WO2014015539A1 - Method of recycling of waste easy-open aluminum cans - Google Patents
Method of recycling of waste easy-open aluminum cans Download PDFInfo
- Publication number
- WO2014015539A1 WO2014015539A1 PCT/CN2012/079789 CN2012079789W WO2014015539A1 WO 2014015539 A1 WO2014015539 A1 WO 2014015539A1 CN 2012079789 W CN2012079789 W CN 2012079789W WO 2014015539 A1 WO2014015539 A1 WO 2014015539A1
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- WO
- WIPO (PCT)
- Prior art keywords
- aluminum
- cans
- aluminum alloy
- aluminum liquid
- liquid
- Prior art date
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- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 143
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 142
- 238000000034 method Methods 0.000 title claims abstract description 44
- 238000004064 recycling Methods 0.000 title claims abstract description 25
- 239000002699 waste material Substances 0.000 title abstract description 38
- 229910000838 Al alloy Inorganic materials 0.000 claims abstract description 91
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000003973 paint Substances 0.000 claims abstract description 21
- 238000005266 casting Methods 0.000 claims abstract description 19
- 229910052742 iron Inorganic materials 0.000 claims abstract description 14
- 230000004048 modification Effects 0.000 claims abstract description 9
- 238000012986 modification Methods 0.000 claims abstract description 9
- 238000007885 magnetic separation Methods 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims abstract description 4
- 238000002844 melting Methods 0.000 claims abstract description 4
- 230000008018 melting Effects 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims description 63
- 239000000203 mixture Substances 0.000 claims description 41
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 36
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 34
- 239000003546 flue gas Substances 0.000 claims description 34
- 239000012535 impurity Substances 0.000 claims description 26
- 230000008569 process Effects 0.000 claims description 25
- 239000007789 gas Substances 0.000 claims description 24
- 229910052710 silicon Inorganic materials 0.000 claims description 23
- 239000000919 ceramic Substances 0.000 claims description 14
- 230000005496 eutectics Effects 0.000 claims description 14
- 229910052751 metal Inorganic materials 0.000 claims description 14
- 239000002184 metal Substances 0.000 claims description 14
- 239000002245 particle Substances 0.000 claims description 14
- 239000010703 silicon Substances 0.000 claims description 14
- 239000000126 substance Substances 0.000 claims description 14
- 229910052799 carbon Inorganic materials 0.000 claims description 13
- 238000011282 treatment Methods 0.000 claims description 13
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 12
- 239000000956 alloy Substances 0.000 claims description 12
- 229910045601 alloy Inorganic materials 0.000 claims description 11
- 230000007613 environmental effect Effects 0.000 claims description 10
- 238000007670 refining Methods 0.000 claims description 9
- 239000011734 sodium Substances 0.000 claims description 9
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 claims description 8
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims description 8
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 8
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 8
- 230000015572 biosynthetic process Effects 0.000 claims description 8
- 239000011575 calcium Substances 0.000 claims description 8
- 229910052791 calcium Inorganic materials 0.000 claims description 8
- 229910052802 copper Inorganic materials 0.000 claims description 8
- 238000006477 desulfuration reaction Methods 0.000 claims description 8
- 230000023556 desulfurization Effects 0.000 claims description 8
- 239000001257 hydrogen Substances 0.000 claims description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims description 8
- 229910052749 magnesium Inorganic materials 0.000 claims description 8
- 229910052748 manganese Inorganic materials 0.000 claims description 8
- 239000001301 oxygen Substances 0.000 claims description 8
- 229910052760 oxygen Inorganic materials 0.000 claims description 8
- 229910052708 sodium Inorganic materials 0.000 claims description 8
- 229910052725 zinc Inorganic materials 0.000 claims description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- 230000000185 dioxinlike effect Effects 0.000 claims description 7
- 239000010687 lubricating oil Substances 0.000 claims description 7
- 230000001172 regenerating effect Effects 0.000 claims description 7
- 230000005294 ferromagnetic effect Effects 0.000 claims description 6
- 239000006148 magnetic separator Substances 0.000 claims description 6
- 229910052757 nitrogen Inorganic materials 0.000 claims description 6
- 239000003921 oil Substances 0.000 claims description 6
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 claims description 5
- 229910052719 titanium Inorganic materials 0.000 claims description 5
- 229910052786 argon Inorganic materials 0.000 claims description 4
- 239000003795 chemical substances by application Substances 0.000 claims description 4
- 229910052804 chromium Inorganic materials 0.000 claims description 4
- 239000006260 foam Substances 0.000 claims description 4
- 238000007872 degassing Methods 0.000 claims description 3
- 239000012634 fragment Substances 0.000 claims 3
- YEBIHIICWDDQOL-YBHNRIQQSA-N polyoxin Chemical compound O[C@@H]1[C@H](O)[C@@H](C(C=O)N)O[C@H]1N1C(=O)NC(=O)C(C(O)=O)=C1 YEBIHIICWDDQOL-YBHNRIQQSA-N 0.000 claims 1
- 239000002994 raw material Substances 0.000 abstract description 3
- 238000012545 processing Methods 0.000 abstract description 2
- 238000007781 pre-processing Methods 0.000 abstract 1
- 238000002485 combustion reaction Methods 0.000 description 17
- 238000005516 engineering process Methods 0.000 description 14
- 238000011084 recovery Methods 0.000 description 13
- 238000003723 Smelting Methods 0.000 description 12
- 238000009749 continuous casting Methods 0.000 description 7
- 150000002013 dioxins Chemical class 0.000 description 7
- 238000001179 sorption measurement Methods 0.000 description 7
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 6
- 238000005336 cracking Methods 0.000 description 6
- 239000013078 crystal Substances 0.000 description 6
- 239000000428 dust Substances 0.000 description 6
- 229910001297 Zn alloy Inorganic materials 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 229910000881 Cu alloy Inorganic materials 0.000 description 4
- 229910000861 Mg alloy Inorganic materials 0.000 description 4
- 229910000914 Mn alloy Inorganic materials 0.000 description 4
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 3
- 229910000640 Fe alloy Inorganic materials 0.000 description 3
- 229910001069 Ti alloy Inorganic materials 0.000 description 3
- 239000004411 aluminium Substances 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 229910000599 Cr alloy Inorganic materials 0.000 description 2
- 229910000676 Si alloy Inorganic materials 0.000 description 2
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 239000012466 permeate Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 229910018575 Al—Ti Inorganic materials 0.000 description 1
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 1
- 238000005903 acid hydrolysis reaction Methods 0.000 description 1
- VRAIHTAYLFXSJJ-UHFFFAOYSA-N alumane Chemical compound [AlH3].[AlH3] VRAIHTAYLFXSJJ-UHFFFAOYSA-N 0.000 description 1
- KCZFLPPCFOHPNI-UHFFFAOYSA-N alumane;iron Chemical compound [AlH3].[Fe] KCZFLPPCFOHPNI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- -1 calcium and sodium Chemical compound 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 238000006864 oxidative decomposition reaction Methods 0.000 description 1
- 238000005554 pickling Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000012756 surface treatment agent Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B21/00—Obtaining aluminium
- C22B21/0007—Preliminary treatment of ores or scrap or any other metal source
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B21/00—Obtaining aluminium
- C22B21/0038—Obtaining aluminium by other processes
- C22B21/0069—Obtaining aluminium by other processes from scrap, skimmings or any secondary source aluminium, e.g. recovery of alloy constituents
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Definitions
- the invention provides a method for recycling aluminum aluminum cans, belonging to the field of circular economy technology and environmental protection, and particularly relates to a method for recycling green recycling of waste aluminum cans. Background technique
- Waste aluminum cans have thin texture, large surface area, severe smelting and oxidation loss, and low metal recovery rate; (4) Waste aluminum cans have wide sources and difficult pretreatment. It is easy to introduce impurities into the aluminum alloy melt during smelting, which makes the alloy composition complicated and the adjustment difficulty is increased. (5) The aluminum alloy ingot can be difficult to control the structure of the aluminum alloy ingot.
- the can body of the waste aluminum can is different from the aluminum alloy of the cover and the pull ring (see Table 1).
- Table 1 Theoretically, the separation, recycling and reuse of the can body, the cover and the pull ring are beneficial for re-use and reuse. Due to the serious deformation of the recovered aluminum cans, it is usually packed and compacted for convenient transportation. From the economic and practical conditions, it is impossible to separate the tank, the cover and the pull ring, and directly return the parts of the aluminum cans. Percentage)
- the inner and outer surface paints of waste aluminum cans are prone to pollution during recycling and affect the quality of recycled aluminum alloys. Therefore, the broken aluminum cans must be stripped. Take off The lacquer method and paint stripping rate directly affect the quality of the finished aluminum or aluminum alloy material as well as the cost of use and environmental pollution. In the recycling of waste aluminum cans, stripping is one of the core technologies for the recycling of used aluminum cans, and it is also one of the difficulties.
- the waste aluminum can has a thin texture and a large surface area.
- the double-chamber reverberatory furnace is generally used to melt, so that the aluminum piece is not in contact with the flame but directly added to the molten aluminum liquid, thereby avoiding waste.
- the burning of aluminum improves the metal recovery rate.
- the waste aluminum cans have a wide range of sources, and are difficult to pretreat. It is easy to introduce impurities into the aluminum alloy melt during smelting, resulting in complex alloy composition and difficulty in adjusting composition and structure.
- Waste aluminum can recycling and recycling technology is one of the important areas for comprehensive utilization of renewable resources. Since the widespread use of scrap aluminum cans, people have spontaneously recycled and reused cans, forming relevant technologies and intellectual property rights.
- the invention aims at the complex composition of the waste aluminum can, the organic coating on the inner and outer surfaces, and the complicated source.
- the dioxin is decomposed by the secondary combustion of flue gas, the flue gas is quenched, and the technology is such as bag dust removal, activated carbon adsorption, and desulfurization (nitrogen).
- the gas from the rotary paint stripping kiln and the carbon particles are passed into the high temperature furnace for secondary combustion.
- the combustion is in the anoxic reduction zone, the temperature is controlled at about 850 °C, the flue gas continues to be sent to the secondary combustion chamber for complete oxidative decomposition, and the temperature in the secondary combustion chamber is relatively high, usually above 1000 °C.
- the dioxin-like substances have been basically eliminated. Studies have shown that the dioxin removal rate can reach 99.999%.
- the quenching technology is used to rapidly cool the flue gas temperature to 90-130 °C through the heat exchanger, and quickly pass over the temperature zone which is easy to generate dioxin, thereby suppressing it again.
- the cooled flue gas is dedusted by bag, activated carbon adsorption and purification of flue gas after combustion, can absorb newly formed dioxins, reduce the content of dioxins in the flue gas, and finally reach the environmental protection requirements through the treatment of desulfurization and denitration tower.
- Controlling the chemical composition of aluminum alloy is the key to ensuring the reutilization of waste aluminum cans. It is necessary to strictly control the content of impurities Si, Fe, Cu, Mn, Zn, Cr, and Mg to suppress the brittleness caused by the element Na.
- the direct reading spectrometer is used to quickly detect the composition of the aluminum alloy melt, and the melt composition is adjusted according to the monitoring data, and finally meets the requirements for the aluminum alloy for the can.
- Degassing is mainly one of the key processes for determining the quality of recycled aluminum alloys by removing hydrogen, sodium and calcium from molten aluminum.
- High temperature nitrogen or argon is used as the deaerator.
- the deaerator forms fine bubbles in the molten aluminum solution, and the bubbles contact the aluminum liquid, adsorbing the surrounding hydrogen and oxides such as calcium and sodium, and then flowing over the aluminum liquid.
- Metamorphism and refinement of grain treatment In order to improve the morphology and size of the eutectic silicon, the formation of coarse needles and plate-like eutectic silicon is prevented, and the microstructure of the alloy is refined, and Al-Ti-B or Al-Ti is added. -C grain refiner to prevent cracking of ingots.
- Static insulation The refined aluminum liquid is allowed to stand in the furnace for a certain period of time. First, it is convenient for the refining carrier to float and remove the gas and fine non-metallic inclusions in the aluminum liquid from the upper surface of the aluminum liquid, and the second is to facilitate the sinking of large non-metallic inclusions to the bottom of the furnace.
- the invention has the advantages that the stripping treatment of the inner and outer surfaces of the waste aluminum can and the subsequent flue gas treatment are realized, and the environmental pollution of the recycling process is eliminated; the aluminum alloy for the cans is produced by using the waste aluminum cans as the raw material, and the relegation is achieved. Recycling; easy to industrialize, with significant economic, environmental and social benefits.
- FIG. 1 is a flow chart showing the overall process of the method of the present invention. detailed description
- the scrap aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
- the cans were hot stripped for 120 min at an oxygen partial pressure of 8% and a temperature of 450 °C.
- the flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a temperature of 1000 ° C or higher.
- the temperature of the flue gas is rapidly cooled to below 130 ° C by a heat exchanger to suppress the re-synthesis of dioxins.
- the cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitration tower treatment, and discharges after meeting environmental protection requirements.
- the hot-drawn paint cans are shaken to remove the adhered carbon particles by vibrating the sieve to prevent secondary pollution caused by the combustion of the carbon particles during the smelting process.
- the stripping of the aluminum sheet After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate.
- Outer chamber aluminum liquid temperature control At about 700 ° C, the temperature of the aluminum liquid in the inner chamber is controlled at about 850 ° C.
- the molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
- the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Zn and Ti in the aluminum liquid and the impurity content are analyzed by a direct reading spectrometer.
- the Si, Fe, Cu, Mn, Mg, Zn and Zn alloy elements reach the range required for the aluminum alloy for cans, and the content of the single impurity element is less than 0.05%, and the total impurity content is less than 0.15%.
- 500 ° C nitrogen as a deaerator it is evenly introduced into the aluminum alloy melt to form fine bubbles, which absorb hydrogen and calcium, sodium and other oxides in the aluminum liquid, and then float above the aluminum liquid.
- a grain refiner is added to prevent cracking of the ingot.
- the large non-metallic inclusions sink to the bottom of the furnace; then the aluminum alloy melt is filtered by a ceramic filter to remove inclusions; the filtered aluminum alloy flows into the semi-continuous casting machine Continuous continuous casting, lubricating oil and casting gas penetrate into the surface of the crystallizer through the graphite ring, forming a layer of oil and gas film between the aluminum alloy melt and the crystallizer, so that the crystal grains of the ingot are fine and uniform, and the surface is smooth.
- Table 2 shows the composition of the aluminum alloy prepared in this example, which meets the requirements of the 3104 aluminum alloy composition specified in "GB/T3190-2008 Chemical composition of deformed aluminum and aluminum alloy".
- the waste aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
- the cans were hot stripped for 80 min at a partial pressure of oxygen of 0 and a temperature of 500 °C.
- the flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a high temperature of 1000 ° C or higher.
- the temperature of the flue gas is rapidly cooled to below 130 ° C by a heat exchanger to suppress the re-generation of dioxins.
- the cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitrification tower, and discharged after meeting environmental protection requirements.
- the cans of the cans after hot stripping are shaken to remove the adhered carbon particles by the vibrating screen to prevent secondary pollution caused by the combustion of the carbon particles during the smelting process.
- the stripping of the aluminum sheet After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate.
- the temperature of the aluminum liquid in the outer chamber is controlled at about 750 °C
- the temperature of the aluminum liquid in the inner chamber is controlled at about 900 °C.
