CN108726645A - Crystallite clarifier - Google Patents
Crystallite clarifier Download PDFInfo
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- CN108726645A CN108726645A CN201710260053.0A CN201710260053A CN108726645A CN 108726645 A CN108726645 A CN 108726645A CN 201710260053 A CN201710260053 A CN 201710260053A CN 108726645 A CN108726645 A CN 108726645A
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- Prior art keywords
- crystallite
- shell
- hollow out
- clarifier
- cathode electrode
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- 229910052751 metal Inorganic materials 0.000 claims abstract description 5
- 239000002184 metal Substances 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 18
- 239000013081 microcrystal Substances 0.000 claims description 13
- 238000009833 condensation Methods 0.000 claims description 12
- 230000005494 condensation Effects 0.000 claims description 12
- 229910052755 nonmetal Inorganic materials 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 8
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 6
- 239000013078 crystal Substances 0.000 claims description 6
- 230000005611 electricity Effects 0.000 claims description 4
- 229910000838 Al alloy Inorganic materials 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims description 3
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 229910052681 coesite Inorganic materials 0.000 claims description 3
- 229910052906 cristobalite Inorganic materials 0.000 claims description 3
- 238000013461 design Methods 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 235000012239 silicon dioxide Nutrition 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 229910052682 stishovite Inorganic materials 0.000 claims description 3
- 229910052905 tridymite Inorganic materials 0.000 claims description 3
- 239000008187 granular material Substances 0.000 claims description 2
- 238000001816 cooling Methods 0.000 abstract description 9
- 239000007921 spray Substances 0.000 abstract description 8
- 239000000498 cooling water Substances 0.000 abstract description 5
- 238000012545 processing Methods 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 38
- 239000011257 shell material Substances 0.000 description 23
- 238000005260 corrosion Methods 0.000 description 13
- 230000007797 corrosion Effects 0.000 description 13
- 230000000694 effects Effects 0.000 description 11
- 150000002500 ions Chemical class 0.000 description 10
- 239000003513 alkali Substances 0.000 description 8
- 241000894006 Bacteria Species 0.000 description 7
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 6
- 238000012546 transfer Methods 0.000 description 6
- 238000007596 consolidation process Methods 0.000 description 5
- 238000000746 purification Methods 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 230000001408 fungistatic effect Effects 0.000 description 3
- 239000011777 magnesium Substances 0.000 description 3
- 229910052749 magnesium Inorganic materials 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 206010037211 Psychomotor hyperactivity Diseases 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 229910052796 boron Inorganic materials 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 230000005684 electric field Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000002708 enhancing effect Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000002401 inhibitory effect Effects 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 230000000087 stabilizing effect Effects 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 238000010408 sweeping Methods 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- 239000010936 titanium Substances 0.000 description 2
- 229910052726 zirconium Inorganic materials 0.000 description 2
- 206010010356 Congenital anomaly Diseases 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 241000589248 Legionella Species 0.000 description 1
- 208000007764 Legionnaires' Disease Diseases 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 210000001367 artery Anatomy 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 235000019628 coolness Nutrition 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000009851 ferrous metallurgy Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 230000001568 sexual effect Effects 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000002352 surface water Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- 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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/463—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/48—Devices for applying magnetic or electric fields
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/04—Disinfection
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses a kind of crystallite clarifiers, it includes:DC power supply;Cathode electrode carries the metal shell of hollow out;It is placed in several crystallite blocks of the metal shell Inner of hollow out;Anode electrode is placed among two adjacent crystallite blocks;Anode electrode connects the anode of power supply, and cathode electrode connects the cathode of power supply;Controller is connected between DC power supply and cathode electrode or between DC power supply and anode electrode, energization and power-off for controlling anode electrode and cathode electrode, it is mainly used for the processing of vaporation-type cooling device spray recirculated cooling water.
Description
Technical field
The present invention relates to water treatment facilities, more particularly to a kind of vaporation-type cooling(Condensation)Device spray recirculated cooling water
Processing equipment, that is, crystallite clarifier.
