CN105905986B - High-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus - Google Patents
High-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus Download PDFInfo
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- CN105905986B CN105905986B CN201610315474.4A CN201610315474A CN105905986B CN 105905986 B CN105905986 B CN 105905986B CN 201610315474 A CN201610315474 A CN 201610315474A CN 105905986 B CN105905986 B CN 105905986B
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- Prior art keywords
- multipole
- plate
- end cap
- anode
- cathode
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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
-
- 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
- C02F1/463—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
-
- 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
- C02F2201/002—Construction details of the apparatus
- C02F2201/007—Modular design
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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
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/14—Maintenance of water treatment installations
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- 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
High-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is related to sewage electric flocculation process field, the vertical cabinet connected side by side including several, cabinet upper and lower side is provided with intake-outlet, the intake-outlet is made of section changeover portion from big to small and nozzle section, nozzle section end is provided with connecting flange, cabinet any two corresponding side surface is opened wide, connecting flange is provided on two sides, multipole end cap is provided between the docking side of adjacent boxes, flange is correspondingly arranged on multipole end cap, two docking sides of adjacent boxes and multipole end cap are bolted connection, if multipole end cap two sides, which is welded with, constitutes multipole band by the multipole plate of the spaced and parallel setting of dry plate, the multipole plate of the intracorporal multipole band of adjacent tank is alternately inserted in gap each other, the cabinet at both ends is bolted respectively on outermost side Anode end cap and cathode end cap, anode end cap and cathode external face are connected with wiring bronze medal.
Description
Technical field
The present invention relates to sewage electric flocculation process field more particularly to electro-catalysis trash-removal devices.
Background technique
Water may be dirty by the organic and inorganic matter from the various sources for including daily life, municipal administration, industry and agricultural sources
Dye.Pollutant can be in solution, colloid or in suspended matter.The especially negatively charged colloid of colloid is often water pollutant
Principal mode.
Electrocoagulation is a kind of electrochemical method of water for handling and being polluted by various substances, is had in electrocoagulation reactor
Cathode and sacrificial anode.Metal cation (usually iron or aluminium) is caused to discharge from sacrificial anode to electrode supply electric current, and
Hydrogen is formed in cathode.Other chemical substances for helping to remove pollutant from water for participating in kinds of processes can be formed.
Existing electrocatalysis device, electrode utilization rate is not high, and is unenclosed construction, and reaction efficiency is lower, and electrode makes
It is shorter with the service life, and be all unitary structure, it is not possible to it is combined formula use, treatment effeciency is low, transport and cost of manufacture
It is higher, have much room for improvement.
Summary of the invention
In view of the deficiencies of the prior art, the present invention provides a kind of structure is simple, production method, replacement electrode is convenient, electricity
Pole utilization rate is high, long service life, and can modularization making, each module combined disassembly and the high-efficiency automatic control used are vertical
Determine pole electro-catalysis multipole decontamination apparatus.
Purpose to realize the present invention provides following technical scheme: high-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination dress
It sets, it is characterised in that including the vertical cabinet that several are connected side by side, cabinet upper and lower side is provided with intake-outlet, the disengaging
The mouth of a river is made of section changeover portion from big to small and nozzle section, and nozzle section end is provided with connecting flange, and cabinet is any
Two corresponding side surfaces are opened wide, and connecting flange is provided on two sides, is provided with multipole between the docking side of adjacent boxes
End cap is correspondingly arranged on flange on multipole end cap, and two docking sides of adjacent boxes and multipole end cap are fastened by bolts company
It connects, if multipole end cap two sides, which is welded with, constitutes multipole band by the multipole plate of the spaced and parallel setting of dry plate, adjacent tank is intracorporal multiple
The multipole plate of pole band is alternately inserted in gap each other, and anode is bolted on outermost side in the cabinet at both ends respectively
End cap and cathode end cap, if anode tap interior surface is welded with the anode strap being made of the anode plate of the spaced and parallel setting of dry plate,
If cathode terminal interior surface is welded with the Ka band being made of the cathode plate of the spaced and parallel setting of dry plate, the yin, yang of cathode and anode band
Pole plate is respectively alternately plugged with the intracorporal multipole plate of case, and anode end cap and cathode external face are connected with wiring bronze medal.
Preferably, the multipole plate on multipole end cap is set as needed as a face anode plate, a face cathode plate, multipole end
Lid include internal aluminum base, with the consistent anode layer of anode plate material and with the consistent cathode layer of cathode plate material.
Preferably, between adjacent cathode plate and multipole plate or adjacent anode plate and multipole plate or adjacent multipole plate
Gap is less than 10mm.
Preferably, the minimum range of the surrounding and end of yin, yang pole plate and multipole plate between each cabinet is not small
In 20mm.
Preferably, being provided with insulating materials on the joint face of cathode and anode end cap and multipole end cap and each body side
Layer.
Preferably, anode plate is identical with the material of anode end cap, it is 304 or 316 stainless steels.
Preferably, cathode plate is identical with the material of cathode end cap, it is titanium substrate, surface is coated with catalytic coatings layer.
Preferably, offering aperture on cathode plate or anode plate, being provided in aperture prevents yin, yang short-circuit between plates
Plastics knob.
The invention has the advantages that: W-response processes to occur inside this confined space of electro-catalysis cabinet, improves effect
Rate meets the condition sufficiently reflected, and overall space is closed, guarantees that secondary pollution will not be generated during reflection.Pole plate
Arrangement according to electro-catalysis cabinet shape, be arranged to Variable rate arrangement, this ensure that reflection covering space, guarantee be situated between
When matter reflects in electro-catalysis cabinet, without dead zone, process range covers integral medium.Anode and cathode pole plate spacing controls
Within 10mm, the service efficiency of pole plate ensure that.Ka band flange and anode strap flange are all made of flanged joint, maintain easily and
Replacement.And replace under flange and pole plate it is adjusted after can be recycled.Each cabinet is arranged using modularization, a cabinet independence
It at a module, can also be used with combined type, using multipole connection type, assembly is simple, and connection is reliable, can increase by site requirement
Add deduct few module, reaches final process requirement.
Detailed description of the invention
Fig. 1 is main view of the invention.
Fig. 2 is the left view of Fig. 1.
Fig. 3 is the A partial enlarged view of Fig. 2.
Fig. 4 is anode end cap main view.
Fig. 5 is the left view of Fig. 4.
Fig. 6 is the A of Fig. 5 to schematic diagram.
Fig. 7 is cathode end cap main view.
Fig. 8 is the left view of Fig. 7.
Fig. 9 is the A of Fig. 8 to schematic diagram.
Figure 10 is multipole end cap main view.
Figure 11 is the left view of Figure 10.
Figure 12 is the top view of Figure 10.
Figure 13 is the partial enlarged view of Figure 11.
Specific embodiment
Embodiment 1: high-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus, the vertical cabinet connected side by side including 5
1,1 upper and lower side of cabinet is provided with intake-outlet (2,3), changeover portion of the intake-outlet (2,3) by section from big to small
(2.1,3.1) and nozzle section (2.2,3.2) composition, nozzle section (2.2,3.2) end are provided with connecting flange, and each cabinet 1 is left
Right side (1.1,1.2) is opened wide, and is provided with connecting flange on left and right side (1.1,1.2), the docking sides of adjacent boxes 1 it
Between be provided with multipole end cap 4, flange, two docking sides of adjacent boxes 1 and multipole end cap are correspondingly arranged on multipole end cap 4
4 are bolted connection, and are made of the multipole plate 4.1 of the spaced and parallel setting of dry plate again if 4 two sides of multipole end cap is welded with
Pole band, wherein the multipole plate 4.1 on the left side is set as cathode plate, and the multipole plate 4.2 on the right side is set as anode plate, in adjacent boxes 1
Multipole band multipole plate 4.2 alternately be inserted in gap each other, sun is bolted in the left side 1.1 of left end cabinet 1
Extreme lid 5, it is most right if 5 inner surface of anode end cap is welded with the anode strap being made of the anode plate 5.1 of the spaced and parallel setting of dry plate
End cabinet 1 right side 1.2 cathode end cap 6 is bolted, if 6 inner surface of cathode end cap be welded with it is spaced and parallel by dry plate
The Ka band that the cathode plate 6.1 of setting is constituted, the yin, yang pole plate (6.1,5.1) of cathode and anode band are respectively corresponding in cabinet 1
Multipole plate 4.1 alternately plugs, and anode end cap 5 and 6 outer surface of cathode end cap are connected with wiring bronze medal 7.Multipole end cap 4 includes inside
Aluminum base 4.2, with the consistent anode layer 4.3 of anode plate material and with the consistent cathode layer 4.4 of cathode plate material.Adjacent yin
Gap between pole plate 6.1 and multipole plate 4.1 or adjacent anode plate 5.1 and multipole plate 4.1 or adjacent multipole plate 4.1 is less than
10mm.Minimum range of the surrounding and end of yin, yang pole plate (6.1,5.1) and multipole plate 4.1 between each cabinet 1 be not small
In 20mm.Insulation material layer 8 is provided on cathode and anode end cap (6,5) and multipole end cap 4 and the joint face of each 1 side of cabinet.
Anode plate 5.1 is identical with the material of anode end cap 5, is 304 or 316 stainless steels.The material of cathode plate 6.1 and cathode end cap 6
It is identical, it is titanium substrate, surface is coated with catalytic coatings layer.Aperture is offered on cathode plate 6.1 or anode plate 5.1, is set in aperture
It is equipped with the plastics knob for preventing yin, yang short-circuit between plates.It can be fastened after being all made of insulation sleeve at bolt, prevent short circuit.
Above-mentioned each cabinet may be alternatively provided as any shapes such as cuboid, round, rhombogen, be those skilled in the art
Predictable variation, intake-outlet and cabinet upper and lower side can be used welding, it is be bonded, the modes such as be bolted, be conventional skill
Art means, if any any similar malformation again in the protection scope of the application.
The setting of yin, yang pole plate considers the use of maximum area, and Variable rate can be used in the irregular cabinet such as cabinet
Setting.
Claims (8)
1. high-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is characterised in that the vertical case connected side by side including several
Body, cabinet upper and lower side are provided with intake-outlet, and the intake-outlet is by section changeover portion from big to small and nozzle section
Composition, nozzle section end are provided with connecting flange, and cabinet any two corresponding side surface is opened wide, and are provided with connection on two sides
Flange is provided with multipole end cap between the docking side of adjacent boxes, flange is correspondingly arranged on multipole end cap, adjacent boxes
Two docking sides and multipole end cap are bolted connection, and are set if multipole end cap two sides is welded with by dry plate is spaced and parallel
The multipole plate set constitutes multipole band, and the multipole plate of the intracorporal multipole band of adjacent tank is alternately inserted in gap each other, the case at both ends
Anode end cap and cathode end cap is bolted on the outermost side of body respectively, anode tap interior surface is welded with by several
The anode strap that the anode plate of the spaced and parallel setting of piece is constituted, if cathode terminal interior surface is welded with by the spaced and parallel setting of dry plate
The Ka band that cathode plate is constituted, the yin, yang pole plate of cathode and anode band are respectively alternately plugged with the intracorporal multipole plate of case, anode end cap
Wiring bronze medal is connected with cathode external face.
2. high-efficiency automatic control according to claim 1 is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is characterised in that multipole end
The multipole plate covered is set as needed as a face anode plate, a face cathode plate, multipole end cap include internal aluminum base, with sun
The consistent anode layer of pole plate material and with the consistent cathode layer of cathode plate material.
3. high-efficiency automatic control according to claim 1 is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is characterised in that adjacent yin
Gap between pole plate and multipole plate or adjacent anode plate and multipole plate or adjacent multipole plate is less than 10mm.
4. high-efficiency automatic control according to claim 1 is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is characterised in that cathode and anode
Minimum range of the surrounding and end of plate and multipole plate between each cabinet is not less than 20mm.
5. high-efficiency automatic control according to claim 1 is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is characterised in that cathode and anode
Insulation material layer is provided on the joint face of end cap and multipole end cap and each body side.
6. high-efficiency automatic control according to claim 1 is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is characterised in that anode plate
It is identical with the material of anode end cap, it is 304 or 316 stainless steels.
7. high-efficiency automatic control according to claim 1 is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is characterised in that cathode plate
It is identical with the material of cathode end cap, it is titanium substrate, surface is coated with catalytic coatings layer.
8. high-efficiency automatic control according to claim 1 is vertical to determine pole electro-catalysis multipole decontamination apparatus, it is characterised in that cathode plate
Or aperture is offered on anode plate, the plastics knob for preventing yin, yang short-circuit between plates is provided in aperture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201610315474.4A CN105905986B (en) | 2016-05-15 | 2016-05-15 | High-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus |
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CN201610315474.4A CN105905986B (en) | 2016-05-15 | 2016-05-15 | High-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus |
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CN105905986A CN105905986A (en) | 2016-08-31 |
CN105905986B true CN105905986B (en) | 2019-05-03 |
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CN105905996B (en) * | 2016-05-15 | 2019-05-03 | 宜兴市凌泰环保设备有限公司 | High-efficiency automatic control modularization determines pole electro-catalysis multipole decontamination apparatus |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2032629C1 (en) * | 1990-11-16 | 1995-04-10 | Научно-производственное объединение "Ротор" | Electric coagulator for treating dirty liquids |
CN104787858A (en) * | 2015-04-17 | 2015-07-22 | 中石化石油工程机械有限公司研究院 | Vertical electric flocculation reactor |
CN105905996A (en) * | 2016-05-15 | 2016-08-31 | 宜兴市凌泰环保设备有限公司 | High-efficiency self-control modularized fixed-electrode electro-catalysis composite-electrode dirt removal device |
CN205990264U (en) * | 2016-05-15 | 2017-03-01 | 宜兴市凌泰环保设备有限公司 | High-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus |
-
2016
- 2016-05-15 CN CN201610315474.4A patent/CN105905986B/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2032629C1 (en) * | 1990-11-16 | 1995-04-10 | Научно-производственное объединение "Ротор" | Electric coagulator for treating dirty liquids |
CN104787858A (en) * | 2015-04-17 | 2015-07-22 | 中石化石油工程机械有限公司研究院 | Vertical electric flocculation reactor |
CN105905996A (en) * | 2016-05-15 | 2016-08-31 | 宜兴市凌泰环保设备有限公司 | High-efficiency self-control modularized fixed-electrode electro-catalysis composite-electrode dirt removal device |
CN205990264U (en) * | 2016-05-15 | 2017-03-01 | 宜兴市凌泰环保设备有限公司 | High-efficiency automatic control is vertical to determine pole electro-catalysis multipole decontamination apparatus |
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