CN206188547U - Four -phase catalytic oxidation device - Google Patents
Four -phase catalytic oxidation device Download PDFInfo
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- CN206188547U CN206188547U CN201621243644.4U CN201621243644U CN206188547U CN 206188547 U CN206188547 U CN 206188547U CN 201621243644 U CN201621243644 U CN 201621243644U CN 206188547 U CN206188547 U CN 206188547U
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- activated carbon
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Abstract
The utility model discloses a four -phase catalytic oxidation device. It includes the airtight tank body of taking the on -conductive shell, and the cell body bottom lets in the water distributor, the bearing board is established to the water distributor top, and the apopore department on the bearing board is equipped with and strains the cap, establish the cobblestone bed course above the bearing board, the aerator of being connected with blast air fan or ozone generator respectively inserts in the cobblestone bed course, the cell body lower part is loaded the activated carbon catalyse oxidation and is packed, if the piece plate electrode is done to both sides in the cell body, cell body upper portion lets in the spray header, the cell body top is connected with the draught fan. The utility model discloses integrated air / ozone aeration systems, graphite alkene coating activated carbon catalyse filler system, electrode catalytic system, water distribution spray backwash system, exhaust system etc. Through the control of antipodal inter -plate voltage, electric current, polar plate interval, operation pH value etc. Under lower voltage, the electric current condition, form the pollutant was realized to the higher OH group that has the strong oxidizing property of density as intermediate deep oxidation decomposition in unit volume.
Description
Technical field
The utility model belongs to technical field of waste water processing, is related to a kind of four phases catalytic oxidizing equipment.The main pin of the device
To the industrial enterprise such as COD high of the industry such as pharmacy, chemical industry, agricultural chemicals, coking, fuel discharge, it is highly-saline, with bio-toxicity or
The waste water COD of person's biological inhibition effect is removed.
Background technology
High salt, COD high, there are bio-toxicity or the wastewater treatment always enterprise headache the most of biological inhibition effect to ask
Topic, its content of organics is high, and biodegradability is poor, it is difficult to be degraded by microorganisms.For such waste water, more typical handling process bag
Include：(1), absorption method；(2), air/ozone oxidation technology；(3), Feton oxidation technologies；(4), electro-catalytic oxidation technology；(5)、
Incineration technology.But the characteristics of these methods have oneself and limitation.
(1), adsorption treatment process, when high-concentration waste water is processed, is adsorbed mainly for the advanced treating of low concentration wastewater
Agent is very easy to reach adsorption saturation state, and frequent replacement cost is expensive, it is necessary to regenerate in vitro when using regeneration treatment,
It is cumbersome, and loss is big；
(2), air/ozone oxidation technology, air aeration oxidation technology is mainly used in biological treatment aerobic section, for can
The preferable waste water of biochemical, is a kind of most currently used technique according to the advantage for having low energy consumption, but for high concentration COD, tool
There is the waste water of bio-toxicity or inhibitory action, its oxidability is too weak, and treatment effect is excessively poor.Ozone oxidation has oxidability
By force, reaction speed block, science and engineering at the advantages of sludge and secondary pollution, its successive depths generally as wastewater treatment is not produced
Section, when high concentration wastewater treatment is directly applied to, the huge but utilization rate of dosage is low, and ozone oxidation has certain selection
Property, might not well aoxidize many organic pollution materials；
(3), Feton oxidation technologies are produced greatly by a certain proportion of FeSO4 and H2O2 is added in waste water, making in waste water
The OH groups of amount, using poisonous and harmful substance and the organic matter of difficult degradation in the strong oxidation performance and waste water of OH groups
React and generate harmless carbon dioxide and water and reach the purpose of pollutant removal, with quick, efficient, pollution-free etc.
