CN116332440A - Filtering equipment for turbid water solution - Google Patents
Filtering equipment for turbid water solution Download PDFInfo
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- CN116332440A CN116332440A CN202310589712.0A CN202310589712A CN116332440A CN 116332440 A CN116332440 A CN 116332440A CN 202310589712 A CN202310589712 A CN 202310589712A CN 116332440 A CN116332440 A CN 116332440A
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 100
- 238000001914 filtration Methods 0.000 title claims abstract description 72
- 239000000243 solution Substances 0.000 claims abstract description 174
- 230000007246 mechanism Effects 0.000 claims abstract description 118
- 238000006722 reduction reaction Methods 0.000 claims abstract description 33
- 238000001556 precipitation Methods 0.000 claims abstract description 31
- 239000007864 aqueous solution Substances 0.000 claims abstract description 21
- 230000009467 reduction Effects 0.000 claims abstract description 16
- 239000012429 reaction media Substances 0.000 claims abstract description 14
- 239000007788 liquid Substances 0.000 claims description 104
- 238000004062 sedimentation Methods 0.000 claims description 89
- 239000002184 metal Substances 0.000 claims description 75
- 230000005484 gravity Effects 0.000 claims description 58
- 239000001257 hydrogen Substances 0.000 claims description 33
- 229910052739 hydrogen Inorganic materials 0.000 claims description 33
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 32
- 238000010438 heat treatment Methods 0.000 claims description 24
- 239000000696 magnetic material Substances 0.000 claims description 24
- 235000017166 Bambusa arundinacea Nutrition 0.000 claims description 20
- 235000017491 Bambusa tulda Nutrition 0.000 claims description 20
- 241001330002 Bambuseae Species 0.000 claims description 20
- 235000015334 Phyllostachys viridis Nutrition 0.000 claims description 20
- 239000011425 bamboo Substances 0.000 claims description 20
- 230000008859 change Effects 0.000 claims description 12
- 238000009413 insulation Methods 0.000 claims description 2
- 239000013049 sediment Substances 0.000 claims 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 abstract description 41
- 239000012535 impurity Substances 0.000 description 18
- 230000009471 action Effects 0.000 description 13
- 238000010521 absorption reaction Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- 238000004140 cleaning Methods 0.000 description 4
- 230000005389 magnetism Effects 0.000 description 4
- 230000000149 penetrating effect Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000005415 magnetization Effects 0.000 description 3
- 230000001376 precipitating effect Effects 0.000 description 3
- 230000002035 prolonged effect Effects 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 150000002431 hydrogen Chemical class 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 241000221535 Pucciniales Species 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000001174 ascending effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000006388 chemical passivation reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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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
- C02F9/00—Multistage treatment of water, waste water or sewage
-
- 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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
-
- 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
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
- C02F1/484—Treatment of water, waste water, or sewage with magnetic or electric fields using electromagnets
-
- 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
- C02F1/70—Treatment of water, waste water, or sewage by reduction
-
- 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
- C02F2101/20—Heavy metals or heavy metal compounds
- C02F2101/203—Iron or iron compound
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Electromagnetism (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses filtering equipment for turbid aqueous solution, which comprises a bottom plate, a solution treatment box, an annular plate, a solution reduction type precipitation mechanism and an elastic telescopic type filtering mechanism, wherein the solution treatment box is arranged on the upper wall of the bottom plate, the annular plate is arranged on the outer side of the solution treatment box, the solution reduction type precipitation mechanism is arranged on the solution treatment box, the elastic telescopic type filtering mechanism is arranged in the solution treatment box, the solution reduction type precipitation mechanism comprises a split water supply mechanism, a precipitation treatment mechanism, a reduction reaction mechanism and a reaction medium driving mechanism, the split water supply mechanism is arranged on the upper wall of the solution treatment box, the precipitation treatment mechanism is arranged on the bottom wall of the solution treatment box, and the reduction reaction mechanism is arranged on the annular plate. The invention belongs to the technical field of water solution treatment, and particularly relates to filtering equipment for turbid water solution; the invention provides filtering equipment for turbid water solution, which can filter the water solution under the condition that a filter screen is not contacted with rust in turbid water solution.
Description
Technical Field
The invention belongs to the technical field of water solution treatment, and particularly relates to filtering equipment for turbid water solution.
Background
Pipeline cleaning means cleaning the pipeline to recover the surface of the material in the pipeline. After cleaning, a layer of compact chemical passivation film is formed on the clean metal surface, so that the regeneration of dirt can be effectively prevented, equipment can be effectively protected, the equipment is not corroded or otherwise chemically damaged, however, a large amount of aqueous solution containing rust is left after the pipeline is cleaned, and the solution is discharged under the condition of no treatment, so that the environment is easily polluted.
The prior filtering device for turbid water solution has the following problems:
most of the existing water solution filtering equipment adopts a filter screen to filter impurities in the water solution, however, when the water solution containing rust is processed, the spike part of the rust is easy to clamp on the surface of the filter screen, so that the rust penetrating into the surface of the filter screen continuously rusts on the surface of the filter screen under the condition that the filter screen is not used, the filtering effect of the filter screen is affected, and the filtering service life is shortened.
Disclosure of Invention
Aiming at the defects in the prior art, the scheme provides a turbid water solution filtering device, and aims at solving the problem that the surface of the existing filter screen is easy to rust after the sewage is cleaned by the pipeline.
The invention provides filtering equipment for turbid water solution, which can filter the water solution under the condition that a filter screen is not contacted with rust in turbid water solution.
The technical scheme adopted by the scheme is as follows: the utility model provides a muddy aqueous solution's filtration equipment, including bottom plate, solution treatment box, annular slab, solution reduction type precipitation mechanism and elasticity telescopic filtration mechanism, the solution treatment box is located the bottom plate upper wall, the annular slab is located the solution treatment box outside, solution reduction type precipitation mechanism is located on the solution treatment box, elasticity telescopic filtration mechanism is located inside the solution treatment box, solution reduction type precipitation mechanism includes reposition of redundant personnel water supply mechanism, sedimentation treatment mechanism, reduction reaction mechanism and reaction medium actuating mechanism, reposition of redundant personnel water supply mechanism is located the solution treatment box upper wall, sedimentation treatment mechanism locates the solution treatment box diapire, reduction reaction mechanism locates on the annular slab, reaction medium actuating mechanism locates inside the solution treatment box, elasticity telescopic filtration mechanism includes telescopic filtration mechanism and gravity change mechanism, telescopic filtration mechanism locates the solution treatment box inner wall, gravity change mechanism locates on the telescopic filtration mechanism.
As a further preferable scheme, the diversion water supply mechanism comprises a water supply plate, a water supply cavity, turbid liquid joints and purifying pipes, wherein the water supply plate is arranged on the inner wall of the top of the solution treatment tank, the water supply cavity is arranged between the upper wall of the water supply plate and the top wall of the solution treatment tank, the turbid liquid joints are arranged on the upper wall of the solution treatment tank, the turbid liquid joints penetrate through the solution treatment tank and are communicated with the water supply cavity, and a plurality of groups of purifying pipes penetrate through the solution treatment tank and are communicated with the inside of the water supply cavity; the sedimentation treatment mechanism comprises a sedimentation plate, sedimentation ports, sedimentation pipes, sedimentation cavities, gold-absorbing electromagnets and one-way water inlet pipes, wherein the sedimentation plate is arranged on the inner wall of the bottom of the solution treatment tank, a plurality of groups of sedimentation ports are arranged on the upper wall of the sedimentation plate, the sedimentation cavities are arranged between the bottom wall of the sedimentation plate and the bottom wall of the solution treatment tank, the gold-absorbing electromagnets are arranged on the bottom wall of the sedimentation cavities, a plurality of groups of sedimentation pipes penetrate through the solution treatment tank and are communicated with the inside of the sedimentation cavities, and the one-way water inlet pipes are arranged on the outer sides of the sedimentation pipes; the reduction reaction mechanism comprises a heating cylinder, a metal ball cylinder, a high-frequency coil, a heat-insulating annular plate and a metal tube, wherein a plurality of groups of the heating cylinders are penetrated through the upper wall of the annular plate, the heating cylinders are penetrated, the metal ball cylinder is arranged on the bottom wall of the heating cylinder, the high-frequency coil is arranged on the inner wall of the heating cylinder, the heat-insulating annular plate is arranged on one side of the purifying tube far away from the solution treatment box, the metal tube is arranged on one side of the heat-insulating annular plate far away from the purifying tube, one end of the metal tube far away from the heat-insulating annular plate penetrates through the high-frequency coil to be communicated with the upper wall of the metal ball cylinder, and one end of the settling tube far away from the settling chamber is communicated with the bottom wall of the metal ball cylinder; the reaction medium driving mechanism comprises a driving box, a pressure container, a pulse generator, an annular pipe, a jet head, a hydrogen pipe, a pressure relief valve, a one-way air inlet valve and a return pipe, wherein the driving box is respectively arranged on the bottom wall of a water supply plate and the upper wall of a sedimentation plate, the pressure container is arranged between the driving boxes, the pulse generator is arranged inside the driving box, the power end of the pulse generator penetrates through the driving box to be arranged inside the pressure container, the annular pipe penetrates through to be arranged between the metal ball cylinder, the jet head is communicated with the upper wall of the annular pipe inside the metal ball cylinder, the hydrogen pipe penetrates through the solution treatment box to be communicated between the pressure container and the annular pipe, the pressure relief valve is arranged on the outer side of the hydrogen pipe, the return pipe penetrates through the solution treatment box to be communicated between the metal ball cylinder and the pressure container, and the one-way air inlet valve is arranged on the outer side of the return pipe.
During the use, the muddy aqueous solution that produces behind the clearance pipeline enters into the water supply intracavity portion through the muddy liquid joint, the muddy liquid of water supply intracavity portion flows into the metal tube portion through the purge tube, high-frequency coil circular telegram heats the metal tube, metal tube temperature rise is with heat conduction to the metal ball section of thick bamboo inside, metal ball section of thick bamboo temperature rise, pulse generator passes through the power end and launches the pulse wave to pressure vessel inside, the inside pressure of pressure vessel increases the preset pressure value that exceeds the relief valve, the relief valve is opened, the inside hydrogen of pressure vessel enters into the annular tube through the hydrogen pipe, the inside hydrogen of annular tube passes through the jet-propelled head blowout, the inside muddy liquid of metal tube enters into the metal ball section of thick bamboo inside, the muddy liquid contacts with hydrogen, under the effect of metal ball section of thick bamboo high temperature, the rust in the muddy liquid and hydrogen take place the reaction under the condition of high temperature, the muddy liquid whereabouts metal ball section of thick bamboo bottom, the muddy liquid of metal ball section of thick bamboo bottom passes through the sedimentation tube and enters into the sedimentation chamber inside, the inside the interior pulse wave of gold-absorbing electromagnet circular telegram, the muddy liquid of pressure vessel inside enters into solution treatment box inside through the sedimentation mouth and carries out filtration, the inside the magnet, the inside the iron-absorbing electromagnet has carried out the magnetic force to the inside the muddy liquid of the absorption rust is carried out the inside the absorption of the rust under the condition, the high-temperature is more well, the operation is avoided down the muddy liquid is carried out under the high-temperature down in the inside the absorption position of the rust, and the muddy liquid is convenient to be filtered down along with the high-speed.
Preferably, the telescopic filtering mechanism comprises sliding blocks, an elastic filtering layer, a telescopic drainage pipe and a drainage joint, wherein a plurality of groups of sliding blocks are respectively arranged on the inner wall of the solution treatment tank and the side wall of the pressure container in a sliding manner, the elastic filtering layer is arranged between the sliding blocks, the telescopic drainage pipe penetrates through the solution treatment tank and is arranged on the upper wall of the elastic filtering layer, and the drainage joint is communicated with one side, far away from the elastic filtering layer, of the telescopic drainage pipe; the gravity change mechanism comprises a gravity plate, a buoyancy air bag, a magnetic material layer, a buoyancy electromagnet and a gravity ball, wherein a plurality of groups of gravity plates are arranged on the bottom wall of the sliding block, the buoyancy air bag is arranged on the bottom wall of the gravity plate, the magnetic material layer and the buoyancy electromagnet are respectively arranged on the inner wall of the buoyancy air bag, and the gravity ball is arranged on one side of the buoyancy air bag far away from the gravity plate.
When in use, in the initial state, the telescopic drain pipe is in an extension state, the sliding block is positioned at the bottom of the solution treatment tank under the action of the gravity ball, along with turbid liquid entering the solution treatment tank, the buoyancy electromagnet is electrified to generate magnetism, the buoyancy electromagnet magnetizes the magnetic material layer, the magnetic material layer magnetizes and releases heat, the magnetic material layer heats the gas inside the buoyancy air bag, the buoyancy air bag swells and increases buoyancy, the buoyancy of the buoyancy air bag is greater than the gravity of the gravity ball, at the moment, the sliding block slides upwards along the space between the inner wall of the solution treatment tank and the side wall of the pressure container under the action of the buoyancy, the turbid liquid is prevented from directly penetrating through the elastic filter layer, the elastic filter layer stretches and shortens under the action of the elasticity when sliding along the space between the inner wall of the solution treatment tank and the side wall of the pressure container, the turbid liquid entering the solution treatment tank is kept stand and deposited, the current flowing into the interior of the gold-absorbing electromagnet is increased, the magnetic force of the gold-absorbing electromagnet is increased, thereby accelerating the precipitation speed of rust impurities in turbid liquid, reducing the adsorption of more rust when the turbid liquid is filtered on the elastic filter layer, on one hand, the content of impurities in the filtered turbid liquid can be ensured to be lower, on the other hand, the rust can be prevented from eroding the elastic filter layer, the probability of adhering rust on the surface of the elastic filter layer is reduced, the service life of the elastic filter layer is prolonged, after the impurities in the turbid liquid in the solution treatment box are precipitated, the magnetic force of the buoyancy electromagnet is weakened, the magnetization intensity of the buoyancy electromagnet on the magnetic material layer is reduced, the heating degree of the magnetic material layer on the air in the buoyancy air bag is reduced, the buoyancy air bag is reduced by the buoyancy air bag, at the moment, the gravity of the gravity ball is larger than the buoyancy of the buoyancy air bag, and the gravity ball drives the elastic filter layer to reach the position below the liquid level of the turbid liquid, the buoyancy ball drives the elastic filter layer to be always positioned below the liquid level, so that the turbid liquid close to one end of the sedimentation cavity is left with sufficient sedimentation time, and the turbid liquid is filtered.
Specifically, the upper wall of the bottom plate is provided with a controller.
The controller is electrically connected with the gold-attracting electromagnet, the high-frequency coil, the pulse generator and the buoyancy electromagnet respectively.
Preferably, the controller is of the type SYC89C52RC-401.
The beneficial effect that this scheme of adoption above-mentioned structure obtained is as follows:
compared with the prior art, this scheme adopts buoyancy lifting and the mode that subtracts the float and subsides, can make it pass the elastic filter layer after precipitating turbid liquid, under the intervention of hydrogen use, rust impurity in the turbid liquid takes place reduction reaction in high temperature environment, under the magnetic force absorption of magnetic field, can reduce rust impurity and flow along with turbid liquid and ascending probability, and then improve elastic filter layer and to the filtration efficiency of turbid liquid, and can prolong elastic filter layer's life, avoid it to appear the condition of jam, in the in-process that buoyancy gasbag buoyancy reduces, gravity ball drives elastic filter layer gradual decline height, make elastic filter layer be in the position below the liquid level all the time, under the condition that reduces rust impurity and elastic filter layer contact, discharge after filtering the turbid liquid after will depositing, metal ball section of thick bamboo bottom turbid liquid enters into the sedimentation intracavity portion through the sedimentation pipe, the inside turbid liquid that the sedimentation chamber is passed through the sedimentation mouth and is entered into solution treatment box inside and is filtered, the turbid liquid that the electro-magnet has reduced adsorbs, through the drainage equipment and the buoyancy that the drainage is connected with the liquid level, and the buoyancy ball is located down to the following continuous position that the buoyancy is in order to take the following to complete the technical scheme of the completion of the following, and then the filtration solution of the following buoyancy ball is located under the condition that the buoyancy ball is continuous to the completion: the utility model provides a muddy aqueous solution's filtration equipment, including bottom plate, solution treatment box, annular slab, solution reduction type precipitation mechanism and elasticity telescopic filtration mechanism, the solution treatment box is located the bottom plate upper wall, the annular slab is located the solution treatment box outside, solution reduction type precipitation mechanism is located on the solution treatment box, elasticity telescopic filtration mechanism is located inside the solution treatment box, solution reduction type precipitation mechanism includes reposition of redundant personnel water supply mechanism, sedimentation treatment mechanism, reduction reaction mechanism and reaction medium actuating mechanism, reposition of redundant personnel water supply mechanism is located the solution treatment box upper wall, sedimentation treatment mechanism locates the solution treatment box diapire, reduction reaction mechanism locates on the annular slab, reaction medium actuating mechanism locates inside the solution treatment box, elasticity telescopic filtration mechanism includes telescopic filtration mechanism and gravity change mechanism, telescopic filtration mechanism locates the solution treatment box inner wall, gravity change mechanism locates on the telescopic filtration mechanism.
As a further preferable scheme, the diversion water supply mechanism comprises a water supply plate, a water supply cavity, turbid liquid joints and purifying pipes, wherein the water supply plate is arranged on the inner wall of the top of the solution treatment tank, the water supply cavity is arranged between the upper wall of the water supply plate and the top wall of the solution treatment tank, the turbid liquid joints are arranged on the upper wall of the solution treatment tank, the turbid liquid joints penetrate through the solution treatment tank and are communicated with the water supply cavity, and a plurality of groups of purifying pipes penetrate through the solution treatment tank and are communicated with the inside of the water supply cavity; the sedimentation treatment mechanism comprises a sedimentation plate, sedimentation ports, sedimentation pipes, sedimentation cavities, gold-absorbing electromagnets and one-way water inlet pipes, wherein the sedimentation plate is arranged on the inner wall of the bottom of the solution treatment tank, a plurality of groups of sedimentation ports are arranged on the upper wall of the sedimentation plate, the sedimentation cavities are arranged between the bottom wall of the sedimentation plate and the bottom wall of the solution treatment tank, the gold-absorbing electromagnets are arranged on the bottom wall of the sedimentation cavities, a plurality of groups of sedimentation pipes penetrate through the solution treatment tank and are communicated with the inside of the sedimentation cavities, and the one-way water inlet pipes are arranged on the outer sides of the sedimentation pipes; the reduction reaction mechanism comprises a heating cylinder, a metal ball cylinder, a high-frequency coil, a heat-insulating annular plate and a metal tube, wherein a plurality of groups of the heating cylinders are penetrated through the upper wall of the annular plate, the heating cylinders are penetrated, the metal ball cylinder is arranged on the bottom wall of the heating cylinder, the high-frequency coil is arranged on the inner wall of the heating cylinder, the heat-insulating annular plate is arranged on one side of the purifying tube far away from the solution treatment box, the metal tube is arranged on one side of the heat-insulating annular plate far away from the purifying tube, one end of the metal tube far away from the heat-insulating annular plate penetrates through the high-frequency coil to be communicated with the upper wall of the metal ball cylinder, and one end of the settling tube far away from the settling chamber is communicated with the bottom wall of the metal ball cylinder; the reaction medium driving mechanism comprises a driving box, a pressure container, a pulse generator, an annular pipe, a jet head, a hydrogen pipe, a pressure relief valve, a one-way air inlet valve and a return pipe, wherein the driving box is respectively arranged on the bottom wall of a water supply plate and the upper wall of a sedimentation plate, the pressure container is arranged between the driving boxes, the pulse generator is arranged inside the driving box, the power end of the pulse generator penetrates through the driving box to be arranged inside the pressure container, the annular pipe penetrates through to be arranged between the metal ball cylinder, the jet head is communicated with the upper wall of the annular pipe inside the metal ball cylinder, the hydrogen pipe penetrates through the solution treatment box to be communicated between the pressure container and the annular pipe, the pressure relief valve is arranged on the outer side of the hydrogen pipe, the return pipe penetrates through the solution treatment box to be communicated between the metal ball cylinder and the pressure container, and the one-way air inlet valve is arranged on the outer side of the return pipe.
During the use, the muddy aqueous solution that produces behind the clearance pipeline enters into the water supply intracavity portion through the muddy liquid joint, the muddy liquid of water supply intracavity portion flows into the metal tube portion through the purge tube, high-frequency coil circular telegram heats the metal tube, metal tube temperature rise is with heat conduction to the metal ball section of thick bamboo inside, metal ball section of thick bamboo temperature rise, pulse generator passes through the power end and launches the pulse wave to pressure vessel inside, the inside pressure of pressure vessel increases the preset pressure value that exceeds the relief valve, the relief valve is opened, the inside hydrogen of pressure vessel enters into the annular tube through the hydrogen pipe, the inside hydrogen of annular tube passes through the jet-propelled head blowout, the inside muddy liquid of metal tube enters into the metal ball section of thick bamboo inside, the muddy liquid contacts with hydrogen, under the effect of metal ball section of thick bamboo high temperature, the rust in the muddy liquid and hydrogen take place the reaction under the condition of high temperature, the muddy liquid whereabouts metal ball section of thick bamboo bottom, the muddy liquid of metal ball section of thick bamboo bottom passes through the sedimentation tube and enters into the sedimentation chamber inside, the inside the interior pulse wave of gold-absorbing electromagnet circular telegram, the muddy liquid of pressure vessel inside enters into solution treatment box inside through the sedimentation mouth and carries out filtration, the inside the magnet, the inside the iron-absorbing electromagnet has carried out the magnetic force to the inside the muddy liquid of the absorption rust is carried out the inside the absorption of the rust under the condition, the high-temperature is more well, the operation is avoided down the muddy liquid is carried out under the high-temperature down in the inside the absorption position of the rust, and the muddy liquid is convenient to be filtered down along with the high-speed.
Preferably, the telescopic filtering mechanism comprises sliding blocks, an elastic filtering layer, a telescopic drainage pipe, a drainage joint and a water suction port, wherein a plurality of groups of sliding blocks are respectively arranged on the inner wall of the solution treatment tank and the side wall of the pressure container in a sliding manner, the elastic filtering layer is arranged between the sliding blocks, the telescopic drainage pipe penetrates through the solution treatment tank and is arranged on the upper wall of the elastic filtering layer, and the water suction port is arranged at one end, close to the elastic filtering layer, of the drainage joint; the gravity change mechanism comprises a gravity plate, a buoyancy air bag, a magnetic material layer, a buoyancy electromagnet and a gravity ball, wherein a plurality of groups of gravity plates are arranged on the bottom wall of the sliding block, the buoyancy air bag is arranged on the bottom wall of the gravity plate, the magnetic material layer and the buoyancy electromagnet are respectively arranged on the inner wall of the buoyancy air bag, and the gravity ball is arranged on one side of the buoyancy air bag far away from the gravity plate.
When in use, in the initial state, the telescopic drain pipe is in an extension state, the sliding block is positioned at the bottom of the solution treatment tank under the action of the gravity ball, along with turbid liquid entering the solution treatment tank, the buoyancy electromagnet is electrified to generate magnetism, the buoyancy electromagnet magnetizes the magnetic material layer, the magnetic material layer magnetizes and releases heat, the magnetic material layer heats the gas inside the buoyancy air bag, the buoyancy air bag swells and increases buoyancy, the buoyancy of the buoyancy air bag is greater than the gravity of the gravity ball, at the moment, the sliding block slides upwards along the space between the inner wall of the solution treatment tank and the side wall of the pressure container under the action of the buoyancy, the turbid liquid is prevented from directly penetrating through the elastic filter layer, the elastic filter layer stretches and shortens under the action of the elasticity when sliding along the space between the inner wall of the solution treatment tank and the side wall of the pressure container, the turbid liquid entering the solution treatment tank is kept stand and deposited, the current flowing into the interior of the gold-absorbing electromagnet is increased, the magnetic force of the gold-absorbing electromagnet is increased, thereby accelerating the precipitation speed of rust impurities in turbid liquid, reducing the adsorption of more rust when the turbid liquid is filtered on the elastic filter layer, on one hand, the content of impurities in the filtered turbid liquid can be ensured to be lower, on the other hand, the rust can be prevented from eroding the elastic filter layer, the probability of adhering rust on the surface of the elastic filter layer is reduced, the service life of the elastic filter layer is prolonged, after the impurities in the turbid liquid in the solution treatment box are precipitated, the magnetic force of the buoyancy electromagnet is weakened, the magnetization intensity of the buoyancy electromagnet on the magnetic material layer is reduced, the heating degree of the magnetic material layer on the air in the buoyancy air bag is reduced, the buoyancy air bag is reduced by the buoyancy air bag, at the moment, the gravity of the gravity ball is larger than the buoyancy of the buoyancy air bag, and the gravity ball drives the elastic filter layer to reach the position below the liquid level of the turbid liquid, the buoyancy ball drives the elastic filter layer to be always positioned below the liquid level, so that the turbid liquid close to one end of the sedimentation cavity is left with sufficient sedimentation time, and the turbid liquid is filtered.
Specifically, the upper wall of the bottom plate is provided with a controller.
The controller is electrically connected with the gold-attracting electromagnet, the high-frequency coil, the pulse generator and the buoyancy electromagnet respectively.
Preferably, the controller is of the type SYC89C52RC-401.
The beneficial effect that this scheme of adoption above-mentioned structure obtained is as follows:
compared with the prior art, this scheme adopts buoyancy lifting and the mode that subtracts the float and subsides, can make it pass the elastic filter layer after depositing to turbid liquid, under the intervention of hydrogen use, rust impurity in the turbid liquid takes place reduction reaction in high temperature environment, magnetic force absorption under the magnetic field, can reduce the probability that rust impurity flows along with turbid liquid and rise, and then improve elastic filter layer and to the filtration efficiency of turbid liquid, and can prolong elastic filter layer's life, avoid its condition that appears blocking, in the in-process that buoyancy gasbag buoyancy reduces, gravity ball drives elastic filter layer gradual decline height, make elastic filter layer be in the position below the liquid level all the time, under the condition that reduces rust impurity and elastic filter layer contact, discharge after filtering the turbid liquid after will depositing, the turbid liquid of metal ball section of thick bamboo bottom enters into the sedimentation intracavity portion through the sedimentation pipe, the inside turbid liquid that the sedimentation chamber is passed through the sedimentation mouth and is gone into solution treatment box inside and is filtered, the turbid liquid that the electro-magnet has reduced adsorbs, through the drainage device and the buoyancy joint that the drainage is connected, and then the time that the buoyancy ball is located the completion is close to the position that the buoyancy is continuous to the sedimentation ball, and then fully filters the operation is accomplished to the buoyancy ball.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present solution;
FIG. 2 is a perspective view of the present solution;
FIG. 3 is a schematic view of the internal structure of the present embodiment;
FIG. 4 is a side view of FIG. 3;
FIG. 5 is a front view of the present solution;
FIG. 6 is a top view of the present solution;
FIG. 7 is a partial cross-sectional view of portion A-A of FIG. 6;
FIG. 8 is a partial cross-sectional view of B-B of FIG. 6;
FIG. 9 is a schematic diagram of the explosive structure of the present solution;
FIG. 10 is an enlarged schematic view of the portion I of FIG. 3;
FIG. 11 is an enlarged schematic view of the portion II of FIG. 4;
fig. 12 is an enlarged schematic view of the portion III of fig. 8.
Wherein 1, bottom plate, 2, solution treatment tank, 3, annular plate, 4, solution reduction type precipitation mechanism, 5, split water supply mechanism, 6, water supply plate, 7, water supply cavity, 8, turbid liquid joint, 9, purifying pipe, 10, precipitation treatment mechanism, 11, precipitation plate, 12, precipitation port, 13, precipitation pipe, 14, reduction reaction mechanism, 15, heating cylinder, 16, metal ball cylinder, 17, high-frequency coil, 18, heat insulation annular plate, 19, metal pipe, 20, reaction medium driving mechanism, 21, driving tank, 22, pressure vessel, 23, pulse generator, 24, annular pipe, 25, jet head, 26, hydrogen pipe, 27, relief valve, 28, unidirectional air inlet valve, 29, elastic telescopic filter mechanism, 30, telescopic filter mechanism, 31, slider, 32, elastic filter layer, 33, telescopic drain pipe, 34, drainage joint, 35, gravity change mechanism, 36, gravity plate, 37, buoyancy air bag, 38, magnetic material layer, 39, buoyancy electromagnet, 40, gravity ball, 41, controller, 42, cavity, 43, backflow pipe, 44, water intake pipe, 46, unidirectional water intake pipe, 46.
The accompanying drawings are included to provide a further understanding of the present disclosure and are incorporated in and constitute a part of this disclosure, illustrate and do not limit the disclosure.
Detailed Description
The technical solutions in the embodiments of the present solution will be clearly and completely described below with reference to the drawings in the embodiments of the present solution, and it is apparent that the described embodiments are only some embodiments of the present solution, but not all embodiments; all other embodiments, based on the embodiments in this solution, which a person of ordinary skill in the art would obtain without inventive faculty, are within the scope of protection of this solution.
In the description of the present embodiment, it should be understood that the terms "upper," "lower," "front," "rear," "left," "right," "top," "bottom," "inner," "outer," and the like indicate orientation or positional relationships based on those shown in the drawings, merely to facilitate description of the present embodiment and to simplify the description, and do not indicate or imply that the devices or elements referred to must have a particular orientation, be configured and operated in a particular orientation, and thus should not be construed as limiting the present embodiment.
As shown in fig. 1-12, the filtering device for turbid aqueous solution provided by the scheme comprises a bottom plate 1, a solution treatment tank 2, an annular plate 3, a solution reduction type precipitation mechanism 4 and an elastic telescopic type filtering mechanism 29, wherein the solution treatment tank 2 is arranged on the upper wall of the bottom plate 1, the annular plate 3 is arranged on the outer side of the solution treatment tank 2, the solution reduction type precipitation mechanism 4 is arranged on the solution treatment tank 2, the elastic telescopic type filtering mechanism 29 is arranged in the solution treatment tank 2, the solution reduction type precipitation mechanism 4 comprises a split water supply mechanism 5, a precipitation treatment mechanism 10, a reduction reaction mechanism 14 and a reaction medium driving mechanism 20, the split water supply mechanism 5 is arranged on the upper wall of the solution treatment tank 2, the precipitation treatment mechanism 10 is arranged on the bottom wall of the solution treatment tank 2, the reduction reaction mechanism 14 is arranged on the annular plate 3, the reaction medium driving mechanism 20 is arranged in the solution treatment tank 2, the elastic telescopic type filtering mechanism 29 comprises a telescopic filtering mechanism 30 and a gravity change mechanism 35, the telescopic filtering mechanism 30 is arranged on the inner wall of the solution treatment tank 2, and the telescopic mechanism 30 is arranged on the telescopic mechanism 35.
The diversion water supply mechanism 5 comprises a water supply plate 6, a water supply cavity 7, turbid liquid joints 8 and purifying pipes 9, the water supply plate 6 is arranged on the inner wall of the top of the solution treatment tank 2, the water supply cavity 7 is arranged between the upper wall of the water supply plate 6 and the top wall of the solution treatment tank 2, the turbid liquid joints 8 are arranged on the upper wall of the solution treatment tank 2, the turbid liquid joints 8 penetrate through the solution treatment tank 2 and are communicated with the water supply cavity 7, and a plurality of groups of purifying pipes 9 penetrate through the solution treatment tank 2 and are communicated with the inside of the water supply cavity 7; the sedimentation treatment mechanism 10 comprises a sedimentation plate 11, a sedimentation port 12, a sedimentation pipe 13, a sedimentation cavity 42, a gold-absorbing electromagnet 43 and a one-way water inlet pipe 45, wherein the sedimentation plate 11 is arranged on the inner wall of the bottom of the solution treatment tank 2, a plurality of groups of sedimentation ports 12 are arranged on the upper wall of the sedimentation plate 11, the sedimentation cavity 42 is arranged between the bottom wall of the sedimentation plate 11 and the bottom wall of the solution treatment tank 2, the gold-absorbing electromagnet 43 is arranged on the bottom wall of the sedimentation cavity 42, a plurality of groups of sedimentation pipes 13 penetrate through the solution treatment tank 2 and are communicated with the inside of the sedimentation cavity 42, and the one-way water inlet pipe 45 is arranged on the outer side of the sedimentation pipe 13; the reduction reaction mechanism 14 comprises a heating cylinder 15, a metal ball cylinder 16, a high-frequency coil 17, a heat-insulating annular plate 18 and a metal tube 19, wherein a plurality of groups of the heating cylinders 15 are penetrated through the upper wall of the annular plate 3, the heating cylinders 15 are penetrated, the metal ball cylinder 16 is arranged on the bottom wall of the heating cylinder 15, the high-frequency coil 17 is arranged on the inner wall of the heating cylinder 15, the heat-insulating annular plate 18 is arranged on one side, far away from the solution treatment tank 2, of the purifying tube 9, the metal tube 19 is arranged on one side, far away from the purifying tube 9, of the heat-insulating annular plate 18, one end, far away from the metal tube 19, penetrates through the high-frequency coil 17 and is communicated with the upper wall of the metal ball cylinder 16, and one end, far away from the precipitating cavity 42, of the precipitating tube 13 is communicated with the bottom wall of the metal ball cylinder 16; the reaction medium driving mechanism 20 comprises a driving box 21, a pressure container 22, a pulse generator 23, an annular pipe 24, a jet head 25, a hydrogen pipe 26, a pressure relief valve 27, a one-way air inlet valve 28 and a return pipe 44, wherein the driving box 21 is respectively arranged on the bottom wall of the water supply plate 6 and the upper wall of the sedimentation plate 11, the pressure container 22 is arranged between the driving boxes 21, the pulse generator 23 is arranged inside the driving box 21, the power end of the pulse generator 23 penetrates through the driving box 21 and is arranged inside the pressure container 22, the annular pipe 24 penetrates through and is arranged between the metal ball cylinders 16, the jet head 25 is communicated with the upper wall of the annular pipe 24 which is arranged inside the metal ball cylinders 16, the hydrogen pipe 26 penetrates through the solution treatment box 2 and is arranged between the pressure container 22 and the annular pipe 24, the pressure relief valve 27 is arranged outside the hydrogen pipe 26, the return pipe 44 penetrates through the solution treatment box 2 and is communicated between the metal ball cylinders 16 and the pressure container 22, and the one-way air inlet valve 28 is arranged outside the return pipe 44.
The telescopic filtering mechanism 30 comprises sliding blocks 31, an elastic filtering layer 32, a telescopic drain pipe 33, a drain joint 34 and a water suction port 46, wherein a plurality of groups of sliding blocks 31 are respectively arranged on the inner wall of the solution treatment tank 2 and the side wall of the pressure container 22 in a sliding manner, the elastic filtering layer 32 is arranged between the sliding blocks 31, the telescopic drain pipe 33 penetrates through the solution treatment tank 2 and is arranged on the upper wall of the elastic filtering layer 32, and the water suction port 46 is arranged at one end, close to the elastic filtering layer 32, of the drain joint 34; the gravity change mechanism 35 comprises a gravity plate 36, a buoyancy air bag 37, a magnetic material layer 38, a buoyancy electromagnet 39 and a gravity ball 40, wherein a plurality of groups of gravity plates 36 are arranged on the bottom wall of the sliding block 31, the buoyancy air bag 37 is arranged on the bottom wall of the gravity plate 36, the magnetic material layer 38 and the buoyancy electromagnet 39 are respectively arranged on the inner wall of the buoyancy air bag 37, and the gravity ball 40 is arranged on one side, far away from the gravity plate 36, of the buoyancy air bag 37.
The upper wall of the base plate 1 is provided with a controller 41.
The controller 41 is electrically connected with the gold-attracting electromagnet 43, the high-frequency coil 17, the pulse generator 23 and the buoyancy electromagnet 39 respectively.
The controller 41 is of the type SYC89C52RC-401.
In specific use, according to the first embodiment, during use, turbid water solution generated after cleaning the pipeline enters the water supply cavity 7 through the turbid liquid joint 8 to be split, and the pressure relief value of the pressure relief valve 27 is adjusted.
Specifically, turbid liquid in the water supply cavity 7 flows into the metal tube 19 through the purifying tube 9, the controller 41 controls the high-frequency coil 17 to start, the high-frequency coil 17 is electrified to heat the metal tube 19, the temperature of the metal tube 19 rises to conduct heat to the interior of the metal ball tube 16, the temperature of the metal ball tube 16 rises, the controller 41 controls the pulse generator 23 to start, the pulse generator 23 emits pulse waves to the interior of the pressure vessel 22 through a power end, the pressure in the interior of the pressure vessel 22 increases to exceed a preset pressure value of the pressure relief valve 27, the pressure relief valve 27 is opened, the hydrogen tube 26 is conducted, hydrogen in the interior of the pressure vessel 22 enters the annular tube 24 through the hydrogen tube 26, the hydrogen in the interior of the annular tube 24 is sprayed out through the jet head 25, the pulse generator 23 intermittently emits pulse waves to the interior of the pressure vessel 22, the hydrogen intermittently sprays turbid aqueous solution from the jet head 25, the hydrogen breaks the aqueous solution under the impact force of the pulse waves, the dispersed aqueous solution falls down along the inner wall of the metal ball tube 16, rust in the aqueous solution is exposed to contact with the hydrogen at high temperature, and the rust in the aqueous solution reacts with the hydrogen at high temperature under the high temperature;
turbid liquid falls to the bottom of the metal ball cylinder 16, turbid liquid at the bottom of the metal ball cylinder 16 enters the inside of the sedimentation cavity 42 through the sedimentation pipe 13, the controller 41 controls the gold-absorbing electromagnet 43 to start, the gold-absorbing electromagnet 43 is electrified to generate magnetism, turbid liquid in the sedimentation cavity 42 enters the inside of the solution treatment box 2 through the sedimentation port 12 to be filtered, the gold-absorbing electromagnet 43 adsorbs and deposits reduced rust, along with rising of turbid liquid, rust which is not completely reduced in the interior is pulled to a position close to the bottom of the solution treatment box 2 under the attraction of the magnetic force of the gold-absorbing electromagnet 43, further, the rising of rust along with the flowing of turbid liquid is avoided, rust impurities in the interior of the turbid liquid close to one end of the elastic filter layer 32 are less, and better filtering operation of turbid liquid is facilitated.
In the second embodiment, based on the above embodiment, in the initial state, the telescopic drain pipe 33 is in an extended state, and the slider 31 is positioned at the bottom of the solution treatment tank 2 under the gravity action of the gravity ball 40.
Specifically, as more turbid liquid enters the solution treatment tank 2, the controller 41 controls the buoyancy electromagnet 39 to start, the buoyancy electromagnet 39 is electrified to generate magnetism, the buoyancy electromagnet 39 magnetizes the magnetic material layer 38, the magnetic material layer 38 magnetizes and releases heat, the magnetic material layer 38 heats the gas in the buoyancy air bag 37, the buoyancy air bag 37 swells to increase the buoyancy, the buoyancy of the buoyancy air bag 37 is larger than the gravity of the gravity ball 40, at the moment, the sliding block 31 slides up along the space between the inner wall of the solution treatment tank 2 and the side wall of the pressure container 22 under the action of the buoyancy, the turbid liquid is prevented from directly penetrating the elastic filter layer 32 under the action of precipitation, and the elastic filter layer 32 stretches and shortens under the action of the elastic force when sliding along the space between the inner wall of the solution treatment tank 2 and the side wall of the pressure container 22;
after all turbid liquid enters the solution treatment tank 2, the turbid liquid entering the solution treatment tank 2 is subjected to standing precipitation, the controller 41 controls the current amount introduced into the gold-absorbing electromagnet 43 to be increased, the magnetic force of the gold-absorbing electromagnet 43 is enhanced, the precipitation speed of rust impurities in the turbid liquid is accelerated, more rust is adsorbed when the turbid liquid is filtered on the elastic filter layer 32, on one hand, the content of the impurities in the filtered turbid liquid is ensured to be lower, on the other hand, the probability of adhering rust on the surface of the elastic filter layer 32 is reduced, the elastic filter layer 32 is prevented from being corroded by rust when the elastic filter layer 32 is not used, and the service life of the elastic filter layer 32 is prolonged;
after impurities in turbid liquid in the solution treatment box 2 are precipitated, the controller 41 controls the magnetic force of the buoyancy electromagnet 39 to weaken, the magnetization intensity of the buoyancy electromagnet 39 to the magnetic material layer 38 is reduced, the heating temperature of the magnetic material layer 38 to the air in the buoyancy air bag 37 is reduced, the volume of the buoyancy air bag 37 is reduced, the buoyancy force of the gravity ball 40 is larger than that of the buoyancy air bag 37, the gravity ball 40 drives the elastic filter layer 32 to reach the position below the turbid liquid level, the water suction port 46 is submerged below the liquid level, the water suction port 46 is connected with the water discharge joint 34 through the external water pumping device, the water solution enters the telescopic water discharge pipe 33 through the water suction port 46, the water solution is discharged through the water discharge joint 34, the buoyancy force of the buoyancy air bag 37 is continuously reduced, along with the discharge of the turbid liquid, the gravity ball 40 drives the elastic filter layer 32 to be always located at the position below the liquid level, sufficient precipitation time is left for the turbid liquid near one end of the precipitation cavity 42, the turbid liquid is convenient for completing reaction inside the turbid liquid or rust impurities which are not completely reacted, contact between rust and the elastic filter layer 32 is greatly reduced, and the turbid liquid is greatly filtered, and the turbid liquid is filtered by the elastic filter layer 32; repeating the above operation when using next time.
It is noted that relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Moreover, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Although embodiments of the present solution have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations may be made to these embodiments without departing from the principles and spirit of the solution, the scope of which is defined in the appended claims and their equivalents.
The present embodiment and the embodiments thereof have been described above with no limitation, and the embodiment shown in the drawings is merely one of the embodiments of the present embodiment, and the actual structure is not limited thereto. In summary, if one of ordinary skill in the art is informed by this disclosure, a structural manner and an embodiment similar to the technical solution should not be creatively devised without departing from the gist of the technical solution.
Claims (10)
1. The utility model provides a muddy water solution's filtration equipment, includes bottom plate (1), solution treatment case (2) and annular plate (3), its characterized in that: still include solution reduction type precipitation mechanism (4) and flexible type filter mechanism (29), solution treatment case (2) are located bottom plate (1) upper wall, solution treatment case (2) outside is located to annular slab (3), solution reduction type precipitation mechanism (4) are located on solution treatment case (2), inside solution treatment case (2) is located to flexible type filter mechanism (29), solution reduction type precipitation mechanism (4) are including reposition of redundant personnel water supply mechanism (5), sediment treatment mechanism (10), reduction reaction mechanism (14) and reaction medium actuating mechanism (20), solution treatment case (2) upper wall is located to reposition of redundant personnel water supply mechanism (5), solution treatment case (2) diapire is located to sediment treatment mechanism (10), on annular slab (3) are located to reduction reaction mechanism (14), solution treatment case (2) are inside is located to reaction medium actuating mechanism (20), flexible type filter mechanism (29) are including flexible filter mechanism (30) and gravity change mechanism (35), flexible change mechanism (30) are located on solution treatment case (2).
2. A filtration device for turbid aqueous solutions according to claim 1, characterized in that: the utility model provides a water supply device, including reposition of redundant personnel water supply mechanism (5), water supply board (6), water supply chamber (7), turbid liquid connect (8) and purifying pipe (9), water supply board (6) are located solution treatment case (2) top inner wall, water supply chamber (7) are located between water supply board (6) upper wall and solution treatment case (2) roof, turbid liquid connects (8) to locate solution treatment case (2) upper wall, turbid liquid connects (8) to run through solution treatment case (2) and water supply chamber (7) intercommunication, multiunit purifying pipe (9) run through solution treatment case (2) intercommunication and locate water supply chamber (7) inside.
3. A filtration device for turbid aqueous solutions according to claim 2, characterized in that: the sedimentation treatment mechanism (10) comprises a sedimentation plate (11), a sedimentation opening (12), a sedimentation pipe (13), a sedimentation cavity (42), a gold-absorbing electromagnet (43) and a one-way water inlet pipe (45), wherein the sedimentation plate (11) is arranged on the inner wall of the bottom of the solution treatment box (2), and a plurality of groups of sedimentation openings (12) are arranged on the upper wall of the sedimentation plate (11).
4. A filtration device for turbid aqueous solutions according to claim 3, characterized in that: the sedimentation chamber (42) is arranged between the bottom wall of the sedimentation plate (11) and the bottom wall of the solution treatment box (2), the gold-absorbing electromagnets (43) are arranged on the bottom wall of the sedimentation chamber (42), a plurality of groups of sedimentation pipes (13) penetrate through the solution treatment box (2) and are communicated with the inside of the sedimentation chamber (42), and the one-way water inlet pipes (45) are arranged on the outer sides of the sedimentation pipes (13).
5. The filtration apparatus for turbid aqueous solutions according to claim 4, wherein: the reduction reaction mechanism (14) comprises a heating cylinder (15), a metal ball cylinder (16), a high-frequency coil (17), a heat insulation annular plate (18) and a metal tube (19), wherein a plurality of groups of heating cylinders (15) are penetrated through the upper wall of the annular plate (3), the heating cylinders (15) are penetrated, the metal ball cylinder (16) is arranged on the bottom wall of the heating cylinder (15), and the high-frequency coil (17) is arranged on the inner wall of the heating cylinder (15).
6. The filtration apparatus for turbid aqueous solutions according to claim 5, wherein: the utility model discloses a solution treatment box, including purifying tube (9), metal tube (19) are located purifying tube (9), metal tube (18) are located one side of keeping away from purifying tube (9), metal tube (19) are kept away from one end of thermal-insulated annular plate (18) and are run through high frequency coil (17) intercommunication and locate metal ball section of thick bamboo (16) upper wall, one end intercommunication that sedimentation chamber (42) was kept away from to sedimentation tube (13) is located metal ball section of thick bamboo (16) diapire.
7. The filtration apparatus for turbid aqueous solutions according to claim 6, wherein: the reaction medium driving mechanism (20) comprises a driving box (21), a pressure vessel (22), a pulse generator (23), an annular pipe (24), a jet head (25), a hydrogen pipe (26), a pressure release valve (27), a one-way air inlet valve (28) and a return pipe (44), wherein the driving box (21) is respectively arranged on the bottom wall of the water supply plate (6) and the upper wall of the sedimentation plate (11), the pressure vessel (22) is arranged between the driving boxes (21), the pulse generator (23) is arranged inside the driving boxes (21), and the power end of the pulse generator (23) penetrates through the driving boxes (21) to be arranged inside the pressure vessel (22).
8. The filtration apparatus for turbid aqueous solutions according to claim 7, characterized in that: the utility model discloses a hydrogen gas treatment device, including metal ball section of thick bamboo (16), annular pipe (24), jet head (25) intercommunication is located between metal ball section of thick bamboo (16), annular pipe (24) upper wall inside metal ball section of thick bamboo (16) is located in jet head (25) intercommunication, hydrogen pipe (26) run through solution treatment case (2) intercommunication and locate between pressure vessel (22) and annular pipe (24), the relief valve (27) are located hydrogen pipe (26) outside, back flow (44) run through solution treatment case (2) intercommunication and locate between metal ball section of thick bamboo (16) and pressure vessel (22), one-way admission valve (28) are located back flow (44) outside.
9. The filtration apparatus for turbid aqueous solutions according to claim 8, wherein: the telescopic filtering mechanism (30) comprises a sliding block (31), an elastic filtering layer (32), a telescopic drainage pipe (33), a drainage joint (34) and a water suction port (46), wherein a plurality of groups of sliding blocks (31) are respectively arranged on the inner wall of the solution treatment box (2) and the side wall of the pressure container (22) in a sliding mode, the elastic filtering layer (32) is arranged between the sliding blocks (31), the telescopic drainage pipe (33) penetrates through the solution treatment box (2) to be arranged on the upper wall of the elastic filtering layer (32), and the water suction port (46) is arranged at one end, close to the elastic filtering layer (32), of the drainage joint (34).
10. The filtration apparatus for turbid aqueous solutions according to claim 9, characterized in that: the gravity change mechanism (35) comprises a gravity plate (36), a buoyancy air bag (37), a magnetic material layer (38), a buoyancy electromagnet (39) and a gravity ball (40), wherein a plurality of groups of gravity plates (36) are arranged on the bottom wall of the sliding block (31), the buoyancy air bag (37) is arranged on the bottom wall of the gravity plate (36), the magnetic material layer (38) and the buoyancy electromagnet (39) are respectively arranged on the inner wall of the buoyancy air bag (37), and the gravity ball (40) is arranged on one side, far away from the gravity plate (36), of the buoyancy air bag (37).
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