CN205398737U - Anode effect processing apparatus - Google Patents

Anode effect processing apparatus Download PDF

Info

Publication number
CN205398737U
CN205398737U CN201620177961.4U CN201620177961U CN205398737U CN 205398737 U CN205398737 U CN 205398737U CN 201620177961 U CN201620177961 U CN 201620177961U CN 205398737 U CN205398737 U CN 205398737U
Authority
CN
China
Prior art keywords
effect
anode
electrolyte
control machine
aluminium oxide
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.)
Active
Application number
CN201620177961.4U
Other languages
Chinese (zh)
Inventor
贺永东
孙郅程
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Xinjiang University
Original Assignee
Xinjiang University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Xinjiang University filed Critical Xinjiang University
Priority to CN201620177961.4U priority Critical patent/CN205398737U/en
Application granted granted Critical
Publication of CN205398737U publication Critical patent/CN205398737U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Electrolytic Production Of Metals (AREA)

Abstract

The utility model discloses an electrolytic aluminum in -process anode effect processing apparatus, processing apparatus includes distributing device, distributing device's the end of giving vent to anger is connected with and extinguishes a dose storage tank, the end of giving vent to anger that extinguishes dose storage tank extinguishes the union coupling through hose and effect, processing apparatus is still including being used for lift, rotation, bending the effect is extinguish the effect of pipe and is extinguish a tub transmission. The utility model discloses an effect processing procedure is accomplished in positive pole bottom interface department, does not stir aluminium liquid, and do not produce hydrogen to electrolytic aluminum liquid and the aluminium oxide is mingled with the pollution, has very high economic value and social.

