CN110204013A - A kind of Modular electrical catalysis oxidation sewage disposal system - Google Patents
A kind of Modular electrical catalysis oxidation sewage disposal system Download PDFInfo
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- CN110204013A CN110204013A CN201910497827.0A CN201910497827A CN110204013A CN 110204013 A CN110204013 A CN 110204013A CN 201910497827 A CN201910497827 A CN 201910497827A CN 110204013 A CN110204013 A CN 110204013A
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- 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
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
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Abstract
The present invention relates to a kind of Modular electrical catalysis oxidation sewage disposal systems, including catalysis oxidation pond, with water inlet, water outlet and interior structural support frame, are equipped with multiple installation units in frame；Electrocatalysis oxidation apparatus, it is equipped with multiple groups, and it is respectively arranged in each installation unit, every group of electrocatalysis oxidation apparatus includes shell and at least a pair of of electrolysis basket, catalyst is filled in each electrolysis basket, catalyst and the sewage contact free entered inside electrolysis basket are equipped with water coke slurry hole wherein being connected separately with anode and cathode on each electrolysis basket on each shell；Anode electrode film is electrically connected with the anode of each electrolysis basket respectively；Cathode electrode sheet is electrically connected with the cathode of each electrolysis basket respectively.Advantage: being able to achieve electrocatalytic oxidation sewage disposal technology and the modularization of technique and combine, improve treatment effeciency and the adaptability to sewage composition and changes in flow rate, greatly simplifies the process of its O&M and reduces O&M expense.
Description
Technical field
The present invention relates to sewage disposal technology, in particular to a kind of Modular electrical catalysis oxidation sewage disposal system.
Background technique
Current representational sewage disposal technology includes biochemical technology, membrane technology.Although in some sewage treatments
It attempted using technologies such as electro-catalytic oxidation technology and Ozonations, but to some source of sewage, treatment effect can not expire
Foot requires, and operation cost also has exceeded the range that can be born.
The biochemical sewage processing technique being widely used at present, advantage are the sewage to certain biochemical processing, operating expenses
With can be relatively low, but there is at least following problem to be difficult to avoid that: 1) generally requiring to build up volume or occupied area is larger
Treatment tank；2) the biochemical reaction time needed for it is longer；3) to some nondecomposable pollution sources parts containing microorganism
The pollutant, such as dyeing and printing sewage, trade effluent, coked waste water etc. of i.e. non-BOD class, biochemical technology is generally unable to satisfy processing and wants
It asks, if processing cost is often excessively high in conjunction with other technologies, enterprise is difficult to bear.
Membrane technology can accomplish a degree of miniaturization to a certain extent, but often also have multinomial deficiency.For example, fortune
Seek at high cost and other than the purified water after film, membrane technology cannot directly separate pollutant from sewage, film
Before can only play the role of concentration, inherently fail to complete independently sewage treatment.
Common its oxidation efficiency of electrocatalytic oxidation sewage disposal technology is not high at present, and similarly, Ozonation is thrown
Money and operation cost are all very high, and treatment effect is also undesirable.
Emerging one kind realizes height by using technologies such as special catalysts based on efficient electro-catalytic oxidation technology
Micro- active oxygen of effect occurs and oxidation reaction, can be directly by pollutant oxygenolysis, and the pollutant after decomposition is divided from water
From, reach drop the targets such as COD, BOD and dephosphorization denitrogenation.The technology has extensive adaptability to pollutant, but the disadvantage is that electricity is urged
Changing oxidation, the device is complicated, design and installation, difficult in maintenance, it is difficult to realize that the large-scale industrial of such sewage disposal technology is answered
With.The modular design of electrocatalytic oxidation has well solved this problem with building technology.
Summary of the invention
Technical problem to be solved by the invention is to provide a kind of Modular electrical catalysis oxidation sewage disposal systems, can be effective
Ground overcomes the technological deficiency of existing electrocatalytic oxidation application.
