CN102978659B - A kind of Deep method of comprehensive utilization of electrolytic cell overhaul slag - Google Patents

A kind of Deep method of comprehensive utilization of electrolytic cell overhaul slag Download PDF

Info

Publication number
CN102978659B
CN102978659B CN201210511713.5A CN201210511713A CN102978659B CN 102978659 B CN102978659 B CN 102978659B CN 201210511713 A CN201210511713 A CN 201210511713A CN 102978659 B CN102978659 B CN 102978659B
Authority
CN
China
Prior art keywords
block
useless
refractory brick
water logging
powder
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
CN201210511713.5A
Other languages
Chinese (zh)
Other versions
CN102978659A (en
Inventor
邹建明
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.)
Zhou Junhe
Original Assignee
Zhou Junhe
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 Zhou Junhe filed Critical Zhou Junhe
Priority to CN201210511713.5A priority Critical patent/CN102978659B/en
Publication of CN102978659A publication Critical patent/CN102978659A/en
Application granted granted Critical
Publication of CN102978659B publication Critical patent/CN102978659B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

The invention discloses the Deep method of comprehensive utilization of a kind of electrolytic cell overhaul slag, it is characterized in that, electrolytic cell overhaul slag is sorted, respectively obtain electrolyte block, cathode bar, waste cathode carbon block, useless refractory brick, useless insulating brick, useless heat-insulating shield, give up to prick and stick with paste, and remaining mixing slag charge;The block of sorting being carried out water logging respectively, selects broken, water logging again after block, the block selected reclaims, remaining powder pulverizing, flotation, selects carbon dust therein, refractory material powder, and remaining powder makes metallurgical slag former.The fluoride salt being difficult in electrolytic cell overhaul slag remove is separated by the present invention, and the recycling that improve electrolytic cell overhaul slag is worth so that it is turns waste into wealth, it is achieved that electrolytic cell overhaul slag economy, pollution-free recovery, is inherently eliminated pollution hidden trouble.

Description

A kind of Deep method of comprehensive utilization of electrolytic cell overhaul slag
Technical field
The present invention relates to the Deep method of comprehensive utilization of a kind of electrolytic cell overhaul slag, belong to electrolytic cell overhaul slag processing technology field.
Background technology
Aluminium cell typically needs to carry out large repairs after using 4~5 years, and the average groove life of majority enterprise of China was at about 1500 days, and during overhaul, the waste liner of removing, is electrolytic cell overhaul slag, and this slag is contained within soluble fluoride.Slag from delining mainly includes waste cathode carbon block, useless refractory brick, pricks paste, useless insulating brick, refractory powder, fire mortar and useless heat-insulating shield etc..Its generation amount is about 30kg/t Al(relative number, becomes with groove length in age), whole nation electrolytic aluminium production capacity is more than 9,000,000 t/a at present, then slag from delining generation amount is at about 270,000 t/a.
Aluminum electrolysis uses fused salt electrolysis process.I.e. with aluminium oxide as raw material, with fluoride salt (cryolite, aluminium fluoride) as flux, during electrolysis production, a part of fluorine-containing electrolyte is absorbed by carbonaceous Pot Lining, then is diffused in other furnace building material.
" discriminating of hazardous waste judging standard corrosivity " (GB5085.1 1996) and " hazardous waste judging standard leaching characteristic identification " (GB5085.3 1996) just promulgated for 1996 according to country;Electrolytic cell overhaul slag belongs to hazardous solid waste because of absorption fluoride and a small amount of cyanide, if the most effectively comprehensively utilized and harmless treatment or store mishandling, soil and groundwater will exist the most potential pollution effect.
In prior art, as follows to the processing method of aluminium cell overhaul groove slag:
1, adding Calx in waste cathode carbon block to be allowed to react with electrolyte therein, obtain calcium fluoride, sodium fluoride and aluminium fluoride, make fluorine obtain solidifying to re-use, the charcoal of recovery is reused for manufacturing cathode material, but processing cost is the highest.
2, utilize cement kiln internal reaction temperature high, the conditions such as carbon block time of staying length on stream, making the harmful substance in waste cathode carbon block carry out decomposing displacement in hot environment, and be finally solidificated in clinker, the carbon in waste cathode carbon block reduces the consumption of coal as fuel simultaneously.But, use the shortcoming of the method the most clearly: fluorine has infringement to refractory brick, and fluorine easily enters air with fume emission and causes atmospheric pollution;In waste cathode carbon block, the content of sodium is high, can have an impact cement later strength.
3, Shandong Aluminum Plant began to utilize useless carbon block to add the replacement part anthracite use of alumina clinker calcining kiln as far back as nineteen eighty-two, although by state verification, obtains preferable effect, but can not accomplish big argument, high value added utilization.
4, the domestic and international research that useless SiC-Si3N4's refractory brick treatment technology gives up is substantially at blank.
5, the research recycled electrolytic aluminium fluorine-containing waste disposal industrial water both at home and abroad is substantially at blank.
The method of above-mentioned process electrolytic cell overhaul slag all because of can not argument, high value added utilization electrolytic cell overhaul slag greatly, it is achieved that commercial Application and few, cause most aluminium cell overhaul groove slag still to be thrown aside.
Electrolytic cell overhaul slag is either stored or fills, and will put into huge investment cost and operational and administrative expenses, and there is long-term potential pollution hidden danger.Therefore slag from delining is carried out harmless treatment, turned waste into wealth, be inherently eliminated pollution hidden trouble, be then optimal and final scheme.
Summary of the invention
It is an object of the invention to, it is provided that the Deep method of comprehensive utilization of a kind of electrolytic cell overhaul slag.After carbon, fluoride salt, electrolyte, insulation material, refractory material separation in overhaul groove slag, purifying, become the raw material meeting commercial Application standard, for improving the comprehensive utilization of overhaul groove slag, eliminate environmental pollution, economize the land resource, and form the utilization of big argument, high added value.
Technical scheme.The Deep method of comprehensive utilization of electrolytic cell overhaul slag, comprises the steps:
A, electrolytic cell overhaul slag is sorted, respectively obtain electrolyte block, cathode bar, waste cathode carbon block, useless refractory brick, useless insulating brick, useless heat-insulating shield, useless bundle are stuck with paste, and remaining mixing slag charge;
B, waste cathode carbon block is carried out water logging, obtain soaking the powder scattered and block, block therein is selected, the block selected is passed through broken, water logging again, again selects block therein after drying as the aggregate making cathode carbon pieces, remaining powder carries out pulverizing process, then flotation, obtains carbon dust;The cathode carbon pieces aggregate of gained and carbon dust, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtains highly purified carbon materials;
C, useless refractory brick are alumina firebrick, alumina firebrick is carried out water logging, obtain soaking the powder scattered and block, block being selected, the block selected is passed through broken, water logging again, select block, reclaiming as the aggregate making refractory brick after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
Useless refractory brick is silicon-carbide-silicon nitride refractory brick, silicon-carbide-silicon nitride refractory brick is carried out water logging, obtain soaking the powder scattered and block, block therein is selected, the block selected is by broken, water logging again, again selecting the block therein aggregate as making refractory brick, remaining powder carries out pulverizing process, then flotation, obtain refractory brick powder, the refractory brick aggregate of gained and powder, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, sodium fluoride therein is gasified, obtains highly purified refractory brick material;