Description

A kind of anode effect processes device
Technical field
This utility model relates to aluminium electroloysis and purifying aluminium alloy melt field, particularly relates to a kind of anode effect not producing hydrogen and alumina inclusion and processes device.
Background technology
Aluminum is the second largest structural metallic materials being only second to iron and steel, and aluminum melt quality affects aluminum product quality, and clean liquid metals is the guarantee obtaining fine aluminum goods.Hydrogen is the gas that uniquely can be dissolved in aluminum melt in a large number, and aluminum liquid solidifies defects such as precipitating out pore produced by hydrogen, loosen, directly affects the quality of aluminum products, performance, is the reason of air blister defect in annealing and solution treatment aluminium alloy.Al2O3It is mingled with the key factor being to affect aluminum melt metallurgical quality, destroy the seriality of aluminum substrate, reduce matrix strength, worsening aluminum profile extrusion performance, decay resistance and Resisting fractre toughness, the germinating for fatigue crack provides core (paper " electrolysis process influence research to electrolytic aluminium liquid quality " referring to He Yongdong, Zhang Xinming).
In electrolytic aluminium liquid, alumina inclusion content is typically in 1%-2%, hydrogen content average out to 0.34ml/100gAl in your aluminum actual measurement electrolytic aluminium liquid.For these reasons, in the initial last 100 years of Hall-Ai Lute molten-salt electrolytic aluminum, people cannot directly utilize high-temperature electrolysis aluminum liquid casting ingot casting always.Along with technological progress, the abbreviated system directly utilizing high-temperature electrolysis aluminum liquid production strand is used widely, the hydrogen produced in electrolytic process and the oxide inclusion pollution to aluminum melt, become the main contributor (paper " metallurgical heredity of aluminum and Dissolved H in Liquid Al-Si Alloy and oxide inclusion " referring to He Yongdong) affecting aluminum melt metallurgical quality.
He Yongdong, Zhang Xinming, Chen Mingan etc. are at its paper " Al in electrolytic aluminium liquid2O3The formation mechenism of field trash " in point out: anode effect be on carbon anode interface precipitate out CO2The current blockade process that gas can not be discharged in time and be caused, the frequency that effect occurs is relevant with the cold-hot condition of alumina concentration fluctuation in electrolyte, electrolysis bath.Effect itself is not resulted in aluminum liquid containing assorted, hydrogenation, and putting out effect operation can increase hydrogen and oxide inclusion content in electrolytic aluminium liquid to a certain extent.In actual production, often adopt compression air and wet batten extinguishes effect, first in electrolyte, add enough Al2O3, wetter batten is inserted in aluminum liquid-electrolyte, there is strong dehydration, the H of generation in wet batten2O and CO2Aluminum liquid is stirred by gas, and aluminum liquid, through air film barrier layer and anode in short circuit, reaches to extinguish the purpose of effect.Or high-pressure blast is directly blown in aluminum liquid, aluminum liquid produces strong wallop, stir aluminum liquid and form short circuit, reach to extinguish the purpose of effect.Compression air or wet batten dehydration product can react with high temperature aluminum liquid, generate substantial amounts of Al2O3It is mingled with and hydrogen:
4Al+6H20=2 (α-Al2O3)+6H2-395.7KJ/mol;
2Al+3CO2=(α-Al2O3)+3CO-550.38KJ/mol.
4Al+3O2=2Al2O3-1109KJ/mol;
Fig. 1 for putting out in effect process, H2O、CO2The interfacial oxide film layer that bubble produces with aluminum effect and hydrogen interaction process schematic diagram, the H of generation2、CO、CO2Contact with the oxide-film of bubble surface Deng gas, oxidized film inwall adsorbs, high temperature aluminum liquid flows into bubble by oxide-film gap, causes aluminum liquid hydrogen and alumina inclusion to pollute (paper " in electrolytic aluminium liquid hydrogen evolution Exploration of Mechanism " referring to He Yongdong, Zhang Xinming).Traditional method is adopted to extinguish the process of effect, it is actually the process of slag making in aluminum liquid, gas making, the electrolytic aluminium liquid major reason that produces that hydrogen and aluminium oxide pollute, and there is manipulation strength height, environmental pollution is big, material consumption is high, easily form the deficiencies such as a large amount of precipitation of alumina at bottom land.
Utility model content
The purpose of this utility model is aiming at the deficiency that above-mentioned prior art exists, it is provided that a kind of anode effect not producing hydrogen and alumina inclusion processes device.
Above-mentioned purpose is realized by following proposal:
A kind of electrolytic aluminium anodic effect processes device, it is characterized in that, described process device includes air distributing device (1), the outlet side of described air distributing device (1) is connected to quencher storage tank (2), the outlet side of described quencher storage tank (2) is extinguished pipe (3) by flexible pipe with effect and is connected, and described process device also includes extinguishing for lifting, rotate, bend described effect the effect of pipe (3) and extinguishes pipe actuating device (4).
According to above-mentioned process device, it is characterised in that it is metal hose that described effect extinguishes pipe (3), and is arranged with carbon protective sleeve outside this metal hose.