Advantage, but technology PH accommodations are narrow, it is necessary to adjust PH for 3-5, while Fe2+ consumptions are big, can produce after the reaction substantial amounts of
Iron containing sludge is precipitated, and H2O2 consumptions are big, and processing cost is high；
(4), widely, advantage is a lot, mainly there is treatment for electro-catalytic oxidation technology application study in the treatment of waste water
Efficiency high, easy to operate, applied widely, controllability easily realizes by force automation, the advantages of environment compatibility is good, but due to pole plate
The reasons such as material, processing solution electric conductivity, filler composition material limit, its often oxygen evolution potential it is low, in catalytic degradation water
Organic matter when, can cause that current efficiency reduction, electrode life are short, substantial amounts of energy consumption is used for the shortcomings of produce hydrogen, oxygen.
Such as：Two-dimentional electrocatalytic oxidation, its mainly produce hydroxyl radical free radical position be battery lead plate plan-position；Conventional three-dimensional electrocatalytic oxidation
Change, although produce hydroxyl radical free radical to occur in whole container space, but its filling system cost when using noble metal catalyst
Higher, the easy dissolution of noble metal, carbon distribution lose catalysis activity.Equally when using dissolution formula irony battery lead plate, can produce a large amount of
Molysite sludge settling, and use the pole plate of non-dissolution and during relatively low water quality treatment salinity, its needs takes operation electricity higher
(voltage is raised pressure, and the speed of electrolysis water accelerates, and substantial amounts of energy consumption is used for electrolysis water rather than hydroxyl radical free radical is produced, while producing
The substantial amounts of hydrogen of life and oxygen), or add electrolyte in addition (such as NaCl increases extra processing cost)；
(5), the incineration treatment technology of waste water is mainly for COD>100000ml/L, calorific value>4.1868*2500kJ/kg's
High-concentration waste water, the waste water burning method treatment relatively low for COD concentration is more consumed energy than other method, does not possess actual behaviour
The property made.When higher containing chlorine ion concentration in solution, incinerator corrosion is very serious.
Utility model content
The purpose of this utility model is to overcome the deficiencies in the prior art, there is provided a kind of deep oxidation that can realize pollutant
The four phase catalytic oxidizing equipments for decomposing.
Design of the present utility model is as follows：
The ability for producing hydroxyl radical free radical is a judging quota of advanced oxidation processes quality, conventional advanced oxidation work
Although can more or less realize producing hydroxyl radical free radical in skill, often there is certain limitation, such as：Two-dimentional electrocatalytic oxidation
Change, its mainly produce hydroxyl radical free radical position be battery lead plate plan-position；Conventional three-dimensional electrocatalytic oxidation, although produce hydroxyl
Free radical occurs in whole container space, but its filling system is relatively costly when using noble metal catalyst, and noble metal is easy
Dissolution, carbon distribution, lose catalysis activity；Fonten reagents and group technology are in order to obtain substantial amounts of hydroxyl radical free radical, it is necessary to adjust
Water quality is highly acid (PH：3-5), substantial amounts of sulfuric acid is expended, while needing additional hydrogen peroxide and ferrous iron, and many sludge is produced；
Activated carbon systems saturation and will soon need frequent external regeneration when high concentrated organic wastewater is processed, and not possess actual behaviour
Make type；The oxidability of chlorine system oxidant and ozone is weaker (oxidizing potential is low compared with hydroxyl radical free radical), and many organic matters can not
It is oxidized.