D, useless insulating brick or useless heat-insulating shield are carried out water logging respectively, obtain soaking the powder scattered and block, block is selected, the block selected is by broken, water logging again, selects block, reclaims respectively as the aggregate making insulating brick or heat-insulating shield after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
E, mixing slag charge being carried out pulverizing process, then flotation, select carbon dust therein, refractory material powder, remaining powder makes metallurgical slag former.
The Deep method of comprehensive utilization of above-mentioned electrolytic cell overhaul slag, described step b is, waste cathode carbon block is carried out water logging 2-3 days, obtains soaking the powder scattered and block, the particle diameter block more than 1-5 centimetre is selected, the block selected, by being crushed to particle diameter 0.5-2 centimetre, again water logging, selects the particle diameter block more than 0.3-1 centimetre, after drying as the aggregate making cathode carbon pieces, remaining powder carries out pulverizing, flotation, obtains carbon dust.
The Deep method of comprehensive utilization of above-mentioned electrolytic cell overhaul slag, described step c is, useless refractory brick is useless alumina firebrick, useless alumina firebrick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 1-5 centimetre is selected, the block selected is by being crushed to particle diameter 0.5-2 centimetre, water logging again, select the particle diameter block more than 0.3-1 centimetre, reclaiming as the aggregate making refractory brick after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
Useless refractory brick is silicon-carbide-silicon nitride refractory brick, silicon-carbide-silicon nitride refractory brick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 1-5 centimetre is selected, the block selected is by being crushed to particle diameter 0.5-2 centimetre, water logging again, again select the particle diameter block more than 0.3-1 centimetre as the aggregate making refractory brick, remaining powder carries out pulverizing process, flotation again, obtain refractory brick powder, the refractory brick aggregate of gained and powder, by after drying, high-temperature calcination is carried out at 1700-1900 DEG C, sodium fluoride therein is gasified, obtain highly purified refractory brick material.
The Deep method of comprehensive utilization of above-mentioned electrolytic cell overhaul slag, in described step d, useless insulating brick or useless heat-insulating shield are carried out water logging 2-3 days respectively, obtain soaking the powder scattered and block, the particle diameter block more than 1-5 centimetre is selected, the block selected is by being crushed to particle diameter 0.5-2 centimetre, water logging again, select the particle diameter block more than 0.3-1 centimetre, reclaim respectively as the aggregate making useless insulating brick or useless heat-insulating shield after drying, remaining powder carries out pulverizing process, makes metallurgical slag former.
The Deep method of comprehensive utilization of above-mentioned electrolytic cell overhaul slag, useless bundle in described step a is stuck with paste, processed by pulverizing, then flotation, select carbon dust therein, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtain highly purified carbon materials.
The Deep method of comprehensive utilization of above-mentioned electrolytic cell overhaul slag, being reclaimed by reverse osmosis water treatment system with water in described each step, the clear water of isolated recycles, and the high fluorine residue obtained makes metallurgical slag former.
For electrolytic cell overhaul slag, as a example by the 160KA pre-baking tank of certain electrolytic aluminium factory, in slag from delining, all kinds of materials composition situation is shown in Table 1.
Table 1 160KA pre-baking tank slag from delining composition situation
Wherein, the main component that cathode carbon pieces, bundle are stuck with paste is carbon, and refractory brick is divided into again alumina firebrick and SiC-Si3N4Composite fireproof brick, also the insulating brick of in bulk and heat-insulating shield etc. can sort out.Meanwhile, electrolytic cell overhaul slag also has a small amount of electrolyte and cathode bar, is recoverable after sorting out.The method of the present invention, first pass through preliminary sorting, obtain various block, then pass through water logging, owing to fluoride salt can be soluble in water, and adsorb fluoride salt (sodium fluoride is main) high block and will soak and scatter, remaining block absorption fluoride salt is low, sorting residue block again broken, soak after, highly purified block can be obtained, such as cathode carbon pieces material, refractory brick block, insulating brick block and heat-insulating shield block etc., economic worth can be improve as the aggregate of various products.For remaining powder, cathode carbon pieces and the useless powder stuck with paste of pricking by ball milling, after flotation, it is possible to obtain carbon dust, then calcine through electric furnace high-temperature, obtain high-purity carbon raw, remain various fluorine-containing slag charge and can make replacement CaF2Metallurgical slag former.For during recycling with water, reclaimed by reverse osmosis water treatment system, the clear water of isolated recycles, and the high fluorine residue obtained makes metallurgical slag former, it is achieved the recycling of industrial water.Invention carries out harmless resource utilization advanced treating to electrolytic cell overhaul slag, use advanced Technology and measure, the fluoride salt being difficult in electrolytic cell overhaul slag remove is separated, the recycling that improve electrolytic cell overhaul slag is worth, make it turn waste into wealth, achieve electrolytic cell overhaul slag economy, pollution-free recovery, be inherently eliminated pollution hidden trouble.The Technology of the present invention can turn waste into wealth, and energy consumption is low, does not has secondary pollution problem in production process, it is achieved that itself clean produces, and is suitable for the big argument of electrolytic cell overhaul slag, the utilization of high added value.
Detailed description of the invention
Embodiments of the invention 1.The Deep method of comprehensive utilization of electrolytic cell overhaul slag, comprises the steps:
