CN206278963U - A kind of process units of the electrochemical stone as water body dephosphorized filtrate - Google Patents
A kind of process units of the electrochemical stone as water body dephosphorized filtrate Download PDFInfo
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- CN206278963U CN206278963U CN201620950035.6U CN201620950035U CN206278963U CN 206278963 U CN206278963 U CN 206278963U CN 201620950035 U CN201620950035 U CN 201620950035U CN 206278963 U CN206278963 U CN 206278963U
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- raw material
- lower roll
- process units
- filtrate
- water body
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 39
- 238000000034 method Methods 0.000 title claims abstract description 28
- 239000000706 filtrate Substances 0.000 title claims abstract description 26
- 239000004575 stone Substances 0.000 title claims abstract description 25
- 230000008569 process Effects 0.000 title claims abstract description 22
- 239000002994 raw material Substances 0.000 claims abstract description 31
- 230000008676 import Effects 0.000 claims abstract description 18
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000003756 stirring Methods 0.000 claims abstract description 12
- 239000000047 product Substances 0.000 claims abstract description 9
- 230000032258 transport Effects 0.000 claims abstract description 8
- 238000007493 shaping process Methods 0.000 claims abstract description 7
- 238000007599 discharging Methods 0.000 claims abstract description 5
- 239000000843 powder Substances 0.000 claims description 38
- 239000000463 material Substances 0.000 claims description 16
- 239000007787 solid Substances 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 3
- 238000003466 welding Methods 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 abstract description 14
- 239000002184 metal Substances 0.000 abstract description 14
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000000470 constituent Substances 0.000 abstract description 3
- 238000012545 processing Methods 0.000 abstract description 3
- 239000002351 wastewater Substances 0.000 abstract description 3
- 238000002161 passivation Methods 0.000 abstract description 2
- 238000005245 sintering Methods 0.000 abstract description 2
- 229910021645 metal ion Inorganic materials 0.000 abstract 1
- 239000003054 catalyst Substances 0.000 description 14
- 238000011282 treatment Methods 0.000 description 10
- 229910052698 phosphorus Inorganic materials 0.000 description 9
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 8
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 239000011574 phosphorus Substances 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 7
- 239000011230 binding agent Substances 0.000 description 7
- 239000012190 activator Substances 0.000 description 5
- 238000002360 preparation method Methods 0.000 description 5
- 241000195493 Cryptophyta Species 0.000 description 4
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 4
- 239000004411 aluminium Substances 0.000 description 4
- 229910052782 aluminium Inorganic materials 0.000 description 4
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 4
- 230000009467 reduction Effects 0.000 description 4
- 239000002689 soil Substances 0.000 description 4
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 235000019353 potassium silicate Nutrition 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 3
- 238000011953 bioanalysis Methods 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 238000001311 chemical methods and process Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000000571 coke Substances 0.000 description 2
- 238000012851 eutrophication Methods 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- -1 iron filings Chemical class 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000007769 metal material Substances 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical group [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 241000295146 Gallionellaceae Species 0.000 description 1
- 241000238631 Hexapoda Species 0.000 description 1
- 102000018779 Replication Protein C Human genes 0.000 description 1
- 108010027647 Replication Protein C Proteins 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 239000003463 adsorbent Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 238000000498 ball milling Methods 0.000 description 1
- 230000003851 biochemical process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910001431 copper ion Inorganic materials 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011118 depth filtration Methods 0.000 description 1
- 238000011026 diafiltration Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000003487 electrochemical reaction Methods 0.000 description 1
- 238000005868 electrolysis reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 239000013528 metallic particle Substances 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model is related to a kind of process units of the electrochemical stone as water body dephosphorized filtrate, including raw material agitator tank and product forming machine, the raw material agitator tank includes first charging aperture, second charging aperture, agitator, discharging opening, stirring fangs and journal stirrup, the product forming machine includes mainframe, column, upper roller, lower roll, lower roll pedestal, lower roll moving parts, push rod, push rod cylinder, import pallet and exit tray, the import pallet transports the raw material of raw material agitator tank outlet at bottom to roller, and the exit tray transports the water body dephosphorized filtrate electrification stone of shaping.Compared with prior art, the features such as the utility model has simple structure, easy to operate, low cost, and the water body dephosphorized filtrate electrification stone of its production is without sintering processes and using the useful metal ion in waste water, non-secondary pollution, processing cost is greatly reduced, active constituent content is high, can preferably overcome metal problem of passivation, and efficiency high, timeliness is long.
Description
Technical field
The utility model is related to purification of water quality production equipment technical field, more particularly to a kind of as water body dephosphorized filtrate
The process units of electrochemical stone.
Background technology
" body eutrophication " has been one of environmental pollution arch-criminal common to all.The growing production of the mankind and life
Activity, the eutrophication of abundant N, P nutrient source-i.e. is provided to water body, as a result result in the excessive multiplication of algae.Particularly
Phosphorus, except algae focuses on dephosphorization, i.e. landscape water body purification focuses on dephosphorization.
The method of dephosphorization includes physico-chemical process, biochemical process, bioanalysis and treatment etc. naturally.Physico-chemical process often with chemical precipitation, from
Sub- exchange, electrofloatation, adsorbent absorption and in-depth filtration etc., but such method high cost, troublesome poeration, it is difficult to continue；It is raw
Change method often uses activated sludge process, is isolated after also can absorbing phosphorus using culture algae, or culture iron bacteria precipitation high ferro phosphorus
Methods such as hydrochlorate, but such method limited by conditions such as C/N, C/P, sunlight, it is difficult to which continuous and effective goes dephosphorization；Bioanalysis
Algivorous insect is such as cultivated, effect substantially, but requires there are enough areas, also there are problems that season, or even two can be formed because rotting
Secondary pollution；Naturally using wetland or artificial swamp, adsorption by soil diafiltration etc., effect is good, but needs to manage well and bar for treatment
Part difficulty is sought.
Chinese patent CN104920465A discloses a kind of composition for suppressing algal grown, and its is simple, efficient, suitable
With scope extensively and better than above-mentioned phosphorus removing method, this composition is nonmetallic based on the raw metals such as iron filings, activated carbon etc., mixture
The compositions such as catalyst, organic bond, pore former, through the treatment such as shaping, dry, high temperature anoxybiotic sintering, it can be in phosphorus-containing wastewater
By when, using internal electrolysis principle, carry out extraordinary electrochemical reaction, water miscible positive phosphorus is changed into water-insoluble metal phosphorus
Hydrochlorate and separate out, therefore it can apply sewage disposal upgrading, landscape and urban river water except algae purification etc. wide field.But this
The composition that class suppresses algal grown has following disadvantage：Composition is expensive, and treatment process apparatus expensive, cost is too high；Gold
Easily oxidation is passivated category element under the environment for having water aerobic, ageing shorter.
Utility model content
The purpose of this utility model is to overcome defect of the prior art, designs a kind of electricity as water body dephosphorized filtrate
The water body dephosphorized filtrate of the process units of fossil, low cost, and its production（Electrochemical stone）Phosphorus content in water body can effectively be reduced.
To achieve the above object, the utility model is adopted the following technical scheme that：
A kind of process units of electrochemical stone as water body dephosphorized filtrate, including raw material agitator tank and product forming machine, on
State raw material agitator tank including first charging aperture, second charging aperture, agitator, discharging opening, stirring fangs and journal stirrup, the said goods into
Type machine include mainframe, column, upper roller, lower roll, lower roll pedestal, lower roll moving parts, push rod, push rod cylinder, import pallet and
Exit tray；Above-mentioned upper roller and lower roll are constituted to roller and are arranged between column, and the roll shaft two ends of above-mentioned lower roll are located at lower roll base
On seat, push rod cylinder is provided with below lower roll pedestal, above-mentioned lower roll base bottom is connected with the push rod of push rod cylinder, above-mentioned upper roller
And agitator drives by motor；Above-mentioned mainframe side is provided with import pallet, and opposite side is provided with exit tray, above-mentioned import support
Disk top is provided with raw material agitator tank, and the journal stirrup of above-mentioned raw materials agitator tank is connected with column, and above-mentioned import pallet transports raw material stirring
To roller, above-mentioned exit tray transports the water body dephosphorized filtrate of shaping to the raw material of pot bottom outlet（Electrochemical stone）.
Preferably, above-mentioned lower roll moving parts includes being arranged at the guide wheel of lower roll pedestal both sides and is arranged at leading in column
Groove, above-mentioned guide wheel is arranged in above-mentioned guide groove.
Preferably, the connected mode of above-mentioned journal stirrup and column is for welding, flange are connected or are threadedly coupled.
Preferably, above-mentioned agitator is provided with Double-layer stirring paddle.
Preferably, above-mentioned import pallet is downward-sloping in above-mentioned mainframe, and angle of inclination is 15 ° ~ 30 °.
Preferably, above-mentioned water body dephosphorized filtrate（Electrochemical stone）It is spheroid shape.
Preferably, the raw material of above-mentioned first charging aperture is solid powder, and the raw material of second charging aperture is water.
Preferably, the particle diameter of above-mentioned solid powder is not less than 300 mesh.
Preferably, above-mentioned solid powder is the mixing of metal powder material, binding agent powder, activator powder and catalyst powder
Thing, wherein：The metal powder material is one or more in iron powder material, aluminium powder material or magnesium powder material；The binding agent powder is water
One or more in mud powder, essence soil powder, waterglass powder, activated carbon powder or coke powder；The activator powder
It is polyvalent metal strong acid salt powder；The catalyst powder is reduction carrier catalyst powder.
On the other hand, the utility model is matched somebody with somebody there is provided the component and volume of a kind of electrochemical stone as water body dephosphorized filtrate
Than：
Metal material 0.5 ~ 30%；
Binding agent 0.5 ~ 80%；
Activator 1 ~ 40%；
Catalyst 0.5 ~ 15%；
Preferably, the metal material is at least one in iron, aluminium, magnesium.
Preferably, the binding agent is at least one in cement, smart soil, waterglass, activated carbon, coke.
Preferably, the activating agent is at least one in iron, aluminium, magnesium, zinc, the strong acid salt of copper；It is furthermore preferred that the work
Property agent be ferrous sulfate, aluminum sulfate at least one.
Preferably, the catalyst is reduction carrier catalyst, and wherein carrier is ferrous metal or non-metallic particle, on carrier
Carried metal copper.
Additionally, the utility model also provides a kind of preparation method for water body dephosphorized filtrate, including：
Step 1：Component to electrochemical stone carries out miniaturization, nanosizing treatment；
Step 2：Component after step 1 is processed is well mixed with water；
Step 3：The material mixed in step 2 is carried out into non-sintered shaping；
Step 4：Maintenance is carried out to the shaped article in step 3 to dry and pack.
Preferably, the above-mentioned preparation method also preparation process including reduction carrier catalyst.
Preferably, above-mentioned miniaturization, nanosizing treatment using mechanical lapping by the way of, preferably ball milling or to roller grinding.
Preferably, the fineness of component is not less than 300 mesh after the miniaturization, nanosizing treatment.
Preferably, the shaping is included to roller extrusion forming, shaped by fluid pressure.
Compared with prior art, the utility model has the advantages that：
The utility model provide a kind of electrochemical stone as water body dephosphorized filtrate process units, with simple structure,
The features such as easy to operate, low cost, while setting raw material mixed stirring device, reduce artificial operation；And ensure that product water body
Dephosphorization filtrate（Electrochemical stone）Uniformity, processing cost is greatly reduced, active constituent content is high, can preferably overcome metal to be passivated
Problem, and efficiency high, timeliness are long.
Brief description of the drawings
Fig. 1 is structural representation of the utility model as the process units of the electrochemical stone of water body dephosphorized filtrate；
Reference in figure is：1st, mainframe；2nd, column；3rd, upper roller；4th, lower roll；5th, lower roll pedestal；6th, lower roll movement
Part；7th, push rod；8th, push rod cylinder；9th, import pallet；10th, exit tray；11st, first charging aperture；12nd, second charging aperture；13、
Agitator；14th, discharging opening；15th, bearing；16th, journal stirrup.
Specific embodiment
With reference to the accompanying drawings and examples, specific embodiment of the present utility model is further described.Hereinafter implement
Example is only used for clearly illustrating the technical solution of the utility model, and protection model of the present utility model can not be limited with this
Enclose.
Embodiment one
The present embodiment is a kind of process units of water body dephosphorized filtrate electrification stone.
As shown in Figure 1：The utility model is a kind of process units of water body dephosphorized filtrate electrification stone, including raw material stirring
Tank and product forming machine, above-mentioned raw materials agitator tank include first charging aperture 11, second charging aperture 12, agitator 13, discharging opening 14,
Stirring fangs 15 and journal stirrup 16, the said goods forming machine include mainframe 1, column 2, upper roller 3, lower roll 4, lower roll pedestal 5, lower roll
Moving parts 6, push rod 7, push rod cylinder 8, import pallet 9 and exit tray 10；Above-mentioned upper roller 3 and lower roll 4 are constituted to roller and set
It is placed between column 2, the roll shaft two ends of above-mentioned lower roll 4 are located on lower roll pedestal 5, and push rod cylinder is provided with below lower roll pedestal 5
8, the above-mentioned bottom of lower roll pedestal 5 is connected with the push rod 7 of push rod cylinder 8, and above-mentioned upper roller 3 and agitator 12 drive by motor；On
State the side of mainframe 1 and be provided with import pallet 9, opposite side is provided with exit tray 10, and the top of above-mentioned import pallet 9 is provided with raw material stirring
Tank 11, the journal stirrup 16 of above-mentioned raw materials agitator tank 11 is connected with column 2, and above-mentioned import pallet 9 transports the bottom of raw material agitator tank 11 and goes out
To roller, above-mentioned exit tray 10 transports the water body dephosphorized filtrate of shaping to the raw material of mouth（Electrochemical stone）.
Above-mentioned lower roll moving parts 6 includes the guide wheel for being arranged at lower roll pedestal both sides and the guide groove being arranged in column, on
Guide wheel is stated to be arranged in above-mentioned guide groove；The connected mode of above-mentioned journal stirrup 16 and column 2 is for welding, flange are connected or are threadedly coupled；
Above-mentioned agitator 12 is provided with Double-layer stirring paddle；Above-mentioned import pallet 9 is downward-sloping in above-mentioned mainframe 1, and angle of inclination is 15 ° ~
30°；Above-mentioned water body dephosphorized filtrate（Electrochemical stone）It is spheroid shape；The raw material of above-mentioned first charging aperture 11 is solid powder, and second enters
The raw material of material mouth 12 is water；The particle diameter of above-mentioned solid powder is not less than 300 mesh；Above-mentioned solid powder is metal powder material, binding agent
The mixture of powder, activator powder and catalyst powder, wherein：The metal powder material is iron powder material, aluminium powder material or magnesium powder material
In one or more；The binding agent powder is cement powders, essence soil powder, waterglass powder, activated carbon powder or coke
One or more in powder；The activator powder is polyvalent metal strong acid salt powder；The catalyst powder is also published originally
Body catalyst powder.
The present embodiment also includes a kind of water body dephosphorized filtrate（Electrochemical stone）Preparation method, including：
Step 1：By above-mentioned water body dephosphorized filtrate（Electrochemical stone）Component metals material, binding agent, activator, catalyst enter
Row miniaturization, nanosizing treatment, the fineness of material is not less than 300 mesh after treatment；
Step 2：Solid powder after miniaturization, nanosizing treatment is added into raw material agitator tank, while adding water, is stirred
Mix mixing；
Step 3：The raw material feeding product forming machine of mixing is carried out into extrusion forming.
Step 4：Maintenance is carried out to shaped article to dry, pack.
Wherein above-mentioned catalyst use reduction carrier catalyst, its preparation process be using waste water recycling device oxidation also
Original removes process for copper, and copper ion is reverted on carrier.
From above-described embodiment, the features such as the utility model simple structure, easy to operate, low cost, while setting former
Material mixed stirring device, reduces artificial operation；And ensure that the water body dephosphorized filtrate of product（Electrochemical stone）Uniformity, be greatly reduced
Processing cost, active constituent content is high, can preferably overcome metal problem of passivation, and efficiency high, and timeliness is long.
Specific embodiment of the utility model has been described in detail above, but it is only used as example, the utility model
It is not restricted to particular embodiments described above.To those skilled in the art, it is any to being equal to that the practicality is carried out
Modifications and substitutions are also all among category of the present utility model.Therefore, the institute in the case where spirit and scope of the present utility model are not departed from
The impartial conversion and modification of work, should all cover in the range of the utility model.
Claims (8)
1. the process units of a kind of electrochemical stone as water body dephosphorized filtrate, it is characterised in that including raw material agitator tank and product
Forming machine, the raw material agitator tank include first charging aperture (11), second charging aperture (12), agitator (13), discharging opening (14),
Stirring fangs (15) and journal stirrup (16), the product forming machine including mainframe (1), column (2), upper roller (3), lower roll (4), under
Roller pedestal (5), lower roll moving parts (6), push rod (7), push rod cylinder (8), import pallet (9) and exit tray (10)；It is described
Upper roller (3) and lower roll (4) are constituted to roller and are arranged between column (2), and the roll shaft two ends of the lower roll (4) are located at lower roll pedestal
(5) on, the push rod of push rod cylinder (8), lower roll pedestal (5) bottom and push rod cylinder (8) is provided with lower roll pedestal (5) lower section
(7) connect, the upper roller (3) and agitator (13) drive by motor；Mainframe (1) side is provided with import pallet (9),
Opposite side is provided with exit tray (10), and import pallet (9) top is provided with raw material agitator tank, the journal stirrup of the raw material agitator tank
(16) it is connected with column (2), the import pallet (9) transports the raw material of raw material agitator tank outlet at bottom to roller, the outlet
Pallet (10) transports the water body dephosphorized filtrate electrification stone of shaping.
2. process units according to claim 1, it is characterised in that the lower roll moving parts (6) is including being arranged at down
The guide wheel of roller pedestal both sides and the guide groove being arranged in column, the guide wheel are arranged in the guide groove.
3. process units according to claim 1, it is characterised in that the connected mode of the journal stirrup (16) and column (2)
It is welding, flange connection or threaded connection.
4. process units according to claim 1, it is characterised in that the agitator (13) is provided with Double-layer stirring paddle.
5. process units according to claim 1, it is characterised in that the import pallet (9) is downward-sloping in the master
Frame (1), angle of inclination is 15 °~30 °.
6. process units according to claim 1, it is characterised in that the water body dephosphorized filtrate electrification stone is spheroid shape.
7. process units according to claim 1, it is characterised in that the raw material of the first charging aperture (11) is solid powder
Material, the raw material of second charging aperture (12) is water.
8. process units according to claim 7, it is characterised in that the particle diameter of the solid powder is not less than 300 mesh.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620950035.6U CN206278963U (en) | 2016-08-26 | 2016-08-26 | A kind of process units of the electrochemical stone as water body dephosphorized filtrate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620950035.6U CN206278963U (en) | 2016-08-26 | 2016-08-26 | A kind of process units of the electrochemical stone as water body dephosphorized filtrate |
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| Publication Number | Publication Date |
|---|---|
| CN206278963U true CN206278963U (en) | 2017-06-27 |
Family
ID=59084165
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|---|---|---|---|
| CN201620950035.6U Expired - Fee Related CN206278963U (en) | 2016-08-26 | 2016-08-26 | A kind of process units of the electrochemical stone as water body dephosphorized filtrate |
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| Country | Link |
|---|---|
| CN (1) | CN206278963U (en) |
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2016
- 2016-08-26 CN CN201620950035.6U patent/CN206278963U/en not_active Expired - Fee Related
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| CF01 | Termination of patent right due to non-payment of annual fee |
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