Four phase catalytic oxidation technologies have taken into full account above waste water treatment process defect and have made the appropriate adjustments.Mutually urged using four
Change oxidation technology, in the case of any molysite and irony pole plate the is not added, (PP/PVC in a nonconducting outer casing container
Deng) in, integrated speciality activated carbon catalysis oxide filler is (with porosity characteristic, under catalyst and DC Electric Field, organic dirt
Dye material adsorb and decompose (parsing) online), (under extra electric field, oxygen/ozone is used as raw material for air/ozone aerator
And produce the utilization rate of hydroxyl radical free radical, oxygen/ozone to be substantially improved, and oxidation does not possess selectivity, can almost aoxidize institute
Some organic matters), speciality coated electrode plate (be coated with ruthenium iridium palladium platinum coating titanium-matrix electrode plate, coating makes liberation of hydrogen, analysis oxygen more hold
Easily, catalysis activity is improve, makes electric energy mainly for generation of hydroxyl radical free radical rather than electrolysis water, the oxidation of speciality activated carbon catalysis
Filler is coated with graphite ene coatings, and Graphene has good electric conductivity, reduces operating voltage, whole hydroxyl radical free radical
Produce and occur in whole container space, and not only in two-dimensional electrode plate plane, the addition of speciality activated carbon catalysis oxide filler
Have and non-precious metal catalyst and electronic auxiliary, metal is difficult dissolution, carbon distribution and loses activity, without using irony pole plate and
Stabilization produces hydroxyl radical free radical in the case of adding ferrous salt, hydrogen peroxide, and OH groups are with oxidizing electrode current potential higher
(2.8V), compares O3(2.07V) and H2O2(1.76V) respectively high 35% and 59%, oxidability is only second to fluorine), back washing device, spray
Shower device, exhaust system, Current Voltage control device etc..By voltage, electric current, pole plate spacing, operation pH value etc. between pole plate
Control, under lower voltage, current conditions, density OH bases with strong oxidizing property higher are formed in unit volume
Group realizes that the deep oxidation of pollutant is decomposed as intermediate product.
The technical solution of the utility model is as follows：
The utility model four phase catalytic oxidizing equipments of one kind, the device includes a closed container with non-conductive shell
That is catalysis oxidation groove cell body, cell body bottom is passed through water distributor, and water distributor is provided with many water distributing pores；Water distribution tube inlet respectively with enter
Exit of pump, backwash water pump outlet connection；Water distributor top is provided with supporting plate, and supporting plate is provided with many apopores, apopore
Place is provided with filter cap；Cobblestone bed course is provided with above supporting plate (being piled up on supporting plate has cobblestone)；Aerator inserts cobblestone
In bed course, aerator entrance is connected with air blast fan outlet or ozone generator outlet respectively；Groove above cobblestone bed course
Activated carbon catalysis oxide filler is filled with body lower space；Cell body inside both sides are respectively provided with some electrode plates, wherein one
Part is positive plate, and another part is minus plate, and positive plate, minus plate are connected with the both positive and negative polarity of power supply (are provided with power supply respectively
Ammeter and voltmeter)；Cell body top is provided with effluent weir；Spray header, spray header are passed through above the effluent weir of cell body top
Entrance is connected with feeding spraying pump outlet；Spray header bottom is provided with nozzle；Cell body top is connected by induced duct with air-introduced machine；Urge
Change oxidation trough rear and connect effluent trough (weir flow connection)；Feeding spraying pump entrance is connected with effluent trough middle part delivery port.
Further, catalysis oxidation groove cell body both sides inwall is provided with groove, and positive plate, minus plate insert both sides respectively
In groove.
Further, backwash water pump entrance is connected with effluent trough bottom delivery port；Go out pump entrance and effluent trough middle and lower part
Delivery port is connected.
Further, the positive plate, the electrode plate of minus plate two are ruthenium according to palladium platinum coating titanium-matrix electrode plate.
Further, the activated carbon catalysis oxide filler is Graphene coated activated carbon catalysis oxidation filler.
Further, the non-conductive enclosure material is PP or PVC.
Four phases catalytic oxidation technologies of the present utility model are employed：
1st, air/ozone aerating system provides hydroxyl free based raw material；
2nd, Graphene coated activated carbon catalytic filler system, filler adds rare earth catalyst manganese cerium oxide (Mn-Ce-O)
With electronic auxiliary (K2O)；
3rd, the titanium-matrix electrode plate of ruthenium iridium palladium platinum coating is scribbled；
4th, spray equipment；
5th, exhaust system
6th, backwashing system
The beneficial effects of the utility model：
Four phases catalytic oxidizing equipment of the present utility model is in a container with non-conductive shell (PP/PVC etc.)
It is interior, it is integrated into water cloth water system, air/ozone aerating system, Graphene coated activated carbon catalytic filler system, electrode catalyst system
System, spray system, backwashing system, exhaust system, outlet system, control system etc., by voltage, electric current, pole plate between pole plate
The control of spacing, operation pH value etc., under lower voltage, current conditions, forms that density is higher to be had in unit volume
The OH groups of strong oxidizing property realize that the deep oxidation of pollutant is decomposed as intermediate product.OH groups are in degrading waste water
Have the characteristics that：
1. OH groups have oxidizing electrode current potential (2.8V) higher, compare O3(2.07V) and H2O2(1.76V) is high respectively
35% and 59%, oxidability is only second to fluorine；
2. OH groups have electronegativity high (electrophilicity), and its electron affinity energy is 569.3kj, easy attack electron cloud high
Density points；
3. OH groups are the intermediate products of catalytic oxidation process, and chain reaction is induced as initiator, to biological difficult drop
Solution organic matter is particularly suitable；
4. OH groups non-selectivity in oxidation stain thing, and by oxidation operation be directly CO2、H2O or mineral salt,
The purpose that harmful substance is further destroyed is realized, new environmental pollution is not resulted in；
5. OH radical oxidations are a kind of physical and chemical processes, are easier control；
OH radical oxidations reaction condition is gentle, is easily controlled.
Four phases catalytic oxidizing equipment of the present utility model is realized：
1st, activated carbon physical absorption/online desorption in vivo；
2nd, optimize single air/ozone as oxidizing oxidability it is weaker (oxidizing potential be less than hydroxyl free
Base), the characteristics of many organic matters can not be oxidized, directly produced as raw material by the use of air/ozone in the presence of electric field/catalyst
Raw hydroxyl radical free radical, improves the utilization ratio of air/ozone；
3rd, overcoming conventional electro-catalysis technology can only lose activity in single plane catalysis oxidation, catalyst dissolution, carbon distribution,
(when using high voltage, system can spend more electric energy to produce hydrogen and oxygen due to electrolysis water to need offer high voltage more to consume energy
Gas is rather than generation hydroxyl radical free radical) the characteristics of, by adding manganese cerium oxide (Mn-Ce-O), electronics in active carbon filler
Auxiliary agent (K2O), liberation of hydrogen, oxygen evolution potential are lifted using the titanium-matrix electrode plate of ruthenium iridium palladium platinum coating, realizes the hydroxyl high under low energy consumption
Base free radical yield；
4th, sacrificial anode is not being used (such as：Irony anode) and it is a large amount of using acid, hydrogen peroxide, ferrous salt, do not produce big
Hydroxyl radical free radical more highdensity than Fenton oxidation is obtained in the case of amount sludge.
Brief description of the drawings
Fig. 1 is a kind of structural representation of four phases catalytic oxidizing equipment of the utility model.
In figure：1st, intake pump, 2, water distributor, 3, filter cap, 4, supporting plate, 5, aerator, 6, cobblestone bed course, 7, air blast wind
Machine, 8, Graphene coated activated carbon catalysis oxidation filler, 9, effluent weir, 10, ruthenium according to palladium platinum coating titanium-matrix electrode plate, 11, nozzle,
12nd, air-introduced machine, 13, ammeter, 14, voltmeter, 15, power supply, 16, catalysis oxidation groove, 17, feeding spraying pump, 18, backwash water pump,
19th, effluent trough, 20, go out water pump, 21, ozone generator, 22, automatic control system.
Specific embodiment
The utility model is further described below in conjunction with drawings and Examples.
Embodiment 1
As shown in figure 1, the utility model four phase catalytic oxidizing equipments of one kind, the device is including one with non-conductive shell
Closed container be catalysis oxidation groove cell body 16, cell body bottom is passed through water distributor 2, and water distributor 2 is provided with many water distributing pores；Water distribution
Tube inlet is exported with intake pump 1 respectively, the outlet of backwash water pump 18 is connected；Water distributor top is provided with supporting plate 4, is set on supporting plate 4
There are many apopores, filter cap 3 (preventing filler from falling blocking duct) is installed at apopore；Supporting plate 4 is provided with cobblestone above
Bed course 6 (being piled up on supporting plate 4 has cobblestone)；In the insertion of aerator 5 cobblestone bed course 6, the entrance of aerator 5 respectively with air blast wind
Machine 7 is exported or outlet connection of ozone generator 21 both (air blast blower fan and ozone generator, selecting one when using)；
Graphene coated activated carbon catalysis oxidation filler 8 is filled with cell body lower space above cobblestone bed course 6；Catalysis oxidation groove
The inside both sides of cell body 16 are respectively provided with some pieces of (being illustrated as two pieces) rutheniums according to palladium platinum coating titanium-matrix electrode plate 10, and one of is sun
Pole plate, another piece is minus plate, and two electrode plates are connected with the both positive and negative polarity of power supply 15 (ammeter 13 and electricity are provided with power supply respectively
Pressure table 14)；Cell body top is provided with effluent weir 9；On cell body top, the top of effluent weir 9 is passed through spray header 2, spray header entrance with
The outlet connection of feeding spraying pump 17；The bottom of spray header 2 is provided with nozzle 11；Cell body top is connected by induced duct with air-introduced machine 12；
The rear of catalysis oxidation groove 16 connects effluent trough 19 (weir flow connection)；The entrance of feeding spraying pump 17 connects with the middle part delivery port of effluent trough 19
Connect；The entrance of backwash water pump 18 is connected with effluent trough bottom delivery port；Go out the entrance of water pump 20 to be connected with effluent trough middle and lower part delivery port.
The both sides inwall of catalysis oxidation groove cell body 16 is provided with groove, and positive plate, minus plate are inserted in the groove of both sides respectively.
The device also includes automatic control system 22, and water pump, the wind to whole system are realized by automatic control system 22
Mechanical, electrical stream, voltage are automatically controlled.
Four phases catalytic oxidizing equipment of the present utility model, whole device agent structure includes：Water inlet water distribution system, air/
Ozonation aerated system, Graphene coated activated carbon catalytic filler system, electrode catalyst system, spray system, backwashing system, air draft
System, outlet system, control system；Wherein：
Water inlet water distribution system：The bottom of device is arranged on, by the power conveying of intake pump 1, the water distribution of water distributor 2, will
Pending high salt, with bio-toxicity or inhibitory action, high-COD waste water uniform water distribution, be allowed to be covered with whole system space；
Air/ozone aerating system：Air-source or ozone source are optional, and electricity is catalyzed in the titanium-based for scribbling ruthenium iridium palladium platinum coating
Pole plate 10 and it is coated with the space of Graphene coated activated carbon catalysis oxidation filler 8, in the clear of additional DC current and voltage
Under condition, the O that the air-source produced using air blast blower fan 7 is provided2Or the O that the ozone source of the generation of ozone generator 21 is provided3As
, there are a series of electrochemical reactions and produce more conventional two dimension, the more highdensity hydroxyl radical free radical of three-dimensional electrolysis in raw material, meanwhile,
O2Or O3Conventional oxidant is also served as, the organic substance in oxidized waste water is directly participated in；Air/ozone aerating system aerator 5
The top of supporting plate 4 is fixed on, top is piled up cobblestone bed course 6；
Graphene coated activated carbon catalytic filler system：Active carbon filler has porous characteristic, can be big in waste water
Organic pollution in amount Adsorption waste water, but single activated carbon is used as physical absorbent, can only be by pollutant
Solid phase is transferred to from liquid phase, not from truly removing decomposing organic pollutant, and its adsorption capacity is limited, easily reaches
Saturation, when high-concentration organic substance wastewater is adsorbed, the replacement cycle is very short.The Graphene coated activated carbon that the utility model is used
Catalytic filler adds Mn-Ce-O (manganese cerium oxide) as catalyst while adding electronic auxiliary (K in active carbon filler2O),
Effectively prevent metal dissolving, it is ensured that catalysis activity.The presence of graphite ene coatings, substantially increases the conduction of overall space
Performance, accomplishes current density higher at lower voltages, improves the ability that system catalytic oxidation produces hydroxyl radical free radical.
In the presence of highdensity hydroxyl radical free radical, the organic matter being tightly held by activated carbon is carbon dioxide by hydroxyl radical free radical oxidation Decomposition
And water, activated carbon absorption while desorbed, be always ensured that the organic matter removal ability of system.Graphite ene coatings activity
Charcoal catalytic filler system is arranged on into water water distribution system top, and centre is separated using supporting plate, and filter cap 3 is installed on supporting plate 4, is prevented
Only filler falls and is lost in, and cobblestone bed course 6, cobblestone bed course top arrangement Graphene coated activated carbon are placed in supporting plate top
Catalytic filler 8；
Electrode catalyst system：By maintaining certain DC voltage, a certain amount of current density between two battery lead plates,
The electronics for providing electric phase participates in reaction, produces the hydroxyl radical free radical of strong oxidizing property.Ruthenium iridium palladium platinum coating is scribbled on electrode, is improve
The liberation of hydrogen of battery lead plate, oxygen evolution potential, are easier generation hydroxyl radical free radical.Electrode catalyst system is arranged on the top of supporting plate 4, stone
Black ene coatings activated carbon catalysis filler 8 is uniformly covered with the space that whole battery lead plate is formed；
Spray system：Due to being provided with air/ozone aerating system in system, and in catalytic oxidation process, have a small amount of
Hydrogen, oxygen are produced, and these gases can produce substantial amounts of foam while rising in system, going out after being processed using system
Water sprays to eliminate the foam of surface generation as shower water.Spray system is arranged on the top of whole device；By shower water
Pump 17, nozzle 11 spray shower water.
Backwashing system：Due to being filled with filler in system, when system water inlet SS is too high, the feelings of blocking may be produced
Condition, backwashing system carries out backwash to it with the catalysis oxidation function of recovery system when filler is blocked.Backwashing system is utilized
Water inlet water distribution system realizes the thoroughly cleaning to whole system as backwash water distribution；
Exhaust system：Four phase catalytic oxidizing equipments integrally use sealed design, the reaction that is not able to do in time in system by
The O that air/ozone aerating system is provided2Or O3And hydrogen, oxygen, the carbon dioxide etc. that catalytic oxidation process is produced are by arranging
Place system is drawn.Exhaust system is arranged on the top of whole device, is produced using in negative suction system by air-introduced machine 12
Gas；
Outlet system：The effluent trough 19 at rear is flowed into by the waste water weir flow after the treatment of catalysis oxidation groove 16, then passes through
Water pump 20 is discharged, and is realized the draining of system and is transported to next handling process.
Control system：By automatic control system 22 realize water pump to whole system, blower fan, electric current, voltage it is automatic
Control.
Claims (8)
1. a kind of four phases catalytic oxidizing equipment, it is characterised in that the device includes a closed container with non-conductive shell
That is catalysis oxidation groove cell body, cell body bottom is passed through water distributor, and water distributor is provided with many water distributing pores；Water distribution tube inlet respectively with enter
Exit of pump, backwash water pump outlet connection；Water distributor top is provided with supporting plate, and supporting plate is provided with many apopores, apopore
Place is provided with filter cap；Cobblestone bed course is provided with above supporting plate；In aerator insertion cobblestone bed course, aerator entrance and air blast
Fan outlet or ozone generator outlet are connected；Activated carbon catalysis are filled with cell body lower space above cobblestone bed course
Oxide filler；Cell body inside both sides are respectively provided with some electrode plates, and a portion is used as positive plate, and another part is used as the moon
Pole plate, positive plate, minus plate are connected with the both positive and negative polarity of power supply respectively；Cell body top is provided with effluent weir；In cell body top effluent weir
Top is passed through spray header, and spray header entrance is connected with feeding spraying pump outlet；Spray header bottom is provided with nozzle；Cell body top
It is connected with air-introduced machine by induced duct；Catalysis oxidation groove rear connects effluent trough；Feeding spraying pump entrance and effluent trough middle part water outlet
Mouth connection.
2. four phases catalytic oxidizing equipment as claimed in claim 1, it is characterised in that set on the inwall of catalysis oxidation groove cell body both sides
Fluted, positive plate, minus plate are inserted in the groove of both sides respectively.
3. four phases catalytic oxidizing equipment as claimed in claim 1 or 2, it is characterised in that under backwash water pump entrance and effluent trough
Portion's delivery port connection；Go out pump entrance to be connected with effluent trough middle and lower part delivery port.
4. four phases catalytic oxidizing equipment as claimed in claim 1 or 2, it is characterised in that the battery lead plate is that ruthenium is applied according to palladium platinum
Layer titanium-matrix electrode plate.
5. four phases catalytic oxidizing equipment as claimed in claim 1 or 2, it is characterised in that the activated carbon catalysis oxide filler
It is Graphene coated activated carbon catalysis oxidation filler.
6. four phases catalytic oxidizing equipment as claimed in claim 1 or 2, it is characterised in that the non-conductive enclosure material is PP
Or PVC.
7. four phases catalytic oxidizing equipment as claimed in claim 1 or 2, it is characterised in that ammeter and voltage are provided with power supply
Table.
8. four phases catalytic oxidizing equipment as claimed in claim 1 or 2, it is characterised in that the device also include automatically controlling be
System, realizes automatically controlling the water pump of whole system, blower fan, electric current, voltage by automatic control system.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621243644.4U CN206188547U (en) | 2016-11-16 | 2016-11-16 | Four -phase catalytic oxidation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621243644.4U CN206188547U (en) | 2016-11-16 | 2016-11-16 | Four -phase catalytic oxidation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206188547U true CN206188547U (en) | 2017-05-24 |
Family
ID=58726919
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621243644.4U Expired - Fee Related CN206188547U (en) | 2016-11-16 | 2016-11-16 | Four -phase catalytic oxidation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206188547U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111592153A (en) * | 2020-05-30 | 2020-08-28 | 侯梦斌 | Multifunctional water treatment equipment and process containing graphene carbon catalytic particles |
| CN112456715A (en) * | 2020-12-06 | 2021-03-09 | 江苏金碧源环保科技有限公司 | Formaldehyde waste water catalytic unit |
| CN115521022A (en) * | 2022-09-21 | 2022-12-27 | 陕西尚远水务有限公司 | Pre-concentration separation process for sewage by comprehensive utilization of water resources |
| CN115536183A (en) * | 2022-10-30 | 2022-12-30 | 南京理工大学 | Based on DSA (MnO) X -Ti) cathode ozone/electrochemical coupling printing and dyeing wastewater treatment method of water treatment system |
-
2016
- 2016-11-16 CN CN201621243644.4U patent/CN206188547U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111592153A (en) * | 2020-05-30 | 2020-08-28 | 侯梦斌 | Multifunctional water treatment equipment and process containing graphene carbon catalytic particles |
| CN112456715A (en) * | 2020-12-06 | 2021-03-09 | 江苏金碧源环保科技有限公司 | Formaldehyde waste water catalytic unit |
| CN115521022A (en) * | 2022-09-21 | 2022-12-27 | 陕西尚远水务有限公司 | Pre-concentration separation process for sewage by comprehensive utilization of water resources |
| CN115536183A (en) * | 2022-10-30 | 2022-12-30 | 南京理工大学 | Based on DSA (MnO) X -Ti) cathode ozone/electrochemical coupling printing and dyeing wastewater treatment method of water treatment system |
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