CN117049658A - Preparation of high-concentration charged solution and purified water by using hysteresis static repulsive deionized full potential energy conversion self-powered heating method - Google Patents
Preparation of high-concentration charged solution and purified water by using hysteresis static repulsive deionized full potential energy conversion self-powered heating method Download PDFInfo
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- CN117049658A CN117049658A CN202311029408.7A CN202311029408A CN117049658A CN 117049658 A CN117049658 A CN 117049658A CN 202311029408 A CN202311029408 A CN 202311029408A CN 117049658 A CN117049658 A CN 117049658A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 133
- 238000000034 method Methods 0.000 title claims abstract description 35
- 238000005381 potential energy Methods 0.000 title claims abstract description 15
- 230000003068 static effect Effects 0.000 title claims abstract description 8
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 7
- 239000008213 purified water Substances 0.000 title claims abstract description 7
- 238000010438 heat treatment Methods 0.000 title claims description 7
- 238000002360 preparation method Methods 0.000 title description 4
- 150000002500 ions Chemical class 0.000 claims abstract description 68
- 238000000926 separation method Methods 0.000 claims abstract description 55
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 150000001450 anions Chemical class 0.000 claims abstract description 10
- 150000001768 cations Chemical class 0.000 claims abstract description 10
- 238000001704 evaporation Methods 0.000 claims abstract description 7
- 230000008020 evaporation Effects 0.000 claims abstract description 6
- 230000005484 gravity Effects 0.000 claims abstract description 5
- 239000000243 solution Substances 0.000 claims description 44
- 239000008367 deionised water Substances 0.000 claims description 17
- 229910021641 deionized water Inorganic materials 0.000 claims description 17
- 239000007864 aqueous solution Substances 0.000 claims description 12
- 230000000694 effects Effects 0.000 claims description 6
- 239000002245 particle Substances 0.000 claims description 6
- 230000009471 action Effects 0.000 claims description 5
- 239000003990 capacitor Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 230000000087 stabilizing effect Effects 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 230000008859 change Effects 0.000 claims description 3
- 239000002800 charge carrier Substances 0.000 claims description 3
- 229910000838 Al alloy Inorganic materials 0.000 claims description 2
- XMWRBQBLMFGWIX-UHFFFAOYSA-N C60 fullerene Chemical compound C12=C3C(C4=C56)=C7C8=C5C5=C9C%10=C6C6=C4C1=C1C4=C6C6=C%10C%10=C9C9=C%11C5=C8C5=C8C7=C3C3=C7C2=C1C1=C2C4=C6C4=C%10C6=C9C9=C%11C5=C5C8=C3C3=C7C1=C1C2=C4C6=C2C9=C5C3=C12 XMWRBQBLMFGWIX-UHFFFAOYSA-N 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- 229910000990 Ni alloy Inorganic materials 0.000 claims description 2
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 claims description 2
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 2
- 229910001080 W alloy Inorganic materials 0.000 claims description 2
- 239000011358 absorbing material Substances 0.000 claims description 2
- 239000006229 carbon black Substances 0.000 claims description 2
- 239000002041 carbon nanotube Substances 0.000 claims description 2
- 229910021393 carbon nanotube Inorganic materials 0.000 claims description 2
- 229920001940 conductive polymer Polymers 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000010949 copper Substances 0.000 claims description 2
- 229910003472 fullerene Inorganic materials 0.000 claims description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052737 gold Inorganic materials 0.000 claims description 2
- 239000010931 gold Substances 0.000 claims description 2
- 230000003993 interaction Effects 0.000 claims description 2
- 150000003839 salts Chemical class 0.000 claims description 2
- 229910052709 silver Inorganic materials 0.000 claims description 2
- 239000004332 silver Substances 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 229910001220 stainless steel Inorganic materials 0.000 claims description 2
- 230000008569 process Effects 0.000 abstract description 10
- 230000005355 Hall effect Effects 0.000 abstract description 6
- 238000010248 power generation Methods 0.000 abstract description 6
- 238000010612 desalination reaction Methods 0.000 abstract description 5
- 239000013535 sea water Substances 0.000 abstract description 5
- 230000002159 abnormal effect Effects 0.000 abstract description 3
- 230000009286 beneficial effect Effects 0.000 abstract description 3
- 238000005286 illumination Methods 0.000 abstract description 3
- 238000002242 deionisation method Methods 0.000 abstract 1
- 230000005684 electric field Effects 0.000 description 3
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000003111 delayed effect Effects 0.000 description 2
- 230000005518 electrochemistry Effects 0.000 description 2
- 239000002322 conducting polymer Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005485 electric heating Methods 0.000 description 1
- 238000001962 electrophoresis Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000009827 uniform distribution Methods 0.000 description 1
Classifications
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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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/4608—Treatment of water, waste water, or sewage by electrochemical methods using electrical discharges
-
- 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
- C02F1/02—Treatment of water, waste water, or sewage by heating
