CN105254079B - Purifying pool water device - Google Patents
Purifying pool water device Download PDFInfo
- Publication number
- CN105254079B CN105254079B CN201410276321.4A CN201410276321A CN105254079B CN 105254079 B CN105254079 B CN 105254079B CN 201410276321 A CN201410276321 A CN 201410276321A CN 105254079 B CN105254079 B CN 105254079B
- Authority
- CN
- China
- Prior art keywords
- shell block
- pipe fitting
- shell
- water
- valve
- 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.)
- Active
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Physical Water Treatments (AREA)
Abstract
A kind of purifying pool water device, to solve the problems, such as that current purifying pool water is ineffective.The purifying pool water device of the present invention includes：One coarse filtration module, tool are placed in there are one coarse filtration part in first shell block；One electrolysis module, tool to be assembled in second shell block and in second shell block that stretches through respectively there are two electrode and a ultraviolet tube, which is electrically connected a chargers；One refined filtration module, tool are placed in there are one refined filtration part in a third shell block；And a pipeline assembly, it is concatenated by several pipe fittings and connects first shell block, the second shell block and third shell block, and the connected state between several pipe fittings is controlled by several valves.
Description
Technical field
The present invention relates to a kind of aqueous processing units, and especially one kind is in the ponds such as purifying aquaculture pond or landscape pond
Aqueous purifying pool water device.
Background technology
In the ponds such as aquaculture pond or landscape pond, the pollution sources of aqueous are fallen leaves essentially from natural dust fall, organism in water
Excreta or feeding organism in water the itrogenous organic substances such as feed residual bait, after being decomposed by the microorganisms because of those itrogenous organic substances,
The accumulation of the inorganic nitrogen compounds such as ammonia nitrogen and nitrate nitrogen in water is often resulted in, causes water eutrophication, influences pond ecology very
It is huge；Particularly for aquaculture pond, when ammonia nitrogen concentration is too high or even murder by poisoning can be generated to aquatic livestock, cause aquatic livestock
Mortality so that reducing cultivation effect, therefore the ammonia nitrogen in water must be removed.
In some existing technologies, vehicle of fetching water can be used constantly to stir liquid level, increase the dissolved oxygen amount in water, by nitre
Mineralized nitrogen is less toxic nitrate nitrogen, but the nitrate nitrogen of high concentration contributes to algae largely to increase again by change effect
It is raw, and excessive algae often results in the death of water quality deterioration, even aquatic livestock, therefore cultivate dealer and have to reuse chemistry
Medicament controls water quality；Though this measure can promote yield, aquatic livestock quality and the market price are also reduced.
In other existing technologies, then by the way of probiotics is administered to water, by nitrous acid Pseudomonas, nitric acid
The microorganisms such as Pseudomonas and denitration Pseudomonas, the inorganic nitrogen compounds such as ammonia nitrogen and nitrate nitrogen are nitrified, denitration the effects that.So
And though this processing mode more naturally, causes slowly there are reaction speed, treatment effeciency is poor, is easily limited by weather condition and only fitted
The problems such as handling low-concentration ammonia-nitrogen aqueous；Furthermore the cost for buying probiotics is quite high, and when the battalion of strain in processing water
When supporting salt deficiency, it is necessary to which additional addition nutritive salt more causes the burden in cost in aqueous.
Also, in addition to going in water removal other than ammonia nitrogen, it is still necessary to comprising the programs such as contaminant filter and disinfection, can just make for the purification of water
Water maintains good water quality；Separately preferably can also water temperature over-high or it is too low when, the effect of lower water temperature is provided.However, existing
The effects that " inorganic nitrogen compound in removal water ", " impurity screening ", " disinfection " or " lower water temperature " in some technologies, can be provided
Device all set respectively so that purifying the flow of aqueous must carry out, and the fortune of each different function device stage by stage
Work sequence also needs labor intensive operation adjustment, can not automatically work continuously, not only cause aqueous purification efficiency poor, be more likely to
Because of the misoperation of sequence of operations, make aqueous clean-up effect bad；Moreover, the device of each different function also occupies respectively
Huge storage space forms the puzzlement of operating environment moving-wire management, and it is really necessary to be improved.
Invention content
The object of the present invention is to provide a kind of purifying pool water devices, can generate the hypochloric acid water of tool biocidal efficacies（HClO）,
Or the ammonia nitrogen in water is directly transformed into nitrogen, to greatly improve the treatment effeciency to inorganic nitrogen compound, and have both sterilization
Effect.
Time purpose of the present invention is to provide a kind of purifying pool water device, incorporate carry out it is several needed for purification water
Different function module, and aqueous purification operation can be carried out continuously, to promote aqueous purification efficiency and reduce the required storage occupied
Space.
To reach foregoing purpose, the present invention with technology contents include：
A kind of purifying pool water device, comprising：One coarse filtration module, there are one the first shell blocks for coarse filtration module tool, and one thick
Filter part is placed in first shell block；One electrolysis module, electrolysis module tool is there are one the second shell block, two electrodes and one
Ultraviolet tube is assembled in second shell block and respectively in second shell block that stretches through, which is electrically connected a power supply
Device；One refined filtration module, there are one third shell block, a refined filtration part is placed in the third shell block refined filtration module tool；And one
A pipeline assembly, the pipeline assembly have several pipe fittings and several valves, which connects the first shell block, the second shell
Seat and third shell block, several valves are set on several pipe fittings to control the connected state between several pipe fittings.
Wherein, the operating voltage of the charger is preferably adjustable.
Wherein, which is set between two electrodes, and flickering for the ultraviolet tube is controlled.
Wherein, a sodium chloride supply tank connects the inside of second shell block.
Wherein, exhaust pipe there are one being set at the top of second shell block.
Wherein, several potsherds are placed in the bottom in second shell block, the second shell seat tool there are two infusion port, wherein
One infusion port is to being located at several potsherds.
The purifying pool water device can also additionally comprise a lower water temperature module, and there are one the 4th shells for lower water temperature module tool
Seat, a pyrogenicity part and a cooling component, the pyrogenicity part and cooling component are assembled in the 4th shell block and stretch through into the 4th respectively
In shell block, the pyrogenicity part and cooling component are started by control, and once only start the alternative one；4th shell block is by the pipeline group
Another pipe fitting of part connects the third shell block and the valve by being set on the pipe fitting control the 4th shell block and the third shell block it
Between connected state.
