CN205258204U - Water treatment device - Google Patents

Abstract

The utility model provides a water treatment device, include: pipeline, ion generator, ejector, vortex sediment device, suspension filter equipment and remove the chlorine device, the vortex precipitates the vortex generator that the device further includes the tube -shape casing and sets up bottom in the tube -shape casing, the ejector is plugged into in the pipeline, has rivers entry, the rivers export of the air inlet of input anion air, the pipeline of plugging into, rivers pass through ejector, vortex sediment device, suspension filter equipment in proper order and remove the chlorine device, the air inlet of ejector is connected to the ion generator for produce the anion, the anion inhales to the ejector in from air inlet under the effect of ejector, so that the water intensive mixing in anion and the ejector, and then the heavy metal ion who makes anion and aquatic takes place oxidation reduction reaction, with the heavy metal ion reduction of aquatic for the atom, appear nextly from the aquatic.

Description

Water treatment facilities

Technical field

The utility model relates to the technical field of water treatment, particularly a kind of water treatment facilities.

Background technology

Along with industrial expansion, water pollution problems is also more and more serious, and how obtaining clean, healthy drinking water has become problem urgently to be resolved hurrily.

People are not only cleaning to the requirement of quality of drinking water at present, but also wish that it has good biologically active, and such water can promote the metabolism of human body, the health being beneficial to man. Dissolving power, penetration, surface tension, density and the biochemical reaction of the size of hydrone on water self has impact more by force. Under the effect of magnetic field and electric field, hydrone syntagmatic each other can change, and in water, the large micel of concluding can be dissociated into little micel and the simple hydrone concluded, thereby water is activated. Strengthen the osmosis of cell membrane through the water of overactivation, be convenient to absorption of human body, promoted thus human body metabolism, strengthened liver function, contributed to get rid of vivotoxin, improved immunity of organisms. In the process of activated water, the mineral matter simultaneously adding can infiltrate alkalescence in electrolytic process bears child in water, has increased health necessary trace element, particularly soluble calcium, and to health, prevention various diseases plays a part positive. The device effect of the current nanometer for water is limited, and the hydrone of formation is still larger water clusters.

The antiscale of water, scale removal adopt magnetization processing to be approved by users. It is to adopt to need magnetized water by the method in magnetic field, water generates magnetization effect to be realized. In the time that water passes through magnetic field, hydrone is under the effect in magnetic field, change the physical arrangement of water, make the acicular crystal of calcium in water, magnesium salts foulant change over crystalline particulate body, making them can not weave in become hard incrustation scale is attached on wall or tube wall, and become small solids precipitation in bottom, discharge with blowdown, thereby reach the effect that prevents incrustation scale, also can be by the effect of treated water to original old incrustation scale, make it to degrade gradually, soften, become flexible, chap, until come off, reach the object of scale removal. In prior art, the device of preparing magnetized drinking water comprises two kinds of magneto and electromagnetic types, reach the object that makes magnetic water, but magnetization effect is not fine, can not solve the processing problem of large flow water quality by the path form of selecting different magnetic materials and current.

The method of the removal heavy metal in waste water of Application and Development mainly contains chemical method, physical-chemical process and bioanalysis at present, comprises the methods such as chemical precipitation, electrolysis, ion-exchange, film separation, activated carbon and silica gel absorption, bioflocculation, biological adsorption, phytoremediation. Generally speaking, adopt chemical method, physical-chemical process all by remaining years pollution transportation, easily cause secondary pollution, and pollute and be difficult to process for the harmful heavy metal of large watershed, low concentration.

In addition, the process for purifying water of prior art is generally and utilizes filter core to filter granular cloud thing in water, then carry out sterilizing to passing into chlorine in water, but this kind of method exists following shortcoming: 1, filter core needs often to change and clean, complicated operation; If filter core is changed not in time, the impurity meeting breed bacteria retaining at filter core place, and then pollute water to be clean; 2, owing to retaining chlorine in water, and chlorine is poisonous, can produce harm to directly drinking the people of this water; 3, the process for purifying water of prior art has only carried out simple filtration and sterilization to water, cannot regulate micronutrient levels in the acid-base value, water of water benefit materials such as (especially) metasilicic acids, and then obtain the drinking water to health; 4, cannot be except harmful substances such as the bacteriums that can not be killed by chlorine in anhydrating.

Utility model content

The utility model provides a kind of water treatment facilities, can solve complicated its of water treatment facilities in prior art and cannot ensure the technical problem of water quality.

For addressing the above problem, the utility model provides a kind of water treatment facilities, comprise: pipeline, ion generator, ejector, vortex settling device, suspension filter device and dechlorination device, described vortex settling device further comprises tubular shell and is arranged on the vortex generator of described tubular shell inner bottom part; Described vortex generator further comprises the wind wheel blade of motor and driven by motor rotation, and described vortex generator produces whirlpool in tubular shell bottom, and solid granular impurity heavier in water is assembled to place of bottom centre in the shape of a spiral under the effect of whirlpool; Described ejector is docked with in described pipeline, has air intake, the flow inlet of the pipeline of plugging into, the water export of input anion air; Current pass through described ejector, described vortex settling device, suspension filter device and dechlorination device successively; Described ion generator connects the air intake of described ejector, for generation of anion, described anion is sucked into described ejector from described air intake under the effect of ejector, so that described anion is fully mixed with the water in ejector, and then make the heavy metal ion generation redox reaction in described anion and water, described heavy metal ion in water is reduced to atom, from water, separates out.

According to the utility model one preferred embodiment, described ejector is tubular body, the internal diameter of described tubular body is the large distribution in middle little two in the axial direction, the two open ends of described tubular body is respectively described flow inlet, water export, and described air intake is opened in the less centre position of internal diameter of described tubular body.

According to the utility model one preferred embodiment, described water treatment facilities also comprises exciting bank and container, described container is provided with water inlet and delivery port, described exciting bank encourages the water of storing in described container, makes the water clusters in described water be split at least two water clusters or hydrone.

According to the utility model one preferred embodiment, described exciting bank is generating far infrared rays.

According to the utility model one preferred embodiment, the wavelength of described far infrared is 8 to 14 microns.

According to the utility model one preferred embodiment, in the water clusters that each described water clusters splits off, hydrone quantity is all no more than two.

According to the utility model one preferred embodiment, the upper opening of described container.

According to the utility model one preferred embodiment, the upper transparent of described container, can see through far infrared.

With respect to prior art, the water treatment facilities that the utility model provides, processes water by ion generator, ejector, vortex settling device, suspension filter device and dechlorination device etc. are multiple, can obtain the drinking water of health, safety.

Brief description of the drawings

In order to be illustrated more clearly in the technical scheme in the utility model embodiment, below the accompanying drawing of required use during embodiment is described is briefly described, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skill in the art, do not paying under the prerequisite of creative work, can also obtain according to these accompanying drawings other accompanying drawing.

Fig. 1 is the structural representation of a part of device of the utility model water treatment facilities the first embodiment;

Fig. 2 is the method for making Nano schematic diagram of the water of the utility model the first embodiment;

Fig. 3 is the schematic flow sheet of the method for the nanometer of the water of the utility model the first embodiment;

Fig. 4 is the structural representation of the water treatment facilities for removal heavy metal of the utility model the first embodiment;

Fig. 5 is the structural representation of the water treatment facilities for de-sludging of the utility model the first embodiment;

Fig. 6 is the cross-sectional structure schematic diagram of the water treatment facilities two halves annular magnet for de-sludging of the utility model the first embodiment; And

Fig. 7 is the structural representation of water treatment facilities another part device in Fig. 1 embodiment.

Detailed description of the invention

Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is clearly and completely described, obviously, described embodiment is only a part of embodiment of the present utility model, instead of whole embodiment. Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtaining under creative work prerequisite, all belong to the scope of the utility model protection.

Refer to Fig. 1, Fig. 1 is the structural representation of a part of device of the utility model water treatment facilities the first embodiment, as shown in Figure 1, the water treatment facilities 10 of the nanometer for water of the present embodiment comprises container 11, water inlet 12, delivery port 13 and exciting bank 14, and arrow represents the flow direction of water. Container 11 is for storing pending water, and exciting bank 14 encourages the water of storage in container 11, makes the water clusters in water be split at least two water clusters or hydrone.

In the utility model embodiment, water flows to from water inlet 12, after container 11 is processed, flows out from delivery port 13. Water in container 11 is made up of many large water clusters. Large water clusters is to be formed by Hydrogenbond by many single hydrones, and the energy of hydrogen bond is not high, can produce resonance with far infrared. Exciting bank 14 is far infrared generating means, is the far infrared of 8 to 14 microns for generation of wavelength. The top of container 11 can be opening, can be also transparent, to facilitate far-infrared engergy to be irradiated in pending water. Far-infrared radiation is in container 11, and the hydrogen bond between far infrared and hydrone produces resonance, and then interrupts the hydrogen bond between hydrone. As shown in Figure 2,2 hydrones form water clusters by Hydrogenbond, while producing resonance when far-infrared radiation and with this hydrogen bond, between 2 hydrones, the hydrogen bond of combination ruptures under the effect of resonance, makes these 2 molecular water clusters of moisture split into 2 single hydrones. Herein, 2 hydrones can be also water clusters, and both form large water clusters by Hydrogenbond, and the far infrared of this large water clusters and irradiation produces resonance, and hydrogen bond rupture, is split at least two water clusters or hydrone. So, under the Persistent Excitation of far infrared, in water, a large water clusters constantly splits into the water clusters of little, further splits into the even single hydrone of less water clusters. In the water clusters that final each water clusters splits off, hydrone quantity is no more than the water clusters ratio of two and reaches requirement, thereby forms the water of nanometer, and the water clusters splitting off can be sprayed directly on plant surface, is easy to be absorbed by plant; Certainly, also can be sprayed in soil, entered the root of plant by soil.

Refer to Fig. 3, Fig. 3 is the method flow schematic diagram of the nanometer of the water of the utility model the first embodiment. As shown in Figure 3, the method comprises:

S10: the water being stored in container 11 is encouraged.

Pending current are through container 11, and encourage in container 11. First produce wavelength and be the far infrared of 8 to 14 microns, such as 9,10,11,12 or 13 microns, recycling far infrared encourages the water being stored in container 11. The top of container 11 can be opening, can be also transparent, to facilitate far-infrared engergy to be irradiated in pending water. Before far-infrared radiation, pending water is made up of many large water clusters. Large water clusters is to be formed by Hydrogenbond by many single hydrones. The energy of hydrogen bond is not high, can produce resonance with far infrared.

S11: the water clusters in water is split at least two water clusters or hydrone.

In S11, under the excitation of far infrared, hydrogen bond in hydrone constantly ruptures under the effect of resonance, hydrone is split at least two water clusters or hydrone, in the water clusters that final each water clusters splits off, hydrone quantity is all no more than two, and then forms the water of nanometer, the water clusters splitting off is sprayed directly on plant surface, is easy to be absorbed by plant.

Refer to Fig. 4, Fig. 4 is the structural representation of the water treatment facilities for removal heavy metal of the utility model the first embodiment. As shown in Figure 4, the water treatment facilities 20 for removal heavy metal of the present embodiment comprises: ejector 21, ion generator 22 and pipeline, wherein, ejector 21 is docked with in pipeline, has air intake 23, the flow inlet 24 of the pipeline of plugging into, the water export 25 of input anion air. The direction of arrow represents the flow direction of current. Ion generator 22 connects the air intake 23 of ejector 21, for generation of anion. Anion is sucked into ejector 21 from air intake 23 under the effect of ejector 21, so that anion is fully mixed with the water in ejector 21, and then make the heavy metal ion generation redox reaction in anion and water, described heavy metal ion in water is reduced to atom, from water, separate out, and along with current are discharged. So, this water treatment facilities 20 can greatly reduce the heavy metal ion content in water, and water is carried out disinfection, and purifies.

In the utility model embodiment, ejector 21 is tubular body, the internal diameter of tubular body is the large distribution in middle little two in the axial direction, and the two open ends of tubular body is respectively flow inlet 24, water export 25, and air intake 23 is opened in the less centre position of internal diameter of tubular body. In other embodiment of the present utility model, ejector 21 also can be by other structure, as long as can make anion fully mix with water.

Refer to Fig. 5, Fig. 5 is the structural representation of the water treatment facilities for de-sludging of the utility model the first embodiment. As shown in Figure 5, the water treatment facilities 30 for de-sludging of the present embodiment comprises: iron pipe 303 and two are respectively the first magnet 301 and the second magnet 302 that semi-circular arranges, the first magnet 301 wraps respectively with the second magnet 302 the relative both sides that are attached to iron pipe 303, the first magnet 301 and the second magnet 302 are arranged in and on the axis direction of iron pipe 303, produce enough large rate of change of magnetic so that along the ion in the mobile water of the axis direction of iron pipe 303 be accelerated into iron pipe wall on the di-iron trioxide effect generation tri-iron tetroxide that produces. The cross section of the first magnet 301 and the second magnet 302 as shown in Figure 6, the first magnet 301 and the constant magnetic field of the each self-forming of the second magnet 302, the magnetic field intensity in magnetic field equates, is all B. The magnetic line of force of these two semiorbicular the first magnet 301 and the second magnet 302 is all closed, and does not mutually intersect, and taking border AA ' and border CC ' as boundary, within two borders, has magnetic field, outside two borders, there is no magnetic field.

The power F that charged particle produces in variation magnetic field meets following relational expression:

F∝ΔB/Δt,

It is the rate of change that power F is proportional to magnetic field. The first magnet 301 and the constant magnetic field of the each self-forming of the second magnet 302, two magnetic fields are high-strength magnetic field, size is all B. Locate magnetic field at border AA ' and grow out of nothing, the rate of change Δ B/ Δ t in magnetic field is very large, and therefore power F is larger. On the tube wall of iron pipe 303, be attached with the di-iron trioxide of generation, produce tri-iron tetroxide with the ionization in water. Electromagnetic field strengthens hydrone and composition of scale molecular activity, and original old dirt on the tube wall of iron pipe 303, comes off under the effect of the tri-iron tetroxide on the tube wall of active water molecule and iron pipe 303 and electromagnetic field dipole-dipole force F, subsequently along with current are discharged. More stable under tri-iron tetroxide normal temperature, after old dirt is removed, tri-iron tetroxide is formed for the diaphragm of avoiding incrustation scale to adhere at the tube wall of iron pipe 303, make no longer fouling of tube wall, can forever keep pipeline unimpeded. In the utility model embodiment, carrying the pipeline of water can be all iron pipe, also can be just being wrapped attached part by the first magnet 301 and the second magnet 302 is iron pipe 303, and the pipeline that the pipeline that is arranged at iron pipe 303 both sides is all the other materials, as plastic conduit, its effect of removing incrustation scale is the same.

Please continue to refer to Fig. 1, water treatment facilities comprises previously described for the water treatment facilities 20 of removal heavy metal, for the water treatment facilities 10 of the nanometer of water and for the water treatment facilities 30 of de-sludging. Current are flowed through successively for the water treatment facilities 20 of removal heavy metal, for the water treatment facilities 30 of de-sludging and for the water treatment facilities 10 of the nanometer of water, to reach the effect of better water treatment. Certainly, in other embodiment of the present utility model, these three kinds of water treatment facilities also can be linked in sequence by other, or only have one or both water treatment facilities compositions.

Refer to Fig. 7, Fig. 7 is the structural representation of water treatment facilities another part device in Fig. 1 embodiment, current are at the water treatment facilities 20 through removal heavy metal, for being connected with the water inlet I of this partial devices again after the water treatment facilities 10 of the nanometer of water and the water treatment facilities 30 for de-sludging, this partial devices comprises: water inlet I, vortex settling device 200, suspension filter device 300, dechlorination device 400, microelement adding device 500, pH value regulator 600, bactericidal device 700, metasilicic acid adding set 800, hydrone nanometer processor 900, drain outlet S and delivery port O.

Particularly, this vortex settling device 200 comprises tubular shell (not indicating in figure) and is arranged on the vortex generator of housing inner bottom part, this vortex generator comprises driver element and rotating vane, wherein, this driver element can be direct current generator or servomotor, rotating vane can be wind wheel blade, be specially the wind wheel blade of driven by motor rotation, produce whirlpool in tubular shell bottom, solid granular impurity heavier in water is assembled to bottom to center in the shape of a spiral simultaneously under the effect of whirlpool, accumulation of impurities flows into the blow-off line S that is positioned at water treatment facilities bottom afterwards to bottom, and then discharge from sewage draining exit D. water after whirlpool settler 200 filters can flow in suspension filter device 300 by connecting water pipe 203.

In addition, this vortex settling device 200 can also comprise control module, this control module for the rotating speed of the driver element of controlled vortex flow generator, the parameter such as turn to, within the scope of those skilled in the art's understanding, repeat no more herein.

Preferably, for preventing that vortex generator from, because the invasion of particulate contamination is damaged, can arrange protection network in the periphery of vortex generator, the mesh density of protection network is very little, can filter out most particulate contamination in water.

This suspension filter device 300 is communicated with from housing top with vortex settling device 200 by water flow passage 203, because 200, vortex settling device is removed particulate contamination heavier in water, suspended impurity lighter in water is removed by this suspension filter device 300. Remove principle and process as follows: water flows in suspension filter device 300 via water flow passage 203 from vortex settling device 200, suspended impurity can be positioned at water surface top, when suspension filter device 300 pours after certain water gaging, close water flow passage 203, open simultaneously and be positioned at the water pipe 304 that its bottom is connected with dechlorination device 400, move the water to flow in dechlorination device 400. Simultaneously, the outside of suspension filter device 300 can also be provided with liquid level charactron (not shown), for the level condition of observing suspension filter device 300 inside, after arriving certain position, the water yield of liquid level charactron instruction closes water pipe 304, now interior remaining suspended impurity and the small part water of being of suspension filter device 300, at this moment, open the water pipe that is positioned at suspension filter device 300 bottoms, suspended impurity and remaining small part water are flowed into drain outlet S, and then discharge from sewage draining exit D.

This process that circulates successively, water is constantly full of, discharges in suspension filter device 300, to reach the object of removing suspended impurity in water.

In addition, the inwall of suspension filter device 300 can also be provided with accurate dechlorination pottery, for water chlorine is tentatively removed, this precision dechlorination pottery can be sticked in the inner wall surface of filter 300, or be mesh-like and be located at the inside cavity of suspension filter device 300, but will be as the criterion not affect removal suspended impurity. The form that arranges about dechlorination pottery in suspension filter device 300, within the scope of those skilled in the art's understanding, will not enumerate herein.

Wherein, dechlorination pottery can be the one of living in porcelain. The porcelain of living is burnt till by 20 several kinds of mineral elements, oxidized metal and ceramic raw material allotment. It has following effect: 1. dechlorination: can be by the chlorine fast decoupled in water, vibration volatilization; 2. deodorizing: activated water diminishes hydrone, peculiar smell removal and absorption in decomposition water; 3. toxin expelling: long-term drinking can be decomposed heavy metal, body fat, the blood fat in residual body, discharges through metabolism; 4. antibacterial: to decompose unicellular germ and other bacteriums because of vibration, it cannot be bred. In addition, the far infrared function that the porcelain of living discharges can become micromolecular water by large hydrone, improves the absorption of human body to water, strengthens immunity. The porcelain of living can not only allow wine and various beverage moment become delicious, also allows more of a specified duration that food preserves, the cell in more can activating human body. Also can get rid of toxin and heavy metal in body, stimulate circulation, help metabolism, skin maintenance, make people be difficult for aging, improve allergic skin, reduce hypertension, eliminate the fatigue of aching. Certainly, the porcelain of living does not form the ceramic restriction that dechlorinates in the present embodiment, and other accurate dechlorination potteries also can be used in the embodiment of the present application, for example, and Tourmaline pottery etc.

This dechlorination device 400 comprises housing, is located at removing chlorine generator (not shown) and being positioned at the exhaust outlet 410 on housing top of enclosure interior. Certainly, in the present embodiment, the shell shape of each device is not limited to cylindric shown in figure, can be cube-shaped, ellipsoid shape etc., and the shape of each crust of the device does not form the restriction to the present embodiment water treatment facilities.

Wherein, should can be pulse gas supplying machine except chlorine generator, by the bottom from dechlorination device 400 to the interior air pulse that constantly pours of dechlorination device 400, make the water in dechlorination device 400 continue rolling, and then chlorine is separated from water, along with the gas pouring is discharged from the exhaust outlet 410 that is positioned at dechlorination device 400 housing tops together.

In addition, should can be also pulse aerating machine except chlorine generator, oxygen constantly pours from the bottom of dechlorination device 400, on the one hand with to pour air similar, due to gas injection, water in dechlorination device 400 can continue rolling, and then chlorine is separated from water, along with gas injection is discharged from the exhaust outlet 410 that is positioned at dechlorination device 400 housing tops together. On the other hand, the oxygen pouring can with chlorine generation chemical reaction in water, play the effect of the chlorine in further removal water.

Preferably, for preventing that airborne pollutant from entering in this dechlorination device 400, exhaust ports on dechlorination device 400 tops of the present embodiment water treatment facilities is also provided with gas purification units 420, this gas purification units 420 can filter and absorb from the chlorine of dechlorination device 400 interior discharges on the one hand, prevents from that chlorine is discharged in outside air, to cause secondary pollution. On the other hand, also can purify the gas that enters into dechlorination device 400 inside from outside air, prevent that outside air from polluting the water in dechlorination device 400.

Wherein, air cleaning member 420 can be air purifier of the prior art or air purification box etc. Air cleaning member 420 can comprise a variety of according to the difference of technology and medium. For example, conventional air purifying process has: adsorption technology, negative (just) ion technology, catalysis technique, photocatalyst technology, superstructure light mineralising technology, HEPA high efficiency filter technology, electrostatic precipitation technology etc.; And conventional scavenging material technology mainly contains: photocatalyst, active carbon, utmost point charcoal heart filter core technology, synthetic fibers, the efficient material of HEAP, anion generator etc. Preferably, the air cleaning member 420 in the present embodiment adopts compound material and technology, has adopted multiple purification techniques and material medium simultaneously. Within the scope of those skilled in the art's understanding, also no longer describe in detail herein.

Microelement adding device 500 comprises between the first adding tube 510 and the second adding tube 520, the first adding tubes and the second adding tube and connecting by the tube connector 505 that is positioned at top. The first adding tube 510 and the second adding tube 520 inside are respectively equipped with micro-adding device 530, this trace element adding device 530 can be medical stone, and medical stone is a kind of to biological nontoxic, harmless and have certain bioactive complex mineral or a medicinal rock. The main chemical compositions of medical stone is inorganic alumino-silicate. Comprising SiO2, Al2O3, Fe2O3, FeO, MgO, CaO, K2O, Na2O, TiO2, P2O5, MnO etc., also contain the required whole macroelements of animal, as: trace element and the rare earth elements such as K, Na, Ca, Mg, Cu, Mo, approximately 58 kinds more than.

Medical stone has following characteristics: (1) absorption affinity is strong; So-called absorption is the whole solvations of solid with porous, huge surface area, and reaction chemistry, physics occurs. Medical stone, is particularly drawn out the pus to skin disease as Chinese medicine, and effect is fine. Medical stone is porous, and adsorption capacity is very strong, because its main component is silica, aluminium oxide. Putting to consider from this, is that appearance is intelligible. In the electron micrograph of medical stone attritive powder, be spongy porous, this is its maximum reason with good adsorptivity. That is to say, because of porous, surface is just very large so, due to the weathering of feldspar part, becomes kaolin shape etc., therefore remain very strong suction-operated and exchange interaction.

Certainly, in the application, be mainly to utilize in medical stone to be rich in abundant mineral matter, play the effect to trace element adds in water. In addition, medical stone also has well water purification effect, Xiang Shuizhong add micro-in, can also further purify water. Medical stone is a kind of neutral alkali half igneous rock, close to volcanic rock. The natural mineral matter comprising in medical stone is easy to discharge in apertures countless from medical stone and discharges oxygen. By absorbing bleaching powder, chlorine and other noxious material, to reach the object of purifying waste water. The mineral matters such as the calcium that gives out in medical stone, iron, sodium can be improved drinking water.

In the present embodiment, trace element adding device 530 is located at respectively the inside of the first adding tube 510 and the second adding tube 520, it arranges form and is preferably bulk and is suspended at the first adding tube 510 and the second adding tube 520 inside cavity, because micro-adding device 530 has porous, both ensured that water can pass through the first adding tube 510 and the second adding tube 520, increased again the contact area of micro-adding device 530 and water.

In addition, in the microelement adding device 500 in the present embodiment, be preferably by the mode of current: pulsed is passed through. control the open and close of the water pipe 405 between dechlorination device 400 and microelement adding device 500, make mode sectional the flow through microelement adding device 500 of current with pulse, or at the interior by-pass valve control (not shown) that arranges of water pipe 405, by regulate the opening time of this by-pass valve control to control the water yield entering in microelement adding device 500 at every turn, like this at each current the flow velocity by microelement adding device 500 identical, the micro-amount of adding in the water of microelement adding device 500 of can ensureing at every turn to flow through is identical, be immersed in water and compare compared to microelement adding device of the prior art, can make in water micro-addition more even, also can extend the life-span of micro-adding device 530 simultaneously.

In addition, can also be provided with magnetic field generator 540 microelement adding device 500 is interior, for the harmful heavy metal ion of Adsorption water, about magnetic field generator 540 concrete structure and operation principle, within the scope of those skilled in the art's understanding, repeat no more herein.

PH value regulator 600 is located at the top of adjustable pipe 666, in the present embodiment, pH value regulator 600 adopts the mode of brine electrolysis to regulate the acid-base value of water, and its structure comprises electrolysis construction unit (not indicating in figure), sour water delivery pipe 610 and sour water collecting box 620. Particularly, this electrolysis construction unit comprises that positive and negative electrode and two accommodate respectively the electrolytic cell of this positive electrode and negative electrode, the different ion producing in different electrolytic cells due to two electrodes, and then obtain two kinds of different liquid of Acidity of Aikalinity, wherein, acidic liquid enters sour water collecting box 620 via sour water delivery pipe 610, and akaline liquid is retained in water, because weak base water is helpful to human body, so regulate its essence for making water present alkalescent to the acid-base value of water. Wherein, sour water collecting box 620 can be connected to drain outlet S (not shown) equally, so that the acidic liquid of generation is drained from drain outlet S. Sour water collecting box 620 preferably adopts transparent material to make, and can conveniently observe the amount of the interior collection acidic liquid of sour water collecting box 620.

Preferably, this positive electrode and negative electrode adopt plating ruthenium titanium material. Number of electrodes in each electrolytic cell can be multiple. PH value regulator 600 also comprises control circuit, and control circuit is used to positive electrode and negative electrode that stabling current is provided.

Bactericidal device 700 can be close to pH value regulator 600, is arranged at equally the top of adjustable pipe 666. Bactericidal device 700 in the present embodiment preferably adopts the structural principle of electrion, concrete structure can comprise the sparking electrode and the high-voltage generator that stretch into water pipe inside, this high-voltage generator can utilize the direct current of low-voltage DC voltage-stabilizing power supply output to become high-tension electricity after conversion, and then is connected on sparking electrode. Sparking electrode is preferably two boards shape sheet material and is oppositely arranged, and between two boards shape sheet material, produces powerful current field. The material of sparking electrode is that the material of the good conductivity such as copper, aluminium, stainless steel and titanium alloy is made. Can also utilize one section of water pipe sparking electrode the most insulating with other part water pipes, to the logical high-tension electricity of this section of water pipe, to the sterilization of discharging through the current of this water pipe. It should be noted that the insulated working that will carry out this section of water pipe and other part water pipes, so as not to other part water pipes charged, hurt sb.'s feelings. Certainly, the quantity of sparking electrode can be multiple, and shape can be also bar-shaped etc. irregularly shaped, distributes and is arranged on the diverse location in water pipe, will not enumerate herein.

Similarly, bactericidal device 700 also will comprise the high-tension electricity regulating circuit being connected with sparking electrode and high-voltage generator, to guarantee the sterilization of can discharging safely, smoothly of this bactericidal device 700.

The degerming method of the high electric current of high pressure adopting in the present embodiment is to utilize electric physical characteristic to kill the bacterium in water, can not exert an influence to the chemical property of water, also can not introduce any pollution.

800 of metasilicic acid adding sets mainly comprise heater 810 and metasilicic acid adder 820. Metasilicic acid adder 820 is connected with water pipe 708 by conduit. In the present embodiment, it is box-like that metasilicic acid adder 820 is circle, and adopt the magnetic conductions such as metal, heat-resisting material to make, to this metasilicic acid adder 820 is heated by magnetic induction way. Heater 810 can be electric heater or electromagnetic heater, and form and kind to heater 810 do not limit. Heater 810 removably connects with metasilicic acid adder 820, to change metasilicic acid adder 820 or to the interior interpolation metasilicic acid of metasilicic acid adder 820.

In addition, the version of metasilicic acid adding set 800 is not limited to a heater 810 shown in figure and coordinates a metasilicic acid adder 820 to use, and can be also that a heater 810 coordinates multiple metasilicic acid adders 820 to use. Metasilicic acid adding set 800 can also dispose control cabinet, is provided with circuit and processor in control cabinet, for heated condition and the heating-up temperature etc. of control heater. Preferably, be also provided with temperature sensor (not shown) on heater 810, temperature sensor is for monitoring the heating-up temperature of heater 810.

Metasilicic acid is a kind of weak diacid, ionization equilibrium constant K1=2 × 10-10 (room temperature). Be insoluble to hydrochloric acid, sulfuric acid, be dissolved in hydrofluoric acid. Be dissolved in potassium hydroxide or sodium hydroxide solution, generate potassium silicate K2SiO3 or sodium metasilicate Na2SiO3 and water. Its fusing point is 150 DEG C, while being heated to 150 DEG C, decomposes. Heater 810 is located at metasilicic acid adder 820 bottoms metasilicic acid adder 820 is heated, and the metasilicic acid in metasilicic acid adder 820 is decomposed, and then enter into water pipe 708 by conduit, reaches the object of Xiang Shuizhong interpolation metasilicic acid.

Metasilicic acid is easily absorbed by the body, and can effectively maintain electrolyte balance and the physiological function of human body, has the blood vessel elasticity of recovery, increases skin elasticity, promotes the effects such as skeleton development.

Hydrone nanometer processor 900 carrys out by applying high pressure the charged water purification particle that Separation of Water molecule produces, to reach the object that hydrone is more easily absorbed.

Drain outlet S is located at the bottom of whole water treatment facilities, be connected with the bottom of vortex settling device 200, suspension filter device 300, dechlorination device 400, microelement adding device 500 and adjustable pipe 666 respectively, for emitting the separation refuse producing in each device.

Below the complete workflow of this water treatment facilities is described.

Water to be clean enters into vortex settling device 200 from water inlet I, vortex generator in vortex settling device 200 produces whirlpool, solid granular impurity heavier in water is assembled to bottom to center in the shape of a spiral simultaneously under the effect of whirlpool, accumulation of impurities flows into the blow-off line S that is positioned at water treatment facilities bottom afterwards to bottom, and then discharges from sewage draining exit D. Water after whirlpool settler 200 filters can flow in suspension filter device 300 by connecting water pipe 203.

Water flows in suspension filter device 300 via water flow passage 203 from vortex settling device 200, suspended impurity can be positioned at water surface top, when suspension filter device 300 pours after certain water gaging, close water flow passage 203, open simultaneously and be positioned at the water pipe 304 that its bottom is connected with dechlorination device 400, move the water to flow in dechlorination device 400, the outside of suspension filter device 300 can also be provided with liquid level charactron (not shown), for the level condition of observing suspension filter device 300 inside, after arriving certain position, the water yield of liquid level charactron instruction closes water pipe 304, now interior remaining suspended impurity and the small part water of being of suspension filter device 300, at this moment, open the water pipe that is positioned at suspension filter device 300 bottoms, suspended impurity and remaining small part water are flowed into drain outlet S, and then discharge from sewage draining exit D.

Water enters dechlorination device 400 through water pipe 304, dechlorination device 400 interior settings except chlorine generator from the bottom of dechlorination device 400 to the interior air pulse that constantly pours of dechlorination device 400, make the water in dechlorination device 400 continue rolling, and then chlorine is separated from water, along with gas injection is discharged from the exhaust outlet 410 that is positioned at dechlorination device 400 housing tops together, on the other hand, the oxygen pouring can with chlorine generation chemical reaction in water, play the effect of the chlorine in further removal water. Meanwhile, for preventing that airborne pollutant from entering in this dechlorination device 400 and preventing that chlorine is discharged into outside air and causes secondary pollution, is also provided with gas purification units 420 in the exhaust ports on dechlorination device 400 tops.

Current continue from water pipe 405, with the mode of pulse flow through successively the first adding tube 510 and second adding tube 520 of microelement adding device 500, current to be added micro-by the micro-adding device 530 (being preferably medical stone) in the first adding tube 510 and the second adding tube 520. Meanwhile, the magnetic field generator 540 of microelement adding device 500 interior settings carries out absorption type removal to the harmful heavy metal ion in current.

Current flow into adjustable pipe 666 from the second adding tube 520 through water pipe 506, and the top of adjustable pipe 666 is provided with pH value regulator 600. PH value regulator 600 carries out acid-base value adjusting by the mode of brine electrolysis to current. Bactericidal device 700 is located at adjustable pipe 666 outsides equally, and bactericidal device 700 carries out degree of depth sterilization processing by the form of the high current discharge of high pressure to current.

Current enter water pipe 708, and water pipe 708 is connected with metasilicic acid adding set 800 and hydrone nanometer processor 900 in turn. Metasilicic acid adding set 800 heats metasilicic acid adder 820 so that the current in water pipe 708 are added to metasilicic acid by heater 810. Finally by crossing hydrone nanometer processor 900, current are carried out to nanometer processing, the healthy drinking water obtaining is discharged from delivery port O, and whole water treatment procedure finishes.

Wherein, the bottom of the water treatment facilities of the present embodiment is communicated with drain outlet S respectively, to discharge at any time the separation refuse of the process generation of purifying waste water at each device.

The water treatment facilities of Part II, undertaken doing degree of depth degerming, metasilicic acid adding set 800 in water add metasilicic acid and hydrone nanometer processor 900 to water carry out nanometer processing compared with light impurity, dechlorination device 400 except micronutrient levels, pH value regulator 600 in residual chlorine, microelement adding device 500 supplementing water in anhydrating obtain meta-alkalescence healthy water, bactericidal device 700 compared with heavy seeds processing, 300 separation place of suspension filter device by vortex settling device 200 successively, finally obtain clean, healthy drinking water. Compared to prior art, this water treatment facilities, by special purifier structure (vortex settling device 200 and suspension filter device 300), can not need often to change and clean filter core, simple to operate; There will not be the impurity retaining at the filter core place meeting breed bacteria producing not in time because of filter element replacing, and then pollute the problem of water to be clean; Thoroughly remove in water chlorine and utilize bactericidal device 700 degree of depth to remove bacterium in water by dechlorination device 400, even if treated water is directly drunk, also can people not produce any harm; Also utilize in addition microelement adding device 500, pH value regulator 600, metasilicic acid adding set 800 and hydrone nanometer processor 900 further to optimize water quality, obtain not only clean but also healthy drinking water.

The foregoing is only part embodiment of the present utility model; not thereby limit protection domain of the present utility model; every equivalent device or conversion of equivalent flow process that utilizes the utility model description and accompanying drawing content to do; or be directly or indirectly used in other relevant technical fields, be all in like manner included in scope of patent protection of the present utility model.

Claims (8)

1. a water treatment facilities, it is characterized in that, comprise: pipeline, ion generator, ejector, vortex settling device, suspension filter device and dechlorination device, described vortex settling device further comprises tubular shell and is arranged on the vortex generator of described tubular shell inner bottom part; Described vortex generator further comprises the wind wheel blade of motor and driven by motor rotation, and described vortex generator produces whirlpool in tubular shell bottom, and solid granular impurity heavier in water is assembled to place of bottom centre in the shape of a spiral under the effect of whirlpool; Described ejector is docked with in described pipeline, has air intake, the flow inlet of the pipeline of plugging into, the water export of input anion air; Current pass through described ejector, described vortex settling device, suspension filter device and dechlorination device successively; Described ion generator connects the air intake of described ejector, for generation of anion, described anion is sucked into described ejector from described air intake under the effect of ejector, so that described anion is fully mixed with the water in ejector, and then make the heavy metal ion generation redox reaction in described anion and water, described heavy metal ion in water is reduced to atom, from water, separates out.

2. water treatment facilities according to claim 1, it is characterized in that, described ejector is tubular body, the internal diameter of described tubular body is the large distribution in middle little two in the axial direction, the two open ends of described tubular body is respectively described flow inlet, water export, and described air intake is opened in the less centre position of internal diameter of described tubular body.

3. water treatment facilities according to claim 1, it is characterized in that, described water treatment facilities also comprises exciting bank and container, described container is provided with water inlet and delivery port, described exciting bank encourages the water of storing in described container, makes the water clusters in described water be split at least two water clusters or hydrone.

4. water treatment facilities according to claim 3, is characterized in that, described exciting bank is generating far infrared rays.

5. water treatment facilities according to claim 4, is characterized in that, the wavelength of described far infrared is 8 to 14 microns.

6. water treatment facilities according to claim 3, is characterized in that, in the water clusters that each described water clusters splits off, hydrone quantity is all no more than two.

7. water treatment facilities according to claim 3, is characterized in that, the upper opening of described container.

8. water treatment facilities according to claim 3, is characterized in that, the upper transparent of described container can see through far infrared.