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B1/00—Conductors or conductive bodies characterised by the conductive materials; Selection of materials as conductors
- H01B1/14—Conductive material dispersed in non-conductive inorganic material
- H01B1/16—Conductive material dispersed in non-conductive inorganic material the conductive material comprising metals or alloys
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B13/00—Apparatus or processes specially adapted for manufacturing conductors or cables
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B13/00—Apparatus or processes specially adapted for manufacturing conductors or cables
- H01B13/0026—Apparatus for manufacturing conducting or semi-conducting layers, e.g. deposition of metal
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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
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Manufacturing & Machinery (AREA)
- General Chemical & Material Sciences (AREA)
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Abstract
The invention provides a self-powered electrothermal method for preparing high-concentration charged solution and purified water by using a hysteresis static repulsion deionization full potential energy conversion method. Electrostatic attraction, gravity separation and positive feedback are used for separating anions from cations in the solution. The middle area of the delay electrostatic separation pipeline can separate clean water containing a small amount or a very small amount of ions, the edge area can separate high-concentration charged solution, and the diversion of the clean water and the ionized water improves the concentration of the charged solution. The tesla turbine utilizes gravitational potential energy of liquid to generate electric energy to provide electrostatic attraction and heat the charged solution, and evaporation of water in the charged solution is beneficial to improving the concentration of the charged solution. In addition, the gravitational potential energy of the charged solution falling into the bottom container is also converted into liquid internal energy, and the hot plate can absorb energy such as illumination and the like to heat the liquid. The high-concentration charged solution prepared by the method provides a research object and a practice medium for operation for principle research and application practice of electrochemical, clean energy, sea water desalination, photovoltaic power generation, friction power generation, hall effect, abnormal Hall effect and other physicochemical processes.
Description
Technical Field
The invention relates to the field of preparation of charged solution and deionized water, in particular to a method for preparing high-concentration charged solution and purified water by a full potential energy conversion self-powered heating method through delayed electrostatic repulsion deionized water.
Background
Along with the continuous expansion of the research fields of the water-based science and technology, water purification and friction nano-generator, the charged solution gradually shows the research and practical value. The controllable preparation method of the high-concentration charged solution has promotion effect on principle research and application practice of electromagnetic related materialization processes such as electrochemistry, clean energy, sea water desalination, photovoltaic power generation, friction power generation, hall effect, abnormal Hall effect and the like.
When the traditional electrophoresis method is used for sea water desalination, an electric field generated by positive and negative electrodes is adopted to directly treat the sea water solution containing positive and negative ions, the positive and negative ions in the solution have mutual attraction, have a uniform distribution trend when no constraint force exists, have no obvious desalination effect when the electric field force is weak, and obviously strengthen the mutual attraction of the positive and negative ions of the solution under the strong electric field, thereby increasing the separation difficulty.
Disclosure of Invention
The invention fully utilizes the gravitational potential energy of the liquid to generate electric energy and internal energy for preparing high-concentration charged solution, and simultaneously utilizes electrostatic attraction and electrostatic repulsion to efficiently separate anions and cations.
The invention is based on the following principle and mechanism:
firstly, electrostatic attraction, gravity separation and positive feedback are adopted to realize the separation of anions and cations in the solution.
Secondly, the electrostatic repulsion, electrostatic attraction and retardation electrostatic separation pipeline are adopted to realize the partition of the same-electric ions, the middle area of the retardation electrostatic separation pipeline can separate clean water containing a small amount or a very small amount of ions, the edge area can separate high-concentration charged solution, and the concentration of the charged solution is improved by the diversion of the clean water and the ionized water.
Then, a tesla turbine is adopted to generate electric energy by utilizing gravitational potential energy of liquid to provide electrostatic attraction and heat the charged solution, and evaporation of water in the charged solution is beneficial to improving the concentration of the charged solution. In addition, the gravitational potential energy of the charged solution falling into the bottom container is also converted into liquid internal energy, and the hot plate can absorb energy such as illumination and the like to heat the liquid.
Finally, the ion water tank is connected with the delay electrostatic separation pipeline and the electrostatic plate outside the Tesla turbine to form an equipotential body, and forms a capacitor with the delay electrostatic separation pipeline and the charged solution inside the Tesla turbine, so that the ion water tank has a stabilizing effect on the high-concentration charged solution, and meanwhile, the liquid splashing phenomenon at the water inlet of the delay electrostatic separation pipeline is reduced or eliminated.
The invention adopts the following technical scheme:
the method for preparing high-concentration charged solution and purified water by using the hysteresis static repulsive deionized full potential energy conversion self-powered heating method comprises the following steps of:
(1) The water tank and the water outlet are configured, positive and negative charge carriers in the aqueous solution respectively flow into one water outlet under the action of electrostatic attraction of the conductive ring and the electrostatic plate, charged water drops do not contact with the conductive ring under the action of gravity and anions and cations in the aqueous solution are separated;
(2) A cylindrical delay electrostatic separation pipeline and a Tesla turbine are arranged right below the conducting ring, the Tesla turbine is arranged inside the delay electrostatic separation pipeline, the outside of the delay electrostatic separation pipeline and the Tesla turbine are provided with electrostatic plates, the delay electrostatic separation pipeline is spiral, the electrostatic plates with the same electrical property enable charges to move to the periphery through the electrostatic repulsive interaction of the electrostatic plates after the ions enter the delay electrostatic separation pipeline from a water inlet, the external electrostatic plates are provided with different electrical charges, the ions are further gathered to the edge, the ions are fully subjected to decentralization separation in the spiral pipeline from high to low and from low to high through long distances, a charged aqueous solution enters the Tesla turbine through a deionized water inlet at the center and ion water inlets at the two sides, the kinetic energy of the liquid is converted into the rotating mechanical energy of the Tesla turbine, and the liquid flows out of the Tesla turbine from the deionized water pipeline and the ion water pipeline;
(3) The ion water flows into a cylindrical delay electrostatic separation pipeline and an ion water tank below the Tesla turbine, a hot plate is arranged below the ion water tank, the hot plate can heat the ion water tank through current and sunlight absorption, water molecules are subjected to phase change and rapid evaporation, and charged ions are left in the solution to increase the concentration of the charged solution;
(4) The ion water tank is connected with an electrostatic plate near the upper water tank in a crossing way by using a lead to form a positive feedback circuit, and the same-electricity ion water is gradually accumulated after entering the ion water tank to form a strong attraction effect, so that more same-electricity charges in the upper water tank enter the ion water tank;
(5) The Tesla turbine is connected with a generator through a driving belt, the positive electrode and the negative electrode of the generator are respectively connected with an electrostatic plate near the water tank, initial electrostatic attraction is provided, positive and negative electrical properties of each ion water tank are determined, and the positive and negative electrodes of the generator are simultaneously connected with a hot plate to generate heat to heat liquid;
(6) The delay electrostatic separation pipeline is crossed and connected with the conducting ring near the upper water tank through a thin strip electrode lead-out wire, the area of the thin strip electrode is small, and the electrostatic attraction of the conducting ring is also increased sharply along with the gradual enhancement of the electrostatic force;
(7) The ion water tank is connected with the delay electrostatic separation pipeline and the electrostatic plate at the outer side of the Tesla turbine through the lead-out wire to form an equipotential body, and forms a capacitor with the delay electrostatic separation pipeline and the charged solution at the inner side of the Tesla turbine, so that the ion water tank has a stabilizing effect on the high-concentration charged solution, and meanwhile, the liquid splashing phenomenon at the water inlet of the delay electrostatic separation pipeline is relieved or eliminated.
The positive and negative charges in the aqueous solution in step (1) include Na + 、K + 、Mg 2+ 、Ca 2+ 、H + 、Cl - 、Br - 、SO 4 2- 、CO 3 2- 、OH - 、C 3 H 7 COO － 、C 8 H 17 COO － Sol particles and charged particles that adsorb or carry anions and cations.
The conducting ring and the electrostatic plate in the step (1) are made of copper, silver, gold, stainless steel, high nickel alloy, high aluminum alloy, titanium alloy, tungsten alloy, conducting polymer, carbon black, fullerene and carbon nano tube.
The area ratio of the deionized water inlet at the contact part of the delay electrostatic separation pipeline in the step (2) and the Tesla turbine and the area ratio of the ionized water inlets at the two sides can be adjusted, the salt content in the deionized water is 0.01-200mg/L, and the concentration lifting ratio of charged particles is 17-45%.
The diameter of the Tesla turbine in the step (2) is 16-1000cm, the distance between the turbine blades in the Tesla turbine is 0.3-10mm, and the rotating speed of the turbine blades is controlled to be 1000-30000r/min.
The material of the hot plate in the step (3) is a common electric heating material, and the hot plate integrates a common solar heat absorbing material.
The static voltage of the high-concentration charged solution in the step (3) is 10-100000V.
The invention has the following advantages:
(1) The high-concentration charged solution prepared by the method provides a research object and a practice medium for operation for principle research and application practice of electromagnetic related materialization processes such as electrochemistry, clean energy, sea water desalination, photovoltaic power generation, friction power generation, hall effect, abnormal Hall effect and the like.
(2) According to the method, firstly, anions and cations are separated through electrostatic attraction and external force, then electrostatic repulsive force of the same-electricity ions is utilized, partial water and ions are separated in the annular delay electrostatic separation pipeline, the delay electrostatic separation pipeline adopts an annular structure to enlarge a path so that the electrostatic repulsive force fully realizes functions, and high and low positions exist, so that the charged liquid is stored partially, the electrostatic repulsive process is delayed, and the charge separation efficiency is improved.
(3) The Tesla turbine and the delay electrostatic separation pipeline are integrated together in a seamless way, the viscous force of the liquid is adopted to convert potential energy of the liquid into mechanical energy, and finally the mechanical energy is converted into electric energy through a motor, so that the electric property of ions in each pipeline can be determined, electrostatic attraction external force is increased to separate anions and cations, the concentration of the charged liquid is increased by evaporating moisture, and the positive feedback process is enhanced.
(4) The method of the invention can produce clean water containing a small amount or a very small amount of ions while preparing high-concentration charged solution.
(5) According to the method, the ion water tank is connected with the delay electrostatic separation pipeline and the electrostatic plate at the outer side of the Tesla turbine to form an equipotential body, and the equipotential body and the delay electrostatic separation pipeline form a capacitor with the charged solution at the inner side of the Tesla turbine, so that the high-concentration charged solution is stabilized, and meanwhile, the liquid splashing phenomenon at the water inlet of the delay electrostatic separation pipeline is reduced or eliminated.
(6) According to the method, a Tesla turbine is adopted, electric energy is generated by utilizing gravitational potential energy of liquid to provide electrostatic attraction and heat the charged solution, and evaporation of water in the charged solution is beneficial to improving the concentration of the charged solution. In addition, the gravitational potential energy of the charged solution falling into the bottom container is also converted into liquid internal energy, and the hot plate can absorb energy such as illumination and the like to heat the liquid.
(7) The method has the advantages of clear principle, clear structure, complete design, simple process, easily available materials and lower requirements, and can be used for mass production.
Drawings
FIG. 1 is a schematic diagram of the principle of the invention for preparing high-concentration charged solution and purified water by adopting a hysteresis static repulsive deionized full potential energy conversion self-powered heating method. 1 is a water tank, 2 is a water outlet, 3 is a water outlet, 4 is ionized water, 5 is ionized water, 6 is a conducting ring, 7 is a conducting ring, 8 is an electrostatic plate, 9 is an electrostatic plate, 10 is an electrostatic plate, 11 is an electrostatic plate, 12 is a water inlet, 13 is a water inlet, 14 is a delay electrostatic separation pipeline, 15 is a delay electrostatic separation pipeline, 16 is a tesla turbine, 17 is a tesla turbine, 18 is a deionized water pipeline, 19 is a deionized water pipeline, 20 is an ionized water pipeline, 21 is an ionized water pipeline, 22 is an ionized water inlet, 23 is an ionized water inlet, 24 is a deionized water inlet, 25 is a turbine blade, 26 is a turbine blade, 27 is a turbine blade, 28 is a rotating shaft, 29 is a transmission belt, 30 is a transmission belt, 31 is a generator, 32 is a generator, 33 is a wire, 34 is a wire, 35 is a wire, 36 is a wire, 37 is a wire, 38 is a wire, 39 is an ion water tank, 40 is an ion water tank, 41 is an electrostatic plate, 42 is an electrostatic plate, 43 is a wire, 44 is a wire, 45 is a hot plate, 46 is a hot plate, 47 is a wire, 48 is a wire, 49 is a wire, 50 is a wire, 51 is an electrostatic plate, 52 is an electrostatic plate, 53 is a wire, and 54 is a wire.
FIG. 2 is a schematic structural view of a Tesla turbine site. 18 is deionized water pipeline, 20 is ion water pipeline, 22 ion water inlet, 23 ion water inlet, 24 deionized water inlet, 25 is turbine blade, 26 is turbine blade, 27 is turbine blade, 28 is rotation axis, 51 is electrostatic plate.
Detailed Description
To facilitate understanding of the present invention, examples are set forth below. It should be apparent to those skilled in the art that the examples are provided only to aid in understanding the present invention and should not be construed as limiting the invention in any way.
Example 1
(1) The water tank and the water outlet are arranged, a sodium chloride aqueous solution with the salinity of 15 per mill is arranged, positive and negative charge carriers in the aqueous solution respectively flow into one water outlet due to the electrostatic attraction effect of the conductive ring and the electrostatic plate, the charged water drops pass through the hollow conductive ring under the action of gravity, the charged water drops are not contacted with the conductive ring, and anions and cations in the aqueous solution are separated.
(2) The cylindrical delay electrostatic separation pipeline and the Tesla turbine are arranged right below the conducting ring, the Tesla turbine is arranged inside the delay electrostatic separation pipeline, the diameter of the delay electrostatic separation pipeline is 100cm, the diameter of the Tesla turbine is 40cm, the distance between turbine blades in the Tesla turbine is 6mm, and an electrostatic plate is arranged outside the delay electrostatic separation pipeline and the Tesla turbine. The delay electrostatic separation pipeline is spiral, the electrostatic repulsion of the same-electricity ions after entering the delay electrostatic separation pipeline from the water inlet makes the charges move to the periphery, the external electrostatic plate carries different-electricity charges, the ions are further gathered to the edge, the ions are fully subjected to decentralization separation in the spiral pipeline from high to low and from low to high through long-distance delay, the charged aqueous solution enters the Tesla turbine through the deionized water inlet in the center and the ionic water inlets at the two sides, the kinetic energy of the liquid is converted into the rotating mechanical energy of the Tesla turbine, the liquid flows out of the Tesla turbine from the deionized water pipeline and the ionic water pipeline, and the charged ion concentration lifting ratio is 17-27%.
(3) The ion water flows into a cylindrical delay electrostatic separation pipeline and an ion water tank below the Tesla turbine, a hot plate is arranged below the ion water tank, the hot plate can heat the ion water tank through current and sunlight absorption, water molecules are subjected to phase change and rapid evaporation, and charged ions are left in the solution to increase the concentration of the charged solution.
(4) The ion water tank is connected with the static plate near the upper water tank in a crossing way by using a lead to form a positive feedback circuit, and the same-electricity ion water is gradually accumulated after entering the ion water tank to form a strong attraction effect, so that more same-electricity charges in the upper water tank enter the ion water tank.
(5) The Tesla turbine is connected with the generator through a driving belt, the positive electrode and the negative electrode of the generator are respectively connected with the electrostatic plates near the water tanks, initial electrostatic attraction is provided, positive and negative electrical properties of each ion water tank are determined, and the positive and negative electrodes of the generator are simultaneously connected with the hot plate to generate heat to heat liquid.
(6) The delay electrostatic separation pipeline is connected with the conducting ring near the upper water tank in a crossing way through the lead-out wire of the thin strip electrode, the area of the thin strip electrode is small, and the electrostatic attraction of the conducting ring is also increased sharply along with the gradual enhancement of the electrostatic force.
(7) The ion water tank is connected with the delay electrostatic separation pipeline and the electrostatic plate at the outer side of the Tesla turbine through the lead-out wire to form an equipotential body, and forms a capacitor with the delay electrostatic separation pipeline and the charged solution at the inner side of the Tesla turbine, so that the ion water tank has a stabilizing effect on the high-concentration charged solution, and meanwhile, the liquid splashing phenomenon at the water inlet of the delay electrostatic separation pipeline is relieved or eliminated.
(8) The electrostatic voltage of the charged solution was measured to be 30000V by an electrometer.
The applicant states that the detailed process equipment and process flows of the present invention are described by the above examples, but the present invention is not limited to, i.e., does not mean that the present invention must be practiced in dependence upon, the above detailed process equipment and process flows. It should be apparent to those skilled in the art that any modification of the present invention, equivalent substitution of raw materials for the product of the present invention, addition of auxiliary components, selection of specific modes, etc., falls within the scope of the present invention and the scope of disclosure.
Claims (7)
1. The method for preparing high-concentration charged solution and purified water by using the hysteresis static repulsive deionized full potential energy conversion self-powered heating method comprises the following steps of:
(1) The water tank and the water outlet are configured, positive and negative charge carriers in the aqueous solution respectively flow into one water outlet under the action of electrostatic attraction of the conductive ring and the electrostatic plate, charged water drops do not contact with the conductive ring under the action of gravity and anions and cations in the aqueous solution are separated;
(2) A cylindrical delay electrostatic separation pipeline and a Tesla turbine are arranged right below the conducting ring, the Tesla turbine is arranged inside the delay electrostatic separation pipeline, the outside of the delay electrostatic separation pipeline and the Tesla turbine are provided with electrostatic plates, the delay electrostatic separation pipeline is spiral, the electrostatic plates with the same electrical property enable charges to move to the periphery through the electrostatic repulsive interaction of the electrostatic plates after the ions enter the delay electrostatic separation pipeline from a water inlet, the external electrostatic plates are provided with different electrical charges, the ions are further gathered to the edge, the ions are fully subjected to decentralization separation in the spiral pipeline from high to low and from low to high through long distances, a charged aqueous solution enters the Tesla turbine through a deionized water inlet at the center and ion water inlets at the two sides, the kinetic energy of the liquid is converted into the rotating mechanical energy of the Tesla turbine, and the liquid flows out of the Tesla turbine from the deionized water pipeline and the ion water pipeline;
(3) The ion water flows into a cylindrical delay electrostatic separation pipeline and an ion water tank below the Tesla turbine, a hot plate is arranged below the ion water tank, the hot plate can heat the ion water tank through current and sunlight absorption, water molecules are subjected to phase change and rapid evaporation, and charged ions are left in the solution to increase the concentration of the charged solution;
(4) The ion water tank is connected with an electrostatic plate near the upper water tank in a crossing way by using a lead to form a positive feedback circuit, and the same-electricity ion water is gradually accumulated after entering the ion water tank to form a strong attraction effect, so that more same-electricity charges in the upper water tank enter the ion water tank;
(5) The Tesla turbine is connected with a generator through a driving belt, the positive electrode and the negative electrode of the generator are respectively connected with an electrostatic plate near the water tank, initial electrostatic attraction is provided, positive and negative electrical properties of each ion water tank are determined, and the positive and negative electrodes of the generator are simultaneously connected with a hot plate to generate heat to heat liquid;
(6) The delay electrostatic separation pipeline is crossed and connected with the conducting ring near the upper water tank through a thin strip electrode lead-out wire, the area of the thin strip electrode is small, and the electrostatic attraction of the conducting ring is also increased sharply along with the gradual enhancement of the electrostatic force;
(7) The ion water tank is connected with the delay electrostatic separation pipeline and the electrostatic plate at the outer side of the Tesla turbine through the lead-out wire to form an equipotential body, and forms a capacitor with the delay electrostatic separation pipeline and the charged solution at the inner side of the Tesla turbine, so that the ion water tank has a stabilizing effect on the high-concentration charged solution, and meanwhile, the liquid splashing phenomenon at the water inlet of the delay electrostatic separation pipeline is relieved or eliminated.
2. The method of claim 1, wherein the positive and negative charges in the aqueous solution in step (1) comprise Na + 、K + 、Mg2+、Ca2+、H + 、Cl-、Br-、SO42-、CO32-、OH - 、C 3 H 7 COO － 、C 8 H 17 COO － Sol particles and charged particles that adsorb or carry anions and cations.
3. The method according to claim 1, wherein the conductive ring and the electrostatic plate in the step (1) are made of copper, silver, gold, stainless steel, high nickel alloy, high aluminum alloy, titanium alloy, tungsten alloy, conductive polymer, carbon black, fullerene, or carbon nanotube.
4. The method according to claim 1, wherein the area ratio of the deionized water inlet and the ionic water inlets at the two sides of the contacting part of the delay electrostatic separation pipeline and the tesla turbine in the step (2) can be adjusted, the salt content in the deionized water is 0.01-200mg/, and the charged particle concentration increasing ratio is 17-45%.
5. The method according to claim 1, wherein the turbine in step (2) has a diameter of 16-1000cm, a distance between turbine blades in the turbine is 0.3-10mm, and a turbine blade rotation speed is controlled to 1000-30000r/min.
6. The method of claim 1, wherein the material of the hot plate in step (3) is a conventional electrical heating material, and the hot plate integrates a conventional solar heat absorbing material.
7. The method according to claim 1, wherein the high-concentration charged solution in the step (3) has an electrostatic voltage of 10 to 100000V.
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