According to above-mentioned process device, it is characterised in that described effect is extinguished pipe actuating device (4) and included motor, speed change gear, output power shaft and clamping device;Described clamping device clamps described effect by roller and extinguishes pipe (3).
According to above-mentioned process device, it is characterised in that described process device also includes pressure shell tup (5).
A kind of anode effect not producing hydrogen and alumina inclusion of the present utility model processes the bottom that device adopts effect extinguishing means that anode effect quencher is transported to effect anode, relies on carrier gas and effect quencher to extinguish effect.There is the effect alleviating operative employee's labor intensity, minimizing environmental pollution, reduction power consumption and material consumption, raising electrolysis bath yield and production efficiency.Effect processing procedure completes in anode bottom interface, does not stir aluminum liquid, electrolytic aluminium liquid is not produced hydrogen and alumina inclusion pollutes, have significantly high economic worth and social benefit.
Accompanying drawing explanation
Fig. 1 is anode effect extinguishing process schematic diagram;
Fig. 2 is structural representation of the present utility model;
Fig. 3 is that this utility model uses state diagram.
Detailed description of the invention
The utility model discloses a kind of electrolytic aluminium anodic effect and process device, including air distributing device 1, the outlet side of air distributing device 1 is connected to quencher storage tank 2, the outlet side of quencher storage tank 2 is extinguished pipe 3 by flexible pipe with effect and is connected, and process device also includes for lifting, rotating, the effect of curvature effect extinguishing pipe 3 extinguishes pipe actuating device 4.It is metal hose that effect extinguishes pipe 3, and is arranged with carbon protective sleeve outside this metal hose.Effect is extinguished pipe actuating device 4 and is included motor, speed change gear, output power shaft and clamping device;Clamping device clamps described effect by roller and extinguishes pipe 3.Process device and also include pressure shell tup 5.
Anode effect processing method of the present utility model uses above-mentioned process device, and method includes step: (1) is stored in quencher storage tank 2 according to different anode effect Specific disposition quenchers, effect is extinguished pipe 3 and reaches bottom anode;2, when needs antianode effect carries out extinguishing process, discharge quencher by controlling air distributing device 1.
Processing method is classified by following steps antianode effect: using all operating electrolysis baths as potential effect groove, the groove operational factor that slot control machine is obtained by interface message processor (IMP) timing is analyzed, judges, the data of simulated impedance value, electrolysis bath aluminum level and level of electrolyte, electrolyte molecular proportion, alumina concentration, anodic gas change of component, anode ruuning situation are run according to groove pressure, bath temperature, electrolysis bath, judge the critical groove operation conditions of effect, predict effect time of origin, and pairing effect is classified.Anode effect quencher is made up of one or several in cryolite, aluminium fluoride, sodium fluoride, aluminium oxide, industry aluminium powder.
Specifically, the anode effect caused is lacked to because of aluminium oxide, anode effect quencher mass percent component is: (1%-70%) aluminium oxide+surplus is industry aluminium powder, or (0.5%-5%) aluminium fluoride+(1%-60%) aluminium oxide+surplus is industry aluminium powder, or (0.5%-5%) one or more mixture+(1%-60%) aluminium oxide+surplus in sodium fluoride or sodium carbonate or sodium bicarbonate is industry aluminium powder, or (0.5%-5%) cryolite+(1%-60%) aluminium oxide+surplus be industrial aluminium powder;To the anode effect caused because of electrolyte atrophy, anode effect quencher mass percent component is: (0.1%-10%) aluminium oxide+(5%-90%) cryolite, or (0.1%-10%) aluminium oxide+(0.5%-40%) industry aluminium powder+surplus is cryolite, or (0.5%-30%) aluminium fluoride+(5%-60%) cryolite+(0.1%-10%) aluminium oxide+surplus is industry aluminium powder, or (0.5%-50%) one or more mixture+(0.1%-10%) aluminium oxide+surplus in cryolite+(0.5%-30%) sodium fluoride or sodium carbonate or sodium bicarbonate is industry aluminium powder;To the anode effect caused because bath temperature is on the low side, anode effect quencher component is: (1%-10%) aluminium oxide+(0.5%-99%) industry aluminium powder, or (0.5%-30%) cryolite+(1%-10%) aluminium oxide+surplus is industry aluminium powder, or (0.5%-30%) sodium fluoride+(0.1%-10) % aluminium oxide+surplus is industry aluminium powder, or one or more the mixture+surplus in (0.5%-90) % sodium fluoride or sodium carbonate or sodium bicarbonate be industrial aluminium powder.
The carrier gas that air distributing device uses is one or more the mixing in nitrogen, air, carbon dioxide or dry ice powder.
Method of the present utility model is to use when routine is intervened invalid in advance, pre-intervene be judge according to interface message processor (IMP) the critical groove operation conditions of effect, effect forecast situation, prediction effect classification situation, carry out intervention process in advance.The electrolysis bath on the low side to alumina concentration, progressive adjustments alumina feeding amount, make alumina concentration in electrolyte return to normal level.Electrolysis bath to temperature anomaly, adjusts the energy input state of electrolysis bath in advance, eliminates cold trap, heat channel effect.Two liquid levels (aluminum level, level of electrolyte) are unbalance, the electrolysis bath of electrolyte atrophy, adjust aluminum amount and villiaumite addition, recover two liquid levels, stop because two liquid levels are unbalance, the effect of electrolyte atrophy.
The pairing effect unsuccessful electrolysis bath of intervention, or the electrolysis bath of anode effect is there is because technique needs, adopt effect extinguishing means of the present utility model that anode effect quencher is transported to the bottom of effect anode, rely on carrier gas and effect quencher to extinguish effect.
The method that effect described in the utility model is extinguished is to utilize carrier gas device that anode effect quencher is transported to the bottom of effect anode, and effect extinguishing process does not stir negative electrode aluminum liquid, negative electrode aluminum liquid is not produced hydrogen and alumina inclusion pollutes.In Fig. 3, effect extinguishes pipe actuating device 4, the head of metal hose 3 that will be able to bend, send in the air film barrier layer 7 bottom anode 6, the effect quencher that air distributing device 1 will store in effect quencher storage tank 2, it is delivered in air film barrier layer, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion is also breakdown, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, alumina concentration in electrolyte bottom raising anode, improve the wettability of electrolyte and anode, reach the purpose of anode effect terminating.
This utility model can also carry out conventional effect post processing and include: pole span adjustment, groove pressure adjusts, groove face arranges, and requires to make aluminum scheme implementation and supervision according to aluminum liquid horizontal adjustment, requires to formulate villiaumite, additive interpolation scheme implementation and supervision according to electrolyte component adjustment.Effect post-processing operation terminates, and this groove proceeds to the critical slot status of effect and is monitored.
Embodiment 1: the anode effect that electrolyte atrophy causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove electrolyte atrophy of effect, it was predicted that generating effect after 2h.Slot control machine Set-out slide effect intervention program, during blanking operation, a certain proportion of cryolite (aluminium oxide and cryolite ratio are 5:1) is allocated in alumina material, with supplementary cell bath, improve level of electrolyte, heighten tank voltage 10mV simultaneously, increase electrolysis bath heat income, after 3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishes the head of metal hose that pipe actuating device will be able to bend, send in the air film barrier layer bottom anode, the effect quencher (0.5% aluminium oxide+99.5% cryolite) that air distributing device will store in effect quencher storage tank, being delivered in air film barrier layer, the cryolite in effect quencher dissolves, and supplements cell bath, cleaning anode bottom, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 2: the anode effect that electrolyte atrophy causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove electrolyte atrophy of effect, it was predicted that generating effect after 1.5h.Slot control machine Set-out slide effect intervention program, during blanking operation, a certain proportion of cryolite (aluminium oxide and cryolite ratio are 4:1) is allocated in alumina material, with supplementary cell bath, improve level of electrolyte, heighten tank voltage 10mV simultaneously, increase electrolysis bath heat income, after 2.5h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (10% aluminium oxide+90% cryolite), it is delivered in air film barrier layer, cryolite in effect quencher dissolves, supplement cell bath, cleaning anode bottom, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 3: the anode effect that electrolyte atrophy causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove electrolyte atrophy of effect, it was predicted that generating effect after 1.9h.Slot control machine Set-out slide effect intervention program, during blanking operation, a certain proportion of cryolite (aluminium oxide and cryolite ratio are 4:1) is allocated in alumina material, with supplementary cell bath, improve level of electrolyte, heighten tank voltage 10mV simultaneously, increase electrolysis bath heat income, after 2.5h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% aluminium oxide+0.5% industry aluminium powder, cryolite surplus), it is delivered in air film barrier layer, cryolite in effect quencher dissolves, supplement cell bath, cleaning anode bottom, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 4: the anode effect that electrolyte atrophy causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove electrolyte atrophy of effect, it was predicted that generating effect after 1.9h.Slot control machine Set-out slide effect intervention program, during blanking operation, a certain proportion of cryolite (aluminium oxide and cryolite ratio are 4:1) is allocated in alumina material, with supplementary cell bath, improve level of electrolyte, heighten tank voltage 10mV simultaneously, increase electrolysis bath heat income, after 2.5h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (10% aluminium oxide+40% industry aluminium powder, cryolite surplus), it is delivered in air film barrier layer, cryolite in effect quencher dissolves, supplement cell bath, cleaning anode bottom, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 5: the anode effect that electrolyte atrophy causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove electrolyte atrophy of effect, it was predicted that generating effect after 2.2h.Slot control machine Set-out slide effect intervention program, during blanking operation, a certain proportion of cryolite (aluminium oxide and cryolite ratio are 5:1) is allocated in alumina material, with supplementary cell bath, improve level of electrolyte, heighten tank voltage 18mV simultaneously, increase electrolysis bath heat income, after 3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% aluminium fluoride+0.3% aluminium oxide+5% cryolite, surplus is industry aluminium powder), it is delivered in air film barrier layer, cryolite in effect quencher dissolves, supplement cell bath, cleaning anode bottom, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, aluminium fluoride turns down electrolyte molecular proportion, the aluminium oxide liquid added dissolves rapidly, alumina concentration in electrolyte bottom raising anode, anode effect is extinguished.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 6: the anode effect that electrolyte atrophy causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove electrolyte atrophy of effect, it was predicted that generating effect after 2.8h.Slot control machine Set-out slide effect intervention program, during blanking operation, a certain proportion of cryolite (aluminium oxide and cryolite ratio are 5:1) is allocated in alumina material, with supplementary cell bath, improve level of electrolyte, heighten tank voltage 16mV simultaneously, increase electrolysis bath heat income, after 3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (30% aluminium fluoride+10% aluminium oxide+59% cryolite, surplus is industry aluminium powder), it is delivered in air film barrier layer, cryolite in effect quencher dissolves, supplement cell bath, cleaning anode bottom, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, aluminium fluoride turns down electrolyte molecular proportion, the aluminium oxide liquid added dissolves rapidly, alumina concentration in electrolyte bottom raising anode, anode effect is extinguished.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 7: the anode effect that electrolyte atrophy causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove electrolyte atrophy of effect, it was predicted that generating effect after 2.8h.Slot control machine Set-out slide effect intervention program, during blanking operation, a certain proportion of cryolite (aluminium oxide and cryolite ratio are 5:1) is allocated in alumina material, with supplementary cell bath, improve level of electrolyte, heighten tank voltage 16mV simultaneously, increase electrolysis bath heat income, after 3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% sodium fluoride+0.5% aluminium oxide+0.5% cryolite, surplus is industry aluminium powder), it is delivered in air film barrier layer, cryolite in effect quencher dissolves, supplement cell bath, cleaning anode bottom, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, sodium fluoride heightens electrolyte molecular proportion, the aluminium oxide liquid added dissolves rapidly, alumina concentration in electrolyte bottom raising anode, anode effect is extinguished.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 8: the anode effect that electrolyte atrophy causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove electrolyte atrophy of effect, it was predicted that generating effect after 2.8h.Slot control machine Set-out slide effect intervention program, during blanking operation, a certain proportion of cryolite (aluminium oxide and cryolite ratio are 5:1) is allocated in alumina material, with supplementary cell bath, improve level of electrolyte, heighten tank voltage 16mV simultaneously, increase electrolysis bath heat income, after 3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (30% sodium fluoride+10% aluminium oxide+50% cryolite, surplus is industry aluminium powder), it is delivered in air film barrier layer, cryolite in effect quencher dissolves, supplement cell bath, cleaning anode bottom, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, sodium fluoride heightens electrolyte molecular proportion, the aluminium oxide liquid added dissolves rapidly, alumina concentration in electrolyte bottom raising anode, anode effect is extinguished.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 9: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 1.5h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 6% (being foreshortened to 4.7 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 5% (discharge quantity is increased to 3.78kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 14mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 1.9h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (1% aluminium oxide+99% industry aluminium powder), it is delivered in air film barrier layer, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 10: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 1.7h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 6% (being foreshortened to 4.7 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 5% (discharge quantity is increased to 3.78kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 25mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 2.3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (70% aluminium oxide+30% industry aluminium powder), it is delivered in air film barrier layer, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 11: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 1.8h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 6% (being foreshortened to 4.7 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 5% (discharge quantity is increased to 3.78kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 18mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 2.3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% aluminium fluoride+1% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, aluminium fluoride in effect quencher turns down electrolyte molecular proportion, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, and gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 12: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 1.7h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 5% (being foreshortened to 4.5 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 3% (discharge quantity is increased to 3.708kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 10mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 2.5h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (5% aluminium fluoride+60% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, aluminium fluoride in effect quencher turns down electrolyte molecular proportion, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, and gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 13: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 3.5h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 3% (being foreshortened to 4.85 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 2% (discharge quantity is increased to 3.672kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 25mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 3.4h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% sodium fluoride+1% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, sodium fluoride in effect quencher heightens electrolyte molecular proportion, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, and gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 14: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 3.5h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 3% (being foreshortened to 4.85 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 2% (discharge quantity is increased to 3.672kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 19mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 3.9h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (5% sodium fluoride+60% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, sodium fluoride in effect quencher heightens electrolyte molecular proportion, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, and gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 15: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 1.4h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 10% (being foreshortened to 4.5 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 9% (discharge quantity is increased to 3.924kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 25mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 1.6h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (5% sodium fluoride+60% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, sodium fluoride in effect quencher heightens electrolyte molecular proportion, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, and gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improves alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 16: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 1.1h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 10% (being foreshortened to 4.5 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 10% (discharge quantity is increased to 3.96kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 30mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 1.2h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% cryolite+1% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, cryolite in effect quencher supplements electrolyte, increase alumina dissolution amount, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improve alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 17: aluminium oxide lacks the anode effect caused and extinguishes.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that the critical groove aluminium oxide of effect lacks, it was predicted that generating effect after 1.9h.Slot control machine Set-out slide effect intervention program, duty cycle is shortened 8% (being foreshortened to 4.6 minutes by original 5 minutes) in blanking, the alumina amount of each blanking increases by 6% (discharge quantity is increased to 3.816kg/ time) by original 3.6kg/ time, to improve alumina concentration in electrolyte, heighten tank voltage 33mV simultaneously, increase electrolysis bath heat income, to ensure that the aluminium oxide increased dissolves in time, after 2.2h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% cryolite+1% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, cryolite in effect quencher supplements electrolyte, increase alumina dissolution amount, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improve alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 18: the anode effect that the electrolysis bath that bath temperature is on the low side causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that effect critical groove bath temperature is on the low side, it was predicted that generating effect after 1.8h.Slot control machine Set-out slide effect intervention program, blanking is constant for duty cycle, the alumina amount of each blanking reduces by 6% (discharge quantity is increased to 3.384kg/ time) by original 3.6kg/ time, to prevent electrolysis bath from producing precipitation of alumina, heighten tank voltage 45mV simultaneously, increase electrolysis bath heat income, after 2h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (1% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, reaction liberated heat regulating electrolytic tank thermal balance, the heat that effector phase produces makes bath temperature raise, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improve alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 19: the anode effect that the electrolysis bath that bath temperature is on the low side causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that effect critical groove bath temperature is on the low side, it was predicted that generating effect after 2.5h.Slot control machine Set-out slide effect intervention program, blanking is constant for duty cycle, the alumina amount of each blanking reduces by 5% (discharge quantity is increased to 3.42kg/ time) by original 3.6kg/ time, to prevent electrolysis bath from producing precipitation of alumina, heighten tank voltage 38mV simultaneously, increase electrolysis bath heat income, after 2.8h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (10% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, industrial aluminium powder in effect quencher and carbon dioxide vigorous reaction in air film barrier layer, reaction liberated heat regulating electrolytic tank thermal balance, the heat that effector phase produces makes bath temperature raise, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, improve alumina concentration, anode effect extinguishing in electrolyte bottom anode.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 20: the anode effect that the electrolysis bath that bath temperature is on the low side causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that effect critical groove bath temperature is on the low side, it was predicted that generating effect after 3.1h.Slot control machine Set-out slide effect intervention program, blanking is constant for duty cycle, the alumina amount of each blanking reduces by 4% (discharge quantity is increased to 3.456kg/ time) by original 3.6kg/ time, to prevent electrolysis bath from producing precipitation of alumina, heighten tank voltage 30mV simultaneously, increase electrolysis bath heat income, after 3.3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% cryolite+1% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, cryolite electrolyte supplement in effect quencher, improve level of electrolyte, increase alumina dissolution energy, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, reaction liberated heat regulating electrolytic tank thermal balance, the heat that effector phase produces makes bath temperature raise, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, alumina concentration in electrolyte bottom raising anode, anode effect is extinguished.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 21: the anode effect that the electrolysis bath that bath temperature is on the low side causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that effect critical groove bath temperature is on the low side, it was predicted that generating effect after 3.1h.Slot control machine Set-out slide effect intervention program, blanking is constant for duty cycle, the alumina amount of each blanking reduces by 4% (discharge quantity is increased to 3.456kg/ time) by original 3.6kg/ time, to prevent electrolysis bath from producing precipitation of alumina, heighten tank voltage 40mV simultaneously, increase electrolysis bath heat income, after 3.3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (0.5% sodium fluoride+0.3% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, sodium fluoride in effect quencher improves electrolyte molecular proportion, increase electrolyte oxidation aluminum solvability, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, reaction liberated heat regulating electrolytic tank thermal balance, the heat that effector phase produces makes bath temperature raise, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, alumina concentration in electrolyte bottom raising anode, anode effect is extinguished.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.
Embodiment 22: the anode effect that the electrolysis bath that bath temperature is on the low side causes is extinguished.
According to interface message processor (IMP), slot control machine, groove operational factor is analyzed result, it is determined that effect critical groove bath temperature is on the low side, it was predicted that generating effect after 1.2h.Slot control machine Set-out slide effect intervention program, blanking is constant for duty cycle, the alumina amount of each blanking reduces by 10% (discharge quantity is increased to 3.24kg/ time) by original 3.6kg/ time, to prevent electrolysis bath from producing precipitation of alumina, heighten tank voltage 60mV simultaneously, increase electrolysis bath heat income, after 1.3h, electrolysis bath generation anode effect, slot control machine Set-out slide effect extinguishes program.Effect extinguishing means is by effect quencher (30% sodium fluoride+10% aluminium oxide, surplus is industry aluminium powder), it is delivered in air film barrier layer, sodium fluoride in effect quencher improves electrolyte molecular proportion, increase electrolyte oxidation aluminum solvability, industry aluminium powder and carbon dioxide vigorous reaction in air film barrier layer, reaction liberated heat regulating electrolytic tank thermal balance, the heat that effector phase produces makes bath temperature raise, gas expansion also punctures air film barrier layer, the activated alumina that reaction generates dissolves in rapidly electrolyte, the aluminium oxide liquid added dissolves rapidly, alumina concentration in electrolyte bottom raising anode, anode effect is extinguished.Subsequently, slot control machine is by groove pressure and reinforced recovery normal process standard.

Claims (4)

1. an electrolytic aluminium anodic effect processes device, it is characterized in that, described process device includes air distributing device (1), the outlet side of described air distributing device (1) is connected to quencher storage tank (2), the outlet side of described quencher storage tank (2) is extinguished pipe (3) by flexible pipe with effect and is connected, and described process device also includes extinguishing for lifting, rotate, bend described effect the effect of pipe (3) and extinguishes pipe actuating device (4).
2. process device according to claim 1, it is characterised in that it is metal hose that described effect extinguishes pipe (3), and is arranged with carbon protective sleeve outside this metal hose.
3. process device according to claim 1, it is characterised in that described effect is extinguished pipe actuating device (4) and included motor, speed change gear, output power shaft and clamping device;Described clamping device clamps described effect by roller and extinguishes pipe (3).
4. according to the process device one of claim 1-3 Suo Shu, it is characterised in that described process device also includes pressure shell tup (5).
CN201620177961.4U 2016-03-09 2016-03-09 Anode effect processing apparatus Active CN205398737U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620177961.4U CN205398737U (en) 2016-03-09 2016-03-09 Anode effect processing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620177961.4U CN205398737U (en) 2016-03-09 2016-03-09 Anode effect processing apparatus

Publications (1)

Publication Number Publication Date
CN205398737U true CN205398737U (en) 2016-07-27

Family

ID=56443115

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620177961.4U Active CN205398737U (en) 2016-03-09 2016-03-09 Anode effect processing apparatus

Country Status (1)

Country Link
CN (1) CN205398737U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105624729A (en) * 2016-03-09 2016-06-01 新疆大学 Anode effect treatment device and method
CN108595793A (en) * 2018-04-10 2018-09-28 中南大学 Normalization tank voltage data Time-Frequency Analysis Method and equipment for aluminium cell process control

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105624729A (en) * 2016-03-09 2016-06-01 新疆大学 Anode effect treatment device and method
CN105624729B (en) * 2016-03-09 2019-01-22 新疆大学 A kind of anode effect processing unit and method
CN108595793A (en) * 2018-04-10 2018-09-28 中南大学 Normalization tank voltage data Time-Frequency Analysis Method and equipment for aluminium cell process control
CN108595793B (en) * 2018-04-10 2022-03-08 中南大学 Normalizing tank voltage data time-frequency analysis method and equipment for aluminum electrolysis

Similar Documents

Publication Publication Date Title
CN105624737B (en) A kind of method for preparing magnesium-rare earth and rare-earth yttrium neodymium magnesium alloy
CN103484721B (en) A kind of method preparing ferro-titanium
CN106929688B (en) A kind of apparatus and method preparing rafifinal using aluminium lime-ash
CN103834815B (en) A kind of method be separated containing tungsten tantalum in the rich tungsten slag of tantalum
CN205398737U (en) Anode effect processing apparatus
CN106435273B (en) A kind of high-plasticity corrosion-resistance Zn-Cu-Ti alloys and preparation method thereof
CN102703929B (en) Method for preparing Ti-Fe alloy by direct reduction of ilmenite
CN104694973A (en) Process for preparing ferrotitanium alloy
CN106544519A (en) A kind of electroslag remelting nickel base superalloy hollow steel ingot slag system and preparation method thereof
CN102995066A (en) Molten salt electrochemical reduction method for removing sulfide inclusions on solid steel surface
CN107557840A (en) A kind of magnesium alloy differential arc oxidation technique
CN100560741C (en) A kind of refined-smelting ladle furnace calcium carbide deoxidation method
CN105734615B (en) A kind of method that thermoelectricity reduction prepares Titanium in fluoride smelt salt
CN101713082A (en) Low-temperature aluminum electrolysis process and electrolyte
CN105714332A (en) Method for electrodepositing vanadium through fused salt
CN106702175A (en) Composite refining agent of scrap copper
CN108950308A (en) A kind of chemical equipment falling liquid film pure nickel pipe and preparation method thereof
WO2023246367A1 (en) Antimony-sulfide-containing ore-based molten salt electrolysis continuous production method and apparatus
CN105755505A (en) Anode effect termination agent
CN102277595A (en) Deoxidation refining method for titanium and iron alloy
CN105624729B (en) A kind of anode effect processing unit and method
CN105177632B (en) It is rare earth modified to prepare copper aluminium rare earth intermediate alloy molten salt electrolysis method and alloy
CN106283098B (en) A kind of method for recycling continuous electrolysis sodium aluminate solution and preparing aluminium oxide
CN110863213B (en) Method for improving corrosion resistance of nickel electrode in molten salt system
CN104213151B (en) Method for preparing lead-antimony alloy by directly electrolyzing lead-antimony oxide

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant