CN209835820U - Deep purification system for bath water - Google Patents

Deep purification system for bath water Download PDF

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Publication number
CN209835820U
CN209835820U CN201920336339.7U CN201920336339U CN209835820U CN 209835820 U CN209835820 U CN 209835820U CN 201920336339 U CN201920336339 U CN 201920336339U CN 209835820 U CN209835820 U CN 209835820U
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water
pipe
connecting pipe
coagulant
outlet
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CN201920336339.7U
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Chinese (zh)
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许芝
侯婷婷
费庆志
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Dalian Jiaotong University
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Dalian Jiaotong University
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Abstract

The utility model relates to a sewage treatment technical field specifically discloses a bathing water deep purification system, including the inlet tube, the coagulant medical kit, the coagulant advances the pencil, ozone generator, the ozone intake pipe, multi-functional medium pump, the outlet pipe, the second is biked to take over, the flocculant medical kit, the flocculating agent advances the pencil, the pipe-line mixer, the precipitation separation district, go out the dross mouth, the dross collecting vat, the water catch bowl, the dross discharge pipe, curtain-type milipore filter subassembly, the evacuation pipe, the pipe that absorbs water, the pump that absorbs water, go out water connecting pipe and purification back outlet pipe, the one end of inlet tube is established in the pond, the other end and the access connection of multi-functional medium pump, the one end and the water catch bowl of purification back outlet pipe are. The utility model discloses can be integrated in a reactor device with flocculation, air supporting, disinfection, membrane separation's processing method, utilize the purification that adds medicine flocculation, ozone disinfection and air supporting, milipore filter, accomplish the multiple purification reaction of quality of water in the bathing pool.

Description

Deep purification system for bath water
Technical Field
The utility model relates to a sewage treatment technical field especially relates to a bathing water deep purification system.
Background
At present, chemical flocculation and precipitation are mainly adopted in the method for purifying the water quality in the bath pool, chlorine medicines are used for sterilization and disinfection, and then filters are used for filtering, so that the aim of saving heat energy and water cost is achieved. The bath water has the characteristics of large water volume, high temperature and light pollution, and the recycling of the bath water after treatment is a mode for improving the profit. The ultrafiltration filter has micron-scale filtration precision relative to a quartz sand filter and an active carbon filter, the ultrafiltration membrane has nano-scale filtration precision, and a membrane component in the ultrafiltration equipment has a filtration pore diameter of 10nm, so that almost all bacteria, microorganisms, viruses, escherichia coli, macromolecular organic matters, all insoluble colloids in water and the like in raw water can be removed. The ultrafiltration membrane technology is utilized to treat the bath water, the filtration precision is high, the treatment efficiency is high, the treated water quality is clear, no peculiar smell is generated, and the water can be directly reused in a bath basin.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing a bathing water deep purification system to the processing mode integration with flocculation, air supporting, disinfection, membrane separation is in a reactor device, utilizes the purification that adds medicine flocculation, ozone disinfection and air supporting, milipore filter, accomplishes the multiple purification reaction of quality of water in the bathing pool.
In order to solve the technical problem, the utility model provides a bath water deep purification system, which comprises a water inlet pipe, a coagulant medicine box, a coagulant medicine inlet pipe, an ozone generator, an ozone inlet pipe, a multifunctional medium pump, a water outlet pipe, a second joint pipe, a flocculant medicine box, a flocculant medicine inlet pipe, a pipeline mixer, a precipitation separation area, a scum outlet, a scum collecting tank, a water collecting tank, a scum discharging pipe, a curtain type ultrafiltration membrane component, a emptying pipe, a water suction pump, a water outlet connecting pipe and a purified water outlet pipe; the one end of inlet tube is established in the pond, the other end with the access connection of multi-functional medium pump, the coagulant medical kit pass through the coagulant advance the pencil with advance water piping connection, ozone generator passes through the ozone intake pipe with the access connection of multi-functional medium pump, the export of multi-functional medium pump pass through the outlet pipe with the pipe-line mixer is connected, the flocculating agent medical kit passes through the flocculating agent advance the pencil with the pipe-line mixer is connected, the pipe-line mixer pass through the second connecting tube with the lower extreme of sedimentation separation district is connected, the upper end of sedimentation separation district is the drainage opening, it is located the top of sedimentation separation district to go out the dross mouth, the outside that goes out the dross mouth is equipped with dross and water catch bowl in proper order, the dross discharge pipe with the dross catch bowl is connected, curtain ultrafiltration membrane module is located the below of sedimentation separation district, the emptying pipe is located below the curtain type ultrafiltration membrane assembly, the curtain type ultrafiltration membrane assembly passes through the water suction pipe and the inlet connection of the water suction pump, the outlet of the water suction pump passes through the water outlet connecting pipe and the water collecting tank is connected, one end of the purified water outlet pipe is connected with the water collecting tank, and the other end of the purified water outlet pipe is connected with the water tank.
Preferably, the one end of inlet tube in the pond is equipped with the bottom valve, the inlet tube be in with the coagulant advances the both sides of the junction of pencil all to be equipped with the governing valve, still be equipped with first vacuum meter on the inlet tube.
Preferably, the coagulant feeding pipe is connected with the coagulant medicine box through a coagulant metering pump and a coagulant medicine suction pipe, the coagulant feeding pipe is further provided with a first valve, the flocculant feeding pipe is connected with the flocculant medicine box through a flocculant metering pump and a flocculant medicine suction pipe, and the flocculant feeding pipe is further provided with a second valve.
Preferably, the ozone inlet pipe is provided with an ozone flowmeter and an ozone regulating valve.
Preferably, the outlet pipe is provided with an adjusting valve, a pressure gauge and a flowmeter, the flowmeter is connected with the pipeline mixer through a first connecting pipe, and the first connecting pipe is provided with the adjusting valve and a first sampling faucet.
Preferably, still include the equipment box, precipitation separation zone and curtain-type milipore filter subassembly are all established in the equipment box, the precipitation separation zone is for the narrow wide hopper column structure in the lower that is enclosed by first baffle, the inboard of first baffle is equipped with the baffle structure, the upper end of equipment box forms out the dross mouth through the second baffle, separate into dross collecting vat and water catch bowl through the third baffle on the second baffle, the lower extreme of equipment box is the collecting vat structure, the lower extreme of equipment box still is equipped with the equipment stabilizer blade.
Preferably, the water collecting tank is connected with the lower part of the equipment box body through a backflow balancing pipe.
Preferably, the water suction pipe is provided with a regulating valve and a second vacuum meter.
Preferably, the water outlet connecting pipe is connected with the lower part of the curtain type ultrafiltration membrane component through a fourth connecting pipe, the fourth connecting pipe is provided with a regulating valve, the two sides of the joint of the water outlet connecting pipe and the fourth connecting pipe are provided with regulating valves, and the water outlet connecting pipe is further provided with a second sampling faucet.
Preferably, still include cleaner medical kit, cleaner with pencil, running water connecting pipe, penetrate hydrophone and third union coupling, the cleaner medical kit passes through the cleaner with the pencil with penetrate the hydrophone and connect, be equipped with the cleaner governing valve on the cleaner with the pencil, the running water connecting pipe with penetrate the hydrophone and connect be equipped with the governing valve on the running water connecting pipe, penetrate the hydrophone pass through the third connecting pipe with the union coupling that absorbs water.
Preferably, the first and second electrodes are formed of a metal,
the utility model discloses a bathing water deep purification system can be integrated in a reactor device with flocculation, air supporting, disinfection, membrane separation's processing method, utilizes the purification that adds medicine flocculation, ozone disinfection and air supporting, milipore filter, accomplishes the multiple purification reaction of quality of water in the bathing pool, and whole device has easy operation of simple to use, area is little, and nontoxic nothing remains, and water yield cyclic utilization is high, the energy-conserving characteristics of water conservation. The utility model discloses an use coagulant and flocculating agent and water after the intensive mixing, make aquatic soluble glue class material (like fat), change the electric potential, the destabilization, the colloidal particle that takes off the stability collides each other, condenses when mixing, makes tiny colloidal particle become great flocculating body, further adsorbs suspended particles, bacterium, just also makes the process of bathing water crescent greasy dirt fine hair body. The flocks are retained outside the ultrafiltration membrane, and the ultrafiltration membrane only allows the solvent (such as water molecules), inorganic salt and small molecular organic matters in the solution to permeate through, and retains suspended substances, colloids, proteins, microorganisms and other macromolecular substances in the solution, thereby achieving the purposes of purification and separation. The pollutants on the surface of the membrane are removed by backwashing after a certain time, so as to achieve the purpose of improving the water quality of the bathing pool. And most of water-insoluble pollutants such as bacteria, carried viruses and dirt on human epidermis, color, smell, taste, phenol, chlorine and the like in water can be decomposed and killed by the strong oxidizing property of ozone, and organic matters and three substances which are difficult to biodegrade are decomposed, so that the water quality is improved without causing secondary pollution.
Drawings
Fig. 1 is a schematic view of a sectional structure of an integrated device for deep purification of bathroom water according to an embodiment of the present invention.
In the figure, 1: a multifunctional medium pump; 2: a water inlet pipe; 3: a first vacuum gauge; 4: adjusting a valve; 5: adjusting a valve; 6: a bottom valve; 7: a pool; 8: an ozone inlet pipe; 9: an ozone regulating valve; 10: an ozone flow meter; 11: an ozone generator; 12: a coagulant tank; 13: a coagulant suction pipe; 14: a coagulant dosing pump; 15: a coagulant inlet pipe; 16: a first valve; 17: a water outlet pipe; 18: adjusting a valve; 19: a pressure gauge; 20: a flow meter; 21: adjusting a valve; 22: a first sampling faucet; 23: a first coupling pipe; 24: a pipeline mixer; 25: adjusting a valve; 26: a flocculant kit; 27: a flocculant drug suction pipe; 28: a flocculant metering pump; 29: a flocculant inlet pipe; 30: a second valve; 31: a second coupler tube; 32: an outlet; 33: a first separator; 34: a second separator; 35: a third partition plate; 36: a scum outlet; 37: a scum collecting tank; 38: a scum discharge pipe; 39: a water suction pump; 40: a suction pipe; 41: a second vacuum gauge; 42: adjusting a valve; 43: a curtain-type ultrafiltration membrane module; 44: a water outlet connecting pipe; 45: adjusting a valve; 46: adjusting a valve; 47: a second sampling faucet; 48: a water collection tank; 49: a reflux balance tube; 50: discharging the purified water out of the pipe; 51: a cleaning agent box; 52: a cleaning agent dosing pipe; 53: a cleaning agent regulating valve; 54: a water ejector; 55: a tap water connecting pipe; 56: adjusting a valve; 57: a third connecting pipe; 58: a fourth connecting pipe; 59: adjusting a valve; 60: emptying the pipe; 61: adjusting a valve; 62: an equipment stand bar; 63: an equipment box body.
Detailed Description
The following describes embodiments of the present invention in further detail with reference to the accompanying drawings and examples. The following examples are intended to illustrate the invention, but are not intended to limit the scope of the invention.
In the description of the present invention, it should be noted that the terms "center", "longitudinal", "lateral", "up", "down", "front", "back", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outer", and the like indicate the orientation or positional relationship based on the orientation or positional relationship shown in the drawings, and are only for convenience of description and simplification of the description, but do not indicate or imply that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation, and thus, should not be construed as limiting the present invention. Furthermore, the terms "first" and "second" are used for descriptive purposes only and are not to be construed as indicating or implying relative importance.
In the description of the present invention, it is to be noted that, unless otherwise explicitly specified or limited, the terms "mounted," "connected," and "connected" are to be construed broadly, and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; they may be connected directly or indirectly through intervening media, or they may be interconnected between two elements. The specific meaning of the above terms in the present invention can be understood in specific cases to those skilled in the art. In addition, in the description of the present invention, "a plurality" means two or more unless otherwise specified.
As shown in fig. 1, the deep purification system for bath water of the present embodiment includes: the device comprises a water inlet pipe 2, a coagulant medicine box 12, a coagulant medicine inlet pipe 15, an ozone generator 11, an ozone inlet pipe 8, a multifunctional medium pump 1, a water outlet pipe 17, a second connecting pipe 31, a flocculant medicine box 26, a flocculant medicine inlet pipe 29, a pipeline mixer 24, a precipitation separation area, a scum outlet 36, a scum collecting tank 37, a water collecting tank 48, a scum outlet pipe 38, a curtain type ultrafiltration membrane assembly 43, an emptying pipe 60, a water suction pipe 40, a water suction pump 39, a water outlet connecting pipe 44 and a purified water outlet pipe 50.
One end of a water inlet pipe 2 is arranged in a water pool, the other end of the water inlet pipe is connected with an inlet of a multifunctional medium pump 1, a coagulant medicine box 12 is connected with the water inlet pipe 2 through a coagulant medicine inlet pipe 15, an ozone generator 11 is connected with an inlet of the multifunctional medium pump 1 through an ozone inlet pipe 8, an outlet of the multifunctional medium pump 1 is connected with a pipeline mixer 24 through a water outlet pipe 17, a flocculant medicine box 26 is connected with the pipeline mixer 24 through a flocculant medicine inlet pipe 29, the pipeline mixer 24 is connected with the lower end of a precipitation separation area through a second connecting pipe 31, the upper end of the precipitation separation area is a water discharge opening, a scum outlet 36 is positioned above the precipitation separation area, the outer side of the scum outlet 36 is sequentially provided with a scum collecting tank 37 and a water collecting tank 48, a scum discharge pipe 38 is connected with the scum collecting tank 37, a curtain type ultrafiltration membrane component 43 is positioned below the, the curtain type ultrafiltration membrane component 43 is connected with the inlet of the water suction pump 39 through the water suction pipe 40, the outlet of the water suction pump 39 is connected with the water collecting tank 48 through the water outlet connecting pipe 44, one end of the purified water outlet pipe 50 is connected with the water collecting tank 48, and the other end is connected with the water tank 7.
One end of the water inlet pipe 2 in the water tank 7 is provided with a bottom valve 6, the two sides of the joint of the water inlet pipe 2 and the coagulant feeding pipe 15 are both provided with a regulating valve 4 and a regulating valve 5, and the water inlet pipe 2 is also provided with a first vacuum meter 3. A coagulant inlet pipe 15 is connected with a coagulant medicine box 12 through a coagulant metering pump 14 and a coagulant medicine suction pipe 13, a first valve 16 is further arranged on the coagulant inlet pipe 15, the coagulant medicine liquid is sucked into the water inlet pipe 2 through the coagulant inlet pipe 15 and the first valve 16 to participate in coagulation reaction, a flocculant inlet pipe 29 is connected with a flocculant medicine box 26 through a flocculant metering pump 28 and a flocculant medicine suction pipe 27, a second valve 30 is further arranged on the flocculant inlet pipe 29, and the flocculant liquid is sucked into the pipeline mixer 24 through the flocculant inlet pipe 29 and the second valve 30 to participate in flocculation reaction. The ozone inlet pipe 8 is provided with an ozone flowmeter 10 and an ozone adjusting valve 9. The water outlet pipe 17 is provided with an adjusting valve 18, a pressure gauge 19 and a flowmeter 20, the flowmeter 20 is connected with a pipeline mixer 24 through a first connecting pipe 23, and the first connecting pipe 23 is provided with an adjusting valve 21 and a first sampling water tap 22. The second connecting pipe 31 is provided with a regulating valve 25, and the outlet 32 of the second connecting pipe 31 is located at the lower part of the sedimentation separator. The water collecting tank 48 is connected with the lower part of the equipment box body 63 through a backflow balancing pipe 49, the effluent purified by the ultrafiltration membrane component is sucked out through a water suction pump 39 and then discharged into the water collecting tank 48, the backflow balancing pipe 49 is arranged in the water collecting tank 48, the purified water flows back to a membrane component purification area through the backflow balancing pipe 49 to realize further purification, and the outer wall of the water collecting tank 48 is connected with a water outlet pipe 50 so that the water in the water collecting tank 48 is discharged to the water tank 7. The suction pipe 40 is provided with a regulating valve 42 and a second vacuum gauge 41. The water outlet connecting pipe 44 is connected with the lower part of the curtain type ultrafiltration membrane assembly 43 through a fourth connecting pipe 58, an adjusting valve 59 is arranged on the fourth connecting pipe 58, an adjusting valve 45 and an adjusting valve 46 are arranged on two sides of the connecting part of the water outlet connecting pipe 44 and the fourth connecting pipe 58, and a second sampling water faucet 47 is further arranged on the water outlet connecting pipe 44. The evacuation pipe 60 is provided with a regulating valve 61.
The deep purification system for bath water in the embodiment further comprises: the equipment box 63, the precipitation separation area and the curtain-type ultrafiltration membrane component 43 are arranged in the equipment box 63, the precipitation separation area is of a hopper-shaped structure which is narrow at the bottom and wide at the top and is surrounded by the first partition plate 33, a baffle structure is arranged on the inner side of the first partition plate 33, incoming water enters from the bottom and overflows from the top to the inner side of the first partition plate 33 according to a small baffle perpendicular to the partition plate, the water flows upwards after entering the water, the small baffle plays a role in blocking the flow so as to form a rotational flow state, and the water body is favorably subjected to full mixing flocculation. Ultrafiltration is a technology capable of purifying and separating a solution, an ultrafiltration membrane system is a solution separation device which takes ultrafiltration membrane filaments as a filter medium and takes pressure difference on two sides of the membrane as a driving force, the ultrafiltration membrane only allows solvents (such as water molecules), inorganic salts and small molecular organic matters in the solution to permeate, and suspended matters, colloids, proteins, microorganisms and other macromolecular substances in the solution to be intercepted, so that the purposes of purification and separation are achieved. The upper end of the equipment box 63 is provided with a scum outlet 36 through a second partition plate 34, the second partition plate 34 is divided into a scum collecting tank 37 and a water collecting tank 48 through a third baffle plate 35, the lower end of the equipment box 63 is of a collecting tank structure, and the lower end of the equipment box 63 is also provided with equipment support legs 62.
The deep purification system for bath water of the embodiment further comprises: the cleaning agent box 51 is connected with the water injector 54 through the cleaning agent feeding pipe 52, the cleaning agent adjusting valve 53 is arranged on the cleaning agent feeding pipe 52, the tap water connecting pipe 55 is connected with the water injector 54, the tap water connecting pipe 55 is provided with an adjusting valve on the tap water connecting pipe 55, and the water injector 54 is connected with the water suction pipe 40 through the third connecting pipe 57.
The working principle of the deep purification system for bath water in the embodiment is as follows: opening a water inlet bottom valve 6, an adjusting valve 4, an adjusting valve 5, a first valve 16 and an ozone adjusting valve 9 in a water tank 7, starting a multifunctional medium pump 1, a coagulant metering pump 14 and an ozone generator 11, simultaneously sucking the water in the water tank 7 and a coagulant PAC (poly aluminum chloride) entering a coagulant inlet pipe 15 into a water inlet pipe 2 by the multifunctional medium pump 1, adjusting the water inlet flow, the PAC dosage and the ozone air inflow by the corresponding adjusting valves, simultaneously sucking the water through the multifunctional medium pump 1, arranging a vacuum meter 3 at the front end of the multifunctional medium pump, arranging a pressure meter 19 and a flow meter 20 at the rear end, opening a front and rear adjusting valve 18 and an adjusting valve 21 of the flow meter, detecting the water sample by a sampling water tap 22, flowing into a pipeline mixer 24 after adjusting the corresponding flow, then opening a second valve 30 and a flocculant metering pump 28, and adding a flocculant into the pipeline mixer through a flocculant inlet pipe 29 after adjusting the dosage, at this time, raw water, PAC, PAM and ozone can be fully mixed, the regulating valve 25 is opened, and the outlet water enters the bottom of the center of the precipitation separation zone of the integrated equipment through the connecting pipe 31 and the outlet 32 behind the mixer. After water is fed into the precipitation separation zone, the water flows upwards, the small baffle plate plays a role in blocking the flow, so that a rotational flow state is formed in the zone, water bodies are fully contacted and mixed, and PAC (poly aluminum chloride) can be oxidized by an oxidant to cause the precipitation of COD (chemical oxygen demand) particulate matters through the effects of a compressed double electric layer of the PAC or a hydrolysate thereof, electric neutralization, tape winding net capture, adsorption bridging and the like; PAM is an organic polymeric flocculant and has the function of forming larger flocs among particles so as to generate huge surface adsorption force, so that fine colloidal particles become larger flocs and further adsorb suspended particles and bacteria, namely the process of gradually increasing oil-contaminated flocs by bath water; the ozone gas forms a large amount of fine bubbles in the precipitation separation area, the floating action of the bubbles enables the suspended pollutants to float to the surface of water, the scum overflows into a scum collecting tank 37 through a scum outlet 36 and is discharged out of the equipment through a scum discharge pipe 38; the bacteria, carried viruses and dirt of human epidermis, and most water-insoluble pollutants such as color, smell, taste, phenol, chlorine and the like in the water can be decomposed and killed by the strong oxidizing property of ozone, and organic matters and substances which are difficult to biodegrade are decomposed; after the mixed liquid in the separation chamber is flocculated, sterilized and disinfected, the mixed liquid continuously flows down to an ultrafiltration membrane purification area, an adjusting valve 42, an adjusting valve 45 and an adjusting valve 46 are opened, a water suction pump 39 is started, a vacuum meter 41 is adjusted, the ultrafiltration membrane takes the pressure difference between two sides of the membrane as a driving force, the ultrafiltration membrane is taken as a filtering medium, under certain pressure, when a raw liquid flows through the surface of the membrane, a plurality of fine micropores densely distributed on the surface of the ultrafiltration membrane only allow water and small molecular substances to pass through to form permeate liquid, substances with the volume larger than the micropore diameter of the surface of the membrane in the raw liquid are intercepted on the liquid inlet side of the membrane, the purposes of purifying, separating and concentrating the raw liquid are realized, and sludge settled at the bottom of the device is discharged through a discharge pipe 60 and; the purified water is sucked by the water suction pump 39 through the water suction pipe 40 and then discharged through the water outlet connecting pipe 44, and the water outlet connecting pipe 44 is connected with the sampling water tap 47 and then discharged into the water collection tank 48 after sampling inspection. A backflow balance pipe 49 is arranged in the water collecting tank, and the purified water flows back to the membrane module purification area through the backflow balance pipe 49, so that further purification can be realized; and the outer wall of the water collecting tank is connected with a water outlet pipe 50, so that the water in the water collecting tank 48 is discharged to the water pool 7 for recycling.
The pressure differential across the membrane of the filtration system increases as particulate matter in the feed water gradually accumulates on the outer surface of the membrane during operation. In order to maintain a certain membrane flux and prolong the service life of the membrane component, the ultrafiltration system stops filtering and carries out periodic backwashing. The backwashing process is to reversely permeate the ultrafiltration produced water or tap water through the hollow fiber membrane and scrub the surface of the hollow fiber membrane filaments to remove sediments. After backwashing is started, the water inlet adjusting valve 25 is closed, the water suction pump 39 continues to operate, the cleaning agent adjusting valve 53, the water injector 54 and the tap water connection adjusting valve 56 are opened, so that after the water suction pump 39 sucks the purified water in the water collecting tank 48, the purified water is mixed with a cleaning agent in a certain proportion when water is discharged, the cleaning agent and the cleaning agent enter the membrane reversely through the water suction pipe multifunctional medium pump 40, after the membrane is soaked for a short time, backwashing water enters the ultrafiltration fibers from the clear liquid side and flows to the concentrated water side through the membrane, pollutants on the surfaces of membrane pore passages and the curtain type ultrafiltration membrane are washed away through large-flow backwashing water, and the washed pollutants are discharged through the emptying pipe 60 and the adjusting valve 61.
The utility model discloses a bathing water deep purification system can be integrated in a reactor device with flocculation, air supporting, disinfection, membrane separation's processing method, utilizes the purification that adds medicine flocculation, ozone disinfection and air supporting, milipore filter, accomplishes the multiple purification reaction of quality of water in the bathing pool, and whole device has easy operation of simple to use, area is little, and nontoxic nothing remains, and water yield cyclic utilization is high, the energy-conserving characteristics of water conservation. The utility model discloses an use coagulant and flocculating agent and water after the intensive mixing, make aquatic soluble glue class material (like fat), change the electric potential, the destabilization, the colloidal particle that takes off the stability collides each other, condenses when mixing, makes tiny colloidal particle become great flocculating body, further adsorbs suspended particles, bacterium, just also makes the process of bathing water crescent greasy dirt fine hair body. The flocks are retained outside the ultrafiltration membrane, and the ultrafiltration membrane only allows the solvent (such as water molecules), inorganic salt and small molecular organic matters in the solution to permeate through, and retains suspended substances, colloids, proteins, microorganisms and other macromolecular substances in the solution, thereby achieving the purposes of purification and separation. The pollutants on the surface of the membrane are removed by backwashing after a certain time, so as to achieve the purpose of improving the water quality of the bathing pool. And most of water-insoluble pollutants such as bacteria, carried viruses and dirt on human epidermis, color, smell, taste, phenol, chlorine and the like in water can be decomposed and killed by the strong oxidizing property of ozone, and organic matters and three substances which are difficult to biodegrade are decomposed, so that the water quality is improved without causing secondary pollution.
The embodiments of the present invention have been presented for purposes of illustration and description, and are not intended to be exhaustive or limited to the invention in the form disclosed. Many modifications and variations will be apparent to those of ordinary skill in the art. The embodiment was chosen and described in order to best explain the principles of the invention and the practical application, and to enable others of ordinary skill in the art to understand the invention for various embodiments with various modifications as are suited to the particular use contemplated.

Claims (10)

1. A deep purification system for bath water is characterized by comprising a water inlet pipe (2), a coagulant medicine box (12), a coagulant medicine inlet pipe (15), an ozone generator (11), an ozone inlet pipe (8), a multifunctional medium pump (1), a water outlet pipe (17), a second connecting pipe (31), a flocculant medicine box (26), a flocculant medicine inlet pipe (29), a pipeline mixer (24), a precipitation separation area, a scum outlet (36), a scum collecting tank (37), a water collecting tank (48), a scum discharge pipe (38), a curtain type ultrafiltration (43), an emptying pipe (60), a water suction pipe (40), a water suction pump (39), a water outlet connecting pipe (44) and a purified water outlet pipe (50); the one end of inlet tube (2) is established in the pond, the other end with the access connection of multi-functional medium pump (1), coagulant medical kit (12) pass through coagulant advance pencil (15) with inlet tube (2) are connected, ozone generator (11) pass through ozone intake pipe (8) with the access connection of multi-functional medium pump (1), the export of multi-functional medium pump (1) pass through outlet pipe (17) with pipeline mixer (24) are connected, flocculating agent medical kit (26) pass through flocculating agent advance pencil (29) with pipeline mixer (24) are connected, pipeline mixer (24) through second joint pipe (31) with the lower extreme of sedimentation separation district is connected, the upper end of sedimentation separation district is the drainage opening, it is located to go out scum mouth (36) the top of sedimentation separation district, go out the outside of dross mouth (36) and be equipped with dross collecting vat (37) and water catch bowl (48) in proper order, dross discharge pipe (38) with dross collecting vat (37) are connected, curtain ultrafiltration membrane subassembly (43) are located deposit the below of disengagement zone, evacuation pipe (60) are located the below of curtain ultrafiltration membrane subassembly (43), curtain ultrafiltration membrane subassembly (43) pass through water suction pipe (40) with the access connection of water suction pump (39), the export of water suction pump (39) is passed through go out water connecting pipe (44) with water catch bowl (48) are connected, purify the one end of back outlet pipe (50) with water catch bowl (48) are connected, and the other end is connected with pond (7).
2. The deep purification system for bath water according to claim 1, wherein a bottom valve (6) is arranged at one end of the water inlet pipe (2) in the water tank (7), adjusting valves are arranged on two sides of the connection part of the water inlet pipe (2) and the coagulant inlet pipe (15), and a first vacuum meter (3) is further arranged on the water inlet pipe (2).
3. The deep purification system for bath water according to claim 1, wherein the coagulant inlet pipe (15) is connected with the coagulant medicine box (12) through a coagulant metering pump (14) and a coagulant medicine suction pipe (13), the coagulant inlet pipe (15) is further provided with a first valve (16), the flocculant inlet pipe (29) is connected with the flocculant medicine box (26) through a flocculant metering pump (28) and a flocculant medicine suction pipe (27), and the flocculant inlet pipe (29) is further provided with a second valve (30).
4. The deep bath water purification system as claimed in claim 1, wherein an ozone flow meter (10) and an ozone regulating valve (9) are provided on the ozone inlet pipe (8).
5. The deep purification system for bath water according to claim 1, wherein the outlet pipe (17) is provided with a regulating valve, a pressure gauge (19) and a flow meter (20), the flow meter (20) is connected with the pipeline mixer (24) through a first connecting pipe (23), and the first connecting pipe (23) is provided with a regulating valve and a first sampling faucet (22).
6. The deep purification system for bath water according to claim 5, further comprising an equipment box (63), wherein the precipitation separation area and the curtain-type ultrafiltration membrane assembly (43) are both arranged in the equipment box (63), the precipitation separation area is of a hopper-shaped structure with a narrow lower part and a wide upper part, which is surrounded by a first partition plate (33), a baffle structure is arranged inside the first partition plate (33), the upper end of the equipment box (63) forms a scum outlet (36) through a second partition plate (34), the second partition plate (34) is separated into a scum collecting tank (37) and a water collecting tank (48) through a third baffle plate (35), the lower end of the equipment box (63) is of a collecting tank structure, and the lower end of the equipment box (63) is further provided with an equipment support leg (62).
7. The deep scrubbing system for bath water according to claim 1, wherein said water collection tank (48) is connected to a lower portion of said equipment cabinet (63) through a return balance pipe (49).
8. The deep purification system for bath water according to claim 1, wherein the suction pipe (40) is provided with a regulating valve and a second vacuum gauge (41).
9. The deep purification system for bath water according to claim 1, wherein the outlet connecting pipe (44) is connected with the lower part of the curtain type ultrafiltration membrane component (43) through a fourth connecting pipe (58), the fourth connecting pipe (58) is provided with a regulating valve, the outlet connecting pipe (44) is provided with a regulating valve on both sides of the connection part of the outlet connecting pipe and the fourth connecting pipe (58), and the outlet connecting pipe (44) is further provided with a second sampling water tap (47).
10. The deep purification system for bath water according to any one of claims 1-9, further comprising a cleaning agent box (51), a cleaning agent feeding pipe (52), a tap water connecting pipe (55), a water injector (54) and a third connecting pipe (57), wherein the cleaning agent box (51) is connected with the water injector (54) through the cleaning agent feeding pipe (52), the cleaning agent feeding pipe (52) is provided with a cleaning agent regulating valve (53), the tap water connecting pipe (55) is connected with the water injector (54), the tap water connecting pipe (55) is provided with a regulating valve, and the water injector (54) is connected with the water suction pipe (40) through the third connecting pipe (57).
CN201920336339.7U 2019-03-18 2019-03-18 Deep purification system for bath water Active CN209835820U (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109734218A (en) * 2019-03-18 2019-05-10 大连交通大学 Bathing advanced water treatment integration apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109734218A (en) * 2019-03-18 2019-05-10 大连交通大学 Bathing advanced water treatment integration apparatus

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