The technical scheme to solve the above technical problems is that a kind of Modular electrical catalysis oxidation sewage treatment system
System, including catalysis oxidation pond, above-mentioned catalysis oxidation pond have inlet and outlet, are equipped with structure inside above-mentioned catalysis oxidation pond
Braced frame, above structure braced frame are interior equipped with multiple uniform or regular distribution installation units；Electrocatalysis oxidation apparatus, on
Electrocatalysis oxidation apparatus is stated equipped with multiple groups, and is installed on correspondingly in each above-mentioned installation unit respectively, every group of above-mentioned electricity
Catalytic oxidizing equipment includes shell and at least a pair of of electrolysis basket, is filled with catalyst inside each above-mentioned electrolysis basket, above-mentioned
Catalyst and enter the blue internal sewage contact free of electrolysis through the mesh in above-mentioned electrolysis basket, in the above-mentioned electrolysis basket of a pair,
It is connected with anode on one of them above-mentioned electrolysis basket, is connected with cathode on another above-mentioned electrolysis basket, on each above-mentioned shell
It is equipped with water coke slurry hole；Anode electrode film, above-mentioned anode electrode film are electrically connected with the anode of each above-mentioned electrolysis basket respectively；Cathode
Electrode slice, above-mentioned cathode electrode sheet are electrically connected with the cathode of each above-mentioned electrolysis basket respectively.
The beneficial effects of the present invention are: it is reasonable in design, it can be realized arbitrary modular combination and extension, improve
The sewage treating efficiency of electrocatalytic oxidation improves adaptability (such as influent quality of the sewage disposal technology of electrocatalytic oxidation
With the variation of inflow), and can greatly simplify operation and attended operation, reduce operating cost.
Based on the above technical solution, the present invention can also be improved as follows.
Further, multiple above-mentioned installation unit rectangular array distributions.
Beneficial effect using above-mentioned further scheme is that arrangement is simple, reasonable, facilitates multiple groups electrocatalysis oxidation apparatus group
It closes and uses.
Further, above-mentioned shell is cuboid shell.
Beneficial effect using above-mentioned further scheme is regular shape, is conducive to multiple groups modularization and is distributed.
Further, in the above-mentioned electrocatalysis oxidation apparatus of same row, the upper end of each above-mentioned shell be respectively equipped with inside it
Above-mentioned anode and cathode correspond and electrical connection positive contact and cathode connection, the lower end of each above-mentioned shell is set respectively
Have and is electrically connected anode interface and cathode interface, underlying above-mentioned shell correspondingly with its internal above-mentioned anode and cathode
Anode interface and yin on the adjacent above-mentioned shell in top are inserted into positive contact and cathode connection on body correspondingly respectively
In the interface of pole, and be electrically connected to each other, the positive contact and cathode connection on the above-mentioned shell in the top respectively with above-mentioned anode
Electrode slice and cathode electrode sheet electrical connection.
Beneficial effect using above-mentioned further scheme is that the design can be realized each column multiple groups electrocatalysis oxidation apparatus
Fast Installation between anode and cathode combines and extension.
Further, to limit multiple row by upward and downward partition mounted thereto in above structure braced frame mutually indepedent
And closed electrocatalytic oxidation compartment, the upper and lower side of the above-mentioned electrocatalytic oxidation compartment of each column are respectively equipped with and above-mentioned catalysis oxidation pond
The water inlet and discharge outlet of internal connection, the above-mentioned electrocatalysis oxidation apparatus of the multiple groups of each column are distributed in often correspondingly respectively
It arranges in above-mentioned electrocatalytic oxidation compartment, the upper and lower side of the shell of each above-mentioned electrocatalysis oxidation apparatus is respectively equipped with above-mentioned water coke slurry
Hole, two neighboring above-mentioned shell by both water coke slurry hole connection close to each other, in same row, two neighbouring connections
Have between the electrolysis basket for being electrolysed between basket and being connected with above-mentioned cathode of above-mentioned anode respectively by through the two corresponding housing
Connecting pipe be connected.
Beneficial effect using above-mentioned further scheme is that the design enables to each column multiple groups electrocatalysis oxidation apparatus string
Connection combination extension, and make between each column multiple groups electrocatalysis oxidation apparatus interior sewage treatment along specifically flowing is flowed through, finally in fact
Existing sewage is effectively treated.
Further, current deflecting is mounted at the water inlet of the above-mentioned electrocatalytic oxidation compartment upper and lower side of each column and discharge outlet
Mouth.
Beneficial effect using above-mentioned further scheme is that the design of current deflecting mouth enables to water in electrocatalytic oxidation
Stable or turbulent or rotation form is kept in apparatus module, conducive to the good flow of sewage.
Further, to limit multilayer by horizontal direction partition mounted thereto in above structure braced frame mutually indepedent
And closed class electrocatalytic oxidation interlayer, be respectively equipped on every layer of above-mentioned class electrocatalytic oxidation interlayer in above-mentioned catalysis oxidation pond
The water inlet and discharge outlet of portion's connection, the above-mentioned electrocatalysis oxidation apparatus of every layer of multiple groups is in corresponding one layer of above-mentioned class electrocatalytic oxidation
Change spatially sequence of positions series connection in interlayer, and the shell of each above-mentioned electrocatalysis oxidation apparatus is in the two sides point in its direction of connecting
Not She You above-mentioned water coke slurry hole, also, two neighboring above-mentioned shell by both water coke slurry hole close to each other be connected, it is same
In layer, two neighboring be connected between the electrolysis basket for being electrolysed between basket and being connected with above-mentioned cathode of above-mentioned anode passes through respectively
Connecting pipe through the two corresponding housing is connected.
Beneficial effect using above-mentioned further scheme is that the design enables to every layer of multiple groups electrocatalysis oxidation apparatus string
Connection combination extension, and make between every layer of multiple groups electrocatalysis oxidation apparatus interior sewage treatment along different and specific flow through stream
It is dynamic, it is final to realize being effectively treated for sewage.
Further, each above-mentioned electrocatalytic oxidation interlayer go out, water inlet be mounted on current deflecting mouth.
Beneficial effect using above-mentioned further scheme is that the design of current deflecting mouth enables to water in electrocatalytic oxidation
Stable or turbulent or rotation form is kept in apparatus module, conducive to the good flow of sewage.
Further, current deflecting is separately installed at the water inlet of every layer of above-mentioned class electrocatalytic oxidation interlayer and discharge outlet
Mouth.
Beneficial effect using above-mentioned further scheme is connection and reasonable arrangement, conducive to the Fast Installation and company of anode and cathode
It connects and subsequent possible maintenance.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of Modular electrical catalysis oxidation sewage disposal system of the invention.
In attached drawing, parts list represented by the reference numerals are as follows:
1, catalysis oxidation pond, 2, structural support frame, 3, electrocatalysis oxidation apparatus, 4, anode electrode film, 5, cathode electrode
Piece.
Specific embodiment
The principle and features of the present invention will be described below with reference to the accompanying drawings, and the given examples are served only to explain the present invention, and
It is non-to be used to limit the scope of the invention.
Embodiment: as shown, the Modular electrical catalysis oxidation sewage disposal system of the present embodiment, including catalysis oxidation pond
1, above-mentioned catalysis oxidation pond 1 has inlet and outlet, and structural support frame 2 is equipped with inside above-mentioned catalysis oxidation pond 1, above-mentioned
Multiple equally distributed installation units are equipped in structural support frame 2；Electrocatalysis oxidation apparatus 3, above-mentioned electrocatalysis oxidation apparatus 3
It equipped with multiple groups, and is installed on correspondingly in each above-mentioned installation unit respectively, every group of above-mentioned electrocatalysis oxidation apparatus 3 wraps
Shell 31 and at least a pair of of electrolysis basket 32 are included, is filled with catalyst inside each above-mentioned electrolysis basket 32, above-mentioned catalyst and thoroughly
The mesh crossed in above-mentioned electrolysis indigo plant 32 enters the sewage contact free of 32 inside of electrolysis indigo plant, in the above-mentioned electrolysis basket 32 of a pair, wherein
It is connected with anode on one above-mentioned electrolysis basket 32, cathode, each above-mentioned shell 31 are connected on another above-mentioned electrolysis basket 32
On be equipped with water coke slurry hole；Anode electrode film 4, anode of the above-mentioned anode electrode film 4 respectively with each above-mentioned electrolysis basket 32 are electrically connected
It connects；Cathode electrode sheet 5, above-mentioned cathode electrode sheet 5 are electrically connected with the cathode of each above-mentioned electrolysis basket 32 respectively.
When being applied in combination, independent assortment splicing can be installed by design between the above-mentioned electrocatalysis oxidation apparatus 3 of multiple groups
With serial or parallel connection, specifically, by the way that multiple baffles are detachably arranged in structural support frame 2, so that being serially connected
Multiple groups electrocatalysis oxidation apparatus 3 between formed a sewage flow path, and ensure be located at upstream beginning (when series connection in first place
One) and downstream end (one when series connection in last bit) electrocatalysis oxidation apparatus 3 shell 31 water coke slurry hole point
Not and into the sewage connection inside catalysis oxidation pond 1, in parallel connection, detachably set by passing through in structural support frame 2
Multiple baffles or valve are set, so that flowing through after parallel connection per sewage all the way all constitutes individual sewage treatment channel, per equal all the way
Can be serially connected by multiple groups electrocatalysis oxidation apparatus 3, and ensure to be located at upstream beginning (when series connection in the first one) and
It is urged respectively with entrance in the water coke slurry hole of the shell 31 of the electrocatalysis oxidation apparatus 3 of downstream end (one when series connection in last bit)
Change the sewage connection inside oxidation pond 1, thus complete processing system it is integrated, it is regular orderly, modular splicing.
As a preferred embodiment, multiple above-mentioned installation unit rectangular array distributions, also, most preferably, on
Stating shell 31 is cuboid shell.
When assembly, in the above-mentioned electrocatalysis oxidation apparatus 3 of same row, the upper end of each above-mentioned shell 31 be respectively equipped with in it
The above-mentioned anode and cathode in portion corresponds and the positive contact 33 and cathode connection 34 of electrical connection, under each above-mentioned shell 31
End is respectively equipped with is electrically connected anode interface and cathode interface with its internal above-mentioned anode and cathode correspondingly, is located below
Above-mentioned shell 31 on positive contact 33 and the adjacent above-mentioned shell 31 in insertion top correspondingly respectively of cathode connection 34
On anode interface and cathode interface in, and be electrically connected to each other, positive contact 33 and yin on the above-mentioned shell 31 in the top
Pole connector 34 is electrically connected with above-mentioned anode electrode film 4 and cathode electrode sheet 5 respectively, which is conducive to multiple groups electrocatalysis oxidation apparatus
Interconnection between 3 Anodics between cathode respectively, simplifies anode and the respective connection arrangement of cathode, reduces
It arranges difficulty, also, is highly convenient for the fast assembling-disassembling combination of neighbouring two electrocatalysis oxidation apparatus 3.
Certainly, multiple groups electrocatalysis oxidation apparatus 3 is also possible to be distributed or Else Rule with cylindrical array manner
Array distribution mode, be not limited in rectangular array arrangement.
By taking rectangular array as an example, the combination between multiple groups electrocatalysis oxidation apparatus 3 has following various ways:
Multiple row is limited independently of each other by upward and downward partition mounted thereto in above structure braced frame 2 and is closed
Electrocatalytic oxidation compartment, the upper and lower side of the above-mentioned electrocatalytic oxidation compartment of each column be respectively equipped with inside above-mentioned catalysis oxidation pond 1
The water inlet and discharge outlet of connection, the above-mentioned electrocatalysis oxidation apparatus 3 of the multiple groups of each column are distributed in each column correspondingly respectively
In above-mentioned electrocatalytic oxidation compartment, the upper and lower side of the shell 31 of each above-mentioned electrocatalysis oxidation apparatus 3 is respectively equipped with above-mentioned water and hands over
Change hole, two neighboring above-mentioned shell 31 by both the mutual connection in water coke slurry hole close to each other, it is neighbouring in same row
Two are connected between the electrolysis indigo plant 32 of above-mentioned anode and are connected between the electrolysis indigo plant 32 of above-mentioned cathode respectively by running through
The connecting pipe of the two corresponding housing 31 is connected, wherein the 3 lower end area non-close knot of electrocatalysis oxidation apparatus of bottom
Structure, and keep the connection whole with catalysis oxidation pond 1, that is, it is exactly and the sewage connection inside catalysis oxidation pond 1；
Wherein, current deflecting is mounted at the water inlet of the above-mentioned electrocatalytic oxidation compartment upper and lower side of each column and discharge outlet
Mouth enables to water to keep stable or turbulent or rotation in electrocatalysis oxidation apparatus module by the design of current deflecting mouth
The form turned, conducive to the good flow of sewage.
It should be understood that connection can be concatenated conducive to same row multiple groups between above-mentioned neighbouring two Electricity Federation indigo plant 32
The supplement or replacement of internal accelerator between electrolysis indigo plant 32.
Multilayer is limited independently of each other by horizontal direction partition mounted thereto in above structure braced frame 2 and is closed
Class electrocatalytic oxidation interlayer, be respectively equipped on every layer of above-mentioned class electrocatalytic oxidation interlayer and join with inside above-mentioned catalysis oxidation pond 1
Logical water inlet and discharge outlet, the above-mentioned electrocatalysis oxidation apparatus 3 of every layer of multiple groups is in corresponding one layer of above-mentioned class electrocatalytic oxidation
In interlayer spatially sequence of positions series connection (specifically: the shell 31 of each multiple electrocatalysis oxidation apparatus 3 of layer press linear space
Position distribution sequential series, the linear spatial position can be full of twists and turns route), and each above-mentioned electrocatalytic oxidation makeup
The shell 31 for setting 3 is respectively equipped with above-mentioned water coke slurry hole in the two sides that it connects direction, also, two neighboring above-mentioned shell 31 passes through
The two mutual connection in water coke slurry hole close to each other, in same layer, between the two neighboring electrolysis indigo plant 32 for being connected with above-mentioned anode
And be connected between the electrolysis indigo plant 32 of above-mentioned cathode respectively by being connected through the connecting pipe of the two corresponding housing 31,
In, in the shell 31 of the multiple groups water route connection (series connection) in same group of electrocatalytic oxidation interlayer, positioned at the first and end shell
31 equal whole connection with catalysis oxidation pond 1 are exactly and the sewage connection inside catalysis oxidation pond 1；
Wherein, it is separately installed with current deflecting mouth at the water inlet of every layer of above-mentioned class electrocatalytic oxidation interlayer and discharge outlet,
The design enables to every layer of 3 tandem compound of multiple groups electrocatalysis oxidation apparatus extension, and makes every layer of multiple groups electrocatalytic oxidation makeup
Set between 3 interior sewage treatment along it is different and it is specific flow through flowing, finally meet being effectively treated for sewage.
3) in the above-mentioned electrocatalysis oxidation apparatus 3 of same row, the upper and lower side of above-mentioned shell 31 is equipped with above-mentioned water coke slurry hole, position
Join in the water coke slurry hole water route of the water coke slurry hole of 31 lower end of above-mentioned shell of top 31 upper end of above-mentioned shell adjacent with lower section
Logical (series connection), also, water coke slurry hole is also offered on side wall close to each other between each layer of all shells 31, so that the two
Mutual water route connection within the same layer, specifically, in each layer of multiple shells 31, two neighboring shell 31 it is close to each other one
Face is equipped with water coke slurry hole, and mutual connection between water coke slurry hole close to each other.
It should be noted that: pass through the connection and connection sequence between the shell 31 of every group of electrocatalysis oxidation apparatus 3
Flow direction of the adjustable sewage inside multiple groups electrocatalysis oxidation apparatus 3, correspondingly, according to sewage on structural support frame 2
Flow direction and multiple groups shell 31 between link relation come any setting partition, thus formed required for sewage treatment road
Diameter reconstructs multiple groups electrocatalysis oxidation apparatus 3 arbitrarily arbitrarily according to the form of serial or parallel connection to meet to dirt
The requirement of water process amount and sewage composition variation.
Embodiment party's examination as one preferred, above-mentioned anode electrode film 4 and cathode electrode sheet 5 are set up in above-mentioned catalysis respectively
The upper end of oxidation pond 1, setting rationally, conducive to anode electrode film 4 and cathode electrode sheet 5 respectively at anode and cathode connection.
Catalysis oxidation pond 1 inlet and outlet and/or the internal position for optionally acting as detection is settable is used for
Detect its flow, temperature, hydraulic pressure, COD, BOD, pH value, total nitrogen, total phosphorus or the one or more monitoring group of turbidity/suspended matter
Part or sampled point, in conjunction with the operating power of 3 internal electrode of acquisition and single or multiple electrocatalysis oxidation apparatus of above- mentioned information
Or voltage, electric current, so that it may constitute the monitoring to entire electrocatalytic oxidation system running state.
Whole system has the advantage that
1) Unified Form or the Modular electrical catalytic oxidizing equipment 3 of standardization, can with large-scale volume production easy to form and
Standardized installation avoids complicated, in disorder, many and diverse installation and detection process, and can greatly improve build guality, drop
Low error and rejection rate；
2) in whole system, modules are easy detection and maintenance.To the unit of damage, the stock that need to only make good use of at the scene
Unit simply replaces damaged unit, and internal each column multiple groups electrolysis blue phase connects, and can be conducive to the benefit of subsequent catalyst
It fills and replaces, integrally reduce the cost of operation and maintenance；
3) in use, can according to need, increase and decrease the quantity and series-parallel assembling form of electrocatalysis oxidation apparatus 31, make
The efficiency of sewage treatment greatly improves or in the case where meeting processing requirement, reduces operating cost, and improve electrocatalytic oxidation
Sewage treating efficiency；
4) in use, can source according to sewage or pollution level, easily reduction or extension electro-catalysis as needed
The element number of oxidation, including being increased and decreased according to series connection and different form in parallel.Multistage depth can be completed when series connection
Reason when in parallel, can complete processing while multi-path sewage, improve processing capacity, and therefore, modular design has non-with technology
The adaptability of Chang Youyi.
The foregoing is merely presently preferred embodiments of the present invention, is not intended to limit the invention, it is all in spirit of the invention and
Within principle, any modification, equivalent replacement, improvement and so on be should all be included in the protection scope of the present invention.
Claims (9)
1. a kind of Modular electrical catalysis oxidation sewage disposal system characterized by comprising
Catalysis oxidation pond (1), the catalysis oxidation pond (1) have inlet and outlet, set inside the catalysis oxidation pond (1)
Have structural support frame (2), equipped with multiple uniform or regular distribution installation units in the structural support frame (2)；
Electrocatalysis oxidation apparatus (3), the electrocatalysis oxidation apparatus (3) are equipped with multiple groups, and are installed on correspondingly respectively every
In a installation unit, electrocatalysis oxidation apparatus described in every group (3) includes shell (31) and at least a pair is electrolysed basket (32),
Each electrolysis basket (32) is internal to be filled with catalyst, the catalyst and through the mesh being electrolysed on blue (32) into
Enter to be electrolysed sewage contact free of blue (32) inside, in a pair of electrolysis basket (32), on one of them described electrolysis basket (32)
It is connected with anode, cathode is connected on another described electrolysis basket (32), is equipped with water coke slurry on each shell (31)
Hole；
Anode electrode film (4), the anode electrode film (4) are electrically connected with the anode of each electrolysis basket (32) respectively；
Cathode electrode sheet (5), the cathode electrode sheet (5) are electrically connected with the cathode of each electrolysis basket (32) respectively.
2. a kind of Modular electrical catalysis oxidation sewage disposal system according to claim 1, it is characterised in that: multiple described
The distribution of installation unit rectangular array.
3. a kind of Modular electrical catalysis oxidation sewage disposal system according to claim 2, it is characterised in that: the shell
It (31) is cuboid shell.
4. a kind of Modular electrical catalysis oxidation sewage disposal system according to claim 2 or 3, it is characterised in that: same
Arrange in the electrocatalysis oxidation apparatus (3), the upper end of each shell (31) be respectively equipped with the anode internal with it and
Cathode corresponds and the positive contact (33) and cathode connection (34) of electrical connection, and the lower end of each shell (31) is set respectively
Have and is electrically connected anode interface and cathode interface, the underlying shell correspondingly with its internal anode and cathode
The adjacent shell (31) in top is inserted into positive contact (33) and cathode connection (34) on body (31) correspondingly respectively
On anode interface and cathode interface in, and be electrically connected to each other, the positive contact (33) being located on shell (31) described in the top
It is electrically connected respectively with the anode electrode film (4) and cathode electrode sheet (5) with cathode connection (34).
5. a kind of Modular electrical catalysis oxidation sewage disposal system according to claim 4, it is characterised in that: the structure
By upward and downward partition mounted thereto limit that multiple row is mutually indepedent in braced frame (2) and closed electrocatalytic oxidation every
Between, the upper and lower side of electrocatalytic oxidation compartment described in each column is respectively equipped with the water inlet with the internal connection of the catalysis oxidation pond (1)
And discharge outlet, electrocatalysis oxidation apparatus (3) described in the multiple groups of each column are distributed in electro-catalysis described in each column correspondingly respectively
It aoxidizes in compartment, the upper and lower side of the shell (31) of each electrocatalysis oxidation apparatus (3) is respectively equipped with the water coke slurry hole, phase
Adjacent two shells (31) by both water coke slurry hole connection close to each other, in same row, two neighbouring shells
It is inside connected between the electrolysis blue (32) of the anode and is connected between the electrolysis blue (32) of the cathode respectively by passing through
The connecting pipe for wearing the two corresponding housing (31) is connected.
6. a kind of Modular electrical catalysis oxidation sewage disposal system according to claim 5, it is characterised in that: described in each column
Current deflecting mouth is mounted at the water inlet and discharge outlet of electrocatalytic oxidation compartment upper and lower side.
7. a kind of Modular electrical catalysis oxidation sewage disposal system according to claim 4, it is characterised in that: the structure
Limit by horizontal direction partition mounted thereto that multilayer is mutually indepedent and closed class electrocatalytic oxidation in braced frame (2)
Interlayer, be respectively equipped on every layer of class electrocatalytic oxidation interlayer with the water inlet of the internal connection of the catalysis oxidation pond (1) and
Discharge outlet, electrocatalysis oxidation apparatus (3) described in every layer of multiple groups in the class electrocatalytic oxidation interlayer of respective layer spatially
Sequence of positions series connection, and the shell (31) of each electrocatalysis oxidation apparatus (3) is respectively equipped in the two sides that it connects direction
The water coke slurry hole, also, the water coke slurry hole connection that the two neighboring shell (31) is close to each other by the two, same layer
In, between the two neighboring electrolysis blue (32) for being connected with the anode and it is connected between the electrolysis blue (32) of the cathode point
Not by being connected through the connecting pipe of the two corresponding housing (31).
8. a kind of Modular electrical catalysis oxidation sewage disposal system according to claim 7, it is characterised in that: described in every layer
Current deflecting mouth is separately installed at the water inlet and discharge outlet of class electrocatalytic oxidation interlayer.
9. according to claim 1 to a kind of Modular electrical catalysis oxidation sewage disposal system described in 3, it is characterised in that: described
Anode electrode film (4) and cathode electrode sheet (5) are set up in the upper end of the catalysis oxidation pond (1) respectively.
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| CN201910497827.0A CN110204013A (en) | 2019-06-10 | 2019-06-10 | A kind of Modular electrical catalysis oxidation sewage disposal system |
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| CN201910497827.0A CN110204013A (en) | 2019-06-10 | 2019-06-10 | A kind of Modular electrical catalysis oxidation sewage disposal system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113862697A (en) * | 2021-09-29 | 2021-12-31 | 中检陆桥(中山市)科技有限公司 | Device for hydrolyzing ozone by using multilayer PEM (proton exchange membrane) |
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2019
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113862697A (en) * | 2021-09-29 | 2021-12-31 | 中检陆桥(中山市)科技有限公司 | Device for hydrolyzing ozone by using multilayer PEM (proton exchange membrane) |
| CN113862697B (en) * | 2021-09-29 | 2022-06-14 | 中检陆桥(中山市)科技有限公司 | Device for hydrolyzing ozone by using multilayer PEM (proton exchange membrane) |
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