CN107749347A - A kind of novel electrolytic bath device and its implementation - Google Patents
A kind of novel electrolytic bath device and its implementation Download PDFInfo
- Publication number
- CN107749347A CN107749347A CN201710929884.2A CN201710929884A CN107749347A CN 107749347 A CN107749347 A CN 107749347A CN 201710929884 A CN201710929884 A CN 201710929884A CN 107749347 A CN107749347 A CN 107749347A
- Authority
- CN
- China
- Prior art keywords
- valve
- electrolytic bath
- filter
- heat exchanger
- bath device
- 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.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/005—Apparatus specially adapted for electrolytic conversion coating
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D11/00—Electrolytic coating by surface reaction, i.e. forming conversion layers
- C25D11/02—Anodisation
- C25D11/04—Anodisation of aluminium or alloys based thereon
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/02—Heating or cooling
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D21/00—Processes for servicing or operating cells for electrolytic coating
- C25D21/06—Filtering particles other than ions
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/042—Electrodes or formation of dielectric layers thereon characterised by the material
- H01G9/045—Electrodes or formation of dielectric layers thereon characterised by the material based on aluminium
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01G—CAPACITORS; CAPACITORS, RECTIFIERS, DETECTORS, SWITCHING DEVICES OR LIGHT-SENSITIVE DEVICES, OF THE ELECTROLYTIC TYPE
- H01G9/00—Electrolytic capacitors, rectifiers, detectors, switching devices, light-sensitive or temperature-sensitive devices; Processes of their manufacture
- H01G9/004—Details
- H01G9/04—Electrodes or formation of dielectric layers thereon
- H01G9/048—Electrodes or formation of dielectric layers thereon characterised by their structure
- H01G9/055—Etched foil electrodes
Abstract
The invention discloses a kind of novel electrolytic bath device, including electrolytic bath, electrolytic bath upper end offers circulation import, electrolytic bath lower end offers loop exit, loop exit is connected by pipeline with circulating pump, circulating pump is connected with filter, backup line is provided between circulating pump and filter, the entrance point of backup line and heater connects, filter outlet end connects the entrance point of standby pipe and heat exchanger respectively, the entrance point of heat exchanger is also associated with flow control tube road, the port of export of heater, the port of export of the control pipeline port of export and heat exchanger is connected to circulation inlet.The invention also discloses a kind of implementation method of novel electrolytic bath device.The present invention has the characteristics that simple in construction, low cost, production efficiency are high, filter, heat and be cooled in electrolytic bath and completed outside.
Description
Technical field
The present invention relates to electrolytic bath technology, specifically a kind of novel electrolytic bath device and its implementation.
Background technology
It is melted on big production line in mesohigh, anode foil for low-voltage aluminum electrolytic capacitor, is needed before normal production to chemical conversion
Tank liquor is preheated, and when carrying out etched foil normal chemical conversion production, then needs to cool down chemical conversion tank liquor to ensure
Tank liquor temperature it is constant.Traditional method is to set several groups of electrically heated rods in chemical conversion trench bottom or side, and and passes through electrical bar
The preheating to being melted into tank liquor is completed in heating.And the cooling for being melted into tank liquor is then to set several groups of coolings in chemical conversion trench bottom or side
Row sets water-cooled heat exchanger outside electrolytic bath, and is completed by the row of cooling or water-cooled heat exchanger to the cold of chemical conversion tank liquor
But.This method has continued to use decades so far, but there is it is obvious the problem of and defect：First, electrically heated rod and electrolytic bath
Liquid directly contacts, but contact area is smaller, easily at surface scale (aluminium hydroxide), influences the efficiency of heating surface.Second, electrically heated rod
Power limited, heat time length.Third, electrically heated rod easily damages, easily pollution chemical conversion tank liquor, and changing frequently, ten are changed
Divide difficulty, or even need to shut down, influence production efficiency.Fourth, cooling row directly contacts with chemical conversion tank liquor, easily in surface scale
(aluminium hydroxide), cooling effectiveness is influenceed, it is necessary to which periodic cleaning, influences production efficiency.Fifth, cooling isostere accumulates larger, occupancyization
Grooving inner space, and cool down row easily occur cooling water leakage accident, pollute electrolytic bath tank liquor, have a strong impact on product quality and
Production efficiency.Sixth, cooling water must be soft water, the easy fouling of inside pipe wall is otherwise cooled down, causes line clogging.The making of soft water
Increase production run cost.Seventh, the usage amount of cooling water is very big, in order to save production run cost, cooling water is followed
Ring is used, it is necessary to build Large Copacity cistern, and needs to cool to cooling water as early as possible using large cooling column,.These
Auxiliary equipment not only increases fund input and production run cost, and also takes up very big place and space.Eighth, cooling
Tower is completed to cool by evaporation water, consumes many water resources.
The content of the invention
It is an object of the invention to overcome above the shortcomings of the prior art, there is provided a kind of thinking is novel, structure letter
The novel electrolytic bath device that list, low cost, production efficiency are high, filter, heat and be cooled in electrolytic bath completes outside.
Another object of the present invention is to provide a kind of implementation method of novel electrolytic bath device.
In order to achieve the above object, the present invention uses following technical scheme：A kind of novel electrolytic bath device, including chemical conversion
Groove, electrolytic bath upper end offer circulation import, and electrolytic bath lower end offers loop exit, and loop exit passes through pipeline and circulating pump
Connection, circulating pump are connected with filter, and backup line, the import of backup line and heater are provided between circulating pump and filter
End connection, filter outlet end connect the entrance point of standby pipe and heat exchanger respectively, and the entrance point of heat exchanger is also associated with
Flow control tube road, the port of export of the port of export of heater, the control pipeline port of export and heat exchanger are connected to circulation inlet.
The pipeline of the circulating pump both sides is provided with the first valve and the second valve.
The filter both sides are provided with the 3rd valve and the 4th valve.
The heater both sides are provided with the 5th valve and the 6th valve.
The heat exchanger both sides are provided with the 7th valve and the 8th valve.
The backup line is provided with the 9th valve, and flow control tube road is provided with the tenth valve.
The implementation method of above-mentioned novel electrolytic bath device, comprises the following steps：
(1), flowed out by the effect of circulating pump, tank liquor from loop exit；
(2), during production line preparation：Tank liquor passes through filter, reaches and is heated at heater, is then return to circulation
Entrance；When filter needs to safeguard, the 3rd valve and the 4th valve are closed, opens the 9th valve, be i.e. backup line is opened, no
Chemical conversion production line is influenceed normally to produce；
(3), during normal production work：The 5th valve and the 6th valve are closed, opens the 7th valve and the 8th valve, tank liquor
Heat exchanger is entered, is then return to circulation inlet；
(4), when needing to adjust electrolytic bath tank liquor temperature, the tenth valve switch degree is adjusted, carries out Flow-rate adjustment, meanwhile,
Air cooler air quantity is adjusted with frequency converter, changes air-cooled amount；When air cooler needs of short duration safeguard, the 7th valve and the 8th valve are closed
Door, the 9th valve is opened, i.e. flow control tube road is opened, and is not influenceed chemical conversion production line and is normally produced.
The pipeline of the circulating pump both sides is provided with the first valve and the second valve；The filter both sides are provided with the 3rd valve
Door and the 4th valve；The heater both sides are provided with the 5th valve and the 6th valve；The heat exchanger both sides are provided with the 7th valve
Door and the 8th valve；The backup line is provided with the 9th valve, and flow control tube road is provided with the tenth valve.
The heating means are the method for Electromagnetic Heating.
The heat exchanger is air-cooled type heat exchanger equipment.
The present invention is had the following advantages and effect relative to prior art：
1st, the present invention includes electrolytic bath, and electrolytic bath upper end offers circulation import, and electrolytic bath lower end offers loop exit,
Loop exit is connected by pipeline with circulating pump, and circulating pump is connected with filter, and standby pipe is provided between circulating pump and filter
The entrance point connection of road, backup line and heater, filter outlet end connect the entrance point of standby pipe and heat exchanger respectively,
The entrance point of heat exchanger is also associated with flow control tube road, the port of export, the control pipeline port of export and the heat exchanger of heater
The port of export be connected to circulation inlet, have that thinking is novel, simple in construction, low cost, production efficiency are high, filtering, heating
Be cooled in outside electrolytic bath the features such as completing.
2nd, the filter in the present invention use blade inserting screen pack, is conveniently replaceable maintenances, and opening bypasses during replacing, does not influence
Circulation is heated or cooled.Mode of heating is heated using great-power electromagnetic, and heater is not directly contacted with chemical conversion tank liquor, service life
It is long, fault rate is low, reduce change, maintenance times, be not easy pollution chemical conversion tank liquor,.Heat exchange area is big, it is not easy to fouling.Power
Greatly, preheating time is substantially reduced, improves operating efficiency.The type of cooling uses air cooling way, is not take up in electrolytic bath empty
Between, chemical conversion tank liquor is not polluted, does not consume water resource, it is not necessary to which cistern and cooling tower, production efficiency is high, and operating cost is low.Adopt
Amount of cooling water is controlled with the mode of frequency converter regulation fan delivery, it is simple and easy to do.
Brief description of the drawings
Fig. 1 is a kind of structural representation of novel electrolytic bath device.
Label and title are as follows in figure：
| 1 | Electrolytic bath | 2 | Circulate import |
| 3 | Loop exit | 4 | Circulating pump |
| 5 | Filter | 6 | Backup line |
| 7 | Heater | 8 | Heat exchanger |
| 9 | Flow control tube road | 10 | First valve |
| 11 | Second valve | 12 | 3rd valve |
| 13 | 4th valve | 14 | 5th valve |
| 15 | 6th valve | 16 | 7th valve |
| 17 | 8th valve | 18 | 9th valve |
| 19 | Tenth valve |
Embodiment
For ease of it will be appreciated by those skilled in the art that below in conjunction with the accompanying drawings and embodiment the present invention is made it is further specifically
It is bright.
Embodiment 1：
As shown in figure 1, a kind of novel electrolytic bath device, including electrolytic bath, electrolytic bath upper end offer circulation import, chemical conversion
Groove lower end offers loop exit, and loop exit is connected by pipeline with circulating pump, and circulating pump is connected with filter, circulating pump with
Backup line is provided between filter, the entrance point connection of backup line and heater, filter outlet end connects standby respectively
The entrance point of pipe and heat exchanger, the entrance point of heat exchanger are also associated with flow control tube road, the port of export of heater, control
Circulation inlet is connected between the port of export of pipe outlet and heat exchanger.
The pipeline of circulating pump both sides in the present embodiment is provided with the first valve and the second valve；Filter both sides are provided with the
Three valves and the 4th valve；Heater both sides are provided with the 5th valve and the 6th valve；Heat exchanger both sides be provided with the 7th valve and
8th valve；Backup line is provided with the 9th valve, and flow control tube road is provided with the tenth valve.
The implementation method of above-mentioned novel electrolytic bath device, comprises the following steps：
(1), flowed out by the effect of circulating pump, tank liquor from loop exit；
(2), during production line preparation：Tank liquor passes through filter, reaches and is heated at heater, is then return to circulation
Entrance；When filter needs to safeguard, the 3rd valve and the 4th valve are closed, opens the 9th valve, be i.e. backup line is opened, no
Chemical conversion production line is influenceed normally to produce；
(3), during normal production work：The 5th valve and the 6th valve are closed, opens the 7th valve and the 8th valve, tank liquor
Heat exchanger is entered, is then return to circulation inlet；
(4), when needing to adjust electrolytic bath tank liquor temperature, the tenth valve switch degree is adjusted, carries out Flow-rate adjustment, meanwhile,
Air cooler air quantity is adjusted with frequency converter, changes air-cooled amount；When air cooler needs of short duration safeguard, the 7th valve and the 8th valve are closed
Door, the 9th valve is opened, i.e. flow control tube road is opened, and is not influenceed chemical conversion production line and is normally produced.
Above-mentioned heating means are the method for Electromagnetic Heating；Heat exchanger is air cooler.
Filter in the present embodiment is accurate filter, and accurate filter uses blade inserting screen pack, is conveniently replaceable dimension
Shield, bypass is opened during replacing, does not influence that circulation is heated or cooled.Heater is electromagnetic heater, and mode of heating is using high-power
Electromagnetic Heating, heater are not directly contacted with tank liquor, service life length, reduce replacing, maintenance times.Heat exchange area is big, no
Easy fouling.Power is big, substantially reduces preheating time, improves operating efficiency.The type of cooling uses air cooling way, does not disappear
Water consumption resource, it is not necessary to which cistern and cooling tower, operating cost are low.Cooling is controlled by the way of frequency converter adjusts fan delivery
Amount, it is simple and easy to do.
Above-mentioned embodiment is the preferred embodiments of the present invention, can not be limited the invention, and others are appointed
The change or other equivalent substitute modes what is made without departing from technical scheme, are included in the protection of the present invention
Within the scope of.
Claims (10)
- A kind of 1. novel electrolytic bath device, it is characterised in that：Including electrolytic bath, electrolytic bath upper end offers circulation import, chemical conversion Groove lower end offers loop exit, and loop exit is connected by pipeline with circulating pump, and circulating pump is connected with filter, circulating pump with Backup line is provided between filter, the entrance point connection of backup line and heater, filter outlet end connects standby respectively The entrance point of pipe and heat exchanger, the entrance point of heat exchanger are also associated with flow control tube road, the port of export of heater, control The port of export of pipe outlet and heat exchanger is connected to circulation inlet.
- 2. novel electrolytic bath device according to claim 1, it is characterised in that：The pipeline of the circulating pump both sides is provided with First valve and the second valve.
- 3. novel electrolytic bath device according to claim 2, it is characterised in that：The filter both sides are provided with the 3rd valve With the 4th valve.
- 4. novel electrolytic bath device according to claim 3, it is characterised in that：The heater both sides are provided with the 5th valve With the 6th valve.
- 5. novel electrolytic bath device according to claim 4, it is characterised in that：The heat exchanger both sides are provided with the 7th valve Door and the 8th valve.
- 6. novel electrolytic bath device according to claim 5, it is characterised in that：The backup line is provided with the 9th valve Door, flow control tube road is provided with the tenth valve.
- 7. the implementation method of the novel electrolytic bath device according to any one of claim 1~6, it is characterised in that including with Lower step：(1), flowed out by the effect of circulating pump, tank liquor from loop exit；(2), during production line preparation：Tank liquor passes through filter, reaches and is heated at heater, is then return to circulation import Place；When filter needs to safeguard, the 3rd valve and the 4th valve are closed, opens the 9th valve, be i.e. backup line is opened, and is not influenceed Chemical conversion production line normally produces；(3), during normal production work：The 5th valve and the 6th valve are closed, opens the 7th valve and the 8th valve, tank liquor enters To heat exchanger, circulation inlet is then return to；(4), when needing to adjust electrolytic bath tank liquor temperature, the tenth valve switch degree is adjusted, carries out Flow-rate adjustment, meanwhile, with change Frequency device adjusts air cooler air quantity, changes air-cooled amount；When air cooler needs of short duration safeguard, the 7th valve and the 8th valve are closed, is beaten The 9th valve is opened, i.e. flow control tube road is opened, and is not influenceed chemical conversion production line and is normally produced.
- 8. the implementation method of novel electrolytic bath device according to claim 7, it is characterised in that：The circulating pump both sides Pipeline is provided with the first valve and the second valve；The filter both sides are provided with the 3rd valve and the 4th valve；The heater Both sides are provided with the 5th valve and the 6th valve；The heat exchanger both sides are provided with the 7th valve and the 8th valve；The standby pipe Road is provided with the 9th valve, and flow control tube road is provided with the tenth valve.
- 9. the implementation method of novel electrolytic bath device according to claim 8, it is characterised in that：The heating means are electricity The method of magnetic heating.
- 10. the implementation method of novel electrolytic bath device according to claim 8, it is characterised in that：The heat exchanger is Air-cooled heat exchange equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710929884.2A CN107749347A (en) | 2017-10-09 | 2017-10-09 | A kind of novel electrolytic bath device and its implementation |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710929884.2A CN107749347A (en) | 2017-10-09 | 2017-10-09 | A kind of novel electrolytic bath device and its implementation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN107749347A true CN107749347A (en) | 2018-03-02 |
Family
ID=61256009
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710929884.2A Withdrawn CN107749347A (en) | 2017-10-09 | 2017-10-09 | A kind of novel electrolytic bath device and its implementation |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107749347A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108624937A (en) * | 2018-05-11 | 2018-10-09 | 王康 | A kind of magnesium alloy workpiece anode oxidation method |
-
2017
- 2017-10-09 CN CN201710929884.2A patent/CN107749347A/en not_active Withdrawn
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108624937A (en) * | 2018-05-11 | 2018-10-09 | 王康 | A kind of magnesium alloy workpiece anode oxidation method |
| CN108624937B (en) * | 2018-05-11 | 2019-09-13 | 安徽明辉电气有限公司 | A kind of magnesium alloy workpiece anode oxidation method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103398627B (en) | Multi-source fluid waste heat recovery and comprehensive utilization system | |
| CN204006906U (en) | Energy-conservation scale protective type chemical process enclosed cooling recirculation system | |
| CN103835919B (en) | Residual neat recovering system | |
| CN103836862A (en) | Cooling water cooling device and method | |
| CN203352851U (en) | Water circulating cooling apparatus for induction heating equipment | |
| CN104673617A (en) | Water-cooled and air-cooled integrated white spirit cooling equipment | |
| CN107749347A (en) | A kind of novel electrolytic bath device and its implementation | |
| CN207338143U (en) | A kind of novel electrolytic bath device | |
| CN201509149U (en) | Circulation cooling device | |
| CN207437355U (en) | A kind of combination type air compressor cooling system | |
| CN204420978U (en) | A kind of energy saving drainage system of boiler hydrophobic development unit | |
| CN217591420U (en) | Immersed liquid cooling system for server | |
| CN204313671U (en) | A kind of water-cooling type ASuitable Air Coolerwith Efficiency | |
| CN204359033U (en) | The energy-saving electric system of a kind of power station recirculated cooling water | |
| CN203911671U (en) | Hydropower station unit energy conservation and environment protection phase change cooling device | |
| CN202054818U (en) | Softened water circulating system of air compressors in beer production technology | |
| CN206593079U (en) | The outer draining retracting device of a kind of boiler with tailed air-introduced machine cooling water and rubber ball cleaning | |
| CN201799428U (en) | Wash tank cooled and heated from external | |
| CN202971114U (en) | Water circulating type cooling device of vacuum pump | |
| CN204923962U (en) | Oil cooling cooler | |
| CN214307793U (en) | Self-circulation cooling device | |
| CN209325384U (en) | A kind of grease cold-heat exchange system | |
| CN212615249U (en) | Air compressor machine waste heat utilization system | |
| CN103243503B (en) | A kind of overflow control system | |
| CN208381039U (en) | A kind of hydraulic station cooling system |
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 | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20180302 |
|
| WW01 | Invention patent application withdrawn after publication |