Wherein, for third shell block tool there are two infusion port, one of pipe fitting of the pipeline assembly connects the third shell block
One of infusion port, and set on the pipe fitting there are one Venturi tube, a snorkel connects the Venturi tube by one end
At larynx, the other end of the snorkel is in open shape.
Wherein, which is filtering element (cartridge) made of charcoal or activated carbon material or most particles.
Wherein, which is divided into the upper and lower layer being connected, and the upper strata of the coarse filtration part is most corundum particles, should
The lower floor of coarse filtration part is most zeolite granulars, and there are two infusion ports for the first shell seat tool, and one of infusion port is to being located at this
The upper strata of coarse filtration part, another infusion port is to being located at the lower floor of the coarse filtration part.
The purifying pool water device can also additionally comprise hypochlorous acid water generation module, and there are one hypochloric acid water generation module tools
5th shell block and two electrodes, two electrodes are assembled in the 5th shell block and in the 5th shell block that stretches through respectively, this two
Electrode is electrically connected a charger；5th shell block connects the first shell block, second by other several pipe fittings of the pipeline assembly
Shell block and third shell block and control the in addition company between several pipe fittings and other pipe fittings by other several valves of the pipeline assembly
Logical state.
Wherein, a sodium chloride supply tank connects the inside of the 5th shell block.
Accordingly, purifying pool water device of the invention can generate the hypochloric acid water of tool biocidal efficacies（HClO）Or directly will
Ammonia nitrogen in water is transformed into nitrogen, to greatly improve the treatment effeciency to inorganic nitrogen compound, and has both bactericidal effect；In addition,
The purifying pool water device of the present invention incorporates the several different function modules carried out needed for purification water, and can be carried out continuously aqueous
Operation is purified, to promote aqueous purification efficiency and reduce the required storage space occupied.
Description of the drawings
Fig. 1：The planar structure schematic diagram of first embodiment of the invention.
Fig. 2：First embodiment of the invention generates the implementation schematic diagram of hypochloric acid water.
Fig. 3：First embodiment of the invention removes ammonia nitrogen in water removal and increases the implementation schematic diagram of dissolved oxygen amount.
Fig. 4：First embodiment of the invention removes ammonia nitrogen in water removal and adjusts the implementation schematic diagram of water temperature.
Fig. 5：The inverse implementation schematic diagram for rinsing the first stage of first embodiment of the invention.
Fig. 6：The inverse implementation schematic diagram for rinsing second stage of first embodiment of the invention.
Fig. 7：The inverse implementation schematic diagram for rinsing the phase III of first embodiment of the invention.
Fig. 8：The planar structure schematic diagram of second embodiment of the invention.
Fig. 9：Second embodiment of the invention generates the implementation schematic diagram of hypochloric acid water.
Figure 10：Second embodiment of the invention removes ammonia nitrogen in water removal and increases the implementation schematic diagram of dissolved oxygen amount.
Figure 11：Second embodiment of the invention generation hypochloric acid water removes in water removal ammonia nitrogen and increases the implementation of dissolved oxygen amount to show simultaneously
It is intended to.
Figure 12：Second embodiment of the invention removes ammonia nitrogen in water removal and adjusts the implementation schematic diagram of water temperature.
Figure 13：The inverse implementation schematic diagram for rinsing the first stage of second embodiment of the invention（One）.
Figure 14：The inverse implementation schematic diagram for rinsing the first stage of second embodiment of the invention（Two）.
Figure 15：The inverse implementation schematic diagram for rinsing second stage of second embodiment of the invention.
Figure 16：The inverse implementation schematic diagram for rinsing the phase III of second embodiment of the invention.
【Main element symbol description】
1 coarse filtration module, 11 first shell block
11a the first infusion port the second infusion ports of 11b
12 coarse filtration parts
2 electrolysis 21 second shell blocks of module
The 4th infusion ports of 21a third infusion ports 21b
211 exhaust pipe of 21c discharge outlet
22 electrode, 23 charger
24 ultraviolet tube, 25 potsherd
3 refined filtration module, 31 third shell block
The 6th infusion ports of the 5th infusion port 31b of 31a
311 exhaust pipe, 32 refined filtration part
4 pipeline assembly 41a ~ 41k, 41m, 41n pipe fitting
411 Venturi tube, 412 snorkel
42a ~ 42k, 42m, 42n, 42p, 42q valve
43 effluent outfalls
The 4th shell block of 5 lower water temperature module 51
The 8th infusion ports of the 7th infusion port 51b of 51a
511 exhaust pipe, 52 pyrogenicity part
53 cooling components
6 hypochloric acid waters generate the 5th shell block of module 61
The tenth infusion ports of the 9th infusion port 61b of 61a
611 exhaust pipe, 62 electrode
63 chargers
M Water-pumping motor P hydraulic gages
T1 sodium chloride supply tanks T2 is formulated supply tank.
Specific embodiment
For above and other objects, features and advantages of the invention can be clearer and more comprehensible, it is cited below particularly the present invention compared with
Good embodiment, and coordinate institute's accompanying drawings, it is described in detail below：
Fig. 1 is please referred to, is the first embodiment of purifying pool water device of the present invention, which generally includes one
Coarse filtration module 1, one is electrolysed module 2, a refined filtration module 3 and a pipeline assembly 4, which is concatenated by several pipe fittings and connected
The coarse filtration module 1, electrolysis module 2 and refined filtration module 3 and the circulation status by several valves control aqueous.
The coarse filtration module 1 has one first shell block 11, and first shell block 11 is defeated with one first infusion port 11a and one second
Liquid mouth 11b, the first infusion port 11a for the pipeline assembly 4 a pipe fitting 41a connections, a valve 42a be set on pipe fitting 41a on,
Valve 42a is a unidirectional relief valve, and second infusion port 11b then for a pipe fitting 41b connections of the pipeline assembly 4, makes aqueous
First shell block 11 can be passed in and out by the pipe fitting 41a, 41b.One coarse filtration part 12 is placed in first shell block 11, the coarse filtration part 12
It can be used to filter out impurities in water（Such as：Silt, fallen leaves, the excreta of organism in water or feed residual bait of feeding organism in water etc.
Substance）, in the present embodiment, which can be divided into the upper and lower layer being connected, and upper strata is most corundum particles, under
Layer is then most zeolites（zeolite）Particle.Wherein, the first infusion port 11a of first shell block 11 is to being located at the coarse filtration part
12 upper strata, the second infusion port 11b of first shell block 11 is to being located at the lower floor of the coarse filtration part 12.