A, electrolytic cell overhaul slag is sorted, respectively obtain electrolyte block, cathode bar, waste cathode carbon block, useless refractory brick, useless insulating brick, useless heat-insulating shield, useless bundle are stuck with paste, and remaining mixing slag charge.Wherein, electrolyte block is mainly aluminum, can directly be recovered to electrolytic aluminium factory, and cathode bar is iron staff, it is possible to directly reclaim.
B, waste cathode carbon block being carried out water logging, fluoride salt is soluble in water, and the cathode carbon pieces having adsorbed fluoride salt can scatter, obtain soaking the powder scattered and block, block therein being selected, the fluoride salt of the block absorption selected is few, by the block selected by crushing, water logging again, removing fluoride salt further, again select block therein after drying as the aggregate of making cathode carbon pieces, remaining powder carries out pulverizing process, flotation again, obtains carbon dust.The cathode carbon pieces aggregate of gained and carbon dust, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtains highly purified carbon materials.
C, useless refractory brick are alumina firebrick, alumina firebrick is carried out water logging, and the alumina firebrick having adsorbed fluoride salt can scatter, and obtains soaking the powder scattered and block, block is selected, the fluoride salt of the block absorption selected is few, by again crushing, and water logging again, select block, reclaiming as the aggregate making refractory brick after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
Useless refractory brick is silicon-carbide-silicon nitride refractory brick, owing to silicon-carbide-silicon nitride refractory brick is worth higher, the recovery process of cathode blocks in step b can be used to process, specific as follows, silicon-carbide-silicon nitride refractory brick is carried out water logging, obtain soaking the powder scattered and block, block therein is selected, the block selected is by broken, water logging again, again select block therein as the aggregate making refractory brick, remaining powder carries out pulverizing process, flotation again, obtain refractory brick powder, the refractory brick aggregate of gained and powder, by after drying, high-temperature calcination is carried out at 1700-1900 DEG C, sodium fluoride therein is gasified, obtain highly purified refractory brick material.
D, useless insulating brick or useless heat-insulating shield are carried out water logging respectively, obtain soaking the powder scattered and block, block is selected, the block selected is by broken, water logging again, selects block, reclaims respectively as the aggregate making insulating brick or heat-insulating shield after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
E, mixing slag charge being carried out pulverizing process, then use existing floatation process, select carbon dust therein, refractory material powder, remaining powder makes metallurgical slag former.The carbon dust floatingly selected can pass through high-temperature calcination, obtains highly purified carbon dust.
Useless bundle is stuck with paste, can be processed by pulverizing, then flotation, select carbon dust therein, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtain highly purified carbon materials.
Use water in each step of present invention process, is reclaimed by reverse osmosis water treatment system, and the clear water of isolated recycles, the high fluorine residue obtained, and makes metallurgical slag former together with the powder obtained before.
Embodiments of the invention 2.The Deep method of comprehensive utilization of electrolytic cell overhaul slag, comprises the steps:
A, electrolytic cell overhaul slag is sorted, respectively obtain electrolyte block, cathode bar, waste cathode carbon block, useless refractory brick, useless insulating brick, useless heat-insulating shield, useless bundle are stuck with paste, and remaining mixing slag charge.
B, waste cathode carbon block is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 5 centimetres is selected, the block selected, by being crushed to particle diameter 2 centimetres, water logging again, selects the particle diameter block more than 1 centimetre, as the aggregate making cathode carbon pieces, remaining powder carries out pulverizing, flotation, obtains carbon dust.The cathode carbon pieces aggregate of gained and carbon dust, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtains highly purified carbon materials.
C, useless refractory brick are useless alumina firebrick, useless alumina firebrick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 1-5 centimetre being selected, the block selected is by being crushed to particle diameter 0.5-2 centimetre, again water logging, select the particle diameter block more than 0.3-1 centimetre, reclaiming as the aggregate making refractory brick after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
Useless refractory brick is silicon-carbide-silicon nitride refractory brick, silicon-carbide-silicon nitride refractory brick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 1-5 centimetre is selected, the block selected is by being crushed to particle diameter 0.5-2 centimetre, water logging again, again select the particle diameter block more than 0.3-1 centimetre as the aggregate making refractory brick, remaining powder carries out pulverizing process, flotation again, obtain refractory brick powder, the refractory brick aggregate of gained and powder, by after drying, high-temperature calcination is carried out at 1700-1900 DEG C, sodium fluoride therein is gasified, obtain highly purified refractory brick material.
D, useless insulating brick or useless heat-insulating shield are carried out water logging respectively, obtain soaking the powder scattered and block, block is selected, the block selected is by broken, water logging again, selects block, reclaims respectively as the aggregate making insulating brick or heat-insulating shield after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
E, mixing slag charge being carried out pulverizing process, then use existing floatation process, select carbon dust therein, refractory material powder, remaining powder makes metallurgical slag former.
Useless bundle is stuck with paste, can be processed by pulverizing, then flotation, select carbon dust therein, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtain highly purified carbon materials.
Use water in above steps, is reclaimed by reverse osmosis water treatment system, and the clear water of isolated recycles, the high fluorine residue obtained, and makes metallurgical slag former together with the powder obtained before.
Embodiments of the invention 3.The Deep method of comprehensive utilization of electrolytic cell overhaul slag, comprises the steps:
A, electrolytic cell overhaul slag is sorted, respectively obtain electrolyte block, cathode bar, waste cathode carbon block, useless refractory brick, useless insulating brick, useless heat-insulating shield, useless bundle are stuck with paste, and remaining mixing slag charge.
B, waste cathode carbon block is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 1 centimetre is selected, the block selected, by being crushed to particle diameter 0.5 centimetre, water logging again, selects the particle diameter block more than 0.3 centimetre, after drying as the aggregate making cathode carbon pieces, remaining powder carries out pulverizing, flotation, obtains carbon dust.The cathode carbon pieces aggregate of gained and carbon dust, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtains highly purified carbon materials.
C, useless refractory brick are useless alumina firebrick, useless alumina firebrick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 1 centimetre being selected, the block selected is by being crushed to particle diameter 0.5 centimetre, water logging again, select the particle diameter block more than 0.3 centimetre, reclaiming as the aggregate making refractory brick after drying, remaining powder carries out pulverizing process, makes metallurgical slag former.
When useless refractory brick is silicon-carbide-silicon nitride refractory brick, owing to silicon-carbide-silicon nitride refractory brick is worth higher, the recovery process of cathode blocks in step b can be used to process, specific as follows, silicon-carbide-silicon nitride refractory brick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 1 centimetre is selected, the block selected is by being crushed to particle diameter 0.5 centimetre, water logging again, again select the particle diameter block more than 0.3 centimetre after drying as the aggregate making refractory brick, remaining powder carries out pulverizing process, flotation again, obtain refractory brick powder.Obtain refractory brick powder, the refractory brick aggregate of gained and powder, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, sodium fluoride therein is gasified, obtain highly purified refractory brick material.
D, useless insulating brick or useless heat-insulating shield are carried out water logging respectively, obtain soaking the powder scattered and block, block is selected, the block selected is by broken, water logging again, selects block, reclaims respectively as the aggregate making insulating brick or heat-insulating shield after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
E, mixing slag charge being carried out pulverizing process, then use existing floatation process, select carbon dust therein, refractory material powder, remaining powder makes metallurgical slag former.
Use water in above steps, is reclaimed by reverse osmosis water treatment system, and the clear water of isolated recycles, the high fluorine residue obtained, and makes metallurgical slag former together with the powder obtained before.
Embodiments of the invention 4.The Deep method of comprehensive utilization of electrolytic cell overhaul slag, comprises the steps:
A, electrolytic cell overhaul slag is sorted, respectively obtain electrolyte block, cathode bar, waste cathode carbon block, useless refractory brick, useless insulating brick, useless heat-insulating shield, useless bundle are stuck with paste, and remaining mixing slag charge.
B, waste cathode carbon block is carried out water logging 2 days, obtain soaking the powder scattered and block, the particle diameter block more than 3 centimetres is selected, the block selected, by being crushed to particle diameter 1 centimetre, water logging again, selects the particle diameter block more than 0.6 centimetre, after drying as the aggregate making cathode carbon pieces, remaining powder carries out pulverizing, flotation, obtains carbon dust.The cathode carbon pieces aggregate of gained and carbon dust, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtains highly purified carbon materials.
C, useless refractory brick are useless alumina firebrick, useless alumina firebrick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 3 centimetres being selected, the block selected is by being crushed to particle diameter 1 centimetre, water logging again, select the particle diameter block more than 0.6 centimetre, reclaiming as the aggregate making refractory brick after drying, remaining powder carries out pulverizing process, makes metallurgical slag former.
When useless refractory brick is silicon-carbide-silicon nitride refractory brick, owing to silicon-carbide-silicon nitride refractory brick is worth higher, the recovery process of cathode blocks in step b can be used to process, specific as follows, silicon-carbide-silicon nitride refractory brick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 3 centimetres is selected, the block selected is by being crushed to particle diameter 1 centimetre, water logging again, again select the particle diameter block more than 0.6 centimetre after drying as the aggregate making refractory brick, remaining powder carries out pulverizing process, flotation again, obtain refractory brick powder.Obtain refractory brick powder, the refractory brick aggregate of gained and powder, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, sodium fluoride therein is gasified, obtain highly purified refractory brick material.
D, useless insulating brick or useless heat-insulating shield are carried out water logging respectively, obtain soaking the powder scattered and block, block is selected, the block selected is by broken, water logging again, selects block, reclaims respectively as the aggregate making insulating brick or heat-insulating shield after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
E, mixing slag charge being carried out pulverizing process, then use existing floatation process, select carbon dust therein, refractory material powder, remaining powder makes metallurgical slag former.
Use water in above steps, is reclaimed by reverse osmosis water treatment system, and the clear water of isolated recycles, the high fluorine residue obtained, and makes metallurgical slag former together with the powder obtained before.

Claims (6)

1. the Deep method of comprehensive utilization of an electrolytic cell overhaul slag, it is characterised in that: comprise the steps:
A, electrolytic cell overhaul slag is sorted, respectively obtain electrolyte block, cathode bar, waste cathode carbon block, useless refractory brick, useless insulating brick, useless heat-insulating shield, useless bundle are stuck with paste, and remaining mixing slag charge;
B, waste cathode carbon block is carried out water logging, obtain soaking the powder scattered and block, block therein is selected, the block selected is passed through broken, water logging again, again selects block therein after drying as the aggregate making cathode carbon pieces, remaining powder carries out pulverizing process, then flotation, obtains carbon dust;The cathode carbon pieces aggregate of gained and carbon dust, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtains highly purified carbon materials;
C, useless refractory brick are alumina firebrick, alumina firebrick is carried out water logging, obtain soaking the powder scattered and block, block being selected, the block selected is passed through broken, water logging again, select block, reclaiming as the aggregate making refractory brick after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
Useless refractory brick is silicon-carbide-silicon nitride refractory brick, silicon-carbide-silicon nitride refractory brick is carried out water logging, obtain soaking the powder scattered and block, block therein is selected, the block selected is by broken, water logging again, again selecting the block therein aggregate as making refractory brick, remaining powder carries out pulverizing process, then flotation, obtain refractory brick powder, the refractory brick aggregate of gained and powder, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, sodium fluoride therein is gasified, obtains highly purified refractory brick material;
D, useless insulating brick or useless heat-insulating shield are carried out water logging respectively, obtain soaking the powder scattered and block, block is selected, the block selected is by broken, water logging again, selects block, reclaims respectively as the aggregate making insulating brick or heat-insulating shield after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
E, mixing slag charge being carried out pulverizing process, then flotation, select carbon dust therein, refractory material powder, remaining powder makes metallurgical slag former.
The Deep method of comprehensive utilization of electrolytic cell overhaul slag the most according to claim 1, it is characterized in that: described step b is, waste cathode carbon block is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 5 centimetres is selected, the block selected, by being crushed to particle diameter 0.5-2 centimetre, again water logging, selects the particle diameter block more than 1 centimetre, after drying as the aggregate making cathode carbon pieces, remaining powder carries out pulverizing, flotation, obtains carbon dust.
The Deep method of comprehensive utilization of electrolytic cell overhaul slag the most according to claim 1, it is characterized in that: described step c is, useless refractory brick is useless alumina firebrick, useless alumina firebrick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 5 centimetres is selected, the block selected is by being crushed to particle diameter 0.5-2 centimetre, water logging again, select the particle diameter block more than 1 centimetre, reclaiming as the aggregate making refractory brick after drying, remaining powder carries out pulverizing process, makes metallurgical slag former;
Useless refractory brick is silicon-carbide-silicon nitride refractory brick, silicon-carbide-silicon nitride refractory brick is carried out water logging 2-3 days, obtain soaking the powder scattered and block, the particle diameter block more than 5 centimetres is selected, the block selected is by being crushed to particle diameter 0.5-2 centimetre, water logging again, again select the particle diameter block more than 1 centimetre as the aggregate making refractory brick, remaining powder carries out pulverizing process, flotation again, obtain refractory brick powder, the refractory brick aggregate of gained and powder, by after drying, high-temperature calcination is carried out at 1700-1900 DEG C, sodium fluoride therein is gasified, obtain highly purified refractory brick material.
The Deep method of comprehensive utilization of electrolytic cell overhaul slag the most according to claim 1, it is characterized in that: in described step d, useless insulating brick or useless heat-insulating shield are carried out water logging 2-3 days respectively, obtain soaking the powder scattered and block, the particle diameter block more than 5 centimetres is selected, the block selected is by being crushed to particle diameter 0.5-2 centimetre, water logging again, select the particle diameter block more than 1 centimetre, reclaim respectively as the aggregate making useless insulating brick or useless heat-insulating shield after drying, remaining powder carries out pulverizing process, makes metallurgical slag former.
The Deep method of comprehensive utilization of electrolytic cell overhaul slag the most according to claim 1, it is characterized in that: the useless bundle in described step a is stuck with paste, processed by pulverizing, then flotation, select carbon dust therein, by after drying, carry out high-temperature calcination at 1700-1900 DEG C, by sodium fluoride therein, sulfur gasification, obtain highly purified carbon materials.
6. according to the Deep method of comprehensive utilization of the electrolytic cell overhaul slag described in any one of claim 1-5, it is characterized in that: being reclaimed by reverse osmosis water treatment system with water in described each step, the clear water of isolated recycles, and the high fluorine residue obtained makes metallurgical slag former.
CN201210511713.5A 2012-12-04 2012-12-04 A kind of Deep method of comprehensive utilization of electrolytic cell overhaul slag Active CN102978659B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210511713.5A CN102978659B (en) 2012-12-04 2012-12-04 A kind of Deep method of comprehensive utilization of electrolytic cell overhaul slag

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210511713.5A CN102978659B (en) 2012-12-04 2012-12-04 A kind of Deep method of comprehensive utilization of electrolytic cell overhaul slag

Publications (2)

Publication Number Publication Date
CN102978659A CN102978659A (en) 2013-03-20
CN102978659B true CN102978659B (en) 2016-08-10

Family

ID=47852990

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210511713.5A Active CN102978659B (en) 2012-12-04 2012-12-04 A kind of Deep method of comprehensive utilization of electrolytic cell overhaul slag

Country Status (1)

Country Link
CN (1) CN102978659B (en)

Families Citing this family (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104141153B (en) * 2013-08-15 2016-05-04 郑州发祥铝业有限公司 A kind of processing method of electrolytic cell carbon slag
CN103864402B (en) * 2014-01-25 2015-06-24 云南蓝天铝业环保科技有限公司 Insulation brick produced from waste insulation material of aluminum electrolysis cells and preparation method thereof
CN103949459B (en) * 2014-01-25 2016-01-27 云南蓝天铝业环保科技有限公司 A kind of electrolytic aluminium breeze of recycling produces aluminium electrolyte and the method reclaiming carbon
CN105772486B (en) * 2016-04-26 2017-09-29 中南大学 A kind of method of cyanide in removal aluminum cell waste cathode carbon
CN105964659B (en) * 2016-05-27 2018-02-23 中南大学 A kind of aluminum cell waste cathode carbon block comprehensive recovering process
CN107626712A (en) * 2017-08-29 2018-01-26 陕西三秦能源长宏铝业有限公司 A kind of aluminium electroloysis danger solid waste integrated conduct method and recycling
CN107720723B (en) * 2017-11-09 2020-08-11 北京科技大学 Method for comprehensively treating waste cell lining of aluminum electrolysis cell
CN108787718B (en) * 2018-08-01 2021-05-07 湘潭大学 Mechanochemical conversion and recovery method for sodium-containing and fluorine-containing compounds in aluminum electrolysis waste carbon slag
CN109437823A (en) * 2018-11-02 2019-03-08 中南大学 A kind of processing method and sapecial coating of silicon carbide solid waste
CN112756082B (en) * 2021-02-04 2022-12-06 昆明理工大学 Green regeneration method of electrolytic aluminum waste tank lining mixture
CN113173777A (en) * 2021-03-24 2021-07-27 湖南国发控股有限公司 Formula and process method for preparing ceramsite by using overhaul residues
CN113231436B (en) * 2021-04-13 2022-04-22 北京科技大学 High-temperature recycling treatment method for aluminum electrolysis waste cell lining

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4113832A (en) * 1977-11-28 1978-09-12 Kaiser Aluminum & Chemical Corporation Process for the utilization of waste materials from electrolytic aluminum reduction systems
CN1358581A (en) * 2001-11-20 2002-07-17 舒大平 Harmless treatment and comprehensive utilization method for aluminium electrolytic carbon slag and waste cathode material
CN101386017A (en) * 2008-10-17 2009-03-18 东北大学 Method for treating aluminum electrolysis waste cathode carbon block using acid and alkali combination method
CN102161049A (en) * 2011-04-01 2011-08-24 陈俊贤 Comprehensive utilization method of waste and old cathode carbon blocks of aluminium electrolytic bath

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA2588929A1 (en) * 2007-05-11 2008-11-11 Institut National De La Recherche Scientifique (Inrs) Process for treating aluminum smelter waste contaminated with polycyclic aromatic hydrocarbons (pahs) and fluorides

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4113832A (en) * 1977-11-28 1978-09-12 Kaiser Aluminum & Chemical Corporation Process for the utilization of waste materials from electrolytic aluminum reduction systems
CN1358581A (en) * 2001-11-20 2002-07-17 舒大平 Harmless treatment and comprehensive utilization method for aluminium electrolytic carbon slag and waste cathode material
CN101386017A (en) * 2008-10-17 2009-03-18 东北大学 Method for treating aluminum electrolysis waste cathode carbon block using acid and alkali combination method
CN102161049A (en) * 2011-04-01 2011-08-24 陈俊贤 Comprehensive utilization method of waste and old cathode carbon blocks of aluminium electrolytic bath

Also Published As

Publication number Publication date
CN102978659A (en) 2013-03-20

Similar Documents

Publication Publication Date Title
CN102978659B (en) A kind of Deep method of comprehensive utilization of electrolytic cell overhaul slag
CN102989744B (en) Method for recycling mixed material dreg of overhauling groove slag of electrolytic cell
CN103397128B (en) Method used for extracting iron from red mud by drastic reduction and method used for preparing gel material from secondary tailings
CN101357367B (en) Method for processing waste cell-lining of aluminum cell using coal slack
Zhao et al. Recycling and utilization of spent potlining by different high temperature treatments
CN107401746B (en) Treatment system and treatment method for aluminum electrolysis overhaul slag
CN104975308A (en) Aluminum electrolytic waste slot lining closed-loop recycling method
CN105964660B (en) A kind of method of harmless treatment aluminium electrolytic tank
CN107720723B (en) Method for comprehensively treating waste cell lining of aluminum electrolysis cell
CN102992298B (en) A kind of recoverying and utilizing method of electrolytic cell overhaul slag waste cathode carbon block
CN107352819A (en) A kind of aluminium cell carbonaceous waste material is used for the method for producing calcium aluminum fluoride clinker
CN107363074B (en) A kind of aluminium cell carbonaceous materials recycling is the method for alternative fire coal
CN103343363A (en) Method for producing electrolyte for electrolytic aluminum
CN112958587A (en) Method and device for co-processing and utilizing aluminum ash and overhaul slag
CN103028592B (en) A kind of circulation utilization method of electrolytic cell overhaul slag recovery water
CN117123591A (en) Method for dry dechlorination of waste incineration fly ash and synchronous preparation of liquid chlorine and solidified soil
CN206069804U (en) With the anthracitic system of electrolytic aluminium waste cathode carbon block production high graphite
RU2472865C1 (en) Method of processing fluorine-containing wastes from electrolytic production of aluminium
CN204685646U (en) The treating apparatus of aluminium electroloysis waste lining
CN107200488B (en) Method for producing fluoroaluminate cement by using carbon waste of aluminum electrolytic cell in dry-process rotary kiln plant
CN109127657A (en) Mechanochemistry conversion and recovery method in a kind of aluminium electroloysis slag from delining containing sodium, fluorochemical
CN102653403B (en) Process method for preparing calcium carbide by recycling calcium carbide slag
CN107159688A (en) A kind of aluminium cell carbonaceous materials recycling make a living electricity production stone raw material method
CN102976776B (en) A kind of recoverying and utilizing method of electrolytic cell overhaul slag refractory brick
CN107381534A (en) A kind of cleaning recoverying and utilizing method of aluminium cell carbonaceous waste material

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
ASS Succession or assignment of patent right

Owner name: ZOU JIANMING

Free format text: FORMER OWNER: GUIZHOU LVCHENG ALUMINUM MATERIAL RESEARCH AND DEVELOPMENT CO., LTD.

Effective date: 20130711

C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20130711

Address after: 1, unit 3, building 99, 550014 Yucai Road, Baiyun District, Guizhou, Guiyang, 601

Applicant after: Zou Jianming

Address before: 550014, Guizhou Guiyang Baiyun District aluminum and aluminum processing base, East Ring Road Aluminum City Aluminum

Applicant before: Guizhou Lvcheng Raw Material of Aluminum Research and Development Co., Ltd.

ASS Succession or assignment of patent right

Owner name: WANG GANG

Free format text: FORMER OWNER: ZOU JIANMING

Effective date: 20130807

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 550014 GUIYANG, GUIZHOU PROVINCE TO: 102206 CHANGPING, BEIJING

TA01 Transfer of patent application right

Effective date of registration: 20130807

Address after: 102206, Beijing, Huilongguan, Changping District, Yue long, four, 3-1-4-501

Applicant after: Wang Gang

Address before: 1, unit 3, building 99, 550014 Yucai Road, Baiyun District, Guizhou, Guiyang, 601

Applicant before: Zou Jianming

ASS Succession or assignment of patent right

Owner name: GUIZHOU LVCHENG ALUMINUM MATERIAL RESEARCH AND DEV

Free format text: FORMER OWNER: WANG GANG

Effective date: 20130930

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 102206 CHANGPING, BEIJING TO: 550014 GUIYANG, GUIZHOU PROVINCE

TA01 Transfer of patent application right

Effective date of registration: 20130930

Address after: 550014, Guizhou Guiyang Baiyun District aluminum and aluminum processing base, East Ring Road Aluminum City Aluminum

Applicant after: Guizhou Lvcheng Raw Material of Aluminum Research and Development Co., Ltd.

Address before: 102206, Beijing, Huilongguan, Changping District, Yue long, four, 3-1-4-501

Applicant before: Wang Gang

ASS Succession or assignment of patent right

Owner name: ZOU JIANMING

Free format text: FORMER OWNER: GUIZHOU LVCHENG ALUMINUM MATERIAL RESEARCH AND DEVELOPMENT CO., LTD.

Effective date: 20131119

Owner name: DU YANHUA

Effective date: 20131119

C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20131119

Address after: 1, unit 3, building 99, 550014 Yucai Road, Baiyun District, Guizhou, Guiyang, 601

Applicant after: Zou Jianming

Applicant after: Du Yanhua

Address before: 550014, Guizhou Guiyang Baiyun District aluminum and aluminum processing base, East Ring Road Aluminum City Aluminum

Applicant before: Guizhou Lvcheng Raw Material of Aluminum Research and Development Co., Ltd.

SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20151009

Address after: 550004, hawthorn alley, Yunyan District, Guizhou, Guiyang 40

Applicant after: Zhou Junhe

Applicant after: Du Yanhua

Address before: 1, unit 3, building 99, 550014 Yucai Road, Baiyun District, Guizhou, Guiyang, 601

Applicant before: Zou Jianming

Applicant before: Du Yanhua

C14 Grant of patent or utility model
GR01 Patent grant