WO2016095227A1 - 一种水处理系统 - Google Patents

一种水处理系统 Download PDF

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Publication number
WO2016095227A1
WO2016095227A1 PCT/CN2014/094440 CN2014094440W WO2016095227A1 WO 2016095227 A1 WO2016095227 A1 WO 2016095227A1 CN 2014094440 W CN2014094440 W CN 2014094440W WO 2016095227 A1 WO2016095227 A1 WO 2016095227A1
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Prior art keywords
water
water treatment
treatment system
addition
trace element
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PCT/CN2014/094440
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English (en)
French (fr)
Inventor
孙福军
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深圳市同盛绿色科技有限公司
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Priority to PCT/CN2014/094440 priority Critical patent/WO2016095227A1/zh
Publication of WO2016095227A1 publication Critical patent/WO2016095227A1/zh

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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water

Definitions

  • the present invention relates to the technical field of water treatment, and in particular to a water treatment system.
  • the prior art water purification method generally only performs simple filtration and disinfection of water, and cannot adjust the pH of the water, the trace element content in the water (especially the beneficial substances such as metasilicate), and thereby obtain drinking water for human health;
  • the prior art water purification method cannot remove harmful substances such as bacteria that cannot be killed by chlorine in water.
  • the present invention provides a water treatment system to solve the technical problems in the prior art that a deep sterilizing and mineral-rich healthy drinking water cannot be obtained.
  • the present invention provides a water treatment system including a micro-element addition device, a pH adjustment device, and a sterilization device sequentially connected, wherein the trace element addition device includes a first addition a tube, a second addition tube, and a trace element addition unit disposed in the first and second addition tubes, wherein the trace element addition unit is medical stone.
  • the water treatment system further comprises a metasilicate addition device in communication with the sterilization device.
  • the water treatment system further comprises a water molecule nanotechnology processor in communication with the metasilicate addition device.
  • the pH adjusting device comprises an electrolytic structural unit, an acid water discharge pipe, and an acid water collecting tank.
  • the electrolytic structural unit comprises positive and negative electrodes and two electrolytic cells respectively accommodating the positive electrode and the negative electrode, and the two electrodes generate different ions in different electrolytic cells, and further Two liquids having different acidity and alkalinity are obtained, wherein the acidic liquid is discharged into the acid water collecting tank through the acid water discharge pipe, and the alkaline liquid remains in the water.
  • the sterilization device is disposed adjacent to the pH adjusting device, and the sterilization device includes a discharge electrode extending into a water pipe and a high voltage electric generator, and the high voltage electric generator utilizes a low voltage
  • the DC power output from the DC stabilized power supply is converted into high voltage power and then connected to the discharge electrode.
  • the metasilicate addition device includes a heater and a metasilicate additive, and the metasilicate additive is connected to a water treatment pipe through a conduit, and the heater is disposed on the silicon
  • the meta-acid adder is heated at the bottom of the acid adder to decompose the meta-silicic acid in the meta-silicate adder, and then enters the water treatment pipe through the conduit to add meta-silicic acid to the water.
  • the heater is an electric heater.
  • the trace element adding device further includes a magnetic field generator disposed inside the cavity of the trace element adding device, and the magnetic field generator is configured to adsorb and remove harmful heavy metal ions in the water.
  • the water treatment system further includes a sewage passage communicating with the water treatment pipe, the sewage passage for discharging the separated waste generated in the water treatment pipe.
  • the water treatment system provided by the embodiment of the invention sequentially supplements the trace element content in the water by the trace element adding device, obtains the alkaline health water by the pH adjustment device, performs deep sterilization by the sterilization device, and adds silicon to the water by the metasilicate adding device.
  • the acid and water molecule nanotechnology processor nanometerizes the water to a clean, healthy drinking water.
  • the water treatment system provided by the invention can deeply sterilize water and add substances such as silicic acid to make drinking water safer; rich in various minerals and alkaline water, More beneficial to the human body.
  • Figure 1 is a schematic illustration of the structural principle of a preferred embodiment of the water treatment system of the present invention.
  • FIG. 1 is a schematic view showing the structure of a preferred embodiment of the water treatment system of the present invention.
  • the water treatment system of the embodiment of the present invention includes a water inlet I, a vortex sedimentation device 200, a suspension filtration device 300, a chlorine removal device 400, a trace element addition device 500, a pH adjustment device 600, a sterilization device 700, The metasilicate addition device 800, the water molecule nanotechnology processor 900, the sewage channel S, and the water outlet O.
  • the vortex precipitating device 200 includes a cylindrical casing (not shown) and a vortex generator disposed at the bottom of the casing, the vortex generator including a driving unit and a rotating blade, wherein the driving unit may be a direct current
  • the rotating blade may be a rotor blade, specifically a rotor blade driven by a motor
  • a vortex is generated at the bottom of the cylindrical casing, and the heavier solid particulate impurities in the water spiral toward the center under the action of the vortex.
  • it gathers toward the bottom, and the impurities gather at the bottom and then flow into the sewage pipe S located at the bottom of the water treatment system, and are discharged from the sewage outlet D.
  • the water filtered by the vortex sedimentation device 200 flows into the suspension filtration device 300 through the connection water pipe 203.
  • the eddy current precipitating device 200 may further include a control unit for controlling the rotational speed, steering, and the like of the driving unit of the vortex generator, which are beyond the scope of those skilled in the art and will not be described herein.
  • a protective net may be disposed on the outer circumference of the vortex generator, and the mesh density of the protective net is small, and most of the particulate impurities in the water may be filtered out.
  • the suspension filter device 300 communicates with the vortex precipitator 200 from the upper portion of the casing through the water flow passage 203. Since the vortex sedimentation device 200 removes only the heavier particulate impurities in the water, the lighter suspended impurities in the water pass through the suspension filter. Device 300 performs the removal.
  • the removal principle and process are as follows: water flows from the vortex precipitation device 200 into the suspension filtration device 300 via the water flow channel 203, and the suspended impurities are located on the upper surface of the water. When the suspension filtration device 300 flushes a certain amount of water, the water flow channel 203 is closed and the opening is located at the same time.
  • the water pipe 304 connected to the chlorine removal device 400 at the bottom thereof allows water to flow into the chlorine removal device 400.
  • the outside of the suspension filter device 300 may further be provided with a liquid level display tube (not shown) for observing the liquid level inside the suspension filter device 300, and closing the water pipe when the water amount indicated by the liquid level display tube reaches a certain position. 304, at this time, the remaining in the suspension filtering device 300 is suspended impurities and a small amount of water. At this time, the water pipe located at the bottom end of the suspension filtering device 300 is opened, and the suspended impurities and the remaining small amount of water are flowed into the sewage channel S, thereby discharging the sewage. D is discharged.
  • a liquid level display tube not shown
  • the process is sequentially cycled, and the water is continuously filled and discharged in the suspension filtration device 300 to achieve the purpose of removing suspended impurities in the water.
  • the inner wall of the suspension filtering device 300 may further be provided with a precision dechlorination ceramic for preliminary removal of chlorine gas in the water.
  • the precision dechlorination ceramic may be attached to the inner wall surface of the filtering device 300 or may be suspended in a mesh shape.
  • the interior of the chamber of the filter device 300 is filtered, but is not affected by the removal of suspended impurities.
  • the arrangement of the dechlorination ceramics in the suspension filtration device 300 is within the understanding of those skilled in the art and will not be enumerated here.
  • the dechlorination ceramic can be one of the active porcelain. Porcelain is made from more than 20 kinds of mineral elements, oxidized metals and ceramic materials. It has the following effects: 1. Dechlorination: The chlorine in the water can be rapidly decomposed and oscillated and volatilized; Deodorization: Activate water quality to make water molecules smaller, decompose water odor and remove and adsorb; Detoxification: long-term drinking can decompose residual heavy metals, body fat, blood fat, and metabolism; Bacteriostatic: Decomposes single-cell pathogens and other bacteria by oscillation, making them unable to multiply.
  • the far-infrared function released by the living porcelain can turn large water molecules into small molecule water, improve the body's absorption of water and enhance immunity.
  • Living porcelain not only makes wine and various drinks instantly delicious, but also preserves food for a longer period of time, and activates cells in the human body. It can also eliminate toxins and heavy metals in the body, promote blood circulation, help metabolism, beauty and beauty, make people not easy to age, improve allergic skin, reduce high blood pressure, eliminate soreness and fatigue.
  • the living porcelain does not constitute a limitation on the chlorine removal ceramic in the present embodiment, and other precision dechlorination ceramics can also be used in the embodiments of the present application, for example, tourmaline ceramics.
  • the chlorine removal device 400 includes a casing, a chlorine removal generator (not shown) disposed inside the casing, and an exhaust port 410 at the top end of the casing.
  • a chlorine removal generator (not shown) disposed inside the casing
  • an exhaust port 410 at the top end of the casing.
  • the shape of the outer casing of each device in the present embodiment is not limited to the cylindrical shape shown in the drawing, and may be a square shape, an ellipsoid shape, or the like, and the shape of each device casing does not constitute a limitation of the water treatment system of the embodiment.
  • the chlorine removal generator may be a pulse air supply device, and the water in the chlorine removal device 400 is continuously tumbling by continuously pulsing the pulse air flow from the bottom of the chlorine removal device 400 to the chlorine removal device 400, thereby causing chlorine gas to pass from the water. It is separated and discharged together with the rushed gas from the exhaust port 410 located at the top end of the casing of the chlorine removal device 400.
  • the chlorine removal generator may also be a pulse oxygenator, and oxygen is continuously rushed from the bottom of the chlorine removal device 400.
  • the water in the chlorine removal device 400 continues to roll due to the flushing of the gas.
  • chlorine gas is separated from the water and discharged from the exhaust port 410 located at the top end of the casing of the chlorine removal device 400 along with the flushing gas.
  • the rushed oxygen reacts with chlorine in the water to further remove chlorine from the water.
  • a gas purification unit 420 is further disposed at the exhaust port of the top of the chlorine removal device 400 of the water treatment system of the present embodiment, and the gas purification unit 420 is further provided.
  • the gas purification unit 420 can filter and absorb the chlorine gas discharged from the chlorine removal device 400 to prevent the chlorine gas from being discharged into the outside air to cause secondary pollution.
  • the air purifying unit 420 may be an air purifier or an air purifying box or the like in the prior art.
  • the air purification unit 420 can include a wide variety depending on the technology and the medium.
  • commonly used air purification technologies include: adsorption technology, negative (positive) ion technology, catalytic technology, photocatalytic technology, superstructure photomineralization technology, HEPA high-efficiency filtration technology, electrostatic dust collection technology, etc.;
  • the air purification unit 420 in this embodiment employs a composite material and technology, that is, a plurality of purification technologies and material media are simultaneously employed. It will not be described in detail herein within the understanding of those skilled in the art.
  • the trace element adding device 500 includes a first addition tube 510 and a second addition tube 520, and the first addition tube and the second addition tube are connected by a connection tube 505 located at the top.
  • the first adding tube 510 and the second adding tube 520 are respectively provided with a trace element adding unit 530, and the trace element adding unit 530 may be a medical stone.
  • the medical stone is a kind of non-toxic, harmless and certain biological creature. Active composite mineral or medicinal rock.
  • the main chemical component of medical stone is inorganic aluminosilicate.
  • the medical stone has the following characteristics: (1) strong adsorption; the so-called adsorption is a complete melting of a porous, large surface area, and a chemical and physical reaction occurs.
  • Maifan Stone is very effective for skin diseases, especially pus.
  • the medical stone is porous and has a strong adsorption capacity because its main components are silica and alumina. From this point of view, it is easy to understand.
  • the electron micrograph of the medical stone fine powder is spongy porous, which is the biggest reason for its excellent adsorption. That is to say, due to the porosity, the surface is very large, and since the feldspar is partially weathered and formed into a kaolin-like shape, it always maintains a strong adsorption and exchange effect.
  • this application mainly uses the rich minerals in the medical stone to play the role of adding trace elements in water.
  • the medical stone also has a good purifying effect on water, and it can further purify the water while adding trace elements to the water.
  • Medical stone is a neutral alkali semi-ignite rock, close to volcanic rocks. The natural minerals contained in the stone are easy to release and release oxygen from numerous pores on the stone. Purify water by absorbing bleach, chlorine and other toxic substances. Minerals such as calcium, iron and sodium emitted from the stone can improve drinking water.
  • the trace element adding unit 530 is disposed inside the first adding tube 510 and the second adding tube 520, respectively, and is disposed in a block form suspended in the first adding tube 510 and the second adding tube 520. Inside the body, since the trace element addition unit 530 has porosity, it is ensured that water can pass through the first addition tube 510 and the second addition tube 520, and the contact area of the trace element addition unit 530 with water is increased.
  • the manner in which the water flow in the trace element adding device 500 in the present embodiment is passed through is preferably pulsed. That is, the opening and closing of the water pipe 405 between the chlorine removing device 400 and the trace element adding device 500 is controlled, so that the water flow flows through the trace element adding device 500 in a pulsed manner, or a control valve is arranged in the water pipe 405 (in the figure) Not shown), the amount of water entering the trace element adding device 500 is controlled by adjusting the opening time of the control valve, so that each time the flow rate of the water flowing through the trace element adding device 500 is the same, each flow can be ensured.
  • the amount of trace elements added in the water of the trace element adding device 500 is the same, and the amount of trace elements added in the water can be more uniform, and the trace element addition can be extended, compared with the immersion in water in the trace element adding device in the prior art.
  • the life of unit 530 is the same, and the amount of trace elements added in the water can be more uniform, and the trace element addition can be extended, compared with the immersion in water in the trace element adding device in the prior art.
  • a magnetic field generator 540 may be disposed in the trace element adding device 500 for adsorbing and removing harmful heavy metal ions in the water.
  • the specific structure and working principle of the magnetic field generator 540 are within the understanding of those skilled in the art. , will not repeat them here.
  • the pH adjustment device 600 is disposed at the top of the adjustment tube 666.
  • the pH adjustment device 600 adjusts the pH of the water by means of electrolyzed water
  • the structure includes an electrolytic structure unit (not shown), an acid water discharge tube 610, and Acid water collection tank 620.
  • the electrolytic structural unit includes positive and negative electrodes and two electrolytic cells respectively accommodating the positive electrode and the negative electrode, and different acid ions are obtained due to different ions generated by the two electrodes in different electrolytic cells.
  • the pH of the water is adjusted to be substantially
  • the water is weakly alkaline.
  • the acid water collection tank 620 can also be connected to the sewage passage S (not shown) to discharge the generated acidic liquid from the sewage passage S.
  • the acid water collection tank 620 is preferably made of a transparent material, and the amount of the acidic liquid collected in the acid water collection tank 620 can be easily observed.
  • the positive electrode and the negative electrode are made of rhodium-plated titanium.
  • the number of electrodes in each electrolytic cell may be plural.
  • the pH adjustment device 600 also includes a control circuit for providing a steady current to the positive and negative electrodes.
  • the sterilization device 700 can be disposed adjacent to the pH adjustment device 600, also disposed on top of the adjustment tube 666.
  • the sterilization device 700 in this embodiment preferably adopts a structural principle of high-voltage discharge, and the specific structure may include a discharge electrode extending into the inside of the water pipe and a high-voltage electric generator, and the high-voltage electric generator can be output by using a low-voltage DC stabilized power supply.
  • the DC power is converted into a high voltage power and then connected to the discharge electrode.
  • the discharge electrode is preferably two plate-like sheets and disposed opposite each other to generate a strong current field between the two sheet-like sheets.
  • the material of the discharge electrode is made of a conductive material such as copper, aluminum, stainless steel or titanium alloy.
  • the most discharge electrode that is, to pass the high voltage electricity to the water pipe, and discharge and sterilize the water flowing through the water pipe. It is necessary to pay attention to the insulation work of this section of water pipes and other parts of the water pipes, so as to avoid other parts of the water pipes from being charged and injuring people.
  • the number of discharge electrodes may be plural, and the shape may also be an irregular shape such as a rod shape, and the distribution is set at different positions in the water pipe, which will not be enumerated here.
  • the sterilization apparatus 700 also includes a high-voltage electric regulation circuit connected to the discharge electrode and the high-voltage electric generator to ensure that the sterilization apparatus 700 can perform discharge sterilization in a safe and smooth manner.
  • the high-pressure and high-current sterilization method adopted in the present embodiment utilizes the physical properties of electricity to kill bacteria in the water, does not affect the chemical properties of water, and does not introduce any pollution.
  • the metasilicate addition device 800 mainly includes a heater 810 and a metasilicate adder 820.
  • the metasilicate adder 820 is connected to the water tube 708 through a conduit.
  • the metasilicate additive 820 is in the shape of a round box and is made of a magnetic or heat-resistant material such as metal to heat the metasilicate adder 820 by magnetic induction.
  • the heater 810 may be an electric heater or an electromagnetic heater, and the form and kind of the heater 810 are not limited.
  • the heater 810 is detachably coupled to the metasilicate adder 820 to replace the metasilicate adder 820 or to add metasilicic acid to the metasilicate adder 820.
  • the configuration of the metasilicate addition device 800 is not limited to use with one heater 810 shown in the drawing in conjunction with one metasilicate adder 820, and one heater 810 may be used in combination with a plurality of metasilicate adders 820.
  • the metasilicate addition device 800 can also be provided with a control box having a circuit and a processor for controlling the heating state and heating temperature of the heater.
  • the heater 810 is further provided with a temperature sensor (not shown) for monitoring the heating temperature of the heater 810.
  • the heater 810 is disposed at the bottom of the metasilicate additive 820 to heat the metasilicate additive 820 to decompose the metasilicate in the metasilicate adder 820, and then enters the water pipe 708 through the conduit to add a bias to the water.
  • the silicic acid is easily absorbed by the human body, can effectively maintain the electrolyte balance and physiological functions of the human body, and has the functions of restoring blood vessel elasticity, increasing skin elasticity, and promoting bone development.
  • the water molecule nanotechnology processor 900 generates charged water purification particles by applying high pressure to separate water molecules to achieve the purpose of making water molecules more easily absorbed.
  • the sewage channel S is disposed at the bottom of the entire water treatment system, and is respectively connected with the vortex sedimentation device 200, the suspension filtering device 300, the chlorine removing device 400, the trace element adding device 500, and the bottom end of the regulating tube 666 for discharging the devices. Separated waste produced internally.
  • the water to be purified enters the vortex sedimentation device 200 from the water inlet I, and the vortex generator in the vortex sedimentation device 200 generates a vortex, so that the heavier solid particulate impurities in the water spiral toward the center and simultaneously toward the bottom under the action of the vortex.
  • the impurities gather at the bottom and then flow into the sewage pipe S located at the bottom of the water treatment system, and are discharged from the sewage outlet D.
  • the water filtered by the vortex sedimentation device 200 flows into the suspension filtration device 300 through the connection water pipe 203.
  • the water flows from the vortex precipitator 200 into the suspension filter device 300 via the water channel 203, and the suspended impurities are located on the upper surface of the water.
  • the suspension filter device 300 flushes a certain amount of water
  • the water channel 203 is closed, and the bottom of the water and the chlorine removal device are simultaneously opened.
  • 400 connected water pipe 304 the water flows into the chlorine removal device 400, and the liquid filter display tube (not shown) may be disposed outside the suspension filter device 300 for observing the liquid level inside the suspension filter device 300.
  • the water pipe 304 is closed.
  • the remaining part of the suspension filter device 300 is suspended impurities and a small amount of water.
  • the water pipe located at the bottom end of the suspension filter device 300 is opened, and the suspended impurities are suspended. A small portion of the remaining water flows into the drain passage S and is discharged from the drain port D.
  • the dechlorination generator provided in the dechlorination device 400 continuously rushes into the pulse gas flow from the bottom of the dechlorination device 400 to the dechlorination device 400, so that the water in the dechlorination device 400 continues to roll.
  • the chlorine gas is separated from the water, and is discharged from the exhaust port 410 located at the top end of the casing of the chlorine removal device 400 along with the flushing gas.
  • the oxygen that is injected reacts with the chlorine gas in the water to further react. The effect of removing chlorine from the water.
  • a gas purification unit 420 is further disposed at the exhaust port at the top of the chlorine removal device 400.
  • the water flow continues to flow from the water pipe 405 in a pulsed manner through the first addition pipe 510 and the second addition pipe 520 of the trace element addition device 500, through the trace addition unit 530 in the first addition pipe 510 and the second addition pipe 520 (
  • the maifan stone adds trace elements to the water stream.
  • the magnetic field generator 540 provided in the trace element adding device 500 adsorbs and removes harmful heavy metal ions in the water stream.
  • the water flow flows from the second addition pipe 520 through the water pipe 506 into the adjustment pipe 666, and the top of the adjustment pipe 666 is provided with a pH adjustment device 600.
  • the pH adjusting device 600 adjusts the pH of the water flow by electrolyzing water.
  • the sterilization device 700 is also disposed outside the adjustment tube 666, and the sterilization device 700 performs deep sterilization treatment on the water flow in the form of high-voltage high-current discharge.
  • the water flows into the water pipe 708, which in turn is connected with the metasilicate addition device 800 and the water molecule nanotechnology processor 900.
  • the metasilicate addition device 800 heats the metasilicate adder 820 through the heater 810 to add metasilicate to the water flow in the water tube 708.
  • the water flow is nano-processed by the water molecule nano-processing processor 900, and the obtained healthy drinking water is discharged from the water outlet O, and the entire water treatment process ends.
  • the bottom ends of the respective devices of the water treatment system of the present embodiment are respectively communicated with the sewage passages S so as to discharge the separated waste generated by the process of purifying water in each device at any time.
  • the water treatment system sequentially performs heavier impurity treatment by the vortex sedimentation device 200, lighter impurities at the separation of the suspension filtration device 300, the chlorine removal device 400 removes residual chlorine gas in the water, and the trace element adding device 500 supplements the trace elements in the water.
  • the content the pH adjustment device 600 obtains the alkaline health water, the sterilization device 700 performs deep sterilization, the metasilicate additive device 800 adds metasilicate to the water, and the water molecule nanometer processor 900 nanometerizes the water, and finally Get clean, healthy drinking water.
  • the water treatment system can pass the special purification device structure (the vortex sedimentation device 200 and the suspension filter device 300), and the cleaning filter element can be replaced frequently, and the operation is simple; there is no occurrence of the filter element replacement.
  • the impurities remaining in the filter element will breed bacteria, thereby contaminating the water to be purified; the chlorine removal device 400 thoroughly removes chlorine from the water and the sterilization device 700 is used to deeply remove bacteria in the water, so that the treated water is not directly consumed, Any harm is caused by the person; in addition, the water element is further optimized by using the trace element adding device 500, the pH adjusting device 600, the metasilicate adding device 800, and the water molecule nanotechnology processor 900 to obtain clean and healthy drinking water.

Abstract

本发明提供一种水处理系统，该水处理系统包括依次连通的微量元素添加装置、酸碱度调节装置、除菌装置、偏硅酸添加装置以及水分子纳米化处理器，其中，所述微量元素添加装置包括第一添加管、第二添加管以及设于所述第一、第二添加管内的微量元素添加单元，所述微量元素添加单元为麦饭石。本发明实施例提供的水处理系统，依次通过微量元素添加装置补充水中微量元素含量、酸碱度调节装置得到偏碱性健康水、除菌装置做深度除菌、偏硅酸添加装置向水中添加偏硅酸以及水分子纳米化处理器对水进行纳米化处理，最终得到除菌彻底、富含多种矿物质以及偏碱性的健康饮用水。

Description

一种水处理系统
【技术领域】
本发明涉及水处理的技术领域，特别是涉及一种水处理系统。
【背景技术】
随着工业的发展，水污染问题也越来越严重，如何得到干净、健康的饮用水已成为了亟待解决问题。
现有技术的净水方法一般只对水进行了简单的过滤和消毒，无法调节水的酸碱度、水中微量元素含量（尤其是偏硅酸等有益物质），进而得到对人体健康的饮用水；另外，现有技术的净水方法也无法除去水中不能被氯气杀死的细菌等有害物质。
【发明内容】
本发明提供一种水处理系统，以解决现有技术中无法得到一种经过深度杀菌以及富含矿物质的健康饮用水的技术问题。
为解决上述技术问题，本发明提供了一种水处理系统，所述水处理系统包括依次连通的微量元素添加装置、酸碱度调节装置以及除菌装置，其中，所述微量元素添加装置包括第一添加管、第二添加管以及设于所述第一、第二添加管内的微量元素添加单元，所述微量元素添加单元为麦饭石。
根据本发明一优选实施例，所述水处理系统还包括与所述除菌装置连通的偏硅酸添加装置。
根据本发明一优选实施例，所述水处理系统进一步包括与所述偏硅酸添加装置连通的水分子纳米化处理器。
根据本发明一优选实施例，所述酸碱度调节装置包括电解结构单元、酸水排放管以及酸水收集箱。
根据本发明一优选实施例，所述电解结构单元包括正、负电极以及两个分别收容所述正电极和负电极的电解槽，两个电极在不同的电解槽内产生的不同的离子，进而得到酸碱性不同的两种液体，其中，酸性液体经由所述酸水排放管排入酸水收集箱，而碱性液体保留在水中。
根据本发明一优选实施例，所述除菌装置紧邻所述酸碱度调节装置设置，所述除菌装置包括伸入水管内部的放电电极以及高压电发生器，所述高压电发生器利用低压直流稳压电源输出的直流电经转换后变成高压电，进而连接到所述放电电极上。
根据本发明一优选实施例，所述偏硅酸添加装置包括加热器和偏硅酸添加器，所述偏硅酸添加器通过导管与水处理管道连接，所述加热器设于所述偏硅酸添加器底部对所述偏硅酸添加器进行加热，使偏硅酸添加器内的偏硅酸分解，进而通过导管进入到水处理管道中，以向水中添加偏硅酸。
根据本发明一优选实施例，所述加热器为电加热器。
根据本发明一优选实施例，所述微量元素添加装置还包括设于所述微量元素添加装置腔体内部的磁场发生器，所述磁场发生器用于吸附去除水中有害的重金属离子。
根据本发明一优选实施例，所述水处理系统还包括与所述水处理管道连通的排污通道，所述排污通道用于排放所述水处理管道内产生的分离废物。
本发明实施例提供的水处理系统，依次通过微量元素添加装置补充水中微量元素含量、酸碱度调节装置得到偏碱性健康水、除菌装置做深度除菌、偏硅酸添加装置向水中添加偏硅酸以及水分子纳米化处理器对水进行纳米化处理，最终得到干净、健康的饮用水。相较于现有技术，本发明所述提供的水处理系统可以对水进行深度杀菌并添加偏硅酸的等物质，使饮用水更加安全；富含多种矿物质以及偏碱性的水，对人体更加有益。
【附图说明】
为了更清楚地说明本发明实施例中的技术方案，下面将对实施例描述中所需要使用的附图作简单地介绍，显而易见地，下面描述中的附图仅仅是本发明的一些实施例，对于本领域普通技术人员来讲，在不付出创造性劳动的前提下，还可以根据这些附图获得其他的附图。
图1是本发明水处理系统一优选实施例的结构原理示意图。
【具体实施方式】
下面结合附图和实施例，对本发明作进一步的详细描述。特别指出的是，以下实施例仅用于说明本发明，但不对本发明的范围进行限定。同样的，以下实施例仅为本发明的部分实施例而非全部实施例，本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其它实施例，都属于本发明保护的范围。
请参阅图1，图1是本发明水处理系统一优选实施例的结构原理示意图。如图1所示，本发明实施例的水处理系统包括进水口I、涡流沉淀装置200、悬浮过滤装置300、除氯装置400、微量元素添加装置500、酸碱度调节装置600、除菌装置700、偏硅酸添加装置800、水分子纳米化处理器900、排污通道S以及出水口O。
具体而言，该涡流沉淀装置200包括筒状壳体（图中未标示）以及设置在壳体内底部的涡流发生器，该涡流发生器包括驱动单元以及旋转叶片，其中，该驱动单元可以为直流电机或者伺服电机，旋转叶片可以为风轮叶片，具体为电机带动旋转的风轮叶片，在筒状壳体底部产生漩涡，水中较重的固体颗粒状杂质在漩涡的作用下呈螺旋状向中心处同时向底部聚集，杂质聚集到底部后流入位于水处理系统底部的排污管道S内，进而从排污口D排出。而经过漩涡沉淀装置200过滤后的水则会通过连接水管203流入到悬浮过滤装置300内。
另外，该涡流沉淀装置200还可以包括控制单元，该控制单元用于控制涡流发生器的驱动单元的转速、转向等参数，在本领域技术人员的理解范围内，此处不再赘述。
优选地，为防止涡流发生器由于颗粒状杂质的入侵而发生损坏，可以在涡流发生器的外周设置防护网，防护网的网孔密度很小，可以过滤掉水中大部分的颗粒状杂质。
该悬浮过滤装置300通过水流道203与涡流沉淀装置200从壳体上部连通，由于涡流沉淀装置200只对水中较重的颗粒状杂质进行了清除，而水中较轻的悬浮杂质则通过该悬浮过滤装置300进行去除。去除原理及过程如下：水从涡流沉淀装置200经由水流道203流入悬浮过滤装置300内，悬浮杂质会位于水面上部，当悬浮过滤装置300冲入一定量水后，关闭水流道203，同时打开位于其底部与除氯装置400连接的水管304，使水流入除氯装置400中。同时，悬浮过滤装置300的外侧还可以设有液位显示管（图中未示），用于观察悬浮过滤装置300内部的液位情况，当液位显示管指示的水量到达一定位置后关闭水管304，此时悬浮过滤装置300内剩余的即为悬浮杂质和少部分水，这时，打开位于悬浮过滤装置300底端的水管，将悬浮杂质和剩余的少部分水流入排污通道S，进而从排污口D排出。
依次循环该过程，水不断在悬浮过滤装置300内充满、排放，以达到去除水中悬浮杂质的目的。
另外，悬浮过滤装置300的内壁还可以设有精密除氯陶瓷，用于对水中氯气进行初步去除，该精密除氯陶瓷可以贴设在过滤装置300的内壁表面，或者呈筛网状设于悬浮过滤装置300的腔体内部，但是要以不影响去除悬浮杂质为准。关于除氯陶瓷在悬浮过滤装置300内的设置形式在本领域技术人员的理解范围内，此处不再一一列举。
其中，除氯陶瓷可以是活瓷中的一种。活瓷是由20多种矿物元素、氧化金属和陶瓷原料调配烧成的。其具有如下作用：1. 除氯： 可将水中的氯快速分解、振荡挥发；2．除臭：活化水质使水分子变小，分解水中异味并去除和吸附；3．排毒：长期饮用可分解残留体内的重金属、体脂肪、血脂肪，经代谢排出；4．抑菌：因振荡分解单细胞病菌和其他细菌，使其无法繁殖。另外，活瓷所释放的远红外线功能可将大的水分子变成小分子水，提高人体对水的吸收，增强免疫力。活瓷不仅能让酒及各种饮料瞬间变得美味，也让食物保存的更久，更可活化人体内的细胞。还可排除体内的毒素和重金属，促进血液循环、帮助新陈代谢、养颜美容，使人不易老化、改善过敏性皮肤、降低高血压、消除酸痛疲劳。当然，活瓷不构成对本实施例中除氯陶瓷的限制，其他精密除氯陶瓷也可用于本申请实施例中，譬如，托玛琳陶瓷等。
该除氯装置400包括壳体、设于壳体内部的除氯发生器（图中未示）以及位于壳体顶端的排气口410。当然，本实施例中各装置的外壳形状并不局限于图中所示的圆筒状，可以为正方体状、椭球状等，各装置外壳的形状都不构成对本实施例水处理系统的限制。
其中，该除氯发生器可以为脉冲供气机，通过从除氯装置400的底部向除氯装置400内不断冲入脉冲气流，使除氯装置400内的水持续翻滚，进而使氯气从水中分离出来，随着冲入的气体一起从位于除氯装置400壳体顶端的排气口410排出。
另外，该除氯发生器也可以为脉冲充氧机，氧气从除氯装置400的底部不断冲入，一方面与冲入空气类似，由于冲入气体，除氯装置400内的水会持续翻滚，进而使氯气从水中分离出来，随着冲入气体一起从位于除氯装置400壳体顶端的排气口410排出。另一方面，冲入的氧气会与水中氯气发生化学反应，起到进一步去除水中的氯气的作用。
优选地，为防止空气中的污染物进入到该除氯装置400内，在本实施例水处理系统的除氯装置400顶端的排气口处还设有气体净化单元420，该气体净化单元420一方面可以过滤并吸收从除氯装置400内排出的氯气，防止氯气排放到外界空气中造成二次污染。另一方面，也可以净化从外界空气中进入到除氯装置400内部的气体，防止外界空气对除氯装置400内的水造成污染。
其中，空气净化单元420可以为现有技术中的空气净化器或者空气净化盒等。空气净化单元420根据技术和介质的不同可以包括很多种。譬如，常用的空气净化技术有：吸附技术、负（正）离子技术、催化技术、光触媒技术、超结构光矿化技术、HEPA高效过滤技术、静电集尘技术等；而常用的净化材料技术主要有：光触媒、活性炭、极炭心滤芯技术、合成纤维、HEAP高效材料、负离子发生器等等。优选地，本实施例中的空气净化单元420采用复合型材料和技术，即同时采用了多种净化技术和材料介质。在本领域技术人员的理解范围内，此处亦不再详述。
微量元素添加装置500包括第一添加管510和第二添加管520，第一添加管和第二添加管之间通过位于顶部的连接管505连接。第一添加管510和第二添加管520内部分别设有微量元素添加单元530，该微量元素添加单元530可以为麦饭石，麦饭石是一种对生物无毒、无害并具有一定生物活性的复合矿物或药用岩石。麦饭石的主要化学成分是无机的硅铝酸盐。其中包括SiO2、Al2O3、Fe2O3、FeO、MgO、CaO、K2O、Na2O、TiO2、P2O5、MnO等，还含有动物所需的全部常量元素，如：K、Na、Ca、Mg、Cu、Mo等微量元素和稀土元素，约58种之多。
麦饭石具有以下特点：（1）吸附力强；所谓吸附乃是具有多孔性、巨大表面积的固体全部溶化作用，而发生化学的、物理的反应。麦饭石作为中药对皮肤病，特别是拔脓，效果很好。麦饭石是多孔性的，吸附能力很强，因其主要成分为二氧化硅、氧化铝。从这点来考虑，是容易理解的。麦饭石微细粉末的电子显微镜照相中是海绵状多孔性的，这是其具有很好的吸附性的最大的原因。也就是说，因多孔性，那么表面就非常大，由于长石部分风化，成高岭土状等，故始终保持很强的吸附作用和交换作用。
当然，本申请中主要是利用麦饭石中富含丰富的矿物质，起到对水中微量元素添加的作用。另外，麦饭石还具有很好的对水的净化作用，在向水中添加微量元素的同时，还可以对水进一步净化。麦饭石是一种中性碱半火成岩，接近于火山岩。麦饭石中包含的天然矿物质易于释放从麦饭石上无数的小孔中释放出氧。通过吸收漂白粉、氯气和其它有毒物质，以达到净化水的目的。麦饭石中散发出的钙、铁、钠等矿物质可改良饮用水。
在本实施例中，微量元素添加单元530分别设于第一添加管510和第二添加管520的内部，其设置形式优选为块状悬设于第一添加管510和第二添加管520腔体内部，由于微量元素添加单元530具有多孔性，既保证了水能够通过第一添加管510和第二添加管520，又增大了微量元素添加单元530与水的接触面积。
另外，本实施例中的微量元素添加装置500内通过水流的方式优选为：脉冲式通过。即控制除氯装置400与微量元素添加装置500之间的水管405的开启与关闭，使水流以脉冲的方式一段一段的流经微量元素添加装置500，或者在水管405内设置控制阀门（图中未示），通过调节该控制阀门的开启时间来控制每次进入微量元素添加装置500内的水量，这样在每次水流通过微量元素添加装置500的流速相同的情况下，可以保证每次流经微量元素添加装置500的水中添加的微量元素的量相同，相较于现有技术中的微量元素添加装置浸泡在水中相比，可以使水中微量元素添加量更加均匀，同时也可以延长微量元素添加单元530的寿命。
另外，在微量元素添加装置500内还可以设置有磁场发生器540，用于吸附去除水中有害的重金属离子，关于磁场发生器540的的具体结构及工作原理，在本领域技术人员的理解范围内，此处不再赘述。
酸碱度调节装置600设于调节管666的顶部，本实施例中酸碱度调节装置600采用电解水的方式来调节水的酸碱度，其结构包括电解结构单元（图中未标示）、酸水排放管610以及酸水收集箱620。具体而言，该电解结构单元包括正、负电极以及两个分别收容该正电极和负电极的电解槽，由于两个电极在不同的电解槽内产生的不同的离子，进而得到酸碱性不同的两种液体，其中，酸性液体经由酸水排放管610排入酸水收集箱620，而碱性液体保留在水中，因为弱碱水对人体有益处，所以对水的酸碱度调节其实质为使水呈现弱碱性。其中，酸水收集箱620同样可以连接到排污通道S（图中未示），以将产生的酸性液体从排污通道S排掉。酸水收集箱620优选采用透明材质制成，可以方便观察到酸水收集箱620内收集酸性液体的量。
优选地，该正电极和负电极采用镀钌钛材质。每个电解槽内的电极数可以为多个。酸碱度调节装置600还包括控制电路，控制电路用于为正电极和负电极提供稳定电流。
除菌装置700可以紧邻酸碱度调节装置600，同样设置于调节管666的顶部。本实施例中的除菌装置700优选采用高压放电的结构原理，具体结构可以包括伸入水管内部的放电电极以及高压电发生器，该高压电发生器可以利用低压直流稳压电源输出的直流电经转换后变成高压电，进而连接到放电电极上。放电电极优选为两块板状片材并相对设置，在两块板状片材之间产生强大电流场。放电电极的材质为铜、铝、不锈钢以及钛合金等导电性好的材料制成。还可以利用一段与其他部分水管绝缘的水管最为放电电极，即对该段水管通高压电，对经过该水管的水流进行放电杀菌。需要注意的是要做好该段水管与其他部分水管的绝缘工作，以免其他部分水管带电、伤人。当然，放电电极的数量可以为多个，形状也可以为棒状等不规则形状，分布设置在水管内的不同位置，此处不再一一列举。
同样地，除菌装置700也要包括与放电电极以及高压电发生器连接的高压电调节电路，以确保该除菌装置700能够安全、顺利进行放电杀菌。
本实施例中采用的高压高电流的除菌方法是利用电的物理特性对水中的细菌进行杀灭，不会对水的化学性质产生影响，也不会引入任何污染。
偏硅酸添加装置800则主要包括加热器810和偏硅酸添加器820。偏硅酸添加器820通过导管与水管708连接。在本实施例中，偏硅酸添加器820呈圆盒状，并采用金属等导磁、耐热材质制成，以便通过磁感应方式对该偏硅酸添加器820进行加热。加热器810可以为电加热器或者电磁加热器，对加热器810的形式和种类不做限定。加热器810与偏硅酸添加器820可拆卸连接，以便更换偏硅酸添加器820或者向偏硅酸添加器820内添加偏硅酸。
另外，偏硅酸添加装置800的结构形式不限于图中所示的一个加热器810配合一个偏硅酸添加器820使用，也可以是一个加热器810配合多个偏硅酸添加器820使用。偏硅酸添加装置800还可以配置有控制箱，控制箱内设有电路和处理器，用于控制加热器的加热状态及加热温度等。优选地，加热器810上还设有温度传感器（图中未示），温度传感器用于监测加热器810的加热温度。
偏硅酸是一种二元弱酸，电离平衡常数K1=2×10-10(室温)。不溶于盐酸、硫酸，溶于氢氟酸。溶于氢氧化钾或氢氧化钠溶液，生成硅酸钾K2SiO3或硅酸钠Na2SiO3和水。其熔点为150℃，即加热到150℃时分解。加热器810设于偏硅酸添加器820底部对偏硅酸添加器820进行加热，使偏硅酸添加器820内的偏硅酸分解，进而通过导管进入到水管708中，达到向水中添加偏硅酸的目的。
偏硅酸易被人体吸收，能有效地维持人体的电解质平衡和生理机能，具有恢复血管弹性、增加皮肤弹性、促进骨骼发育等作用。
水分子纳米化处理器900通过施加高压来分离水分子而产生的带电净水粒子，以达到使水分子更容易吸收的目的。
排污通道S则设于整个水处理系统的底部，分别与涡流沉淀装置200、悬浮过滤装置300、除氯装置400、微量元素添加装置500以及调节管666的底端连接，用于排放掉各装置内产生的分离废物。
下面对该水处理系统的完整工作流程进行描述。
待净化的水从进水口I进入到涡流沉淀装置200，涡流沉淀装置200内的涡流发生器产生漩涡，使水中较重的固体颗粒状杂质在漩涡的作用下呈螺旋状向中心处同时向底部聚集，杂质聚集到底部后流入位于水处理系统底部的排污管道S内，进而从排污口D排出。而经过漩涡沉淀装置200过滤后的水则会通过连接水管203流入到悬浮过滤装置300内。
水从涡流沉淀装置200经由水流道203流入悬浮过滤装置300内，悬浮杂质会位于水面上部，当悬浮过滤装置300冲入一定量水后，关闭水流道203，同时打开位于其底部与除氯装置400连接的水管304，使水流入除氯装置400中，悬浮过滤装置300的外侧还可以设有液位显示管（图中未示），用于观察悬浮过滤装置300内部的液位情况，当液位显示管指示的水量到达一定位置后关闭水管304，此时悬浮过滤装置300内剩余的即为悬浮杂质与少部分水，这时，打开位于悬浮过滤装置300底端的水管，将悬浮杂质和剩余的少部分水流入排污通道S，进而从排污口D排出。
水经过水管304进入除氯装置400，除氯装置400内设置的除氯发生器从除氯装置400的底部向除氯装置400内不断冲入脉冲气流，使除氯装置400内的水持续翻滚，进而使氯气从水中分离出来，随着冲入气体一起从位于除氯装置400壳体顶端的排气口410排出，另一方面，冲入的氧气会与水中氯气发生化学反应，起到进一步去除水中的氯气的效果。同时，为防止空气中的污染物进入到该除氯装置400内以及防止氯气排放到外界空气中造成二次污染，在除氯装置400顶端的排气口处还设有气体净化单元420。
水流继续从水管405以脉冲的方式依次流经微量元素添加装置500的第一添加管510和第二添加管520，通过第一添加管510和第二添加管520内的微量元素添加单元530（优选为麦饭石）对水流进行添加微量元素。同时，微量元素添加装置500内设置的磁场发生器540对水流中的有害的重金属离子进行吸附式去除。
水流从第二添加管520经水管506流入调节管666，调节管666的顶部设有酸碱度调节装置600。酸碱度调节装置600通过电解水的方式对水流进行酸碱度调节。除菌装置700同样设于调节管666外部，除菌装置700通过高压高电流放电的形式对水流进行深度杀菌处理。
水流进入水管708，水管708依次连接有偏硅酸添加装置800和水分子纳米化处理器900。偏硅酸添加装置800通过加热器810加热偏硅酸添加器820以对水管708内的水流进行添加偏硅酸。最后经过水分子纳米化处理器900对水流进行纳米化处理，得到的健康饮用水从出水口O排出，整个水处理过程结束。
其中，本实施例的水处理系统各个装置的底端分别与排污通道S连通，以便随时排出在各装置净化水的过程产生的分离废物。
本发明实施例提供的水处理系统，依次通过涡流沉淀装置200进行较重杂质处理、悬浮过滤装置300分离处较轻杂质、除氯装置400除去水中残留氯气、微量元素添加装置500补充水中微量元素含量、酸碱度调节装置600得到偏碱性健康水、除菌装置700做深度除菌、偏硅酸添加装置800向水中添加偏硅酸以及水分子纳米化处理器900对水进行纳米化处理，最终得到干净、健康的饮用水。相较于现有技术，该水处理系统通过特别的净化装置结构（涡流沉淀装置200和悬浮过滤装置300），可以不需要经常更换清洗滤芯，操作简单；不会出现因滤芯更换不及时产生的在滤芯处存留的杂质会滋生细菌，进而污染待净化的水的问题；通过除氯装置400彻底清除水中氯气以及利用除菌装置700深度去除水中细菌，使处理过的水即使直接饮用，也不会人产生任何危害；另外还利用微量元素添加装置500、酸碱度调节装置600、偏硅酸添加装置800以及水分子纳米化处理器900对水质进一步优化，得到既干净又健康的饮用水。
以上所述仅为本发明的实施例，并非因此限制本发明的专利范围，凡是利用本发明说明书及附图内容所作的等效结构或等效流程变换，或直接或间接运用在其他相关的技术领域，均同理包括在本发明的专利保护范围内。

Claims (10)

  1. 一种水处理系统，其特征在于，所述水处理系统包括依次连通的微量元素添加装置、酸碱度调节装置以及除菌装置，其中，所述微量元素添加装置包括第一添加管、第二添加管以及设于所述第一、第二添加管内的微量元素添加单元，所述微量元素添加单元为麦饭石。
  2. 根据权利要求1所述的水处理系统，其特征在于，所述水处理系统还包括与所述除菌装置连通的偏硅酸添加装置。
  3. 根据权利要求1所述的水处理系统，其特征在于，所述水处理系统进一步包括与所述偏硅酸添加装置连通的水分子纳米化处理器。
  4. 根据权利要求1所述的水处理系统，其特征在于，所述酸碱度调节装置包括电解结构单元、酸水排放管以及酸水收集箱。
  5. 根据权利要求4所述的水处理系统，其特征在于，所述电解结构单元包括正、负电极以及两个分别收容所述正电极和负电极的电解槽，两个电极在不同的电解槽内产生的不同的离子，进而得到酸碱性不同的两种液体，其中，酸性液体经由所述酸水排放管排入酸水收集箱，而碱性液体保留在水中。
  6. 根据权利要求1所述的水处理系统，其特征在于，所述除菌装置紧邻所述酸碱度调节装置设置，所述除菌装置包括伸入水管内部的放电电极以及高压电发生器，所述高压电发生器利用低压直流稳压电源输出的直流电经转换后变成高压电，进而连接到所述放电电极上。
  7. 根据权利要求2所述的水处理系统，其特征在于，所述偏硅酸添加装置包括加热器和偏硅酸添加器，所述偏硅酸添加器通过导管与水处理管道连接，所述加热器设于所述偏硅酸添加器底部对所述偏硅酸添加器进行加热，使偏硅酸添加器内的偏硅酸分解，进而通过导管进入到水处理管道中，以向水中添加偏硅酸。
  8. 根据权利要求7所述的水处理系统，其特征在于，所述加热器为电加热器。
  9. 根据权利要求1所述的水处理系统，其特征在于，所述微量元素添加装置还包括设于所述微量元素添加装置腔体内部的磁场发生器，所述磁场发生器用于吸附去除水中有害的重金属离子。
  10. 根据权利要求3所述的水处理系统，其特征在于，所述水处理系统还包括与所述水处理管道连通的排污通道，所述排污通道用于排放所述水处理管道内产生的分离废物。
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