CN201932938U - Device for preparing ferron used for water treatment - Google Patents
Device for preparing ferron used for water treatment Download PDFInfo
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- CN201932938U CN201932938U CN2010206713279U CN201020671327U CN201932938U CN 201932938 U CN201932938 U CN 201932938U CN 2010206713279 U CN2010206713279 U CN 2010206713279U CN 201020671327 U CN201020671327 U CN 201020671327U CN 201932938 U CN201932938 U CN 201932938U
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/33—Wastewater or sewage treatment systems using renewable energies using wind energy
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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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
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Abstract
The utility model relates to a device for preparing ferron used for water treatment, which comprises a power supply (1), an iron source generator (9) and an electrolyte storage tank (2), wherein the iron source generator (9) consists of one-stage or multistage tubular generating units (10); each tubular generating unit (10) comprises an insulating tube body (6) and an anode layer and a cathode layer which are embedded; an annular channel for liquid circulation is arranged between the anode layer and the cathode layer; the electrolyte storage tank (2) is communicated to one end of the tubular generating unit through a pipeline; and the other end of the generating unit is provided with a liquid outlet (8). The device adopts a method of quickly and efficiently generating the high-concentration molten iron under the action of current and purifying a water body under the action of sedimentation and flocculation. The ferron prepared by the method can purify the water body quickly and has strong instantaneity, economical efficiency, environmental protection and industrial practicability.
Description
[technical field]
The utility model belongs to water technology.More specifically, the utility model relate to a kind of can be efficiently, fast, environmental protection, energy-conservation device and the using method thereof that obtains to be used for the ferron of water treatment.
[background technology]
The body eutrophication phenomenon is serious, a global day by day water environmental problems, its major cause is exactly that the water body that is rich in nutritive substances such as nitrogen, phosphorus enters in river or the lake, make algae and other waterplant hypertrophy in the water, thereby oxygen in water concentration is fallen sharply and cause the mass mortality of hydrocoles such as fish, finally make water body stench Heisui River that becomes, the havoc ecotope.The major cause that studies show that water nutrition phenomenons such as causing lake, reservoir is to cause owing to excessive phosphorus that people enter in the water body.Therefore, the phosphorus of how removing in the water is the subject matter place of control body eutrophication, be one of the key technical problem that can municipal effluent recycling that concerns, to improving the ecological environment and ensureing that the people's ordinary production life has important practical significance.
At present, the treatment technology that contains phosphorus water is mainly contained biological process, chemical method and electric flocculence; There are shortcomings such as floor space is big, dephosphorization efficiency by using is low, fluctuation of service in biological process, makes its application be subjected to certain restriction.Chemical method exists medicament to put easy inefficacy, the frequent preparating liquid of needs for a long time, management negatively charged ion loaded down with trivial details, that bring into causes shortcomings such as secondary pollution easily.
Chinese patent application CN 101269863A proposes to utilize the combination process of electricity flocculation and membrane bioreactor, adopting iron plate or aluminium sheet is that anode electrolysis produces iron ion or aluminum ion, form flco with hydroxide ion, phosphate anion in the sewage, organism forms mud after by the microbiological deterioration in the membrane bioreactor, be removed through the micro-filtrate membrane filtration pollutent, from sewage, remove phosphorus and organic purpose thereby reach.The electrochemical efficiency of this system is lower, and excessive, the electrode group of required electrode area too much in the biological tank, processing cost is bigger, and microorganism easily makes the battery lead plate inactivation, be not easy to problems such as through engineering approaches application.
Chinese patent application CN 101549896A proposes a kind of water treatment method of electrolysis nitrogen and phosphorus removal, adopt graphite and iron plate as electrode, by intermittently changing polarity of electrode, alternately change electrolysis dephosphorization and electrolysis nitrogen process, thereby be implemented in nitrogen, phosphorus nutrition salt and the organic pollutant of removing in the same electrolyzer in the waste water.But the concentration of these inorganic salt is low in municipal effluent, and the specific conductivity of solution is low, and electrolytic efficiency is low, and interelectrode distance is big, and energy consumption is bigger, and processing cost is higher.
In the tap water system, once had report to propose to use technology such as ion exchange method, reverse osmosis method and electroosmose process, but these technology are not suitable for the advanced treatment of phosphor in sewage because efficient is low and use expensive ion-exchange membrane.
[utility model content]
" technical problem that will solve "
The purpose of this utility model is to obtain a kind of ferron that can be used in water treatment, purification of water quality, is particularly conducive to Removal of Phosphorus in Wastewater, comprises the device and the using method thereof that prepare described ferron.
" technical scheme "
Principle of the present utility model is to be seated in the body circular channel that has electrolysis liquid to circulate between the two-layer electrode as the powder electrode is nested with iron or iron filings.Under the power supply effect, be nested in intravital iron of pipe or iron filings and form anode layer and cathode layer respectively.When electrolytic solution passes through in the tubulose generating unit, under electric current and iron effect, can produce high dense iron liquid apace, in the dense iron liquid of this height mainly based on ferrous ion and ferrous salt, the iron cpd reagent that also comprises states such as iron ion, ironic hydroxide, add the ferron that produced in the membrane bioreactor (MBR) then or handle in other staying waters, can play precipitation, flocculation and cleaning action.Particularly, when adopting this ferron to remove phosphorus in the dirty waste water, wherein the ferrous ion in the ferron can with the phosphate radical generation ferrous phosphate that reacts, remove with coprecipitation mode.Simultaneously, iron ion in the ferron and ironic hydroxide also can purify scrubbing to water quality by absorption, throwing out.
To achieve these goals, the utility model provides a kind of preparation facilities that is used for the ferron of water treatment, it is characterized in that this device comprises power supply 1, source of iron generating apparatus 9 and electrolytic solution container for storing liquid 2, wherein, described source of iron generating apparatus 9 is made up of one or more levels tubulose generating unit 10, each tubulose generating unit 10 comprises insulation body 6 and is wrapped in the anode layer and the cathode layer that are made of metal in the described insulation body 6, described anode layer is mutually nested with cathode layer, has the circular channel of circulation for liquid between described anode layer and the cathode layer, anode layer in the anode of described power supply and the tubulose generating unit 10 joins, its negative electrode and described cathode layer join, described electrolytic solution container for storing liquid 2 is communicated to an end of the circular channel of described tubulose generating unit by pipeline, the other end in the circular channel of described tubulose generating unit is provided with liquid outlet 8.
For mutually nested anode layer and cathode layer, which layer is in the outside, which layer is in the inboard, and preparation facilities of the present utility model and implementation result thereof are not constituted obvious visible influence.
For the source of iron generating apparatus of being made up of single-stage tubulose generating unit 10 9, preparation facilities of the present utility model is then comparatively simple, is made of power supply 1, source of iron generating apparatus 9 and electrolytic solution container for storing liquid 2.In tubulose generating unit 10, be provided with concentric anode layer and cathode layer, the circular channel that between anode layer and cathode layer, has electrolysis liquid to pass through.Power supply 1 anode and described anode layer join, and negative electrode and described cathode layer join.Electrolytic solution container for storing liquid 2 is communicated to an end of the circular channel of tubulose generating unit by pipeline, the other end in the circular channel of tubulose generating unit has liquid outlet 8.
Preferred embodiment a kind of according to the preparation facilities of ferron of the present utility model, source of iron generating apparatus 9 is made up of multistage tubulose generating unit 10.Each tubulose generating unit 10 is α °=0～90 ° with horizontal angle.
Wherein, the situation for α °=0 promptly becomes horizontal direction to settle between all tubulose generating units 10.Electrolytic solution in the container for storing liquid 2 by the circular channel of tubulose generating units at different levels, is discharged by the liquid outlet 8 of last step tubulose generating unit then at last by an end of pipeline inflow first step tubulose generating unit circular channel.
For α °=90 ° situation, promptly vertically connect between all tubulose generating units 10.Similarly, electrolytic solution in the container for storing liquid 2 flows into the upper end of first step tubulose generating unit circular channel by pipeline, under the effect of gravitional force, flow downward,, discharge by the liquid outlet 8 of last step tubulose generating unit lower end at last then by tubulose generating units at different levels.
For 0＜α °＜90 ° situation, then become the capable arrangement of Z between the adjacent tubular generating unit 10.Similar with second kind of situation, electrolytic solution in the container for storing liquid 2 flows into an end that is positioned at eminence of first step tubulose generating unit circular channel by pipeline, under the effect of gravitional force, flow downward, then by tubulose generating units at different levels, discharge by the liquid outlet 8 of last step tubulose generating unit lower end at last.Compare α °=90 ° situation, 0＜α °＜90 ° set-up mode more helps controlling flow velocity and reducing equipment volume, is preferred embodiment a kind of therefore.
According to the preparation facilities that is used for the ferron of water treatment of the present utility model, a kind of particularly preferred embodiment be described anode layer and cathode layer include the tubulose porous support materials, attached to the iron filings layer on described tubulose porous support materials surface be used for fixing the netted perviousness material layer of described iron filings layer, described iron filings layer is attached to the side of described tubulose porous support materials surface towards the circular channel.
Because in the utility model, the internal and external relation of anode layer and cathode layer is random.Then: when anode layer is positioned at the cathode layer inboard, in the cross section of tubulose generating unit, be respectively from inside to outside: tubulose porous support materials, iron filings layer (forming anode after connecting power supply), netted perviousness material layer, circular channel (be interelectrode distance, be used for the circulation of electrolytic solution), netted perviousness material layer, iron filings layer (forming negative electrode after connecting power supply), tubulose porous support materials, insulation body.
On the contrary, when cathode layer is positioned at the anode layer inboard, in the cross section of tubulose generating unit, be respectively from inside to outside: tubulose porous support materials, iron filings layer (forming negative electrode after connecting power supply), netted perviousness material layer, circular channel (be interelectrode distance, be used for the circulation of electrolytic solution), netted perviousness material layer, iron filings layer (forming anode after connecting power supply), tubulose porous support materials, insulation body.
In the utility model, preferably, the pipeline of described preparation facilities also comprises under meter 3.
In the utility model, the electrolytic solution that stores in the described electrolytic solution container for storing liquid 2 should be tart, and preferably the pH value is 3-5.More preferably, described electrolytic solution is the acidic solution that total mass concentration is 10% non-oxide reductibility to the maximum.
Term " acidic solution of non-oxide reductibility " should be understood to circular channel when circulation between anode and negative electrode, under galvanic action, in the solution except hydrogen ion and hydroxide ion other ions or group can not get betatopic and the acidic liquid of redox reaction takes place at electrode surface.
Because resistivity of water is bigger from the beginning, if adopt tap water as electrolytic solution, though also can realize the utility model, efficient is lower.Therefore, preferred embodiment select the solution of the salt that contains mineral acid and this mineral acid for use, play the effect that reduces resistance.Therefore, the total mass concentration of salt in solution of mineral acid and this mineral acid need not to surpass 10%.For example select the mixing solutions of the aqueous solution of hydrochloric acid and sodium-chlor for use, as long as hydrochloric acid and the total mass concentration of sodium-chlor in solution are lower than 10%, for example 0.1% hydrochloric acid and 1% sodium-chlor.
Under situation to the solution energising, the mineral acid of redox reaction and the salt of this mineral acid can not take place, specifiable also have for example sodium-acetate and acetic acid (for example sodium-acetate of 0.1% acetic acid+9%), vitriolate of tartar and dilute sulphuric acid etc., or the organic acid of employing difficult generation redox reaction under the energising effect is alternative, for example citric acid.
According to a kind of embodiment of preparation facilities of the present utility model, the length of described tubulose generating unit 10 is 100～1000mm; The thickness of the iron filings layer of described anode layer is 0～15mm; The thickness of the iron filings layer of described cathode layer is 0～15mm; Described circular channel width is 3～15mm; The mesh of described tubulose porous support materials is 40～500 orders, and the iron filings median size of described iron filings layer is 0.1～5mm.
When the iron filings layer thickness of anode layer and/or cathode layer is 0, become a kind of simple embodiment of preparation facilities of the present utility model, promptly do not use iron filings, only with iron tubulose porous support materials as anode layer and/or cathode layer.In this case, also need not to be provided for the fixedly netted perviousness material layer of iron filings naturally.Only also can implement design of the present utility model by electrolytic solution in as the circular channel between anode layer and the cathode layer with iron tubulose porous support materials.Yet in this embodiment, because the effect of electric current and electrolytic solution, meeting consumable anode layer and cathode layer (iron), so anode layer and cathode layer attenuation gradually, the permanent need afterwards changed.Although can implement, spent usefulness is more, and the industrial application feasibility is poor.
To be the preferred implementation of preparation facilities of the present utility model attached to the iron filings layer on the tubulose porous support materials as anode layer and cathode layer, promptly the iron filings layer thickness of anode layer and cathode layer is greater than 0, but need not to surpass 15mm.By netted perviousness material fixing after, when electrolytic solution in the circular channel of tubulose generating unit by the time, the iron filings of anode layer and cathode layer are consumed.Only need regularly to add iron filings and can implement this preparation facilities for a long time, spent reasonable.
In the utility model, described netted perviousness material layer should be understood to a kind ofly can wrap up, fix iron filings that the tubulose porous support materials adheres to outward and make it nonvoluntary and move, and the iron liquid of generation is unhinderedly flowed and durable Web materials.Described netted perviousness material layer can be by suitable stacked the forming of perviousness material in various apertures, for example by being selected from stainless (steel) wire, wire netting, tetrafluoroethylene screen cloth, fabric (for example cotton, gauze) or selecting the stacked composite bed that forms of one or more perviousness materials in the inert metal silk screens such as titanium, platinum, palladium, ruthenium, iridium for use.
In the utility model, described power supply 1 should be the pulse power or has the direct supply of changing positive and negative electrode polarity equipment, and wherein the positive-negative polarity replacement cycle is 5～300s.Described direct supply can be that alternating-current is converted to galvanic direct current of voltage regulation source device, also can be the store battery that is formed by sun power, wind energy, water energy, chemical energy or other Energy conversion.
More preferably, apply electric field between anode and negative electrode, making the average current density in the described tubulose generating unit 10 is 0.5～50mA/cm
2A kind of preferred embodiment is, the current density of each secondary tubulose source of iron producer be upper level current density 30～100%.
The utility model also provides the method that adopts said apparatus to prepare ferron.During use, after being power connection, form anode layer and cathode layer in the tubulose generating unit 10, between described anode layer and cathode layer, the circular channel is arranged, electrolytic solution in the container for storing liquid 2 enters an end of described tubulose generating unit circular channel by pipeline, the tubulose generating unit 10 of flowing through afterwards flows into next stage tubulose generating units 10 under the gravitional force effect, until flowing out from liquid outlet 8, obtain to be used for the ferron of water treatment.In order to make by the adjusted buffering of the acid-basicity of the electrolytic solution behind the opposed polarity zone, need making the length of tubulose generating unit satisfy electrolytic solution, to flow through two adjacent tubular generating unit 10 required times be the integral multiple of described power cycle.
The utility model also provides the employing ferron that said apparatus obtains purposes as flocculation agent in water treatment.
A kind of preferred embodiment of such use is, with described ferron (the ferro element total content is not less than 2g/L) according to iron: the phosphorus mol ratio is 2-5: 1 ratio joins in the pending water of phosphorated, abundant stirring reaction, 0.5h after obtain the water of phosphorus concentration less than 0.1ppm, and after treatment, other ions or the impurity introduced by ferron are very little to the influence of water quality, can ignore.
In the utility model; the ferro element total content of ferron or the measuring method of the phosphate concentration in the solution are to write according to State Environmental Protection Administration's water and effluent monitoring analytical procedure editorial committee; " water and effluent monitoring analytical procedure " (the 4th edition; [), measuring method of stipulating in China Environmental Science Press's publication (2002) carries out assay determination.
" beneficial effect "
The applicant confirms by a large amount of tests, the cost that the ferron that adopts preparation facilities of the present utility model and using method thereof to obtain is used for removing the total phosphorus of sewage is: when total phosphorus concentration is reduced to 0.1ppm by 3ppm in the water, the electric energy consumption of handling one ton of water consumption is 0.003 degree, iron filings that consumed and chemical reagent cost are 0.015 yuan, are about 0.02 yuan/ton altogether.And 0.1～0.3 yuan/ton of the processing cost average out to of the phosphorous water of existing conventional.
Compare with present other dephosphorization technique, the ferron that adopts described preparation method to make is applied to contain the technology that phosphorus water handles and has the following advantages:
1, instantaneity---described ferron can produce instant use immediately, has avoided in the chemical dosing medicament to put the storage problem of easy inefficacy for a long time.Obtained ferron Central Asia iron ion content is higher, has precipitation during dephosphorization simultaneously and flocculate two kinds to act on, and its removal effect and speed are much better than the conventional dephosphorization reagent that throwing out is only arranged.
2, economy---described method can adopt waste iron filing to constitute iron filings layers (promptly as source of iron), greatly reduces Financial cost.And the iron liquid that produces rely on gravity spontaneously to flow, save power and energy.
3, the feature of environmental protection---adopt waste iron filing as the powder electrode, both realized utilization of waste material, turned waste into wealth, increased electrode area again, avoided the problem of the easy passivation of iron plate under the high electric current.
4, practicality---prepared iron liquid concentration is higher, and described plant area area is little, is convenient to replenish after iron filings use and adds the controllability height; Whole source of iron producer is small and exquisite simple, is convenient to operational applications.
[description of drawings]
Fig. 1 is the structural representation of the preparation facilities of the ferron that is used for wastewater treatment of the present utility model;
Fig. 2 is the cross-sectional structure synoptic diagram of tubulose generating unit;
Wherein, 1, power supply; 2, electrolytic solution container for storing liquid; 3, under meter; 4, tubulose porous support materials layer; 5, netted perviousness material layer; 6, insulation tube body case; 7, iron filings layer; 8, liquid outlet; 9, source of iron generating apparatus; 10, tubulose generating unit.
[embodiment]
Following embodiment illustrates the utility model in conjunction with the accompanying drawings without limitation.Those skilled in the art are under the situation that does not break away from spirit and scope of the present utility model; can also make variations and modifications to the technical solution of the utility model; but all equivalent technical schemes all belong to category of the present utility model, and the utility model protection domain is limited by claims.
As shown in Figure 1, the preparation facilities that is used for the ferron of water treatment mainly is made up of power supply 1, tubular iron source generator device 9, electrolytic solution container for storing liquid 2 parts.Present embodiment adopts conversion positive and negative electrode polar direct supply periodically, and be 10s transformation period.Wherein, tubular iron source generator device 9 is made of 10 series connection of 3 tubulose generating units, and each generator unit is long to be 300mm, and each tubulose generating unit 10 is placed to horizontal direction has 30 ° of angles.
Tubulose porous support materials layer is that class conical in shape cast iron constitutes.In the present embodiment, only with inside and outside nested two-layer a tubular support material layer as anode layer and cathode layer (be that the iron filings layer thickness is 0, and netted perviousness material layer 5 is not set), wherein anode layer is positioned at the inboard of cathode layer.Wherein, be 60mm as the tubulose porous support materials bed thickness 2mm external diameter of anode layer, be thick as the tubulose porous support materials layer of cathode layer for the 2mm external diameter is 100mm, wherein sieve number is 40 orders.
Electrolytic solution in the container for storing liquid 2 is the NaCl of mass concentration 0.1% and 0.1% the HCl aqueous solution, pH=3.This electrolytic solution passes through the source of iron producer with the flow velocity of 20ml/min.Adopt respectively and do not apply electric current and the power supply of frequent transposing controlled function is arranged is 5mA/cm to applying current density between two electrodes by subsidiary
2Two kinds of situations of electric field under, measure the concentration of the iron liquid that produces, and the concentration of the iron liquid that produces when relatively no current being arranged.
Contrast and experiment can be found: no current by the time total concentration of iron that produces during only more for galvanization concentration 10%, this iron amount that shows that the reaction of simple iron filings and electrolytic solution produced is very little, and when connecting small electric current, electrode can obviously promote the oxidation stripping of iron, thereby reaches the purpose that improves iron level in the ferron.
Mode is similarly to Example 1 implemented.Different is that anode layer and cathode layer include tubulose porous support materials layer, iron filings layer and netted perviousness material.Wherein, anode layer is positioned at the inboard of cathode layer.The concrete structure of anode layer is: adhere to the iron filings layer outside thick 2mm external diameter for the 60mm sieve number is 100 purpose tubulose porous support materials layers, iron filings layer thickness 10mm, covering by thickness outside the iron filings layer is the overlapping perviousness material layer 5 that obtains of stainless (steel) wire (200 order) of 0.1mm.The concrete structure of cathode layer is: thick be to adhere to the iron filings layer in a tubular support material layer of 100mm for the 2mm external diameter, iron filings layer thickness 10mm, covering by thickness in the iron filings layer is the overlapping perviousness material layer 5 that obtains of stainless (steel) wire (200 order) of 0.1mm.Hollow region between the inside and outside two-layer iron filings layer is as the circular channel, and electrolysis liquid circulates.
The used waste iron filing of present embodiment is that particle diameter is the waste iron filing of 0.5～2mm in the mechanical workout factory.
Electrolytic solution in the container for storing liquid 2 is the aqueous solution of the KCl and 0.05% the HCl of mass concentration 0.5%, pH=5.
Energising obtains ferron.
Embodiment 3
Mode is similarly to Example 2 implemented.Different is, tubular iron source generator device 9 is made of single tubulose generating unit 10, and generator unit is long to be 1000mm.The iron filings layer thickness of each electrode is 5mm.The perviousness material is the thick tetrafluoroethylene screen cloth of 0.5mm (100 order) that is.Connect the solar storage battery with replacing positive and negative electrode polarity equipment between anode and negative electrode, be 20s transformation period, and current density is 10mA/cm
2Electrolytic solution is that concentration is the sodium-acetate of 0.01mol/L and the aqueous mixture of acetic acid, pH=4.5, and this electrolytic solution passes through the source of iron producer with the flow velocity of 50ml/min, obtains the ferron that total concentration of iron is 2g/L.
Embodiment 4
Similar to Example 3.Different is, tubular iron source generator device 9 is made of 10 series connection of 2 tubulose generating units, and each generator unit is long to be 400mm, other parameter constants.The perviousness material is the thick cotton of 0.3mm that is.Electrolytic solution is that concentration is the sodium sulfate of 0.01mol/L and the aqueous mixture of dilute sulphuric acid, pH=3.5, and this electrolytic solution passes through the source of iron producer with the flow velocity of 50ml/min, obtains ferron.
It is 36m that the gained ferron injects day output
3In the MBR pond of/d, adopt the detection method of index of correlation in the water of stipulating in the GB to measure the relevant ions content of introducing by in total phosphorus in the water body before and after the MBR pond and the electrolytic solution, test-results is listed in table 1, and assesses the cost.
Table 1: the contrast of the ferron that produces and dephosphorization medicament phosphor-removing effect
By data in the table 1 as can be seen, use the prepared ferron of the utility model that the total phosphorus in the waste water is removed, total phosphorus in the waste water is reduced to below the 0.2mg/L by 2.396mg/L, and its removal speed and energy consumption are all significantly better than the effect of buying medicament.Simultaneously, correlation water index analysis measurement result shows that the high dense iron liquid of minute quantity adds a large amount of containing in the phosphorus waste liquid, and ion that carries in its electrolytic solution or impurity are treated the water quality impact of treatment solution and can be ignored.
Claims (7)
1. preparation facilities that is used for the ferron of water treatment, it is characterized in that this device comprises power supply (1), source of iron generating apparatus (9) and electrolytic solution container for storing liquid (2), wherein, described source of iron generating apparatus (9) is made up of one or more levels tubulose generating unit (10), each tubulose generating unit (10) comprises insulation body (6) and is wrapped in the anode layer and the cathode layer that are made of iron in the described insulation body (6), described anode layer is mutually nested with cathode layer, has the circular channel of circulation for liquid between described anode layer and the cathode layer, anode layer in the anode of described power supply and the tubulose generating unit (10) joins, its negative electrode and described cathode layer join, described electrolytic solution container for storing liquid (2) is communicated to an end of described tubulose generating unit (10) circular channel by pipeline, and the other end in described circular channel is provided with liquid outlet (8).
2. the preparation facilities that is used for the ferron of water treatment according to claim 1, it is characterized in that source of iron generating apparatus (9) to forming by a plurality of tubulose generating units (10), each tubulose generating unit (10) is α °=0～90 ° with horizontal angle, and the circular channel of adjacent tubulose generating unit (10) communicates by pipeline.
3. the preparation facilities that is used for the ferron of water treatment according to claim 1 and 2, it is characterized in that described anode layer and cathode layer include the tubulose porous support materials, attached to the iron filings layer on described tubulose porous support materials surface be used for fixing the netted perviousness material layer of described iron filings layer, described iron filings layer is attached to the side of described tubulose porous support materials surface towards the circular channel.
4. the preparation facilities that is used for the ferron of water treatment according to claim 1 is characterized in that described pipeline also comprises under meter (3).
5. the preparation facilities that is used for the ferron of water treatment according to claim 3, the length that it is characterized in that described tubulose generating unit (10) is 100～1000mm; The thickness of the iron filings layer of described anode layer is 0～15mm; The thickness of the iron filings layer of described cathode layer is 0～15mm; Described circular channel thickness is 3～30mm; The mesh of described tubulose porous support materials is 40～500 orders, and the iron filings median size of described iron filings layer is 0.1～5mm.
6. the preparation facilities that is used for the ferron of water treatment according to claim 3 is characterized in that described netted perviousness material layer is by the stacked composite bed that constitutes of one or more materials in stainless (steel) wire, wire netting, fabric or the inert metal silk screen.
7. the preparation facilities that is used for the ferron of water treatment according to claim 1 is characterized in that described power supply (1) is the pulse power or has the direct supply of changing positive and negative electrode polarity equipment, and wherein the positive-negative polarity replacement cycle is 5～300s; Apply electric field between described anode and negative electrode, the average current density in the described tubulose generating unit (10) is 0.5～50mA/cm
2
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206713279U CN201932938U (en) | 2010-12-21 | 2010-12-21 | Device for preparing ferron used for water treatment |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010206713279U CN201932938U (en) | 2010-12-21 | 2010-12-21 | Device for preparing ferron used for water treatment |
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| CN201932938U true CN201932938U (en) | 2011-08-17 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102010034A (en) * | 2010-12-21 | 2011-04-13 | 北京碧水源膜科技有限公司 | Preparation device of ferron used for water treatment and application method thereof |
| CN111945184A (en) * | 2020-07-14 | 2020-11-17 | 武汉大学 | Fe2+/Fe3+Electrochemical preparation device, preparation method and application of hydroxide |
-
2010
- 2010-12-21 CN CN2010206713279U patent/CN201932938U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102010034A (en) * | 2010-12-21 | 2011-04-13 | 北京碧水源膜科技有限公司 | Preparation device of ferron used for water treatment and application method thereof |
| CN102010034B (en) * | 2010-12-21 | 2012-07-04 | 北京碧水源膜科技有限公司 | Preparation device of ferron used for water treatment and application method thereof |
| CN111945184A (en) * | 2020-07-14 | 2020-11-17 | 武汉大学 | Fe2+/Fe3+Electrochemical preparation device, preparation method and application of hydroxide |
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