The electrolysis module 2 has one second shell block 21, which has a third infusion port 21a, one the 4th defeated
A liquid mouth 21b and discharge outlet 21c, the third infusion port 21a make second shell block for the pipe fitting 41b connections of the pipeline assembly 4
21 are connected with first shell block 11, and the 4th infusion port 21b is for a pipe fitting 41c connections of the pipeline assembly 4, the discharge outlet
21c then for a pipe fitting 41d connections of the pipeline assembly 4, makes aqueous that can pass in and out the second shell by the pipe fitting 41b, 41c, 41d
Seat 21；Wherein, a valve 42b is set on pipe fitting 41b, and a valve 42c is set on pipe fitting 41c, and a valve 42d is set on pipe fitting 41d
On.In addition, second shell block 21 is separately equipped with an exhaust pipe 211 in top；And if when being intended to the water purified as fresh water, a chlorine
The inside of second shell block 21 can be connected by changing sodium supply tank T1, to give sodium chloride to the aqueous in second shell block 21 is defeated；Relatively
Ground, if be intended to the water purified as seawater, sodium chloride supply tank T1 can need not be set.
The electrolysis module 2 additionally comprises two electrodes 22, a charger 23 and a ultraviolet tube 24, which divides
It is not assembled in second shell block 21 and in second shell block 21 that stretches through, which is a DC power supply, and the charger
23 operating voltage is preferably adjustable, and the anode of the charger 23 is for the electrical connection of one of two electrodes 22, the charger
23 cathode is then electrically connected for another electrode 22；The ultraviolet tube 24 be also assembled in second shell block 21 and stretch through into this second
In shell block 21, which is preferably set between two electrodes 22, and flickering for the ultraviolet tube 24 can be controlled
System.Preferably, the electrolysis module 2, also comprising several potsherds 25, which is placed in second shell block 21
Bottom, the 4th infusion port 21b of second shell block 21 can be to being located at several potsherds 25.
The refined filtration module 3 has a third shell block 31, and the third shell block 31 is defeated with one the 5th infusion port 31a and one the 6th
Liquid mouth 31b, the 5th infusion port 31a make the third shell block 31 and the second shell for the pipe fitting 41c connections of the pipeline assembly 4
Seat 21 is connected and controls the connected state between the third shell block 31 and second shell block 21 by valve 42c；6th infusion
Mouth 31b makes aqueous that can pass in and out the third shell block by the pipe fitting 41c, 41e then for a pipe fitting 41e connections of the pipeline assembly 4
31.Wherein, a valve 42e is set on pipe fitting 41e, to control the connected state between bis- ends of pipe fitting 41e；Preferably, the pipe
A Venturi tube 411 is additionally provided on part 41e, valve 42e is compared with the Venturi tube 411 adjacent to the 6th infusion port of the third shell block 31
31b, which has a reducing diameter part, and forms a larynx, a snorkel 412 in the wide place of most path of the reducing diameter part
The larynx of the Venturi tube 411 is connected by one end, the other end of the snorkel 412 is in open shape to connect the external world.
One refined filtration part 32 is placed in the third shell block 31, which can be used to the fine impurities in absorption water（Example
Such as：Filter out the substances such as free chlorine, oxide, peculiar smell, organic solvent）, in the present embodiment, which may be selected to be wood
Filtering element (cartridge) made of charcoal or activated carbon material or most particles.In addition, the third shell block 31 is separately equipped with an exhaust pipe in top
311；And one formula supply tank T2 can connect the inside of the third shell block 31, with to the aqueous in the third shell block 31 it is defeated give as
Help the formulas such as the probiotics for promoting aquatic health.
The purifying pool water device is also provided with a lower water temperature module 5, which has one the 4th shell block
51, the 4th shell block 51 has one the 7th infusion port 51a and one the 8th infusion port 51b, and the 7th infusion port 51a is for the pipeline
One pipe fitting 41f connections of component 4, a valve 42f are set on pipe fitting 41f, and pipe fitting 41f connects pipe fitting 41e, and the pipe fitting
41f is located at pipe fitting 41e and connects between one end of the 6th infusion port 31b and valve 42e, makes the 4th shell block 51 and the third
Shell block 31 is connected and controls the connected state between the 4th shell block 51 and the third shell block 31 by valve 42f；8th is defeated
Liquid mouth 51b then for a pipe fitting 41g connections of the pipeline assembly 4, makes aqueous that can pass in and out the 4th shell by the pipe fitting 41f, 41g
Seat 51.Wherein, the end of pipe fitting 41e can be connected with pipe fitting 41g, and pipe fitting 41g is equipped with a valve 42g, should with control
Connected state between pipe fitting 41e and the 8th infusion port 51b.4th shell block 51 is separately equipped with an exhaust pipe 511 in top.
The lower water temperature module 5 additionally comprises consistent 52 and one cooling component 53 of warmware, and the pyrogenicity part 52 and cooling component 53 are distinguished
It is assembled in the 4th shell block 51 and in the 4th shell block 51 that stretches through, the pyrogenicity part 52 and cooling component 53 can be started by control, and
It is primary only to start alternative one, with to the aqueous pyrogenicity in the 4th shell block 51 or refrigeration.
In addition to above-mentioned component, the pipeline assembly 4 additionally comprise an a pipe fitting 41h and valve 42h on pipe fitting 41h,
An one pipe fitting 41i and valve 42i, the pipe fitting 41j on the pipe fitting 41i and valve 42j on pipe fitting 41j, a pipe
Part 41k and two valve 42k, 42m and a valve 42n on pipe fitting 41k.Wherein, one end of pipe fitting 41h connects the pipe
The other end of part 41a, pipe fitting 41h then connect a Water-pumping motor M, and water is pumped into pipe fitting 41h, on pipe fitting 41h
A hydraulic gage P can be equipped with, hydraulic gage P abuts Water-pumping motor M, to measure the hydraulic pressure being pumped into pipe fitting 41h.The pipe fitting
One end of 41i connects pipe fitting 41b, and the other end of pipe fitting 41i then connects the pipe fitting 41e, 41f；One end of pipe fitting 41j connects
Lead to pipe fitting 41h, and between Water-pumping motor M and valve 42h, the other end of pipe fitting 41j then connect pipe fitting 41b,
41i；One end of pipe fitting 41k connects pipe fitting 41a, and the other end of pipe fitting 41k then connects pipe fitting 41b, pipe fitting 41k's
An effluent outfall 43 is additionally provided between two ends, and the effluent outfall 43 is located between two valve 42k, 42m；Valve 42n is set
In on pipe fitting 41b, for valve 42b compared with valve 42n adjacent to the third infusion port 21a of second shell block 21, pipe fitting 41k connections should
The end of pipe fitting 41b is located between valve 42b and valve 42n.
Fig. 2 is please referred to, when purifying aqueous using the purifying pool water device of first embodiment of the invention, can control the pipeline group
Valve 42b, 42d, 42h, 42n of part 4 be in opening, the valve 42c, 42i, 42j, 42k, 42m be in closed state, valve 42e,
42f, 42g remain stationary state（It is turned on and off）, and extinguish the ultraviolet tube 24.Accordingly, Water-pumping motor M is by water
After being pumped into pipe fitting 41h, aqueous flows into pipe fitting 41a by valve 42h, continuous to flow into this slightly by the first infusion port 11a
In the first shell block 11 for filtering module 1, impurities in water is tentatively filtered out by the coarse filtration part 12；Then, aqueous passes through second infusion port
11b and flow out first shell block 11, and flow into pipe fitting 41b, it is continuous to be flowed by valve 42n, 42b and the third infusion port 21a
In the second shell block 21 for entering the electrolysis module 2.When water is fresh water, by the sodium chloride supply tank T1 in second shell block 21
Aqueous defeated give sodium chloride（Water is then exempted from when being seawater）, which powers to two electrodes 22, be electrolysed this second
Dissolved with the aqueous of sodium chloride in shell block 21.
Wherein, it will be electrolysed dissolved with the aqueous of sodium chloride by two electrodes 22, generate hydrogen at an electrode 22 wherein（Instead
Ying Shiwei：2Na++ 2H2O+2e-→2NaOH+H2↑）, and hydrogen（H2）It can be discharged from the exhaust pipe 211；At another electrode 22
Then generate chlorine（Reaction equation is：2Cl-→Cl2+2e-）, and chlorine（Cl2）It meets water and is hydrolyzed into hypochlorous acid again（Reaction equation is：Cl2+
H2O→H++Cl-+HClO）, with the hypochloric acid water of generation tool biocidal efficacies（HClO）, and flow back in pond from pipe fitting 41d, with right
Water is sterilized.
Alternatively, when being not desired to inject water the hypochloric acid water of tool biocidal efficacies, Fig. 3 is please referred to, controls the pipeline assembly 4
Valve 42b, 42c, 42h, 42e, 42n in opening, the valve 42d, 42f, 42g, 42i, 42j, 42k, 42m are in closed state,
And light the ultraviolet tube 24.Accordingly, it is same as aforementionedly, water flows into the electrolysis module 2 after by the coarse filtration module 1
It in second shell block 21, and is electrolysed by the aqueous dissolved with sodium chloride by two electrodes 22, at this point, the hypochloric acid water of generation is through the purple
The irradiation of outer light lamp tube 24 and resolve into hydrogen free radical and chlorine radical, and chlorine radical can be further by the ammonia in water
Nitrogen becomes nitrogen（N2）, and discharged from the exhaust pipe 211, achieve the effect that ammonia nitrogen in water removal；Thus, the present invention is not necessary to
By nitrite nitrogen and nitrate nitrogen, you can the ammonia nitrogen in the aqueous dissolved with sodium chloride directly is transformed into nitrogen, is substantially carried
Height is to the treatment effeciency of inorganic nitrogen compound in water.
Then, after removing the ammonia nitrogen in aqueous, aqueous flows out second shell block 21 by the 4th infusion port 21b, and
Pipe fitting 41c is flowed into, it is continuous to be flowed into the third shell block 31 of the refined filtration module 3 by valve 42c and the 5th infusion port 31a；
Wherein, if being equipped with aforementioned several potsherds 25 in second shell block 21, aqueous can also lead to before second shell block 21 is flowed out
It crosses several potsherds 25 and filters out the substances such as bacterium, organic compound, suspended particulate or precipitation absurd creature.Aqueous flows into the third shell
After seat 31, then the fine impurities in water are adsorbed by the refined filtration part 32, further promote the cleanliness of aqueous.
Continuous, aqueous flows out the third shell block 31 by the 6th infusion port 31b, and flows into pipe fitting 41e, then sequentially pass through
Valve 42e, the Venturi tube 411 and flow into pipe fitting 41g, and then flow back in pond；Wherein, since aqueous is passing through this article mound
In pipe 411 larynx at when, the static pressure of aqueous declines, and makes outside air that can input the Venturi tube 411 from the snorkel 412
In, so as to achieving the effect that increase dissolved oxygen amount in aqueous.
In addition to this, Fig. 4 is please referred to, in the case where weather condition is relatively extreme, such as during cold current, then control may be selected
Valve 42b, 42c, 42h, 42f, 42g, 42n of the pipeline assembly 4 are made in opening, valve 42d, 42e, 42i, 42j, 42k,
42m is in closed state, and starts the pyrogenicity part 52 of the lower water temperature module 5.Accordingly, water in such as aforesaid paths sequentially by this
After coarse filtration module 1, electrolysis module 2 and refined filtration module 3 are filtered only, then the pipe fitting 41e, 41f can be sequentially flowed through, and pass through valve 42f
And the 7th infusion port 51a and flow into the 4th shell block 51 of the lower water temperature module 5, the aqueous after making filter net is by the pyrogenicity part
52 heating and heat up, then the 4th shell block 51 is flowed out by the 8th infusion port 51b, and flow into pipe fitting 41g, then flow back to
Chi Zhong achievees the effect that balancing tank water temperature.Similarly, under the weather of high temperature sweltering heat, then it can start the lower water temperature instead
The cooling component 53 of module 5 after the aqueous cooling after making filter net flows back in pond, can reduce extreme climate to aquaculture harvest again
The influence of rate.
Fig. 5 is please referred to, which dirty remains on this after aforementioned various water purification programs, to avoid
In pipeline assembly 4, user can control the purifying pool water device to carry out inverse cleaning procedure.First, it can control the pipeline assembly 4
Valve 42b, 42c, 42h, 42i, 42m are in opening, and the valve 42d, 42e, 42f, 42j, 42k, 42n are in closed state, valve 42g
It remains stationary state（It is turned on and off）；Accordingly, the water after filtering only can be pumped into pipe fitting 41h, aqueous by Water-pumping motor M
Pipe fitting 41a is flowed by valve 42h, continuous the first shell block 11 that the coarse filtration module 1 is flowed by the first infusion port 11a
In, then first shell block 11 flowed out by the second infusion port 11b, it flows through pipe fitting 41b and flows into pipe fitting 41i, pass through
Valve 42i is directly flowed into from the 6th infusion port 31b of the third shell block 31 in the third shell block 31, inverse to rinse the third shell block
After refined filtration part 32 in 31, flowed out from the 5th infusion port 31a of the third shell block 31, by pipe fitting 41c, valve 42c, from this
4th infusion port 21b of two shell blocks 21 is flowed into second shell block 21, then is flowed from the third infusion port 21a of second shell block 21
Go out, by pipe fitting 41b, valve 42b, flow into pipe fitting 41k, which is flowed by valve 42m, to be emitted into
One sump（Figure is not painted）.Thus, not only pipe fitting 41h, 41a, 41i, 41c, 41b can be rinsed totally, the refined filtration part
32 can also be cleaned to prolong the service life.
Fig. 6 is please referred to, next, valve 42j, 42k for then can control the pipeline assembly 4 are in opening, valve 42h,
42i, 42m, 42n are in closed state, and the valve 42b, 42c, 42d, 42e, 42f, 42g remain stationary state（It is turned on and off）；
Accordingly, the water after filtering only can be pumped into pipe fitting 41h, and aqueous is made to flow into pipe fitting 41j by Water-pumping motor M, pass through the valve
42j flows into pipe fitting 41b again, continuous to be flowed into the first shell block 11 of the coarse filtration module 1 by the second infusion port 11b, inverse punching
After washing the coarse filtration part 12 in first shell block 11, flowed out from the first infusion port 11a of first shell block 11, pass through pipe fitting 41a
Pipe fitting 41k is flowed into, which is flowed into, and be emitted into aforementioned sump by valve 42k.Thus,
Not only pipe fitting 41j, 41k can be rinsed totally, which can also be cleaned to prolong the service life.
Fig. 7 is please referred to, finally, controls valve 42h, 42m, 42n of the pipeline assembly 4 in opening, valve 42b, 42i,
42j, 42k are in closed state, and the valve 42c, 42d, 42e, 42f, 42g remain stationary state（It is turned on and off）；Accordingly, the pumping
Water motor M can by filter it is net after water be pumped into pipe fitting 41h, aqueous flows into pipe fitting 41a by valve 42h, continue by this
One infusion port 11a and flow into the first shell block 11 of the coarse filtration module 1, then by the second infusion port 11b and flow out this first
Shell block 11, and pipe fitting 41b is flowed into, pipe fitting 41k is flowed by valve 42n, which is flowed by valve 42m
Pipe 43, and it is emitted into aforementioned sump.Thus, pipe fitting 41h, 41a, 41b can also be rinsed totally.
Accordingly, the present invention is characterized in：Impurities in water is filtered out, then by the electrolysis module 2 by the coarse filtration module 1
Generation has the hypochloric acid water of biocidal efficacies or the ammonia nitrogen in water is transformed into nitrogen, continuous to be adsorbed in water by the refined filtration module 3
Fine impurities；Aqueous purification operation can be not only carried out continuously, to promote aqueous purification efficiency, more reaches effective filtration, purification water
Effect, while have both " disinfection water " and " efficiently removing inorganic nitrogen compound in water removal " and other effects, it is ensured that water quality maintains
Well.In addition, the purifying pool water device of the present invention can also carry out the program of inverse flushing, make each filter part and pipe fitting that can remain clear
It is clean to avoid blocking, help and prolong the service life and then reduce repair and consumables cost.
In addition, it is noted that the electrolysis module 2 of the present invention uses diaphragm-free electrolysis method, can make by aqueous be in
Property partially micro- alkali, be suitble to aquatic livestock existence；Moreover, the electrolysis operating voltage that the present invention can arrange in pairs or groups adjustable, according to the ammonia in water
Nitrogen concentration adjustment electrolysis operating voltage, such as when being used in the higher pond of ammonia nitrogen concentration in water, its is turned up and is electrolysed operating voltage,
Make the improved efficiency of ammonia nitrogen in water removal, can reach quick rescue water quality, avoid the effect of aquatic livestock death.
Fig. 8 is please referred to, is the second embodiment of purifying pool water device of the present invention, which is generally same as aforementioned
First embodiment, main difference is：It is aquatic that the second embodiment of purifying pool water device of the present invention is additionally provided with a hypochlorous acid
Into module 6, with the electrolysis module 2 of arranging in pairs or groups, it is carried out at the same time generation hypochloric acid water and removes ammonia nitrogen in water removal.
In detail, the main difference of the hypochloric acid water generation module 6 and the electrolysis module 2 in：The hypochloric acid water generates mould
The ultraviolet tube 24 of the electrolysis module 2 is omitted in group 6.In other words, hypochloric acid water generation module 6 has one the 5th shell block
61, the 5th shell block 61 has one the 9th infusion port 61a and 1 the tenth infusion port 61b, and the 9th infusion port 61a is for the pipeline
One pipe fitting 41m connections of component 4, the tenth infusion port 61b then for a pipe fitting 41n connections of the pipeline assembly 4, make aqueous can
5th shell block 61 is passed in and out by the pipe fitting pipe fitting 41m, 41n.Wherein, the other end of pipe fitting 41m then connects pipe fitting 41b,
And between valve 42n connects pipe fitting 41b with pipe fitting 41k, enable the 5th shell block 61 and 11 phase of the first shell block
Connection；The other end of pipe fitting 41n then connects pipe fitting 41c, and positioned at the 5th infusion port of valve 42c and the third shell block 31
Between 31a, the 5th shell block 61 is enable to be connected with second shell block 21 and third shell block 31.Also, a valve 42p is set on the pipe fitting
On 41m, a valve 42q is set on pipe fitting 41n, and be connected to the discharge outlet 21c of second shell block 21 in the first embodiment
Pipe fitting 41d then changes be connected with pipe fitting 41n in the present embodiment, and second shell block 21 is no longer equipped with discharge outlet 21c.
In addition, the 5th shell block 61 is separately equipped with an exhaust pipe 611 in top；And if when being intended to the water purified as fresh water,
The sodium chloride supply tank T1 connected in the first embodiment inside second shell block 21 is then connected into the 5th shell block 61 instead
Inside, to give sodium chloride to the aqueous in the 5th shell block 61 is defeated；Similarly, if be intended to the water purified as seawater, the chlorine
Changing sodium supply tank T1 can need not then be set.
Hypochloric acid water generation module 6 additionally comprises two 62 and one chargers 63 of electrode, which assembles respectively
In the 5th shell block 61 and the 5th shell block 61 that stretches through, which is a DC power supply, and the work of the charger 23
Be preferably as voltage it is adjustable, the anode of the charger 63 for the electrical connection of one of two electrodes 62, the charger 63 it is negative
Pole is then electrically connected for another electrode 62.
Structure accordingly please refers to Fig. 9, when purifying aqueous using the purifying pool water device of second embodiment of the invention, controllably
Valve 42d, 42h, 42n, 42p of the pipeline assembly 4 are made in opening, the valve 42b, 42i, 42j, 42k, 42m, 42q are in closing
State, the valve 42c, 42e, 42f, 42g remain stationary state（It is turned on and off）.Accordingly, water is pumped by Water-pumping motor M
After pipe fitting 41h, aqueous flows into pipe fitting 41a by valve 42h, continuous to flow into the coarse filtration mould by the first infusion port 11a
In first shell block 11 of group 1, impurities in water is tentatively filtered out by the coarse filtration part 12；Then, aqueous by the second infusion port 11b and
First shell block 11 is flowed out, flow into pipe fitting 41b and passes through valve 42n, then flows into pipe fitting 41m, continue through valve 42p and is somebody's turn to do
9th infusion port 61a and flow into the hypochloric acid water generation module 6 the 5th shell block 61 in.When water is fresh water, by the chlorination
Sodium supply tank T1 is defeated to the aqueous in the 5th shell block 61 to give sodium chloride（Water is then exempted from when being seawater）, the charger 63 to this two
A electrode 62 is powered, to be electrolysed in the 5th shell block 61 dissolved with the aqueous of sodium chloride, so as to generate chlorine at an electrode 62 wherein
Gas, and chlorine meets water and is hydrolyzed into hypochlorous acid again, with the hypochloric acid water of generation tool biocidal efficacies（HClO）, and from the 5th shell block 61
The tenth infusion port 61b flow into pipe fitting 41n, then flow into pipe fitting 41d, and flow back in pond by valve 42d, with to water
It is sterilized.
Alternatively, when being not desired to inject water the hypochloric acid water of tool biocidal efficacies, Figure 10 is please referred to, controls the pipeline assembly
4 valve 42b, 42c, 42h, 42e, 42n, 42p is in opening, and the valve 42d, 42f, 42g, 42i, 42j, 42k, 42m, 42q are in
Closed state, and light the ultraviolet tube 24.Accordingly, for aqueous after by the coarse filtration module 1, afterflow enters pipe fitting 41b,
In most aqueous the second shell block 21 of the electrolysis module 2 can be flowed by valve 42n, 42b and the third infusion port 21a
In, least a portion of aqueous then flows into pipe fitting 41m, and it is aquatic to flow into the hypochlorous acid by valve 42p and the 9th infusion port 61a
Into in the 5th shell block 61 of module 6；Thus, the higher aqueous of sodium chloride concentration in the 5th shell block 61, it will be by diffusion
Effect, makes the aqueous in second shell block 21 also dissolved with sodium chloride, and then by the electrolysis of two electrodes 22 to generate hypochlorous acid
Water, and hydrogen free radical and chlorine radical are resolved into irradiation of the hypochloric acid water through the ultraviolet tube 24 again, then by chlorine therein
Ammonia nitrogen in water is become nitrogen by free radical（N2）, and discharged from the exhaust pipe 211, achieve the effect that ammonia nitrogen in water removal.
Wherein, if water is seawater, due to having contained sodium chloride in aqueous, therefore valve 42q can be switched to closing shape
State makes aqueous that need not flow into the 5th shell block 61, flows directly into the program that ammonia nitrogen is removed in second shell block 21.
Then, after removing the ammonia nitrogen in aqueous, then with being same as aforementioned first embodiment, guiding aqueous passes through the refined filtration module
3 to promote the cleanliness of aqueous, and continue increases dissolved oxygen amount in aqueous when by the Venturi tube 411, finally flows back in pond.
In addition to this, second embodiment of the invention can more be carried out at the same time generation hypochloric acid water and remove ammonia nitrogen in water removal.In detail
Yan Zhi please refers to Figure 11, controls valve 42b, 42c, 42d, 42h, 42e, 42n, 42p of the pipeline assembly 4 in opening, the valve
42f, 42g, 42i, 42j, 42k, 42m, 42q are in closed state, and light the ultraviolet tube 24 and generate the hypochloric acid water
Two electrodes 62 of module 6 are carried out at the same time electrolysis with two electrodes 22 of the electrolysis module 2.Thus, pass through the coarse filtration mould
Some can be flowed into pipe fitting 41m by the aqueous of group 1, and the 5th shell is flowed by valve 42p and the 9th infusion port 61a
In seat 61, hypochloric acid water is generated, and flow back to by pipe fitting 41d after two electrodes 62 electrolysis by hypochloric acid water generation module 6
Chi Zhong；The aqueous of another part is then flowed by valve 42n, 42b and the third infusion port 21a in second shell block 21, by
Two electrodes 22 of the electrolysis module 2 are electrolysed and are irradiated by the ultraviolet tube 24 to remove ammonia nitrogen in water removal, and in passing through the essence
It is flow back in pond after filter module 3 and the Venturi tube 411.
Figure 12 is please referred to, in the case where weather condition is relatively extreme, such as during cold current, then may be selected to control the pipeline
Valve 42b, 42c, 42h, 42f, 42g, 42n, 42p of component 4 be in opening, valve 42d, 42e, 42i, 42j, 42k, 42m,
42q is in closed state, and starts the pyrogenicity part 52 of the lower water temperature module 5.Accordingly, water in such as aforesaid paths sequentially by this
After coarse filtration module 1, electrolysis module 2 and refined filtration module 3 are filtered only, then the pipe fitting 41e, 41f can be sequentially flowed through, and pass through valve 42f
And the 7th infusion port 51a and flow into the 4th shell block 51 of the lower water temperature module 5, the aqueous after making filter net is by the pyrogenicity part
52 heating and heat up, then the 4th shell block 51 is flowed out by the 8th infusion port 51b, and flow into pipe fitting 41g, then flow back to
Chi Zhong achievees the effect that balancing tank water temperature.Similarly, under the weather of high temperature sweltering heat, then it can start the lower water temperature instead
The cooling component 53 of module 5 after the aqueous cooling after making filter net flows back in pond, can reduce extreme climate to aquaculture harvest again
The influence of rate.
Figure 13 is please referred to, the purifying pool water device of second embodiment of the invention can also carry out inverse cleaning procedure；In detail, it is first
Valve 42b, 42c, 42h, 42i, 42m of the pipeline assembly 4 are first controlled in opening, valve 42e, 42f, 42j, 42k, 42n,
42p, 42q are in closed state, and the valve 42d, 42g remain stationary state（It is turned on and off）；Accordingly, Water-pumping motor M can be incited somebody to action
Water after filter is net is pumped into pipe fitting 41h, and aqueous flows into pipe fitting 41a by valve 42h, continues through first infusion port 11a
And flow into the first shell block 11 of the coarse filtration module 1, then first shell block 11 is flowed out by the second infusion port 11b, it flows through
Pipe fitting 41b simultaneously flows into pipe fitting 41i, and by valve 42i, directly being flowed into from the 6th infusion port 31b of the third shell block 31 should
In third shell block 31, after the refined filtration part 32 in inverse flushing third shell block 31, flowed from the 5th infusion port 31a of the third shell block 31
Go out, by pipe fitting 41c, valve 42c, flowed into second shell block 21 from the 4th infusion port 21b of second shell block 21, then from this
Second shell block 21 third infusion port 21a outflow, by pipe fitting 41b, valve 42b, flow into pipe fitting 41k, by valve 42m and
The effluent outfall 43 is flowed into, to be emitted into aforementioned sump.Thus, not only pipe fitting 41h, 41a, 41i, 41c, 41b
It can be rinsed totally, which can also be cleaned to prolong the service life.
Figure 14 is please referred to, continuous valve 42h, 42i, 42m, 42p, 42q for controlling the pipeline assembly 4 is in opening, the valve
42b, 42c, 42d, 42e, 42f, 42j, 42k, 42n are in closed state, and valve 42g remains stationary state（It is turned on and off）；
Accordingly, the water after filtering only can be pumped into pipe fitting 41h by Water-pumping motor M, and aqueous flows into pipe fitting 41a by valve 42h, continues
By the first infusion port 11a to flow into the first shell block 11 of the coarse filtration module 1, then flowed by the second infusion port 11b
Go out first shell block 11, flow through pipe fitting 41b and flow into pipe fitting 41i, by valve 42i, directly from the third shell block 31
6th infusion port 31b is flowed into the third shell block 31, after the refined filtration part 32 in inverse flushing third shell block 31, from the third shell block
31 the 5th infusion port 31a outflows, pipe fitting 41n is flowed into from pipe fitting 41c, by valve 42q, is flowed from the tenth infusion port 61b
Enter in the 5th shell block 61, then flowed out from the 9th infusion port 61a of the 5th shell block 61, from pipe fitting 41m by valve 42p and
Pipe fitting 41b is flowed into, then flows into pipe fitting 41k, which is flowed by valve 42m, it is aforementioned to be emitted into
Sump.Thus, which not only pipe fitting 41n, 41m can be rinsed totally, pipe fitting 41h, 41a, 41i and the refined filtration part 32 are all
Can cleannes be promoted by secondary cleaning.Wherein, earlier figures 13, the cleaning sequence of Figure 14 may be reversed.
Figure 15 is please referred to, next, valve 42j, 42k for then can control the pipeline assembly 4 are in opening, valve 42h,
42i, 42m, 42n are in closed state, and the valve 42b, 42c, 42d, 42e, 42f, 42g, 42p, 42q remain stationary state（It opens or closes
It closes）；Accordingly, the water after filtering only can be pumped into pipe fitting 41h, and aqueous is made to flow into pipe fitting 41j by Water-pumping motor M,
Pipe fitting 41b is flowed by valve 42j again, continuous the first shell block 11 that the coarse filtration module 1 is flowed by the second infusion port 11b
In, after the coarse filtration part 12 in inverse flushing first shell block 11, flowed out from the first infusion port 11a of first shell block 11, by this
Pipe fitting 41a flows into pipe fitting 41k, and the effluent outfall 43 is flowed into, and be emitted into aforementioned sump by valve 42k.Such as
This one, not only pipe fitting 41j, 41k can be rinsed totally, which can also be cleaned to prolong the service life.
Figure 16 is please referred to, finally, controls valve 42h, 42m, 42n of the pipeline assembly 4 in opening, valve 42b, 42i,
42j, 42k, 42p are in closed state, and the valve 42c, 42d, 42e, 42f, 42g, 42q remain stationary state（It is turned on and off）；
Accordingly, the water after filtering only can be pumped into pipe fitting 41h by Water-pumping motor M, and aqueous flows into pipe fitting 41a by valve 42h, continues
By the first infusion port 11a to flow into the first shell block 11 of the coarse filtration module 1, then flowed by the second infusion port 11b
Go out first shell block 11, and flow into pipe fitting 41b, pipe fitting 41k is flowed by valve 42n, this is flowed by valve 42m
Effluent outfall 43, and it is emitted into aforementioned sump.Thus, pipe fitting 41h, 41a, 41b can also be rinsed totally.
In conclusion the purifying pool water device of the present invention, can generate the hypochloric acid water of tool biocidal efficacies or directly by water
In ammonia nitrogen be transformed into nitrogen, to greatly improve the treatment effeciency to inorganic nitrogen compound, and have both bactericidal effect.
The purifying pool water device of the present invention, incorporates the several different function modules carried out needed for purification water, and can
Aqueous purification operation is carried out continuously, to promote aqueous purification efficiency, and ensures that water quality remains good and reduces required occupy
Storage space.
Claims (11)
1. a kind of purifying pool water device, which is characterized in that it includes：
One coarse filtration module, there are one the first shell block, a coarse filtration part is placed in first shell block coarse filtration module tool；
One electrolysis module, there are one the second shell blocks for electrolysis module tool, and two electrodes and a ultraviolet tube assemble respectively
In second shell block and second shell block that stretches through, which is electrically connected a charger；
One refined filtration module, there are one third shell block, a refined filtration part is placed in the third shell block refined filtration module tool；
One pipeline assembly, the pipeline assembly have several pipe fittings and several valves, several pipe fitting concatenation connection first shell blocks,
Second shell block and third shell block, several valves are set on several pipe fittings to control the connected state between several pipe fittings；And
One hypochloric acid water generates module, and hypochloric acid water generation module tool is there are one the 5th shell block and two electrodes, this two
Electrode is assembled in the 5th shell block and respectively in the 5th shell block that stretches through, which is electrically connected a charger；This
Five shell blocks connect first shell block, the second shell block and third shell block and by the pipeline by other several pipe fittings of the pipeline assembly
Other several valves of component control the in addition connected state between several pipe fittings and other pipe fittings.
2. purifying pool water device as described in claim 1, it is characterised in that：The operating voltage of the charger is adjustable.
3. purifying pool water device as described in claim 1, it is characterised in that：The ultraviolet tube be set on two electrodes it
Between, and flickering for the ultraviolet tube is controlled.
4. purifying pool water device as described in claim 1, it is characterised in that：It is vented there are one being set at the top of second shell block
Pipe.
5. purifying pool water device as described in claim 1, it is characterised in that：Several potsherds are placed in second shell block
Bottom, there are two infusion ports for the second shell seat tool, and one of infusion port is to being located at several potsherds.
6. the purifying pool water device as described in claim 1, it is characterised in that：Separately include a lower water temperature module, the water
Temperature adjusts module tool, and there are one the 4th shell block, a pyrogenicity part and a cooling components, and the pyrogenicity part and cooling component are assembled in respectively
In 4th shell block and the 4th shell block that stretches through, the pyrogenicity part and cooling component are started by control, and once only start the two
One of；4th shell block connects the third shell block and the valve control by being set on the pipe fitting by another pipe fitting of the pipeline assembly
Make the connected state between the 4th shell block and the third shell block.
7. purifying pool water device as described in claim 1, it is characterised in that：There are two infusion port, the pipes for third shell block tool
One of pipe fitting of road component connects one of infusion port of the third shell block, and is set on the pipe fitting there are one venturi
Pipe, a snorkel are connected the larynx of the Venturi tube by one end, and the other end of the snorkel is in open shape.
8. purifying pool water device as described in claim 1, it is characterised in that：The refined filtration part is charcoal or activated carbon material
Manufactured filter core or most particles.
9. purifying pool water device as described in claim 1, it is characterised in that：The coarse filtration part is divided into the upper and lower layer being connected, should
The upper strata of coarse filtration part is most corundum particles, and the lower floor of the coarse filtration part is most zeolite granulars, which has
Two infusion ports, one of infusion port is to being located at the upper strata of the coarse filtration part, another infusion port is to being located under the coarse filtration part
Layer.
10. purifying pool water device as described in claim 1, it is characterised in that：One sodium chloride supply tank connects the 5th shell
The inside of seat.
11. purifying pool water device as described in claim 1, it is characterised in that：One sodium chloride supply tank connects the second shell
The inside of seat.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410276321.4A CN105254079B (en) | 2014-06-19 | 2014-06-19 | Purifying pool water device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410276321.4A CN105254079B (en) | 2014-06-19 | 2014-06-19 | Purifying pool water device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105254079A CN105254079A (en) | 2016-01-20 |
| CN105254079B true CN105254079B (en) | 2018-06-26 |
Family
ID=55094084
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410276321.4A Active CN105254079B (en) | 2014-06-19 | 2014-06-19 | Purifying pool water device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105254079B (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101269894A (en) * | 2008-04-01 | 2008-09-24 | 唐战和 | Equipment and method for preparing demineralized and electrolytic direct drinking water |
| CN103663838A (en) * | 2013-12-10 | 2014-03-26 | 通威股份有限公司 | Integrated and comprehensive water treatment equipment for electrochemical water |
| CN203904127U (en) * | 2014-06-19 | 2014-10-29 | 徐才浚 | Pool water purification device |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100453472C (en) * | 2004-12-15 | 2009-01-21 | 中国科学院生态环境研究中心 | Method and apparatus for highly efficient removal of water organisms by utilizing photoelectric Fenton reaction |
| JP5873771B2 (en) * | 2012-07-06 | 2016-03-01 | 水ｉｎｇ株式会社 | Organic wastewater treatment method and treatment apparatus |
-
2014
- 2014-06-19 CN CN201410276321.4A patent/CN105254079B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101269894A (en) * | 2008-04-01 | 2008-09-24 | 唐战和 | Equipment and method for preparing demineralized and electrolytic direct drinking water |
| CN103663838A (en) * | 2013-12-10 | 2014-03-26 | 通威股份有限公司 | Integrated and comprehensive water treatment equipment for electrochemical water |
| CN203904127U (en) * | 2014-06-19 | 2014-10-29 | 徐才浚 | Pool water purification device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105254079A (en) | 2016-01-20 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US9788533B2 (en) | Aquarium filter | |
| US20130193079A1 (en) | Water Purification System | |
| WO2009100000A2 (en) | Apparatus and method for improved electrolytic water treatment process | |
| BR112013024625B1 (en) | sustainable method for treatment and maintenance of artificial water bodies, suitable for low density recreational uses, affected by bacteria and microalgae at low cost | |
| CN208378598U (en) | Wastewater treatment equipment is used in a kind of production of harmful influence | |
| US8470170B2 (en) | Ozone-assisted fluid treatment system for a reservoir | |
| CN205313291U (en) | Refrigeration cycle water integrated processing system | |
| JP5028566B2 (en) | Seawater purification device for surviving marine seafood and seawater purification method | |
| JP6947602B2 (en) | Water treatment equipment and water treatment method | |
| CN201587893U (en) | Household water purifying equipment with double-absorption and double-filtration ozone sterilization and disinfection | |
| JP2015181973A (en) | Membrane filtration system, membrane filtration method, and apparatus of producing rearing water for aquatic organism | |
| KR100675375B1 (en) | Management system of water for sea-fish nursery | |
| US9475719B2 (en) | Pool water purifying device | |
| US9169137B1 (en) | Water filtering system and method | |
| KR20120124794A (en) | Byproduct generated during the electrolysis of hydrogen processing unit | |
| JP6158658B2 (en) | Purified water production equipment | |
| CN204310906U (en) | A kind of water-purifying device | |
| CN1653004A (en) | Transportable water treatment apparatus | |
| CN105254079B (en) | Purifying pool water device | |
| CN205313294U (en) | But continuous operation's cooling circulating water treatment system | |
| CN203904127U (en) | Pool water purification device | |
| CN108975568A (en) | Marine culture wastewater and seawater aquatic products processing wastewater harmless treatment device | |
| CN108675504A (en) | A kind of circular water treating system for swimming pool | |
| TWI635056B (en) | Pool water purifying device | |
| CN208916979U (en) | Marine culture wastewater and seawater aquatic products processing wastewater harmless treatment device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |