CN110436582A - Water process electricity consumption chemical floatation processing unit - Google Patents
Water process electricity consumption chemical floatation processing unit Download PDFInfo
- Publication number
- CN110436582A CN110436582A CN201910782436.3A CN201910782436A CN110436582A CN 110436582 A CN110436582 A CN 110436582A CN 201910782436 A CN201910782436 A CN 201910782436A CN 110436582 A CN110436582 A CN 110436582A
- Authority
- CN
- China
- Prior art keywords
- electrolysis
- groove body
- electrode plate
- basketry
- power supply
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 19
- 230000005611 electricity Effects 0.000 title claims abstract description 17
- 230000008569 process Effects 0.000 title claims abstract description 17
- 239000000126 substance Substances 0.000 title claims abstract description 14
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 53
- 239000000463 material Substances 0.000 claims abstract description 17
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 10
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 6
- 239000007770 graphite material Substances 0.000 claims description 6
- 239000010936 titanium Substances 0.000 claims description 6
- 229910052719 titanium Inorganic materials 0.000 claims description 6
- 229910052742 iron Inorganic materials 0.000 claims description 5
- 229910001339 C alloy Inorganic materials 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 3
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 3
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 3
- 239000004411 aluminium Substances 0.000 claims description 3
- 229910052782 aluminium Inorganic materials 0.000 claims description 3
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 3
- 230000001413 cellular effect Effects 0.000 claims description 3
- 229910052802 copper Inorganic materials 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- QMQXDJATSGGYDR-UHFFFAOYSA-N methylidyneiron Chemical compound [C].[Fe] QMQXDJATSGGYDR-UHFFFAOYSA-N 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 229910052725 zinc Inorganic materials 0.000 claims description 3
- 239000011701 zinc Substances 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 229910000831 Steel Inorganic materials 0.000 claims 1
- 229910052799 carbon Inorganic materials 0.000 claims 1
- 239000010959 steel Substances 0.000 claims 1
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 19
- 239000012535 impurity Substances 0.000 abstract description 18
- 239000002351 wastewater Substances 0.000 abstract description 16
- 230000000694 effects Effects 0.000 abstract description 12
- 238000009434 installation Methods 0.000 abstract description 5
- 239000003463 adsorbent Substances 0.000 description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 7
- 229910052739 hydrogen Inorganic materials 0.000 description 7
- 239000001257 hydrogen Substances 0.000 description 7
- 239000007789 gas Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 4
- 238000005276 aerator Methods 0.000 description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 3
- 229910000975 Carbon steel Inorganic materials 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000010962 carbon steel Substances 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000006722 reduction reaction Methods 0.000 description 2
- 238000011282 treatment Methods 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 229910021645 metal ion Inorganic materials 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
- C02F1/465—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electroflotation
-
- 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
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46133—Electrodes characterised by the material
-
- 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
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46152—Electrodes characterised by the shape or form
- C02F2001/46157—Perforated or foraminous electrodes
-
- 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
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46152—Electrodes characterised by the shape or form
- C02F2001/46157—Perforated or foraminous electrodes
- C02F2001/46161—Porous electrodes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/10—Inorganic compounds
- C02F2101/20—Heavy metals or heavy metal compounds
-
- 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
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
-
- 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
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
- C02F2201/4616—Power supply
-
- 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
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
- C02F2201/46195—Cells containing solid electrolyte
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General 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)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses a kind of water process electricity consumption chemical floatation processing units, comprising: groove body, the groove body front end are equipped with water inlet, and the rear end of the groove body is equipped with water outlet；Electrode plate, the electrode plate are located inside the groove body；It is electrolysed basketry, the electrolysis basketry is located at the groove body inside and is located above the electrode plate, and the electrolysis basketry inner hollow and filling electrolysis material, and the electrolysis basketry is equipped with aperture；The anode of power supply, the power supply is electrically connected with the electrolysis basketry, and the cathode of the power supply is electrically connected with the electrode plate.The impurity such as the heavy metal in waste water can be effectively removed using the device, and electrolysate is discharged in time, keep the electrolysis activity of electrolysis unit, while tank voltage is effectively reduced, installation area is small and cost is low.
Description
Technical field
The invention belongs to technical field of waste water processing, and in particular to a kind of water process electricity consumption chemical floatation processing unit.
Background technique
Current coloured industry waste water end generallys use electrochemical treatments technique, and Conventional electrochemical processing is generally using opening
Formula electrolytic cell adds the mode of iron plate commutation electrolysis, and this mode is gerotor type, and equipment is simple, is widely adopted.But this work
Skill occupation area of equipment is big, and electric energy efficiency is lower, and anode utilization rate is low, and the iron being electrolysed out is not easy to be discharged, and is attached to pole plate
On continue to aoxidize, lose effect.
Therefore, the existing electrochemical treatments technology suitable for coloured industry waste water is further improved.
Summary of the invention
The present invention is directed to solve at least some of the technical problems in related technologies.For this purpose, of the invention
One purpose is to propose a kind of water process electricity consumption chemical floatation processing unit, can be effectively removed in waste water using the device
The impurity such as heavy metal, and electrolysate is discharged in time, the electrolysis activity of electrolysis unit is kept, while slot electricity is effectively reduced
Pressure, installation area is small and cost is low.
In one aspect of the invention, the invention proposes a kind of water process electricity consumption chemical floatation processing units.According to this
The embodiment of invention, described device include:
Groove body, the groove body front end are equipped with water inlet, and the rear end of the groove body is equipped with water outlet；
Electrode plate, the electrode plate are located inside the groove body；
It is electrolysed basketry, the electrolysis basketry is located inside the groove body and is located above the electrode plate, and the electricity
It solves basketry inner hollow and filling electrolysis material, the electrolysis basketry is equipped with aperture；
The anode of power supply, the power supply is electrically connected with the electrolysis basketry, the cathode of the power supply and electrode plate electricity
Connection.
Water process electricity consumption chemical floatation processing unit according to an embodiment of the present invention by groove body be arranged electrode plate and
The electrode plate is connected with the cathode of power supply, and the anode of setting electrolysis basketry and the electrolysis basketry and power supply above electrode plate
It is connected, in electrolytic process, reduction reaction generation hydrogen and hydroxide ion (2H occur for water around electrode plate2O+2e-=H2+
2OH-), it is electrolysed aborning electrolysis material in basketry and constantly dissolves out generation adsorbent, the suction in conjunction with the hydroxyl that cathode generates
The impurity such as the attached dose of heavy metal that can effectively adsorb in waste water, and the hydrogen that electrode plate generates forms air bearing effect, to make
The adsorbent that the impurity such as heavy metal must be adsorbed floats with gas, finally enters aerator from water outlet and is aerated and adsorbs heavy metal
Equal impurity.The impurity such as the heavy metal in waste water can be effectively removed using the device as a result, and in time arrange electrolysate
Out, the electrolysis activity of electrolysis unit is kept, while tank voltage is effectively reduced, installation area is small and cost is low.
In addition, water process electricity consumption chemical floatation processing unit according to the above embodiment of the present invention can also have it is following attached
The technical characteristic added:
In some embodiments of the invention, the groove body is resin groove body, PVC groove body or concrete groove body.
In some embodiments of the invention, the electrode plate is netted or cellular.
In some embodiments of the invention, the electrode plate is made of stainless steel, titanium, copper, graphite material.
In some embodiments of the invention, the electrolysis basketry is made of graphite material after titanium, titanium alloy.
In some embodiments of the invention, the electrolysis material includes fine aluminium, pure iron, pure zinc, carbon steel and iron-carbon alloy
At least one of.Thus, it is possible to effectively remove the impurity such as heavy metal in waste water.
In some embodiments of the invention, the electrode plate is located in the groove body along the bottom of the parallel groove body
Portion, and the electrode plate is parallel with the electrolysis basketry and arranged for interval.Thus, it is possible to adsorb the impurity such as heavy metal
Adsorbent floats with gas, keeps electrolysis basketry activity.
In some embodiments of the invention, in the short transverse of the groove body, the water inlet is located at the water outlet
Below mouthful.
Additional aspect and advantage of the invention will be set forth in part in the description, and will partially become from the following description
Obviously, or practice through the invention is recognized.
Detailed description of the invention
Above-mentioned and/or additional aspect of the invention and advantage will become from the description of the embodiment in conjunction with the following figures
Obviously and it is readily appreciated that, in which:
Fig. 1 is the vertical section structure signal of water process electricity consumption chemical floatation processing unit according to an embodiment of the invention
Figure；
Fig. 2 is the plan structure signal of water process electricity consumption chemical floatation processing unit according to an embodiment of the invention
Figure.
Specific embodiment
The embodiment of the present invention is described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning to end
Same or similar label indicates same or similar element or element with the same or similar functions.Below with reference to attached
The embodiment of figure description is exemplary, it is intended to is used to explain the present invention, and is not considered as limiting the invention.
In the description of the present invention, it is to be understood that, term " center ", " longitudinal direction ", " transverse direction ", " length ", " width ",
" thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside", " up time
The orientation or positional relationship of the instructions such as needle ", " counterclockwise ", " axial direction ", " radial direction ", " circumferential direction " be orientation based on the figure or
Positional relationship is merely for convenience of description of the present invention and simplification of the description, rather than the device or element of indication or suggestion meaning must
There must be specific orientation, be constructed and operated in a specific orientation, therefore be not considered as limiting the invention.
In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance
Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or
Implicitly include at least one this feature.In the description of the present invention, the meaning of " plurality " is at least two, such as two, three
It is a etc., unless otherwise specifically defined.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " fixation " etc.
Term shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral；It can be mechanical connect
It connects, is also possible to be electrically connected；It can be directly connected, can also can be in two elements indirectly connected through an intermediary
The interaction relationship of the connection in portion or two elements, unless otherwise restricted clearly.For those of ordinary skill in the art
For, the specific meanings of the above terms in the present invention can be understood according to specific conditions.
In the present invention unless specifically defined or limited otherwise, fisrt feature in the second feature " on " or " down " can be with
It is that the first and second features directly contact or the first and second features pass through intermediary mediate contact.Moreover, fisrt feature exists
Second feature " on ", " top " and " above " but fisrt feature be directly above or diagonally above the second feature, or be merely representative of
First feature horizontal height is higher than second feature.Fisrt feature can be under the second feature " below ", " below " and " below "
One feature is directly under or diagonally below the second feature, or is merely representative of first feature horizontal height less than second feature.
In one aspect of the invention, the invention proposes a kind of water process electricity consumption chemical floatation processing units.According to this
The embodiment of invention, with reference to Fig. 1 and 2, which includes: groove body 100, electrode plate 200, electrolysis basketry 300 and power supply 400.
According to an embodiment of the invention, 100 front end of groove body is equipped with water inlet 101, the rear end of groove body 100 is equipped with water outlet
102, it is preferred that in the short transverse of groove body 100, water inlet 101 is located at 102 lower section of water outlet, i.e., waste water is in groove body 100
Bottom in and top out, so that the water inlet 101 that waste water is located at 100 leading portion bottom of groove body enters in groove body 100 and the electrode that successively flows
Between plate 200 and electrolysis basketry 300, the water outlet 102 for being then located at 100 rear end upper end of groove body is discharged groove body and enters aeration dress
It sets aeration and adsorbs the impurity such as heavy metal.A specific embodiment according to the present invention, the material of groove body 100 are wanted there is no special
It asks, as long as being able to achieve insulation effect, for example, resin groove body, PVC groove body or concrete groove body.
According to an embodiment of the invention, electrode plate 200 is located inside groove body 100, it is preferred that electrode plate 200 is along being parallel to
The bottom of groove body 100 is arranged in groove body 100, and in electrolytic process, the water around it that is connected with power cathode of electrode plate 200 occurs also
Original reaction generates hydrogen and hydroxide ion (2H2O+2e-=H2+2OH-), wherein hydroxide ion and electrolysis basketry in generate in
The metal ion that constantly dissolves out of electrolysis material combine and generate adsorbent, which can effectively adsorb the heavy metal in waste water
Equal impurity, and the hydrogen that electrode plate generates forms air bearing effect, so that the adsorbent of the impurity such as absorption heavy metal is on gas
It is floating, to keep electrolysis basketry electrolysis activity.
Further, electrode plate 200 is netted or cellular.Specifically, netted or cavernous electrode plate can be conducive to water
Flowing, keep electrolytic process more thorough, it is more efficient.And electrode plate 200 is that electrode plate is stainless steel, titanium, copper, graphite material
Matter is made.
According to an embodiment of the invention, electrolysis basketry 300 is located at 100 inside of groove body and is located at 200 top of electrode plate, and
It is electrolysed 300 inner hollow of basketry and filling electrolysis material, electrolysis basketry 300 is equipped with the second aperture 31, is electrolysed in basketry and generates
In electrolysis material constantly dissolve out and combine generation adsorbent with the hydroxyl that cathode generates, which can effectively adsorb waste water
In the impurity such as heavy metal, and the hydrogen that electrode plate generates forms air bearing effect, so that the impurity such as absorption heavy metal
Adsorbent floats with gas, finally enters aerator from water outlet and is aerated and adsorbs the impurity such as heavy metal.
Specifically, electrolysis basketry 300 is the square structure of inner hollow, and it is electrolysed material and is filled in its hollow structure
It is interior, and be electrolysed that basketry 300 is parallel with electrode plate 200 and arranged for interval, and be electrolysed office on each face of basketry 300 be equipped with it is more
A aperture 31.
Further, electrolysis basketry 300 is made of graphite material after titanium, titanium alloy.The electrolysis basketry of such material its
Body does not chemically react, and has good adaptability to waste water in addition, the electrolysis material in electrolysis basketry 300 includes pure
At least one of aluminium, pure iron, pure zinc, carbon steel and iron-carbon alloy.The substance is under the action of positive pole as a result, wherein
Electrolysis material constantly dissolve out with cathode reaction generate adsorbent, it is miscellaneous which can effectively adsorb heavy metal in waste water etc.
Matter.According to an embodiment of the invention, the anode 41 of power supply 400 is electrically connected with electrolysis basketry 300, the cathode 42 and electricity of power supply 400
Pole plate 200 is electrically connected.Specifically, the power supply can be DC power supply commonly used in the art.
Water process electricity consumption chemical floatation processing unit according to an embodiment of the present invention by groove body be arranged electrode plate and
The electrode plate is connected with the cathode of power supply, and the anode of setting electrolysis basketry and the electrolysis basketry and power supply above electrode plate
It is connected, in electrolytic process, reduction reaction generation hydrogen and hydroxide ion (2H occur for water around electrode plate2O+2e-=H2+
2OH-), it is electrolysed aborning electrolysis material in basketry and constantly dissolves out generation adsorbent, the suction in conjunction with the hydroxyl that cathode generates
The impurity such as the attached dose of heavy metal that can effectively adsorb in waste water, and the hydrogen that electrode plate generates forms air bearing effect, to make
The adsorbent that the impurity such as heavy metal must be adsorbed floats with gas, finally enters aerator from water outlet and is aerated and adsorbs heavy metal
Equal impurity.The impurity such as the heavy metal in waste water can be effectively removed using the device as a result, and in time arrange electrolysate
Out, the electrolysis activity of electrolysis unit is kept, while tank voltage is effectively reduced, installation area is small and cost is low.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show
The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example
Point is included at least one embodiment or example of the invention.In the present specification, schematic expression of the above terms are not
It must be directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be in office
It can be combined in any suitable manner in one or more embodiment or examples.In addition, without conflicting with each other, the skill of this field
Art personnel can tie the feature of different embodiments or examples described in this specification and different embodiments or examples
It closes and combines.
Although the embodiments of the present invention has been shown and described above, it is to be understood that above-described embodiment is example
Property, it is not considered as limiting the invention, those skilled in the art within the scope of the invention can be to above-mentioned
Embodiment is changed, modifies, replacement and variant.
Claims (8)
1. a kind of water process electricity consumption chemical floatation processing unit characterized by comprising
Groove body, the groove body front end are equipped with water inlet, and the rear end of the groove body is equipped with water outlet；
Electrode plate, the electrode plate are located inside the groove body；
It is electrolysed basketry, the electrolysis basketry is located inside the groove body and is located above the electrode plate, and the electrolysis basket
Basket inner hollow and filling electrolysis material, the electrolysis basketry is equipped with aperture；
The anode of power supply, the power supply is electrically connected with the electrolysis basketry, and the cathode of the power supply is electrically connected with the electrode plate.
2. the apparatus according to claim 1, which is characterized in that the groove body is resin groove body, PVC groove body or concrete pit
Body.
3. the apparatus according to claim 1, which is characterized in that the electrode plate is netted or cellular.
4. device according to claim 1 or 3, which is characterized in that the electrode plate is stainless steel, titanium, copper, graphite material
It is made.
5. the apparatus according to claim 1, which is characterized in that the electrolysis basketry is graphite material system after titanium, titanium alloy
At.
6. device according to claim 1 or 5, which is characterized in that the electrolysis material includes fine aluminium, pure iron, pure zinc, carbon
At least one of steel and iron-carbon alloy.
7. the apparatus according to claim 1, which is characterized in that the electrode plate is located at institute along the bottom of the parallel groove body
It states inside groove body, and the electrode plate is parallel with the electrolysis basketry and arranged for interval.
8. the apparatus according to claim 1, which is characterized in that in the short transverse of the groove body, the water inlet is set
Below the water outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910782436.3A CN110436582A (en) | 2019-08-23 | 2019-08-23 | Water process electricity consumption chemical floatation processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910782436.3A CN110436582A (en) | 2019-08-23 | 2019-08-23 | Water process electricity consumption chemical floatation processing unit |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110436582A true CN110436582A (en) | 2019-11-12 |
Family
ID=68437287
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910782436.3A Pending CN110436582A (en) | 2019-08-23 | 2019-08-23 | Water process electricity consumption chemical floatation processing unit |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110436582A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021103605A1 (en) * | 2019-11-29 | 2021-06-03 | 无锡小天鹅电器有限公司 | Electrode plate, electrolysis apparatus, and laundry treatment device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104803455A (en) * | 2015-04-13 | 2015-07-29 | 北京华瑞创源环保科技有限公司 | Electrocoagulation equipment for wastewater treatment and electrocoagulation method |
| CN106399045A (en) * | 2015-07-31 | 2017-02-15 | 中国科学院青岛生物能源与过程研究所 | Portable low-energy-consumption air-floatation apparatus used for harvesting of microalgae and application method thereof |
| CN106517427A (en) * | 2016-10-21 | 2017-03-22 | 河海大学 | Wastewater treatment device and method |
| CN107827209A (en) * | 2017-11-09 | 2018-03-23 | 中国恩菲工程技术有限公司 | Electric flocculation wastewater treatment equipment and electric flocculation waste water treatment process |
| CN108046383A (en) * | 2017-11-09 | 2018-05-18 | 中国恩菲工程技术有限公司 | Electric flocculation device |
| CN210825564U (en) * | 2019-08-23 | 2020-06-23 | 中国恩菲工程技术有限公司 | Electrochemical air-float treatment device for water treatment |
-
2019
- 2019-08-23 CN CN201910782436.3A patent/CN110436582A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104803455A (en) * | 2015-04-13 | 2015-07-29 | 北京华瑞创源环保科技有限公司 | Electrocoagulation equipment for wastewater treatment and electrocoagulation method |
| CN106399045A (en) * | 2015-07-31 | 2017-02-15 | 中国科学院青岛生物能源与过程研究所 | Portable low-energy-consumption air-floatation apparatus used for harvesting of microalgae and application method thereof |
| CN106517427A (en) * | 2016-10-21 | 2017-03-22 | 河海大学 | Wastewater treatment device and method |
| CN107827209A (en) * | 2017-11-09 | 2018-03-23 | 中国恩菲工程技术有限公司 | Electric flocculation wastewater treatment equipment and electric flocculation waste water treatment process |
| CN108046383A (en) * | 2017-11-09 | 2018-05-18 | 中国恩菲工程技术有限公司 | Electric flocculation device |
| CN210825564U (en) * | 2019-08-23 | 2020-06-23 | 中国恩菲工程技术有限公司 | Electrochemical air-float treatment device for water treatment |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2021103605A1 (en) * | 2019-11-29 | 2021-06-03 | 无锡小天鹅电器有限公司 | Electrode plate, electrolysis apparatus, and laundry treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107117690A (en) | Electrocatalytic oxidation handles the device and method of Recalcitrant chemicals | |
| CN101423266A (en) | Wastewater treatment device of horizontal polar plate multi-electrodes electrocatalysis reactor | |
| CN107215929A (en) | A kind of electric flocculation unit, electric flocculation device and heavy metal waste water treatment system | |
| CN201325897Y (en) | Waste water treatment equipment of multi-dimensional electrode electrical catalytic reactor of horizontal electrode plate | |
| CN113403630A (en) | Hydrogen producing device by catalytic electrolysis | |
| CN113621980A (en) | Flow type electrochemical device for preparing hydrogen peroxide | |
| CN110436582A (en) | Water process electricity consumption chemical floatation processing unit | |
| CN209383458U (en) | A kind of electricity Fenton oxidation reaction unit | |
| CN211255370U (en) | Electrochemical oxidation device of stirring tank | |
| CN108217861B (en) | Internal circulation type electrocatalytic oxidation reactor and sewage purification treatment method | |
| CN106830204A (en) | A kind of electrochemical cathode excites the method and device of permanganate degraded water pollutant | |
| CN210825564U (en) | Electrochemical air-float treatment device for water treatment | |
| CN110436580A (en) | Water process electrochemical treatments integrated apparatus | |
| CN210825558U (en) | Electrochemical treatment device for water treatment | |
| CN210825559U (en) | Electrochemical treatment integrated device for water treatment | |
| JP2004027267A (en) | Salt electrolytic cell provided with gas diffusion cathode | |
| CN101244854B (en) | Iron carbon micro electrolyser and method for processing ceramic phenol wastewater | |
| CN211255371U (en) | Electrochemical treatment device for stirring tank | |
| CN201545915U (en) | Gas-liquid gravity-flow circulating type hydrogen electrolyzer | |
| CN110436578A (en) | Water process apparatus for electrochemical treatment | |
| CN208814717U (en) | Multistage room multiple catalyzing electrode electro Chemical reactor | |
| WO2020105369A1 (en) | Hydrogen production method | |
| CN110451611A (en) | Composite three-dimensional electrolysis unit | |
| CN208361959U (en) | A kind of electrode group for electrochemical treatments pharmaceutical wastewater | |
| CN111499130A (en) | Electrochemical sludge pretreatment device and sludge treatment method thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination |