlet is fixedly connected with a first trident pipeline, and the lower side of the first trident pipeline extends to a sedimentation cavity; the bottom of the sewage sedimentation tank is provided with a claw water purifier, water outlets are formed in two sides of the upper end of the claw water purifier, and the bottom end of the claw water purifier penetrates through the bottom of the sewage sedimentation tank and is externally connected with a water supply pipe through a switch valve; the bottom of the sedimentation cavity is fixedly connected with a second Y-shaped pipeline, the lower end of the second Y-shaped pipeline is fixedly connected with a underflow pump, and the other end of the underflow pump is communicated with a secondary collection tank; the sewage treatment device mainly treats sewage accompanied with slurry repeatedly through a plurality of processes of precipitation, purification, filtration and sterilization, collects and utilizes finally cleaned pure water, and effectively saves water resources.
Description
Technical Field
The invention relates to the technical field of sewage treatment, in particular to a sewage purification, filtration and sterilization device.
Background
Sewage treatment is a process of purifying sewage to meet the water quality requirement of draining a certain water body or reusing the sewage, is widely applied to various fields of buildings, agriculture, traffic, energy, petrifaction, environmental protection, urban landscape, medical treatment, catering and the like, and increasingly enters the daily life of common people,
mix in the sewage and have the precipitate, especially the sewage that the building discharged, be doped with a large amount of mud in the sewage, on the one hand, the time of discharging back can be for a long time lead to the river course to block up, and the sewage that accompanies in the mud is difficult to the come-up, the processing of neglecting easily, and mud waste water forms black mud easily along with the sewage time for a long time and leads to rotten smelly, be difficult to the mediation, need consume a large amount of manpower and materials and dredge, sewage treatment's cost has been increased, on the other hand mud is discharged and has been formed the wasting of resources, based on the current sewage treatment condition.
Disclosure of Invention
The invention aims to provide a sewage purification, filtration and sterilization device to solve the problems in the background technology.
In order to achieve the purpose, the invention provides the following technical scheme:
a sewage purification, filtration and sterilization device comprises a sewage precipitation tank, wherein the upper end of the sewage precipitation tank is provided with a sewage inlet, the lower end of the sewage inlet is fixedly connected with a first trident pipeline, the lower side of the first trident pipeline extends to a precipitation cavity, the bottom of the sewage precipitation tank is provided with a claw water purifier, both sides of the upper end of the claw water purifier are provided with water outlets, the bottom of the claw water purifier penetrates through the bottom of the sewage precipitation tank and is externally connected with a water supply pipe through a switch valve, the bottom of the precipitation cavity is fixedly connected with a second trident pipeline, the lower end of the second trident pipeline is fixedly connected with a thick slurry pump, the other end of the thick slurry pump is communicated with a secondary collection tank, the first trident pipeline and the second trident pipeline are PVC material pipelines with 2 connectors at one end and one connector at the other end, the claw type trident pipeline can select 2 connectors as input in the forward, and 1 connecting port can be used as an input and 2 connecting ports at the other end can be used as an output in a reverse direction, and the directions of the first trifurcated pipeline and the second trifurcated pipeline can be adjusted according to actual conditions, so that the use is very convenient.
The sewage sedimentation tank upper right corner is equipped with the outlet, and the outlet inboard is equipped with the screen cloth, the outlet other end and purifying tank intercommunication, be equipped with the stirring rod in the purifying tank, and the stirring rod electricity is connected and is installed in the motor at purifying tank outside top, be equipped with four layers of stirring vane in the stirring rod, and all be equipped with the hollow groove of rectangle in the middle of first layer stirring vane and the third layer stirring vane, and first layer stirring vane, third layer stirring vane in proper order respectively with the crisscross installation setting of second floor stirring vane, fourth layer stirring vane.
A sedimentation tank is arranged at the bottom of the purification tank, a slurry pump is fixedly connected to the lower end of the sedimentation tank, and the other end of the slurry pump is communicated with a secondary collection tank; the flow rate of the thick slurry pump is 4.2T/h, the diameter of an inlet and an outlet is 40 cm, and the working pressure is 40 kg; the flow of the slurry pump is 1.5T/h, the diameter of an inlet and an outlet is 25 cm, the working pressure is 10kg, and the caliber, the working pressure and the inlet and outlet flow of the slurry pump are all larger than those of the slurry pump, so that the slurry pump is beneficial to discharging slurry with high density and preventing slurry from being blocked.
The right upper end of the purification tank is provided with a purification port, the purification tank is communicated with the filter tank through a first transmission pipe, two layers of filter screens are arranged in the middle of the interior of the filter tank, a floating ball filter layer is arranged at the top end of the filter tank, the bottom of the filter tank is fixedly connected with a sewage pump, and the other end of the sewage pump is communicated with a secondary collection tank; the filter tank upper right corner is through second transmission pipe and retort intercommunication, the inside top of retort is equipped with the ultraviolet irradiation bactericidal lamp, and the retort has the third transmission pipe outward, the right-hand member rigid coupling that the secondary was collected and is irritated has the mud centrifugal pump, and centrifugal pump other end rigid coupling has the hydroextractor, the hydroextractor output is irritated the secondary intercommunication through transmission pipe and purification, through pouring into sewage additive in the retort and to hydroextractor exhaust sewage secondary purification treatment.
The right-hand member that the secondary was collected and is irritated is provided with the drain in the inner structure that the secondary was collected and is irritated, the one end of drain is less than the other end, is favorable to sewage to flow to the one end of drain automatically on the one hand, is convenient for promote the centrifugal pump with the secondary collect irritate sewage and mud quick separation.
The water supply pipe is externally connected with a dosing pipe, the dosing pipe is integrally L-shaped, the other end of the dosing pipe extends to the bottom of the cavel water purifier from the inner side of the water supply pipe, a jet orifice is arranged at the bottom of the cavel water purifier at the end head of the other end of the dosing pipe, the jet orifice is divided into an upper row of jet orifices and a lower row of jet orifices, the upper row of jet orifices and the lower row of jet orifices are respectively provided with 5 rectangular jet orifices, and the rectangular jet orifices are arranged in two rows in an orderly horizontal manner;
the bottom of the claw water purifier is provided with a circular water inlet which is communicated with a water supply pipe through a nozzle, the claw water purifier is designed to be provided with water at the bottom and water at the top, the water is fed in by adopting the rotational flow of the nozzle, point vortex flow with certain circulation strength is formed in the main claw water purifier, the coagulation reaction effect is favorably enhanced, and the required hydraulic environment in the claw water purifier can be formed;
3 sludge discharge valves are arranged around the circular water inlet, each sludge discharge valve is provided with 8 circular holes which are nested in a circular ring, and the diameter of each circular hole is 1/5 of the diameter of the circular ring;
the bottom of the cavel water purifier is a cone, and the water flow speed is rapidly reduced along with the increase of the sectional area of the cone in the process of water flow rising at the inlet of the cone area, so that the added additive floc is more fully condensed.
Compared with the prior art, the invention has the beneficial effects that: the invention mainly treats the sewage accompanied with the slurry repeatedly through a plurality of processes of precipitation, purification, filtration and sterilization, collects and utilizes the finally cleaned pure water, effectively saves water resources, simultaneously recycles the slurry waste residue accumulated by precipitation for the continuous use of buildings, effectively avoids resource waste, effectively avoids the slurry from being discharged into pipelines to form sludge, and simultaneously reduces the cost of sewage treatment.
Drawings
FIG. 1 is a schematic view of the internal structure of the present invention;
FIG. 2 is a schematic view of the structure of the stirring blade of the present invention;
FIG. 3 is a schematic bottom structure view of the water purifier for sheep's horn according to the present invention;
FIG. 4 is a schematic view of the structure of the injection port of the present invention;
FIG. 5(a) is a graph showing the reaction rate of organic substances attached to slurry according to the present invention;
FIG. 5(b) is a schematic diagram showing the effect of continuous sludge discharge on the removal rate when the dosage is 500L/h;
FIG. 5(c) is a schematic diagram showing the effect of continuous sludge discharge on the removal rate when the water inflow is 1000L/h.
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 given herein without making any creative effort, shall fall within the protection scope of the present invention.
Referring to fig. 1, an embodiment of the present invention: a sewage purification, filtration and sterilization device, a sewage sedimentation tank 1, wherein the upper end of the sewage sedimentation tank 1 is provided with a sewage inlet 2, the lower end of the sewage inlet 2 is fixedly connected with a first three-fork pipeline 3, the lower side of the first three-fork pipeline 3 extends to a sedimentation cavity 4, the bottom of the sewage sedimentation tank 1 is provided with a goat horn water purifier 5, both sides of the upper end of the goat horn water purifier 5 are provided with water outlets 6, the bottom end of the goat horn water purifier 5 penetrates through the bottom of the sewage sedimentation tank 1 and is externally connected with a water supply pipe 7 through a switch valve, the bottom of the sedimentation cavity 4 is fixedly connected with a second three-fork pipeline 8, the lower end of the second three-fork pipeline 8 is fixedly connected with a thick slurry pump 9, the other end of the thick slurry pump 9 is communicated with a secondary collection tank 10, the first three-fork pipeline 3 and the second three-fork pipeline 8 are both made of PVC pipelines with 2 connectors at one end and a single connector at the other end, the goat, or 1 connector can be reversely used as input and 2 connectors at the other end can be used as output, the directions of the first three-way pipeline and the second three-way pipeline are adjusted according to actual conditions, the use is very convenient, a water outlet 11 is arranged at the upper right corner of the sewage settling tank 1, a screen 12 is arranged at the inner side of the water outlet 11, the other end of the water outlet 11 is communicated with a purification tank 13, sewage mixed with slurry enters the sewage settling tank 1 from the sewage inlet 2, then enters the settling chamber 4 in two ways through the first three-way pipeline 3, a switch valve at the bottom of the claw water purifier 5 is opened, water is supplied into the claw water purifier 5 from a water supply pipe 7, water overflows from the claw water purifier 5 and enters the settling chamber 4, the sewage mixed with the slurry in the settling chamber 4 is subjected to water washing and settling, and then the sewage floats to the upper half part of the sewage settling tank 1 after being washed, after primary filtration by the screen 12, the sludge is discharged into the purifying tank 13 through the water outlet, the sludge sediment is still positioned in the settling chamber 4, and after multiple times of cleaning, the sludge in the settling chamber 4 is discharged by the thick liquid pump 9 for continuous use, thereby effectively saving resources.
Referring to fig. 3 and 4, the feed pipe 7 is externally connected with a chemical feeding pipe 31, the chemical feeding pipe 31 is L-shaped as a whole, the other end of the chemical feeding pipe 31 extends from the inner side of the feed pipe 7 to the bottom of the cavum water purifier 5, and the end of the other end of the chemical feeding pipe 7 at the bottom of the cavum water purifier 5 is provided with a jet orifice 32, the jet orifice 32 is divided into an upper jet orifice 3201 and a lower jet orifice 3202, the upper jet orifice 3201 and the lower jet orifice 3202 are provided with 5 rectangular jet orifices which are arranged in two rows in order and horizontally, the bottom of the cavum water purifier 5 is provided with a circular water inlet 33, the circular water inlet 33 is communicated with the feed pipe 7 through a nozzle 34, the cavum water purifier 5 is designed to be fed with water from the top by the nozzle 34 in a swirling flow, a point vortex flow with a certain circulating intensity is formed in the main cavum, and can form the required hydraulic environment in the cavel water purifier 5, be equipped with 3 mud valves 35 around the circular water inlet, and every mud valve 35 is the nested 8 round holes that set up in the ring, and the diameter of this round hole is 1/5 of ring diameter.
Referring to fig. 1, the bottom of the cavel water purifier 5 is a cone, and the water flow speed is rapidly reduced along with the increase of the sectional area of the cone when the inlet of the cone is at the rising process of the water flow, so that the added additive floc is more fully coagulated. In the final stage of the coagulation reaction of the cone area additive and the slurry, a large amount of floccule micelles are generated, the cone design can increase the collision and combination between the additive and slurry particles while meeting the flow rate so as to be beneficial to the effective formation of a suspended sludge layer, and meanwhile, the inverted cone at the bottom of the cavel water purifier 5 can generate vortex flow to the ascending water flow, so that the concentration of the suspended sludge layer is increased, and the water purification effect is improved; and the flow rate control of injected water and additive in the cavel water purifier 5 is the key of guaranteeing filtration treatment on next step, can form the suspension mud layer in the top in cone region promptly, neither sinks and is not dispersed by rivers, still can realize that the upper surface of mud layer drops gradually along with hydraulic circulation's going on, only can guarantee like this that the suspension mud layer is more stable, is favorable to washing of mud more for mud and top layer organic matter quickly separating and sediment.
Referring to fig. 2, a stirring rod 14 is arranged in the purification tank 13, the stirring rod 14 is electrically connected with a motor 15 installed at the top of the outer side of the purification tank 13, a precipitation tank 16 is arranged at the bottom of the purification tank 13, a small amount of sludge precipitate is further doped in the sewage discharged into the purification tank 13, the small amount of precipitate is precipitated in the precipitation tank 16 after being stirred by the stirring rod 14 driven by the motor 15, four layers of stirring blades 29 are arranged in the stirring rod 14, rectangular hollow grooves are respectively arranged between the first layer of stirring blades and the third layer of stirring blades, and the first layer of stirring blades and the third layer of stirring blades are respectively installed with the second layer of stirring blades and the fourth layer of stirring blades in a staggered manner; and four layers of stirring blades are arranged in the stirring rod, rectangular hollow grooves are formed between the first layer of stirring blades and the third layer of stirring blades, and the first layer of stirring blades and the third layer of stirring blades are respectively and sequentially arranged with the second layer of stirring blades and the fourth layer of stirring blades in a staggered mode. The staggered arrangement of the stirring blades 29 is beneficial to ensuring that the slurry flows through the rectangular hollow grooves of the first layer of stirring blades and then collides with the second layer of stirring blades, and then flows through the rectangular hollow grooves of the third layer of stirring blades and collides with the fourth layer of stirring blades, so that the slurry is stirred more effectively;
referring to fig. 1, a mud pump 17 is fixedly connected to the lower end of the settling tank 16, and the other end of the mud pump 27 is communicated with the secondary collection tank 10; a purification port 18 is formed in the right upper end of the purification tank 13, the purification tank 13 is communicated with a filter tank 20 through a first transmission pipe 19, a decontamination additive is injected through the purification port to decontaminate and purify the sewage in the purification tank 13, the upper layer part subjected to purification treatment is discharged into the filter tank 20 through the first transmission pipe 19, and a small amount of precipitated slurry in the lower layer part is discharged to a secondary collection tank 10 through a slurry pump 17;
the flow rate of the underflow pump 9 is 4.2T/h, the diameter of an inlet and an outlet is 40 cm, and the working pressure is 40 kg; the flow of the slurry pump 17 is 1.5T/h, the diameter of an inlet and an outlet is 25 cm, the working pressure is 10kg, the caliber, the working pressure and the inlet and outlet flow of the slurry pump 9 are all larger than those of the slurry pump 17, so that the slurry with high density can be discharged, the slurry blockage can be prevented, the caliber of the slurry pump 17 is small, the pressure in the caliber is large, and the slurry with water can be discharged conveniently;
suspended matters and other organic substances are attached to the surface layer of the precipitated slurry, the added medicines need to decompose organic substances in water, the decomposed slurry is discharged from a sludge discharge valve at the bottom, and the rising flow rate and the dosing amount of water have great influence on the decomposition rate of the slurry due to the fact that chemical oxygen demand is involved in the reaction of the organic substances and strong oxidants are contained in the added medicines;
referring to fig. 5(a), a graph of the effect of the amount of added chemicals on the raw water removal rate shows the reaction rate of organic matter attached to the slurry;
the chemical oxygen demand removal rate is highest when the medicine adding amount is about 350-600 mg/L, and the required chemical oxygen demand removal rate is highest when the medicine adding amount is 400-600 mg/L, tests show that the utilization rates of the chemical oxygen demand removal rate and the required chemical oxygen demand removal rate are both required to be highest when the chemical oxygen demand removal rate is applied, when the medicine adding amount is too much, alum flowers formed by violent reaction of mud attached organic matters are too loose and not easy to settle, and when the medicine adding amount is too much, the medicine is remained in purified effluent water due to excessive medicine adding, so that the effluent water turns yellow and wastes; the dosage of the medicament is related to the content of suspended matters in raw water, but the device has certain impact resistance to organic load, so the optimal dosage can be preliminarily determined, and the turbidity removal rate is highest when the dosage is less than about 500mg/L by comprehensive consideration, and the sludge can be well settled due to enough density of precipitate.
Referring to FIG. 5(b), the effect of continuous sludge discharge on the removal rate when the dosage is 500L/h;
under the condition of the optimal dosage, the water inflow is changed in sequence, the water yield is changed to analyze the mud-water separation speed, namely the influence of the rising flow velocity of the clear water area of the claw water purifier 5 on the treatment effect, and when the water yield is increased in sequence, the turbidity removal rate of the raw water is kept unchanged basically and is about 90 percent. The chemical oxygen demand removal rate is small in water inflow, the rising flow rate of clean water is small, the hydraulic retention time of inflow water in the claw water purifier 5 is long, sufficient clarification time is provided and basically kept above 80%, the middle curve is reduced due to disturbance of the mud valve on water flow, and removal rate fluctuation occurs.
Referring to FIG. 5(c), the effect of continuous sludge discharge on the removal rate when the water inflow is 1000L/h;
the turbidity removal rate and the chemical oxygen demand removal rate of raw water change slightly with the increase of continuous sludge discharge, the turbidity removal rate is higher and is reduced from 95 percent to about 85 percent, and the chemical oxygen demand removal rate is 70 to 80 percent. The small amplitude change is caused by that the rising flow velocity of the clear water is increased along with the reduction of the continuous sludge discharge rate and the increase of the water yield, the settled alum blossom particles are influenced by the rising flow velocity, the settling effect is slightly reduced, and the removal rate is reduced. But the change is very weak, which shows that the intermittent sludge discharge is completely feasible under the flow, and the rising flow speed of the clear water does not exceed the design range.
Referring to fig. 1, two layers of filter screens 21 are arranged in the middle of the interior of the filter tank 20, a floating ball filter layer 30 is arranged at the top end of the filter tank 20, a sewage pump 22 is fixedly connected to the bottom of the filter tank 20, and the other end of the sewage pump 22 is communicated with a secondary collection tank 10; the upper right corner of the filter tank 20 is communicated with the sterilization tank 24 through a second transmission pipe 23, the sewage in the filter tank 20 is filtered by two layers of filter screens 21 of the filter tank 20 and then is filtered by a floating ball filter layer 30, the moisture in the upper layer part is discharged into the sterilization tank 24 through the second transmission pipe 23, and the moisture of a small amount of sewage doped at the bottom of the filter tank 20 is discharged into the secondary collection tank 10 through a sewage discharge pump 22; the right end of the secondary collection tank 10 is fixedly connected with a slurry centrifugal pump 27, the other end of the centrifugal pump 27 is fixedly connected with a dehydrator 28, the output end of the dehydrator 28 is secondarily communicated with the purification tank 13 through a transmission pipe, and sewage additive is injected into the purification tank 13 to secondarily purify the sewage discharged by the dehydrator 28;
the secondary collection tank 10 is mixed with thick slurry discharged by the sewage sedimentation tank 1, slurry discharged by the purification tank 13 and sewage doped with a small amount of slurry discharged by the filter tank 20, a decontamination additive is added into the secondary collection tank 10 for purification treatment, the treated sewage is subjected to separation of larger particle suspended matters in the slurry by virtue of centrifugal force generated by high-speed operation of equipment through a slurry centrifugal pump 27, the separated slurry is discharged into a dehydrator 28 for dehydration, the dehydrated sewage is transmitted to the purification tank 13 again for purification, and the dehydrated residual slurry can be used for continuous use in buildings; the right end of the secondary collection tank 10 is provided with a sewage draining exit, and in the internal structure of the secondary collection tank 10, one end of the sewage draining exit is lower than the other end, so that on one hand, the sewage can automatically flow to one end of the sewage draining exit, and the centrifugal pump 27 can be promoted to rapidly separate the sewage and the slurry in the secondary collection tank;
in order to more thoroughly treat the water in the sterilization tank 24, an ultraviolet radiation sterilization lamp 25 is arranged at the top end inside the sterilization tank 24, a third transmission pipe 26 is externally connected to the sterilization tank 24, and after the ultraviolet radiation sterilization lamp 25 is used for carrying out irradiation sterilization for a long time, the water can be discharged and utilized safely through the third transmission pipe 26.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that various changes in the embodiments and/or modifications of the invention can be made, and equivalents and modifications of some features of the invention can be made without departing from the spirit and scope of the invention.
Claims (10)
1. The utility model provides a sewage purification, filtration, sterilizing equipment, includes sewage settling tank (1), its characterized in that: the upper end of the sewage sedimentation tank (1) is provided with a sewage inlet (2), the lower end of the sewage inlet (2) is fixedly connected with a first Y-shaped pipeline (3), and the lower side of the first Y-shaped pipeline (3) extends to a sedimentation cavity (4);
the bottom of the sewage settling tank (1) is provided with a claw water purifier (5), two sides of the upper end of the claw water purifier (5) are respectively provided with a water outlet (6), and the bottom end of the claw water purifier (5) penetrates through the bottom of the sewage settling tank (1) and is externally connected with a water supply pipe (7) through a switch valve;
the bottom of the sedimentation cavity (4) is fixedly connected with a second Y-shaped pipeline (8), the lower end of the second Y-shaped pipeline (8) is fixedly connected with a thick slurry pump (9), and the other end of the thick slurry pump (9) is communicated with a secondary collection tank (10);
a water outlet (11) is arranged at the upper right corner of the sewage settling tank (1), a screen (12) is arranged on the inner side of the water outlet (11), and the other end of the water outlet (11) is communicated with a purification tank (13);
a stirring rod (14) is arranged in the purification tank (13), and the stirring rod (14) is electrically connected with a motor (15) arranged at the top of the outer side of the purification tank (13);
a settling tank (16) is arranged at the bottom of the purification tank (13), a slurry pump (17) is fixedly connected to the lower end of the settling tank (16), and the other end of the slurry pump (17) is communicated with the secondary collection tank (10);
a purification port (18) is formed in the right upper end of the purification tank (13), the purification tank (13) is communicated with a filter tank (20) through a first transmission pipe (19), and two layers of filter screens (21) are arranged in the middle of the interior of the filter tank (20);
a sewage pump (22) is fixedly connected to the bottom of the filter tank (20), and the other end of the sewage pump (22) is communicated with the secondary collecting tank (10);
the upper right corner of the filter tank (20) is communicated with a sterilization tank (24) through a second transmission pipe (23), an ultraviolet irradiation sterilization lamp (25) is arranged at the top end inside the sterilization tank (24), and a third transmission pipe (26) is externally connected to the sterilization tank (24);
the right end of the secondary collecting tank (10) is fixedly connected with a slurry centrifugal pump (27), and the other end of the centrifugal pump (27) is fixedly connected with a dehydrator (28).
2. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: the output end of the dehydrator (28) is secondarily communicated with the purifying tank (13) through a transmission pipe, and sewage additive is injected into the purifying tank (13) to secondarily purify the sewage discharged by the dehydrator (28).
3. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: four layers of stirring blades (29) are arranged in the stirring rod (14), rectangular hollow grooves are formed in the middles of the first layer of stirring blades and the middle of the third layer of stirring blades, and the first layer of stirring blades and the third layer of stirring blades are sequentially arranged on the second layer of stirring blades and the fourth layer of stirring blades in a staggered mode.
4. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: the right end of the secondary collection tank (10) is provided with a sewage draining outlet, and in the internal structure of the secondary collection tank (10), one end of the sewage draining outlet is lower than the other end.
5. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: first trident pipeline (3) and second trident pipeline (8) are the goat's horn formula PVC material pipeline of 2 connectors of one end and the single connector of the other end.
6. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: the thick matter pump (9) differs from the thick matter pump (17) in that,
the flow rate of the underflow pump (9) is 4.2T/h, the diameter of an inlet and an outlet is 40 cm, and the working pressure is 40 kg;
the flow of the mud pump (17) is 1.5T/h, the diameter of an inlet and an outlet is 25 cm, and the working pressure is 10 kg.
7. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: the top end of the filtering tank (20) is provided with a floating ball filtering layer (30).
8. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: the feed pipe (7) is externally connected with a dosing pipe (31), the dosing pipe (31) is integrally L-shaped, and the other end of the dosing pipe (31) extends to the bottom of the cavel water purifier (5) from the inner side of the feed pipe (7).
9. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: the spray nozzle (32) is arranged at the bottom of the claw water purifier (5) and the end head of the other end of the chemical feeding pipe (7);
the jet orifice (32) is divided into an upper row of jet orifices (3201) and a lower row of jet orifices (3202), the upper row of jet orifices (3201) and the lower row of jet orifices (3202) are respectively provided with 5 rectangular jet orifices, and the rectangular jet orifices are orderly, horizontally and transversely arranged in two rows.
10. The apparatus for purifying, filtering and sterilizing sewage according to claim 1, wherein: a round water inlet (33) is formed in the bottom of the claw water purifier (5), and the round water inlet (33) is communicated with a water supply pipe (7) through a nozzle (34);
be equipped with 3 mud valve (35) around circular water inlet (33), and every mud valve (35) are nested 8 round holes that set up in the ring, and the diameter of this round hole is 1/5 of ring diameter.
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| CN201911200195.3A CN110902904B (en) | 2019-11-29 | 2019-11-29 | Sewage purification, filtration and sterilization device |
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| CN201911200195.3A CN110902904B (en) | 2019-11-29 | 2019-11-29 | Sewage purification, filtration and sterilization device |
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| RU2547503C1 (en) * | 2014-02-20 | 2015-04-10 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования Волгоградский государственный аграрный университет | Water treatment device |
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| CN110902904B (en) | 2022-03-01 |
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