CN107740155A - A kind of full-automatic anodic oxidation production line - Google Patents

A kind of full-automatic anodic oxidation production line Download PDF

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Publication number
CN107740155A
CN107740155A CN201711160511.XA CN201711160511A CN107740155A CN 107740155 A CN107740155 A CN 107740155A CN 201711160511 A CN201711160511 A CN 201711160511A CN 107740155 A CN107740155 A CN 107740155A
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CN
China
Prior art keywords
cell body
trough
production line
prypole
full
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CN201711160511.XA
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Chinese (zh)
Inventor
蒋昌炉
吴小春
张华明
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Sanming Foctek Photonics Inc
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Sanming Foctek Photonics Inc
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Priority to CN201711160511.XA priority Critical patent/CN107740155A/en
Publication of CN107740155A publication Critical patent/CN107740155A/en
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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D11/00Electrolytic coating by surface reaction, i.e. forming conversion layers
    • C25D11/02Anodisation
    • C25D11/04Anodisation of aluminium or alloys based thereon
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D11/00Electrolytic coating by surface reaction, i.e. forming conversion layers
    • C25D11/005Apparatus specially adapted for electrolytic conversion coating

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)

Abstract

The present invention relates to a kind of full-automatic anodic oxidation production line, including multiple cell bodies of operating console, linear pattern arrangement, it is set up in a pair of guide rails above the both sides of cell body respectively along cell body linear extension direction, being set up between two guide rails has boat car;The vertical hoisting bar being vertically arranged is connected to below the both ends of boat car, horizontally disposed horizontal prypole is provided between two vertical hoisting bars, the riser guide for enabling horizontal prypole Relative vertical prypole to carry out elevating movement is provided with the side surface of each vertical hoisting bar;Scalable heave hand for driving horizontal prypole to lift is provided with boat car;The lower section of horizontal prypole is provided with to hang the conducting rod of pending part, and the lower section both ends of horizontal prypole are also respectively provided with the claw that conducting rod is lifted to level.The present invention sets boat car to drive the conducting rod for hanging part to be handled to be moved between cell body in production line, it is possible to increase efficiency, reduce human factor influences to caused by production.

Description

A kind of full-automatic anodic oxidation production line
Technical field
The present invention relates to oxidation production equipment technology, particularly a kind of full-automatic anodic oxidation production line.
Background technology
Aluminum alloy materials have a series of excellent physics, chemistry, mechanics and processing characteristicies, can meet from kitchen meal apparatus To hard-core technology, from building decoration industry to transportation and the various different requirements such as the every profession and trade such as Aero-Space.But Some performances of aluminium are not ideal, such as the surface property of hardness, wearability and corrosion resistance.The process for treating surface of aluminium just may be used It to make up these weakness, can be improved by anode oxide film, anodic oxidation is turned into aluminium alloy and expand application and prolong Long-life indispensable key.But alumilite process is purely manual for a long time or semi-automatic production technology, low production efficiency, labor Fatigue resistance is big, and being readily incorporated human factor causes unstable product quality, and operating ambient temperature is high, and has certain danger, Caused waste gas has injury to human body.
The content of the invention
In view of this, the purpose of the present invention is to propose to a kind of full-automatic anodic oxidation production line, by being set in production line Putting boat car drives the conducting rod for hanging part to be handled to be moved between each cell body for realizing different processes, so as to enter successively Each procedure of row, it is possible to increase efficiency, reduce human factor influences to caused by production.
The present invention is realized using following scheme:A kind of full-automatic anodic oxidation production line, including operating console and straight line Multiple cell bodies that type is arranged successively, the multiple cell body include set gradually from front to back oil removing groove, ash cleaning slot, delustring groove, Polishing trough, neutralization chamber, oxidation trough, staining trough and enclosed slot, and be provided between two neighboring cell body at least one clear Washing trough, at least one rinse bath is provided with after enclosed slot;The oil removing groove, ash cleaning slot, delustring groove, polishing trough, neutralization chamber, oxidation The charging aperture of groove, staining trough and enclosed slot is connected to corresponding dosage bunker by feed pipe respectively;On the feed pipe It is provided with the charge pump the dispensing in dosage bunker is added in corresponding cell body;
The full-automatic anodic oxidation production line also includes being set up in the two of cell body respectively along cell body linear extension direction A pair of guide rails above side, the boat car being set up between two guide rails and for controlling the boat that boat car moves forward and backward along guide rail Car drive device;The vertical hoisting bar being vertically arranged is connected to below the both ends of the boat car, is connected between two vertical hoisting bars The horizontal prypole of horizontal cross setting is connected to, is provided with the side of each vertical hoisting bar for enabling horizontal prypole Enough Relative vertical prypoles carry out the riser guide of elevating movement;It is provided with to drive horizontal prypole rising on the boat car The scalable heave hand lifted on drop guide rail;Wait to locate to hang provided with what horizontal cross was set in the lower section of the horizontal prypole The conducting rod of part is managed, the lower section both ends of horizontal prypole are also respectively provided with the claw that conducting rod is lifted to level;
The cell body top edge of the oxidation trough is fixed with the aluminium frame being adapted to cell body inner ring, the aluminium frame and power cathode phase Negative electrode when even, to as oxidation uses;The cell body both sides of the oxidation trough are additionally provided with along cell body linear extension direction and set That puts is used for supporting the conducting rod and the conductive seat being conductively connected with conducting rod, and the positive pole of the conductive seat and power supply connects, Conducting rod to make to be in contact with it uses as anode when aoxidizing;
The charge pump and boat car drive device are connected with the control device being arranged on operating console.
Further, liquid level sensor and temperature sensor are provided with each cell body;Part cell body is also associated with adding Thermal, heat abstractor and agitating device;The liquid level sensor, temperature sensor, heater, heat abstractor and stir Device is mixed with the control device being arranged on operating console to be connected.
The production line in production line by setting boat car to drive the conducting rod for hanging part to be handled between cell body It is mobile, it is automatic by mobile carry out of the control device to the liquid level in the cell body of production line, temperature, strength of fluid etc. and the car that navigates Control.The production line hangs personnel in actual use, on part and pending part is hung on the conducting rod by hanger, The control device remote control that operator is manipulated by platform navigates car to control conducting rod to move, and makes part according to production technology It is required that by deoiling to cleaning → ash disposal → cleaning → polishing or delustring → two → neutralization of cleaning → three → anode of cleaning Oxidation → three → dyeing of cleaning → three → closing of cleaning → cleaning two terminates.Wherein, anodic oxidation process is production line In a most key step, the aluminium frame that the cell body top edge of oxidation trough is fixed is connected with power cathode, as negative electrode when aoxidizing Use;The strip conductive seat and the positive pole of power supply that oxidation trough both sides are set connect, and the conducting rod for making to be in contact with it is as oxidation When anode use, hang on conducting rod pending part by contact with conducting rod it is powered after into being aoxidized in oxidation trough Reaction.
Further, the quantity of the boat car is 2, is set up in the leading portion of full-automatic anodic oxidation production line respectively with after Section;Boat parking stall 2m eminences on cell body top edge.
Further, each claw includes two V-type claws one in front and one in back set, and the both ends top of the conducting rod is It is provided with the extension that two sections that can be positioned on the V-type claw are rhombus;The spacing of two V-type claws with two The spacing of the extension of rhombus is identical.
Further, the number of the oxidation trough is 3, and the staining trough, the number of enclosed slot are 2;
The number of rinse bath between the polishing trough and neutralization chamber is 2, clear between the neutralization chamber and oxidation trough The number of washing trough is 3, and the number of the rinse bath between the oxidation trough and staining trough is 3, the staining trough and enclosed slot Between the number of rinse bath be 3, it is 3 that the rear of the enclosed slot, which sets the number of rinse bath,.
Further, the oil removing groove, ash cleaning slot, delustring groove, polishing trough, neutralization chamber, staining trough, enclosed slot and cleaning Groove is length 2.5m, width 0.8m, height 1m common cell body;
Further, the oxidation trough be length 2m, width 0.8m, height 1m cell body, the inner surface of the oxidation trough The aluminium sheet interval 5cm for using polylith thickness to be 1m for 2cm, width 20cm, length uniformly encloses around one, the top of each aluminium sheet Edge is connected with the aluminium frame;The centre of the oxidation trough is provided with the demarcation strip that cell body is divided into two cavitys, the demarcation strip Formed using spaced aluminium sheet.Wherein, the aluminium sheet set in cell body can make the Electric Field Distribution in oxidation trough more uniform, Obtain more preferable oxidation effectiveness.
Further, the cell body periphery upper and lower sides of the polishing trough are respectively arranged with separate upper interlayer lower interlayer, The lower interlayer is connected with steam boiler;The upper interlayer is connected with providing the outside water supply pipe of cooling water;Cell body passes through The two flow is controlled to adjust temperature.
Preferably, the cell body of the polishing trough and enclosed slot is made of stainless steel material, the oil removing groove, ash cleaning slot, Delustring groove, neutralization chamber, staining trough and rinse bath are made of PPR materials.
Further, the control device is DCS control device for synchronization up-down;
The heater includes heating rod and steam(-)coil;
The oil removing groove is made up be provided with to be heated in the cell body of delustring groove of polytetrafluoroethylmaterial material Corrosion-resistant heating rod;
The cell body surface of the staining trough and enclosed slot is laid with the steam(-)coil to be heated to cell body, The steam(-)coil is connected with steam boiler;
The heat abstractor is included into air cooler and plate type heat exchanger;
The cell body of the oxidation trough is connected with plate type heat exchanger, the plate type heat exchanger with providing circulating cooling for it The air cooler of water and the water circulating pump of power is provided for cooling water be connected, form circulating cooling system.
The agitating device is included into Roots blower and admission line;
The oil removing groove, ash cleaning slot, delustring groove, polishing trough, neutralization chamber, staining trough, the cell body of enclosed slot and rinse bath It is respectively connected with to carry out the admission line of pneumatic stirring to the material in cell body, the air inlet of the admission line is provided with sieve Thatch air blower;
Added can by steam boiler coil pipe heating because production line is furnished with steam boiler, when cell body temperature is low Heat.In production line, polishing trough is furnished with plate type heat exchanger by interlayer temperature adjustment, oxidation trough and carries the air cooling of common recirculated cooling water Machine, cooled when oxidation trough temperature is high by plate type heat exchanger, when temperature is in claimed range, temperature control adjusting valve is closed, and cold But water realizes circulation by bypassing.
Preferably, the DCS control device for synchronization up-down is based on microprocessor, disperseed using control function, display is grasped Concentrate, take into account point and the blind controller system of autonomous and comprehensive coordination design principle, at present in electric power, metallurgy, petrochemical industry etc. All trades and professions are all extremely widely applied.
Further, the DCS control device for synchronization up-down is matched somebody with somebody including temperature inversion control system, time controlled system, reagent Drug slot and Loading Control System and mixing control system;
The temperature inversion control system respectively with temperature sensor, heating rod, the steaming being arranged in steam(-)coil The cooling sea water regulating valve of steam control valve and plate type heat exchanger, to the setting value according to cell body temperature and the reality of cell body temperature Value automatically controls the cooling water tune that heating rod carries out heating work, the aperture for controlling steam control valve and switching plate type heat exchanger The aperture of valve is saved, realizes that the temperature of cell body is constant;Different cell body needs different temperature, and the cell body for having temperature requirement must be with Temperature inversion is connected with control system, makes temperature change in controlled range;
The reagent dispensing slot is connected with liquid level sensor and charge pump respectively with Loading Control System, to control The aperture of charge pump is stated, the dispensing in dosage bunker is added in each cell body;When adding dispensing, according to chemical examination concentration results and groove Liquid product should add the amount of corresponding reagent to calculate;When dispensing is liquid reagent, then it can be fed, be passed through using centrifugal pump Increased cell body liquid level understands addition, when dispensing is solid reagent, then needs to be fed by gear wheel metering pump, can learn The addition of dispensing;Wherein charge pump is made of resistant material;
The stirring system and the valve with the power supply of Roots blower and the admission line for being provided with Roots blower It is connected, to control the working condition of the valve, and then the gas in the admission line is carried out the material in cell body Pneumatic stirring;Stirring can be achieved by circulating cooling system in oxidation trough, and other cell bodies are then installed admission line and roused by Roots Blower fan realizes pneumatic stirring;
The time controlled system is connected with boat car drive device, to the car that navigated according to the time control per procedure It is mobile to carry out next process;The time controlled system uses count-down device, and countdown is arrived, and system issues a signal to control Device, control boat car and claw lift conducting rod and continue next process;Therefore operator only need to set per pass work in control terminal The time that sequence needs, boat car can carry out the life of the next step automatically according to set program after the completion of a current procedure Production, until production is completed.
Compared with prior art, the present invention has following beneficial effect:
1st, the present invention in production line by setting boat car to drive the conducting rod for hanging part to be handled between cell body It is mobile, pass through movement of the DCS control device for synchronization up-down to the liquid level in the cell body of production line, temperature, strength of fluid etc. and the car that navigates Automatically controlled, automatization level is high.
2nd, production line of the invention can effectively be reduced the labor intensity of staff, be avoided due to automatization level height Strong acid, highly basic and waste gas staff is damaged.
3rd, production line of the invention reduces the fraction defective caused by human factor, particularly one by automated production The anodic oxidation of a little heavy sections, it is possible to increase efficiency, reduce human factor influences to caused by production.
Brief description of the drawings
Fig. 1 is the setting schematic diagram of the cell body of the production line cathetus type arrangement of the present invention.
Fig. 2 is the production line Air China car of the present invention and the structural representation of cell body.
Fig. 3 is the structural representation of claw in the present invention.
Fig. 4 is the structural representation of the oxidation trough of the present invention.
Fig. 5 is the structural representation of the polishing trough of the present invention.
Fig. 6 is the principle of device schematic diagram of the present invention.
Label declaration:1 is cell body, and 2 be guide rail, and 3 be boat car, and 4 be vertical hoisting bar, and 5 be horizontal prypole, and 6 be lifting Guide rail, 7 be scalable heave hand, and 8 be conducting rod, and 9 be claw, and 1-1 is oxidation trough, and 1-1-1 is aluminium frame, and 1-1-2 is conductive seat, 1-1-3 is aluminium sheet, and 1-2 is polishing trough, and 1-2-1 is the upper interlayer of polishing trough, and 1-2-2 is the lower interlayer of polishing trough.
Embodiment
Below in conjunction with the accompanying drawings and embodiment the present invention will be further described.
As depicted in figs. 1 and 2, a kind of full-automatic anodic oxidation production line, including operating console and linear pattern are arranged successively Multiple cell bodies 1 of cloth, the multiple cell body 1 include set gradually from front to back oil removing groove, ash cleaning slot, delustring groove, polishing trough, Neutralization chamber, oxidation trough, staining trough and enclosed slot, and at least one rinse bath is provided between two neighboring cell body, seal At least one rinse bath is provided with after locked groove;The oil removing groove, ash cleaning slot, delustring groove, polishing trough, neutralization chamber, oxidation trough, dyeing The charging aperture of groove and enclosed slot is connected to corresponding dosage bunker by feed pipe respectively;Use is provided with the feed pipe With the charge pump for adding the dispensing in dosage bunker in corresponding cell body;
The full-automatic anodic oxidation production line also includes being set up in cell body 1 respectively along the linear extension direction of cell body 1 A pair of guide rails 2 above both sides, the boat car 3 being set up between two guide rails 2 and for controlling boat car 3 along before and after guide rail 2 Mobile boat car drive device;The vertical hoisting bar 4 being vertically arranged is connected to below the both ends of the boat car 3, two are vertically risen The horizontal prypole 5 of horizontal cross setting is connected between weight bar 4, is provided with the side of each vertical hoisting bar for making Horizontal prypole 5 is capable of the riser guide 6 of the progress elevating movement of Relative vertical prypole 4;It is provided with the boat car to band Move the scalable heave hand 7 that horizontal prypole 5 lifts on riser guide 6;The lower section of the horizontal prypole 5 is provided with horizontal horizontal To setting to hang the conducting rod 8 of pending part, the lower section both ends of horizontal prypole 5 are also respectively provided with to level Lift the claw 9 of conducting rod 8;
The cell body top edge of the oxidation trough 1-1 is fixed with aluminium the frame 1-1-1, the aluminium frame 1-1- being adapted to cell body inner ring 1 is connected with power cathode, to be used as negative electrode when aoxidizing;The cell body both sides of the oxidation trough 1-1 are additionally provided with along groove Body linear extension direction set for the conductive seat 1-1-2 that supports the conducting rod 8 and be conductively connected with conducting rod 8, it is described The positive pole of conductive seat 1-1-2 and power supply connects, and the conducting rod 8 to make to be in contact with it uses as anode when aoxidizing;
The charge pump and boat car drive device are connected with the control device being arranged on operating console.
Liquid level sensor and temperature sensor are provided with each cell body;Part cell body is also associated with heater, dissipated Thermal and agitating device;The liquid level sensor, temperature sensor, heater, heat abstractor and agitating device are equal It is connected with the control device being arranged on operating console.
The production line in production line by setting boat car to drive the conducting rod for hanging part to be handled between cell body It is mobile, it is automatic by mobile carry out of the control device to the liquid level in the cell body of production line, temperature, strength of fluid etc. and the car that navigates Control.The production line hangs personnel in actual use, on part and pending part is hung on the conducting rod by hanger, The control device remote control that operator is manipulated by platform navigates car to control conducting rod to move, and makes part according to production technology It is required that by deoiling to cleaning → ash disposal → cleaning → polishing or delustring → two → neutralization of cleaning → three → anode of cleaning Oxidation → three → dyeing of cleaning → three → closing of cleaning → cleaning two terminates.Wherein, anodic oxidation process is production line In a most key step, the aluminium frame that the cell body top edge of oxidation trough is fixed is connected with power cathode, as negative electrode when aoxidizing Use;The strip conductive seat and the positive pole of power supply that oxidation trough both sides are set connect, and the conducting rod for making to be in contact with it is as oxidation When anode use, hang on conducting rod pending part by contact with conducting rod it is powered after into being aoxidized in oxidation trough Reaction.
In the present embodiment, the quantity of the boat car 3 is 2, before being set up in full-automatic anodic oxidation production line respectively Section and back segment;The boat car 3 is located at 2m eminences on the top edge of cell body 1.
In the present embodiment, it is described to lead as shown in figure 3, each claw 9 includes two V-type claws one in front and one in back set The extension that two sections that can be positioned on the V-type claw are rhombus is provided with above the both ends of electric pole 8;Two V The spacing of type claw is identical with the spacing of the extension of two rhombuses.
In the present embodiment, the number of the oxidation trough is 3, and the staining trough, the number of enclosed slot are 2;
The number of rinse bath between the polishing trough and neutralization chamber is 2, clear between the neutralization chamber and oxidation trough The number of washing trough is 3, and the number of the rinse bath between the oxidation trough and staining trough is 3, the staining trough and enclosed slot Between the number of rinse bath be 3, it is 3 that the rear of the enclosed slot, which sets the number of rinse bath,.
In the present embodiment, the oil removing groove, ash cleaning slot, delustring groove, polishing trough, neutralization chamber, staining trough, enclosed slot and Rinse bath is length 2.5m, width 0.8m, height 1m common cell body;
In the present embodiment, as shown in figure 4, the oxidation trough 1-1 is length 2m, width 0.8m, height 1m cell body, institute The aluminium sheet 1-1-3 interval 5cm that the inner surface for stating oxidation trough uses polylith thickness to be 1m for 2cm, width 20cm, length are uniform Around a circle, each aluminium sheet 1-1-3 top edge is connected with the aluminium frame 1-1-1;The centre of the oxidation trough 1-1 is provided with groove Body is divided into the demarcation strip of two cavitys, and the demarcation strip is formed using spaced aluminium sheet 1-1-3.Wherein, set in cell body Aluminium sheet the Electric Field Distribution in oxidation trough can be made more uniform, obtain more preferable oxidation effectiveness.
In the present embodiment, as shown in figure 5, the cell body periphery upper and lower sides of the polishing trough 1-2 are respectively arranged with mutually solely Vertical upper interlayer 1-2-1 lower interlayers 1-2-2, the lower interlayer 1-2-2 are connected with steam boiler;The upper interlayer 1-2-1 is with carrying The outside water supply pipe of Cooling Water;Cell body adjusts temperature by the two flow of control.
Preferably, the cell body of the polishing trough and enclosed slot is made of stainless steel material, the oil removing groove, ash cleaning slot, Delustring groove, neutralization chamber, staining trough and rinse bath are made of PPR materials.
In the present embodiment, the control device is DCS control device for synchronization up-down;
The heater includes heating rod and steam(-)coil;
The oil removing groove is made up be provided with to be heated in the cell body of delustring groove of polytetrafluoroethylmaterial material Corrosion-resistant heating rod;
The cell body surface of the staining trough and enclosed slot is laid with the steam(-)coil to be heated to cell body, The steam(-)coil is connected with steam boiler;
The heat abstractor is included into air cooler and plate type heat exchanger;
The cell body of the oxidation trough is connected with plate type heat exchanger, the plate type heat exchanger with providing circulating cooling for it The air cooler of water and the water circulating pump of power is provided for cooling water be connected, form circulating cooling system.
The agitating device is included into Roots blower and admission line;
The oil removing groove, ash cleaning slot, delustring groove, polishing trough, neutralization chamber, staining trough, the cell body of enclosed slot and rinse bath It is respectively connected with to carry out the admission line of pneumatic stirring to the material in cell body, the air inlet of the admission line is provided with sieve Thatch air blower;
Added can by steam boiler coil pipe heating because production line is furnished with steam boiler, when cell body temperature is low Heat.In production line, polishing trough is furnished with plate type heat exchanger by interlayer temperature adjustment, oxidation trough and carries the air cooling of common recirculated cooling water Machine, cooled when oxidation trough temperature is high by plate type heat exchanger, when temperature is in claimed range, temperature control adjusting valve is closed, and cold But water realizes circulation by bypassing.
Preferably, the DCS control device for synchronization up-down is based on microprocessor, disperseed using control function, display is grasped Concentrate, take into account point and the blind controller system of autonomous and comprehensive coordination design principle, at present in electric power, metallurgy, petrochemical industry etc. All trades and professions are all extremely widely applied.
In the present embodiment, as shown in fig. 6, the DCS control device for synchronization up-down includes temperature inversion control system, the time is controlled System, reagent dispensing slot and Loading Control System processed and mixing control system;
The temperature inversion control system respectively with temperature sensor, heating rod, the steaming being arranged in steam(-)coil The cooling sea water regulating valve of steam control valve and plate type heat exchanger, to the setting value according to cell body temperature and the reality of cell body temperature Value automatically controls the cooling water tune that heating rod carries out heating work, the aperture for controlling steam control valve and switching plate type heat exchanger The aperture of valve is saved, realizes that the temperature of cell body is constant;Different cell body needs different temperature, and the cell body for having temperature requirement must be with Temperature inversion is connected with control system, makes temperature change in controlled range;
The reagent dispensing slot is connected with liquid level sensor and charge pump respectively with Loading Control System, to control The aperture of charge pump is stated, the dispensing in dosage bunker is added in each cell body;When adding dispensing, according to chemical examination concentration results and groove Liquid product should add the amount of corresponding reagent to calculate;When dispensing is liquid reagent, then it can be fed, be passed through using centrifugal pump Increased cell body liquid level understands addition, when dispensing is solid reagent, then needs to be fed by gear wheel metering pump, can learn The addition of dispensing;Wherein charge pump is made of resistant material;
The stirring system and the valve with the power supply of Roots blower and the admission line for being provided with Roots blower It is connected, to control the working condition of the valve, and then the gas in the admission line is carried out the material in cell body Pneumatic stirring;Stirring can be achieved by circulating cooling system in oxidation trough, and other cell bodies are then installed admission line and roused by Roots Blower fan realizes pneumatic stirring;
The time controlled system is connected with boat car drive device, to the car that navigated according to the time control per procedure It is mobile to carry out next process;The time controlled system uses count-down device, and countdown is arrived, and system issues a signal to control Device, control boat car and claw lift conducting rod and continue next process;Therefore operator only need to set per pass work in control terminal The time that sequence needs, boat car can carry out the life of the next step automatically according to set program after the completion of a current procedure Production, until production is completed.
In the present embodiment, the production line is in actual use, upper extension personnel part according to hanging in species after, same type Part hangs same batch on conducting rod, product type and dyeing species is reported to operator, by operator according to product class Type and dyeing species setting per pass activity time.
If carrying out brilliant black high-temperature oxydation, i.e., polishing time being set to 30 seconds, delustring is set to 0 second, and high temperature dyestuff is selected in dyeing, when Between fixed 20 minutes, other are such as oil removings 3 minutes, oxidation 45 minutes, closing 10 minutes, constant voltage 14V.Point starts i.e. after the completion of setting Can, system can according to the time control part of setting in the stop of every groove, according to production process since oil removing up to terminate.It is complete Hanger is removed by lower extension personnel after, is put into steam drying box drying, then part is unloaded by lower extension personnel.
If carrying out mute black oxidation, i.e., the delustring time is set to 45 seconds, polishing is set to 0 second, dyes and selects normal temperature dyestuff, and the time is fixed 20 minutes, other such as oil removings 3 minutes, aoxidize 45 minutes, closing 10 minutes, constant voltage 14V.Point starts after the completion of setting, System can according to the time control part of setting in the stop of every groove, according to production process since oil removing up to terminate.Complete Hanger is removed by lower extension personnel afterwards, is put into steam drying box drying, then part is unloaded by lower extension personnel.
The foregoing is only presently preferred embodiments of the present invention, all equivalent changes done according to scope of the present invention patent with Modification, it should all belong to the covering scope of the present invention.

Claims (10)

  1. A kind of 1. full-automatic anodic oxidation production line, it is characterised in that:Arranged successively including operating console and linear pattern more Individual cell body (1), the multiple cell body (1) include set gradually from front to back oil removing groove, ash cleaning slot, delustring groove, polishing trough, in With groove, oxidation trough, staining trough and enclosed slot, and at least one rinse bath is provided between two neighboring cell body, closed At least one rinse bath is provided with after groove;The oil removing groove, ash cleaning slot, delustring groove, polishing trough, neutralization chamber, oxidation trough, staining trough And the charging aperture of enclosed slot is connected to corresponding dosage bunker by feed pipe respectively;Be provided with the feed pipe to The charge pump that dispensing in dosage bunker is added in corresponding cell body;
    The full-automatic anodic oxidation production line also includes being set up in cell body (1) respectively along cell body (1) linear extension direction A pair of guide rails (2) above both sides, the boat car (3) being set up between two guide rails (2) and for controlling boat car (3) along leading The movable boat car drive device of rail (2);The vertical hoisting bar being vertically arranged is connected to below the both ends of the boat car (3) (4) the horizontal prypole (5) of horizontal cross setting, the side of each vertical hoisting bar, are connected between two vertical hoisting bars (4) The riser guide for making horizontal prypole (5) be capable of Relative vertical prypole (4) progress elevating movement is provided with face (6);Scalable heave hand for driving horizontal prypole (5) to be lifted on riser guide (6) is provided with the boat car (7);The lower section of the horizontal prypole (5) be provided with that horizontal cross sets hanging the conducting rod of pending part (8), water The lower section both ends of flat prypole (5) are also respectively provided with the claw (9) that conducting rod (8) are lifted to level;
    The cell body top edge of the oxidation trough (1-1) is fixed with the aluminium frame (1-1-1) being adapted to cell body inner ring, the aluminium frame (1- 1-1) it is connected with power cathode, to be used as negative electrode when aoxidizing;The cell body both sides of the oxidation trough (1-1) are additionally provided with edge Cell body linear extension direction setting be used for support the conducting rod (8) and the conductive seat (1- being conductively connected with conducting rod (8) 1-2), the conductive seat (1-1-2) is connected with the positive pole of power supply, during making the conducting rod (8) that is in contact with it as oxidation Anode uses;
    The charge pump and boat car drive device are connected with the control device being arranged on operating console.
  2. A kind of 2. full-automatic anodic oxidation production line according to claim 1, it is characterised in that:It is respectively provided with each cell body There are liquid level sensor and temperature sensor and strength of fluid sensor;Part cell body be also associated with heater, heat abstractor with And agitating device;The liquid level sensor, temperature sensor, heater, heat abstractor and agitating device are with being arranged at Control device on operating console is connected.
  3. A kind of 3. full-automatic anodic oxidation production line according to claim 1, it is characterised in that:The number of the boat car (3) Measure the leading portion and back segment for for 2, being set up in full-automatic anodic oxidation production line respectively;The boat car (3) is located at cell body (1) top 2m eminences on edge.
  4. A kind of 4. full-automatic anodic oxidation production line according to claim 1, it is characterised in that:Each claw (9) includes Two V-type claws one in front and one in back set, the both ends top of the conducting rod (8), which is provided with two, can be positioned over the V Section on type claw is the extension of rhombus;The spacing of two V-type claws is identical with the spacing of the extension of two rhombuses.
  5. A kind of 5. full-automatic anodic oxidation production line according to claim 1, it is characterised in that:The number of the oxidation trough For 3, the staining trough, the number of enclosed slot are 2;
    The number of rinse bath between the polishing trough and neutralization chamber is 2, the rinse bath between the neutralization chamber and oxidation trough Number be 3, the number of the rinse bath between the oxidation trough and staining trough is 3, between the staining trough and enclosed slot The number of rinse bath be 3, it is 3 that the rear of the enclosed slot, which sets the number of rinse bath,.
  6. A kind of 6. full-automatic anodic oxidation production line according to claim 1, it is characterised in that:The oil removing groove, ash disposal Groove, delustring groove, polishing trough, neutralization chamber, staining trough, enclosed slot and rinse bath are length 2.5m, width 0.8m, height 1m Cell body.
  7. A kind of 7. full-automatic anodic oxidation production line according to claim 1, it is characterised in that:The oxidation trough (1-1) For length 2m, width 0.8m, height 1m cell body, the inner surface of the oxidation trough uses the polylith thickness to be for 2cm, width 20cm, the aluminium sheet (1-1-3) that length is 1m are spaced 5cm uniformly around a circle, the top edge of each aluminium sheet (1-1-3) with it is described Aluminium frame (1-1-1) is connected;The centre of the oxidation trough (1-1) is provided with the demarcation strip that cell body is divided into two cavitys, the separation Plate is formed using spaced aluminium sheet (1-1-3).
  8. A kind of 8. full-automatic anodic oxidation production line according to claim 1, it is characterised in that:The polishing trough (1-2) Cell body periphery upper and lower sides be respectively arranged with separate upper interlayer (1-2-1) lower interlayer (1-2-2), the lower interlayer (1- 2-2) it is connected with steam boiler;The upper interlayer (1-2-1) is connected with providing the outside water supply pipe of cooling water.
  9. A kind of 9. full-automatic anodic oxidation production line according to claim 2, it is characterised in that:
    The control device is DCS control device for synchronization up-down;
    The heater includes heating rod and steam(-)coil;
    The oil removing groove is resistance to made of polytetrafluoroethylmaterial material with being provided with to be heated in the cell body of delustring groove Corrode heating rod;
    The cell body surface of the staining trough and enclosed slot is laid with the steam(-)coil to be heated to cell body, described Steam(-)coil is connected with steam boiler;
    The heat abstractor is included into air cooler and plate type heat exchanger;
    The cell body of the oxidation trough is connected with plate type heat exchanger, the plate type heat exchanger with providing recirculated cooling water for it Air cooler and the water circulating pump of power is provided for cooling water be connected.
    The agitating device includes Roots blower and admission line;
    The oil removing groove, ash cleaning slot, delustring groove, polishing trough, neutralization chamber, staining trough, the cell body of enclosed slot and rinse bath connect It is connected to carry out the admission line of pneumatic stirring to the material in cell body, the air inlet of the admission line is provided with Roots's drum Blower fan.
  10. A kind of 10. full-automatic anodic oxidation production line according to claim 9, it is characterised in that:The collecting and distributing controls of DCS Device includes temperature inversion control system, time controlled system, reagent dispensing slot and Loading Control System and mixing control system System;
    The temperature inversion control system is adjusted with temperature sensor, heating rod, the steam that is arranged in steam(-)coil respectively The cooling sea water regulating valve of valve and plate type heat exchanger is saved, to the actual value of the setting value according to cell body temperature and cell body temperature certainly Dynamic control heating rod carries out the cooling sea water regulating valve of heating work, the aperture for controlling steam control valve and switching plate type heat exchanger Aperture, realize that the temperature of cell body is constant;
    The reagent dispensing slot is connected with liquid level sensor and charge pump respectively with Loading Control System, to control described add Expect the aperture of pump, the dispensing in dosage bunker is added in each cell body;
    The power supply of the stirring system and Roots blower and it is provided with the valve of admission line of Roots blower and is connected, uses To control the working condition of the valve, and then the gas in the admission line is set pneumatically to stir the material in cell body Mix;
    The time controlled system is connected with boat car drive device, to car movement of being navigated according to the time control per procedure Carry out next process.
CN201711160511.XA 2017-11-20 2017-11-20 A kind of full-automatic anodic oxidation production line Pending CN107740155A (en)

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CN108315794A (en) * 2018-05-11 2018-07-24 王康 A kind of almag anodized surface processing equipment
CN108546973A (en) * 2018-05-11 2018-09-18 王康 A kind of manufacturing method of aluminum magnesium alloy bridge frame
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CN111705346A (en) * 2020-07-07 2020-09-25 湖北实美科技有限公司 High-performance aluminum profile anodic oxidation device and coloring process
CN112626585A (en) * 2020-11-30 2021-04-09 中国原子能科学研究院 Device for preparing nonmetal nuclide planar source by anodic oxidation method

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CN110373697A (en) * 2019-07-25 2019-10-25 天长市京发铝业有限公司 A kind of full-automatic Horizontal oxide production line
CN111705346A (en) * 2020-07-07 2020-09-25 湖北实美科技有限公司 High-performance aluminum profile anodic oxidation device and coloring process
CN112626585A (en) * 2020-11-30 2021-04-09 中国原子能科学研究院 Device for preparing nonmetal nuclide planar source by anodic oxidation method

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