Background technology
Vaporation-type cools down(Condensation)Equipment is a kind of to cool down water-cooled(Condensation)Device with open cooling tower be combined to
Air discharges the common apparatus of waste heat.When cooled working medium without phase-change when, referred to as " evaporative type cooler ", and cooled working medium
To be then commonly referred to as when liquid water " closed cooling tower ";When cooled working medium has phase transformation, should be known as " evaporative condenser ".It is this kind of
It is all a dividing wall type heat exchanger that equipment, which has identical structure, core, is cooled(Condensation)Working medium is in dividing wall type heat exchanger
Side is flowed, and spray water and air flows in the outside of dividing wall type heat exchanger, and heat is to be transmitted to shower water, spray through heat exchanger wall surface
Water drenching is transmitted to air by evaporation and heat convection again.Vaporation-type cools down(Condensation)Equipment it is compact-sized, floor space is few, always
Physical efficiency consumption is small, and operating cost is low, and service life is also longer.With increasingly deficient and national energy conservation and emission reduction policy the reality of water resource
It applies, vaporation-type cooling(Condensation)Equipment has obtained extensively in industries such as Ferrous Metallurgy, power electronics, mechanical chemical industry, Heating,Ventilating and Air Conditioning
Application.
It is cooled down in vaporation-type(Condensation)In equipment, since shower water is only used as intermediate heat transfer medium, generally certainly by equipment
The spray pump of band recycles inside equipment, and flow is short, and system volume is small, and closure is good, and windage loss controls also seldom, therefore
The evaporation and concentration of shower water is fast, and fouling tendency is strong;Fouling is fast on cooling tube sheet and filler, not easy cleaning;Variation water quality is big, and system is slow
Punching property is small;Handling of Stabilizing Water Quality workload is opposite big, technical operation workload and economy ratio, income very little.Normal conditions
Under, water-spray system is difficult to stabilizing water quality using traditional chemistry or electronic anti-scaling method, and fouling, corrosion and bacterium algae problem can be very
It is fast out of control, therefore need to often take cleaning operation.Due to " congenital " limitation in Stability Technique of Water Quality, " artificial " factor can not avoid,
Directly influence economical, the efficient and reasonability of operation.
Invention content
Technical problem to be solved by the invention is to provide a kind of coolings of vaporation-type(Condensation)Device spray recirculated cooling water
Processing equipment, that is, crystallite clarifier, technical solution used by it is:A kind of crystallite clarifier, it includes:DC power supply;It is cloudy
Pole electrode carries the shell of hollow out;It is placed in several crystallite blocks of the shell Inner of hollow out;Anode electrode is placed in adjacent
Two crystallite blocks among;Anode electrode connects the anode of power supply, and cathode electrode connects the cathode of power supply;DC power supply and cathode
Controller is connected between electrode or between DC power supply and anode electrode, the energization for controlling anode electrode and cathode electrode
And power-off.
The further technical characteristic of the present invention is:
The cathode electrode is the sheet metal shell with hollow out.
The cathode electrode is the stainless steel materials shell with hollow out, or the carbon sheet shell with hollow out or band
There are the aluminum alloy plate materials shell of hollow out, or the zinc-plated plank shell with hollow out.
The anode electrode is titanium alloy thin slice or lead thin slice.
The crystallite block includes the non-metal shell with hollow design and the micro crystal material that is placed in non-metal shell.
The micro crystal material includes the Na2O of 10--30%, the B2O3 of the SiO2 of 30--50%, 15--55%, 0.50-
It is unformed micro- less than 5 microns to form crystal grain for 5.0% Al2O3,0.05-0.5% ZrO2, the rapid condensation after melt process
Crystal structure.
The size of hollow out is less than the grain for being placed in the micro crystal material in non-metal shell on non-metal shell in the crystallite block
Spend size.
The crystallite block and surrounding cathode electrode are that the gap between the shell with hollow out is 10---150mm.
The beneficial effects of the invention are as follows:
Due to being provided with crystallite block in the present invention, crystallite micro crystal material in the block will produce crystallite member, lure inhale fine suspension at
The nuclei of crystallization adsorb calcium and magnesium and alkali ion enrichment in water and combine, agglomerate for sub-micro crystal grain, consolidation and lose adhesive force, no
The surface for being deposited on heat-transfer equipment easily is analysed, plays the role of clearing up water quality fouling tendency, purification heat-transfer area, it can step solution water quality
Problem.
Traditional Stability Technique of Water Quality is to stablize fouling tendency salinity in water by various technical measures;Crystallite purification techniques phase
Instead, fouling tendency salinity in water is induced to form consolidation particle, the collecting-tank area of slack water for flowing to water system deposits, and directly eliminates and changes
The dirt in hot face, cooling tower and pipe surface analyses hidden danger.Meet second law of thermodynamics principle, practice test dynamic method
It is feasible.
The features such as microstructure has specific surface big, and surface adsorption property is strong, high surface activity.In activated state wafer
Sodium, element silicon overactivity can be enriched with being reacted at dirt ion and alkali ion in water, promote fouling to generate and be condensed into sand
It is granular.Sweeping along in water bacterium and growth matrix to condense upon in nucleus, calcium carbonate simultaneously makes it lose activity, and microorganism is inhibited to grow
Raw, biological clay is adsorbed in dirty grain and loses adhesiveness.
Boron, zr element have resistance to certain corrosion resistance, and the especially corrosion resistance of zirconium is better than titanium, very to the affinity of oxygen
By force, energy crystal grain thinning, hardness and very high strength with superelevation have excellent corrosion resistance to a variety of acid, alkali and salt, reduce table
Sensibility of the surface state to corrosion.Highly enriched water quality belongs to strong fouling tendency simultaneously, itself has certain corrosion inhibitive function.
The energization and power-off that anode electrode and cathode electrode are controlled by controller, can form impulse electric field, in pulse
Under current field condition, enhancing crystallite wafer activity accelerates rate of release, and directional push wafer and scale-forming ion expel crystallite block, and
It is relatively moved with alkali ion, reinforces combining probability.The electric microfield effect of crystallite clarifier, which plays to orient, simultaneously gathers fouling
Effect.
In addition because micro voltage field changes the bioelectrical of bacterium, certain fungistatic effect is also functioned to.
Description of the drawings
Fig. 1 is the structural perspective of one embodiment of the invention;
Fig. 2 is the stereogram of cathode electrode in Fig. 1.
Specific implementation mode
The present invention will be further described below in conjunction with the accompanying drawings:
Fig. 1 is the structural schematic diagram of one embodiment of the invention, and in the present embodiment, a kind of crystallite clarifier includes:DC power supply
1;Cathode electrode 2 carries the shell of hollow out(As shown in Figure 2);It is placed in several crystallite blocks 3 of the shell Inner of hollow out;
Anode electrode 4 is placed among two adjacent crystallite blocks;Anode electrode 4 connects the anode of power supply, and cathode electrode connects 2 and connects power supply
Cathode;Controller 5 is connected between DC power supply 1 and anode electrode 4, for controlling the logical of anode electrode 4 and cathode electrode 2
Electricity and power-off.Wherein the crystallite block 3 includes the non-metal shell with hollow design and the crystallite material that is placed in non-metal shell
Material(Do not show in figure).The micro crystal material includes the Na2O of 10--30%, the B2O3 of the SiO2 of 30--50%, 15--55%,
0.50-5.0% Al2O3,0.05-0.5% ZrO2, the rapid condensation after melt process form the nothing that crystal grain is less than 5 microns
Sizing microstructure.The size of hollow out is less than the micro crystal material being placed in non-metal shell on non-metal shell in the crystallite block
Granule size.The crystallite block 3 and surrounding cathode electrode 2 are that the gap between the shell with hollow out is 10---150mm.
Crystallite block 3 is provided with 8 in this implementation, can moderately be increased according to the amount of the recirculated water of processing in practical applications
Subtract, can also be 9,7,6,5,4,3.
In the present embodiment, the cathode electrode 2 is the stainless steel materials shell with hollow out, may be used also in practical applications
With using the carbon sheet shell with hollow out, or the aluminum alloy plate materials shell with hollow out, or the zinc-plated plank with hollow out
Shell.
In the present embodiment, the anode electrode 4 is titanium alloy thin slice, can also use lead thin slice in practical applications.
In addition in practical applications, controller 5 can also be arranged between DC power supply 1 and cathode electrode 2.
Due to being provided with crystallite block 3 in the present invention, the micro crystal material in crystallite block 3 will produce crystallite member, lures and inhales tiny hang
Float is adsorbed calcium and magnesium and alkali ion enrichment in water and is combined at the nuclei of crystallization, agglomerates for sub-micro crystal grain, consolidation and lose attachment
Power is not easy to analyse the surface for being deposited on heat-transfer equipment, plays the role of clearing up water quality fouling tendency, purification heat-transfer area, can a step solution
Certainly quality problem.
Crystallite clarifier of the present invention is cooled down for vaporation-type(Condensation)The processing of device spray recirculated cooling water, therefore to put
It is placed in recirculated cooling water, can be connected by recirculated water conduction between such anode electrode 4 and cathode electrode 2, pass through electricity
Source controller loads millivolt level micro voltage in two-stage(10--30mV);Under the catalysis of micro-current, microporous surface is continual and steady
Ground generates crystallite member, lures and inhales fine suspension into the nuclei of crystallization, adsorbs water Minerals salt(Based on calcium and magnesium)Enrichment is Asia in conjunction with cohesion
Microcrystal particles, consolidation and lose adhesive force, easily taken out of from circulation by flow, be deposited on area of slack water(Pool bottom
Portion), realize being purified from softening for water quality, it is ensured that system heat transfer clean surface.
Wafer, which equally lures suction bacterium and growth substrate to condense upon in nucleus, calcium carbonate, makes it lose activity.Simultaneously because of micro- electricity
It has a meeting, an audience, etc. well under one's control and changes the bioelectrical of bacterium and play fungistatic effect, eliminate Legionella pathogeny, purify air environment.
Due to being not added with chemical agent, corrosion of metal current potential is reduced, while it is played certainly by the strong fouling sexual orientation of water quality
The rust inhibition of body realizes system corrosion control.
Traditional Stability Technique of Water Quality is to stablize fouling tendency salinity in water by various technical measures;Crystallite purification techniques phase
Instead, fouling tendency salinity in water is induced to form consolidation particle, the collecting-tank area of slack water for flowing to water system deposits, and directly eliminates and changes
The dirt in hot face, cooling tower and pipe surface analyses hidden danger.Meet second law of thermodynamics principle, practice test dynamic method
It is feasible.
The features such as microstructure has specific surface big, and surface adsorption property is strong, high surface activity.In activated state wafer
Sodium, element silicon overactivity can be enriched with being reacted at dirt ion and alkali ion in water, promote fouling to generate and be condensed into sand
It is granular.Sweeping along in water bacterium and growth matrix to condense upon in nucleus, calcium carbonate simultaneously makes it lose activity, and microorganism is inhibited to grow
Raw, biological clay is adsorbed in dirty grain and loses adhesiveness.
Boron, zr element have resistance to certain corrosion resistance, and the especially corrosion resistance of zirconium is better than titanium, very to the affinity of oxygen
By force, energy crystal grain thinning, hardness and very high strength with superelevation have excellent corrosion resistance to a variety of acid, alkali and salt, reduce table
Sensibility of the surface state to corrosion.Highly enriched water quality belongs to strong fouling tendency simultaneously, itself has certain corrosion inhibitive function.
By the energization and power-off of 5 anode electrode 4 processed and cathode electrode 2 of controller control, impulse electric field can be formed, in arteries and veins
It rushes under current field condition, enhancing crystallite wafer activity accelerates rate of release, and directional push wafer and scale-forming ion expel crystallite block,
And relatively moved with alkali ion, reinforce combining probability.While the electric microfield effect of crystallite clarifier plays orientation and gathers fouling
Effect.
In addition because micro voltage field changes the bioelectrical of bacterium, certain fungistatic effect is also functioned to.
The technology contents and technical characterstic of the present invention have revealed that as above, it being understood, however, that in the creative ideas of the present invention
Under, those skilled in the art can make various changes and improve to above structure, including individually disclose or be claimed here
Technical characteristic combination, it will be apparent that other combinations including these features.These deformations and/or combination each fall within institute of the present invention
In the technical field being related to, and fall into the protection domain of the claims in the present invention.
Claims (8)
1. a kind of crystallite clarifier, it is characterised in that including:
DC power supply;
Cathode electrode carries the shell of hollow out;
It is placed in several crystallite blocks of the shell Inner with hollow out;
Anode electrode is placed among two adjacent crystallite blocks;
Anode electrode connects the anode of power supply, and cathode electrode connects the cathode of power supply;
Controller is connected between DC power supply and cathode electrode or between DC power supply and anode electrode, for controlling anode electricity
The energization and power-off of pole and cathode electrode.
2. crystallite clarifier as described in claim 1, it is characterised in that:The cathode electrode is the sheet metal with hollow out
Shell.
3. crystallite clarifier as claimed in claim 2, it is characterised in that:The cathode electrode is the stainless steel plate with hollow out
Material shell, or the carbon sheet shell with hollow out, or the aluminum alloy plate materials shell with hollow out, or the galvanized sheet with hollow out
Material shell.
4. crystallite clarifier as described in claim 1, it is characterised in that:The anode electrode is that titanium alloy thin slice or lead are thin
Piece.
5. the crystallite clarifier as described in any claim in claim 1-4, it is characterised in that:The crystallite block includes band
The non-metal shell of hollow design and the micro crystal material being placed in non-metal shell.
6. crystallite clarifier as claimed in claim 5, it is characterised in that:The micro crystal material includes the Na2O of 10--30%,
The B2O3 of the SiO2 of 30--50%, 15--55%, 0.50-5.0% Al2O3,0.05-0.5% ZrO2, after melt process
Rapid condensation forms the unformed microstructure that crystal grain is less than 5 microns.
7. crystallite clarifier as claimed in claim 6, it is characterised in that:In the crystallite block on non-metal shell hollow out it is big
It is less than the granule size for being placed in the micro crystal material in non-metal shell.
8. crystallite clarifier as described in claim 1, it is characterised in that:The crystallite block and surrounding cathode electrode are band hollow out
Shell between gap be 10---150mm.
Priority Applications (1)
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CN201710260053.0A CN108726645B (en) | 2017-04-20 | 2017-04-20 | Microcrystal purifier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201710260053.0A CN108726645B (en) | 2017-04-20 | 2017-04-20 | Microcrystal purifier |
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Publication Number | Publication Date |
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CN108726645A true CN108726645A (en) | 2018-11-02 |
CN108726645B CN108726645B (en) | 2024-04-30 |
Family
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CN201710260053.0A Active CN108726645B (en) | 2017-04-20 | 2017-04-20 | Microcrystal purifier |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113772864A (en) * | 2021-08-30 | 2021-12-10 | 上海润风智能科技有限公司 | Zero-emission process method for more efficiently utilizing waste heat |
Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08103626A (en) * | 1994-10-06 | 1996-04-23 | Chiyoda Corp | Method for desulfurizing waste gas |
CN1266825A (en) * | 1999-03-05 | 2000-09-20 | 华电(蓬莱)铸石有限公司 | Modified cast stone |
CN2726715Y (en) * | 2004-09-29 | 2005-09-21 | 浙江大学 | Electrochemical regenerating device of active carbon |
CN101613136A (en) * | 2008-06-02 | 2009-12-30 | 世界矿物公司 | Be used to prevent and reduce the method that fouling forms |
CN203144183U (en) * | 2013-02-01 | 2013-08-21 | 武汉新大创新水处理技术有限公司 | Online dirt absorbing device |
CN104230012A (en) * | 2014-10-02 | 2014-12-24 | 蔡宜芳 | Production method and application of high-performance scale inhibiting material |
CN104338424A (en) * | 2013-08-05 | 2015-02-11 | 北京生泰宝科技有限公司 | Ecological air purification system and purification system |
CN105330029A (en) * | 2014-08-07 | 2016-02-17 | 青岛海尔智能技术研发有限公司 | Water supply device and descaling method for same |
CN206680227U (en) * | 2017-04-20 | 2017-11-28 | 韩寒 | Crystallite clarifier |
-
2017
- 2017-04-20 CN CN201710260053.0A patent/CN108726645B/en active Active
Patent Citations (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08103626A (en) * | 1994-10-06 | 1996-04-23 | Chiyoda Corp | Method for desulfurizing waste gas |
CN1266825A (en) * | 1999-03-05 | 2000-09-20 | 华电(蓬莱)铸石有限公司 | Modified cast stone |
CN2726715Y (en) * | 2004-09-29 | 2005-09-21 | 浙江大学 | Electrochemical regenerating device of active carbon |
CN101613136A (en) * | 2008-06-02 | 2009-12-30 | 世界矿物公司 | Be used to prevent and reduce the method that fouling forms |
CN203144183U (en) * | 2013-02-01 | 2013-08-21 | 武汉新大创新水处理技术有限公司 | Online dirt absorbing device |
CN104338424A (en) * | 2013-08-05 | 2015-02-11 | 北京生泰宝科技有限公司 | Ecological air purification system and purification system |
CN105330029A (en) * | 2014-08-07 | 2016-02-17 | 青岛海尔智能技术研发有限公司 | Water supply device and descaling method for same |
CN104230012A (en) * | 2014-10-02 | 2014-12-24 | 蔡宜芳 | Production method and application of high-performance scale inhibiting material |
CN206680227U (en) * | 2017-04-20 | 2017-11-28 | 韩寒 | Crystallite clarifier |
Non-Patent Citations (1)
Title |
---|
屈东凌;: "选矿厂立环强磁机冷却水净化除盐系统的运用", 包钢科技, no. 1 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113772864A (en) * | 2021-08-30 | 2021-12-10 | 上海润风智能科技有限公司 | Zero-emission process method for more efficiently utilizing waste heat |
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