- the molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
- the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Zn and impurities in the aluminum liquid is analyzed by a direct reading spectrometer, and Si, Fe is required.
- the Cu, Mn, Mg, and Zn alloy elements are within the range required for the aluminum alloy for cans, and the content of the single impurity element is less than 0.05%, and the total impurity content is less than 0.15%.
- 600 °C nitrogen as a deaerator the aluminum alloy melt is uniformly introduced to form fine bubbles, which adsorb hydrogen and calcium, sodium and other oxides in the aluminum liquid, and then float above the aluminum liquid.
- 0.1% ⁇ 5 ⁇ 1 was added to the molten aluminum alloy for modification, which improved the morphology and size of the eutectic silicon, prevented the formation of coarse needles and plate-like eutectic silicon, and refined the microstructure of the alloy.
- a grain refiner is added to prevent cracking of the ingot.
- the large non-metallic inclusions sink to the bottom of the furnace; then the aluminum alloy melt is filtered by a ceramic filter to remove inclusions; the filtered aluminum alloy flows into the semi-continuous casting machine Continuous continuous casting, lubricating oil and casting gas penetrate into the surface of the crystallizer through the graphite ring, forming a layer of oil and gas film between the aluminum alloy melt and the crystallizer, so that the crystal grains of the ingot are fine and uniform, and the surface is smooth.
- Table 3 shows the composition of the aluminum alloy prepared in this example, which meets the composition requirements of the 3004 aluminum alloy specified in "Chemical Composition of Modified Aluminum and Aluminum Alloys of GB/T3190-2008".
- 3004 can body 0.30 0.70 0.25 1.00-1.50 0.80-1.30 0.25 1 ⁇ quantity
- Example 3
- the scrap aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
- the cans were hot stripped for 60 min at an oxygen partial pressure of 4% and a temperature of 550 °C.
- the flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a high temperature of 1000 ° C or higher.
- the temperature of the flue gas is rapidly cooled to below 130 °C by a heat exchanger to suppress the re-generation of dioxins.
- the cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitrification tower, and discharged after meeting environmental protection requirements.
- the hot-painted cans of the cans are vibrated by vibrating screen to remove the adhered carbon particles to prevent secondary contamination of the carbon particles during the smelting process.
- the stripping of the aluminum sheet After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate.
- the temperature of the aluminum liquid in the outer chamber is controlled at about 800 °C
- the temperature of the aluminum liquid in the inner chamber is controlled at about 900 °C.
- the molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
- the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Cr, Zn and Ti and the impurity content in the aluminum liquid are analyzed by a direct reading spectrometer. It is required that the Si, Fe, Cu, Mn, Mg, Cr, Zn and Ti alloy elements reach the required range of the aluminum alloy for cans, the content of the single impurity element is less than 0.05%, and the total impurity content is less than 0.15%.
- Argon gas at 650 ° C is used as a deaerator, and fine aluminum bubbles are uniformly introduced into the aluminum alloy melt to adsorb hydrogen and calcium, sodium and the like in the aluminum liquid, and then float above the aluminum liquid.
- a grain refiner is added to prevent cracking of the ingot.
- the composition and the impurity content satisfying the requirement of the 5182 aluminum alloy are allowed to stand in the holding furnace for a certain period of time, and the refining carrier is floated to bring the gas and the fine non-metallic inclusions in the aluminum liquid out of the upper surface of the aluminum liquid.
- the scrap aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
- the cans were hot stripped for 20 min at an oxygen partial pressure of 4% and a temperature of 640 °C.
- the flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a high temperature of 1000 ° C or higher.
- the temperature of the flue gas is rapidly cooled to below 130 °C by a heat exchanger to suppress the re-generation of dioxins.
- the cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitrification tower, and discharged after meeting environmental protection requirements.
- the hot-painted cans of the cans are vibrated by vibrating screen to remove the adhered carbon particles to prevent secondary contamination of the carbon particles during the smelting process.
- the stripping of the aluminum sheet After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate.
- the temperature of the aluminum liquid in the outer chamber is controlled at about 850 °C
- the temperature of the aluminum liquid in the inner chamber is controlled at about 950 °C.
- the molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
- the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Cr, Zn and Ti and the impurity content in the aluminum liquid are analyzed by a direct reading spectrometer. , requires Si, Fe, Cu, Mn, Mg, Cr, Zn, and Ti alloy elements to reach the required range of aluminum alloy for cans, and a single impurity element The amount is less than 0.05%, and the total impurity content is less than 0.15%.
- Argon gas at 700 °C is used as a deaerator, and fine aluminum bubbles are uniformly introduced into the aluminum alloy melt to adsorb hydrogen and calcium, sodium and the like in the aluminum liquid, and then float above the aluminum liquid.
- AlTi5Cl 0.75% AlTi5Cl was added to the molten aluminum alloy for modification, which improved the morphology and size of the eutectic silicon, prevented the formation of coarse needles and plate-like eutectic silicon, and refined the microstructure of the alloy.
- a grain refiner is added to prevent cracking of the ingot.
- the scrap aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
- the cans were hot stripped for 100 min at an oxygen partial pressure of 6% and a temperature of 600 °C.
- the flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a high temperature of 1000 ° C or higher.
- the temperature of the flue gas is rapidly cooled to below 130 ° C by a heat exchanger to suppress the re-generation of dioxins.
- the cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitrification tower, and discharged after meeting environmental protection requirements.
- the cans of the cans after hot stripping are shaken to remove the adhered carbon particles by the vibrating screen to prevent secondary pollution caused by the combustion of the carbon particles during the smelting process.
- After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate.
- the temperature of the aluminum liquid in the outer chamber is controlled at about 800 °C
- the temperature of the aluminum liquid in the inner chamber is controlled at about 880 °C.
- the molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
- the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Zn, Ti and impurities in the aluminum liquid is analyzed by a direct reading spectrometer, and Si is required.
- the Fe, Cu, Mn, Mg, Zn and Ti alloy elements are within the range required for the aluminum alloy for cans, the content of the single impurity element is less than 0.05%, and the total impurity content is less than 0.15%.
- the aluminum alloy melt is uniformly introduced to form fine bubbles, which adsorb hydrogen in the aluminum liquid and oxygen such as calcium and sodium, and then float above the aluminum liquid.
- a grain refiner is added to prevent cracking of the ingot.
- the composition and the impurity content satisfying the requirements of the 3104 aluminum alloy are allowed to stand in the holding furnace for a certain period of time, so that the refining carrier floats to bring the gas and the fine non-metallic inclusions in the aluminum liquid out of the upper surface of the aluminum liquid.
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Abstract
A method of recycling waste easy-open aluminum cans uses waste easy-open aluminum cans as raw materials and performs crushing, iron removal through magnetic separation, preprocessing paint removal, melting, component adjustment, modification processing, filtering, and casting to eventually obtain aluminum alloy for easy-open cans.
Description
一种废铝易拉罐绿色循环保级再利用的方法 技术领域 Method for recycling green recycling of waste aluminum cans
本发明提供了一种废铝易拉罐再利用的方法,属于循环经济技术 及环保领域, 特别涉及废铝易拉罐绿色循环保级再利用的方法。 背景技术 The invention provides a method for recycling aluminum aluminum cans, belonging to the field of circular economy technology and environmental protection, and particularly relates to a method for recycling green recycling of waste aluminum cans. Background technique
据估算, 我国废铝易拉罐的回收率为 96%以上, 每年至少回收 40万吨废罐, 加上少量的进口, 总量在 50万吨左右。 现有的废铝易 拉罐回收再利用档次较低, 再利用过程环境污染严重, 其主要原因是 回收再利用技术水平低, 技术难度大。 需要解决以下五个技术难点: (1)废铝易拉罐的罐体与盖、 拉环的铝合金成分不同, 很难进行体、 盖、 环的分离; (2)废铝易拉罐内外表面漆容易产生污染, 并影响再 生铝合金的质量和回收率; (3)废铝易拉罐质地薄, 表面积大, 熔炼 氧化烧损严重, 金属回收率低; (4)废铝易拉罐来源广泛, 预处理难 度大, 熔炼时易引入杂质到铝合金熔液, 造成合金成分复杂, 调整难 度加大; (5)废铝易拉罐铝合金铸锭组织控制难度大。 It is estimated that the recovery rate of waste aluminum cans in China is over 96%, and at least 400,000 tons of waste cans are recovered every year, plus a small amount of imports, totaling around 500,000 tons. The existing waste aluminum cans are low in recycling and reuse, and the environmental pollution in the reuse process is serious. The main reason is that the recycling technology is low and the technical difficulty is high. The following five technical difficulties need to be solved: (1) The can body of the waste aluminum can is different from the aluminum alloy of the cover and the pull ring, and it is difficult to separate the body, the cover and the ring; (2) The inner and outer surface paint of the waste aluminum can is easily produced. Pollution, and affect the quality and recovery rate of recycled aluminum alloy; (3) Waste aluminum cans have thin texture, large surface area, severe smelting and oxidation loss, and low metal recovery rate; (4) Waste aluminum cans have wide sources and difficult pretreatment. It is easy to introduce impurities into the aluminum alloy melt during smelting, which makes the alloy composition complicated and the adjustment difficulty is increased. (5) The aluminum alloy ingot can be difficult to control the structure of the aluminum alloy ingot.
废铝易拉罐的罐体与盖、 拉环的铝合金成分不同 (见表 1), 从理 论上讲, 将罐体、 盖和拉环进行分离回收再利用有利于保级再利用。 因回收的废铝易拉罐变形严重, 为方便运输通常进行打包压实, 从经 济和实际情况出发, 不可能不进行罐体、 盖和拉环分离, 直接进行回 表 1 铝易拉罐各部分成分 (重量百分比) The can body of the waste aluminum can is different from the aluminum alloy of the cover and the pull ring (see Table 1). Theoretically, the separation, recycling and reuse of the can body, the cover and the pull ring are beneficial for re-use and reuse. Due to the serious deformation of the recovered aluminum cans, it is usually packed and compacted for convenient transportation. From the economic and practical conditions, it is impossible to separate the tank, the cover and the pull ring, and directly return the parts of the aluminum cans. Percentage)
废铝易拉罐内外表面漆在回收利用过程中容易产生污染,并影响 再生铝合金的质量。 因此, 破碎后的铝易拉罐必须进行脱漆处理。 脱
漆方法和脱漆率直接影响到制成的铝或铝合金材料的质量以及利用 的成本和环境污染等。在废铝易拉罐回收利用中, 脱漆是废旧铝易拉 罐回收利用的核心技术之一, 也是难点之一。 The inner and outer surface paints of waste aluminum cans are prone to pollution during recycling and affect the quality of recycled aluminum alloys. Therefore, the broken aluminum cans must be stripped. Take off The lacquer method and paint stripping rate directly affect the quality of the finished aluminum or aluminum alloy material as well as the cost of use and environmental pollution. In the recycling of waste aluminum cans, stripping is one of the core technologies for the recycling of used aluminum cans, and it is also one of the difficulties.
废铝易拉罐质地薄、 表面积大, 为降低熔炼氧化烧损、 提高金属 回收率低, 一般采用双室反射炉熔炼, 使铝片不与火焰接触而是直接 加入熔融的铝液中, 避免了废铝的烧损, 使金属回收率提高。 The waste aluminum can has a thin texture and a large surface area. In order to reduce the smelting oxidation loss and improve the metal recovery rate, the double-chamber reverberatory furnace is generally used to melt, so that the aluminum piece is not in contact with the flame but directly added to the molten aluminum liquid, thereby avoiding waste. The burning of aluminum improves the metal recovery rate.
废铝易拉罐来源广泛, 预处理难度大, 熔炼时易引入杂质到铝合 金熔液, 造成合金成分复杂, 成分和组织调整控制难度加大。 The waste aluminum cans have a wide range of sources, and are difficult to pretreat. It is easy to introduce impurities into the aluminum alloy melt during smelting, resulting in complex alloy composition and difficulty in adjusting composition and structure.
废铝易拉罐回收再利用技术是再生资源综合利用的重要领域之 一。 自从废铝易拉罐广泛应用来, 人们就自发对废旧易拉罐进行回收 再利用, 形成了相关的技术和知识产权。 Waste aluminum can recycling and recycling technology is one of the important areas for comprehensive utilization of renewable resources. Since the widespread use of scrap aluminum cans, people have spontaneously recycled and reused cans, forming relevant technologies and intellectual property rights.
早在 1989年 9月 29日,金大承、关洪国申请了中国发明专利"废 易拉罐回收方法及其分选装置"(申请号 89107289.6), 公开了一种将 易拉罐的盖和底用刀具切割分离,将罐的侧身碾成板材分别收集方法 和装置。由于易拉罐质薄和分散的特点,本专利技术未得到广泛应用。 2007年 3月 5 日, 王均铖、 郝俊文等人申请了实用新型专利 "废易 拉罐金属分离回收机"(申请号 200720067610.9), 设计了一种易拉罐 金属分离回收机, 能够完全分离易拉罐两种金属。 因回收的废铝易拉 罐变形严重, 本专利技术难以得到推广应用。 2009年 10月 14日, 陈定方、张争艳等人申请了中国发明专利 "一种自动分离并压扁铁质 铝质易拉罐装置"(申请号 200910062072.8), 公开了一种铁质和铝质 易拉罐分离、 压扁技术装置, 实际上是电磁分选和压扁技术。 As early as September 29, 1989, Jin Dacheng and Guan Hongguo applied for the Chinese invention patent "Recycling cans and their sorting device" (Application No. 89107289.6), which disclosed a method for cutting and separating the lid and the bottom of the can. The side body of the can is ground into a separate collection method and device. Due to the thin and dispersed nature of the cans, the patented technology has not been widely used. On March 5, 2007, Wang Junyi, Hao Junwen and others applied for the utility model patent “Waste cans metal separation and recovery machine” (application No. 200720067610.9), designed a can metal separation and recovery machine, which can completely separate the two metals of cans. Due to the serious deformation of the recovered waste aluminum cans, this patented technology is difficult to be popularized and applied. On October 14, 2009, Chen Dingfang, Zhang Zhengyan and others applied for the Chinese invention patent "an automatic separation and crushing of iron aluminum cans" (Application No. 200910062072.8), which discloses a separation of iron and aluminum cans, The flattening technology device is actually an electromagnetic sorting and crushing technique.
2008年 10月 30日, 李全祥、 程博闻等人申请了中国发明专利 "一种废旧易拉罐表面处理剂"(申请号 200810152559.0), 公开了一 种能同时去除易拉罐表面烤漆涂层和内壁防腐薄膜表面处理剂,它是 由二氯甲烷、 三氟乙酸和水组成。 2009年 7月 8 日, 康卫民、 陈帮 烈等人申请了中国发明专利 "一种废旧易拉罐表面除漆脱膜处理剂" (申请号 200910069633.7), 公开了一种能同时去除易拉罐表面除漆脱 膜处理剂, 它是由甲酸、 二氯甲烷和水组成。 该两专利采用的事化学 脱漆工艺, 环境负担重。 On October 30, 2008, Li Quanxiang, Cheng Bowen and others applied for the Chinese invention patent "A Waste Can Surface Treatment Agent" (Application No. 200810152559.0), which discloses a surface treatment for the simultaneous removal of the surface of the can coating and the anticorrosive film of the inner wall. The agent is composed of dichloromethane, trifluoroacetic acid and water. On July 8, 2009, Kang Weimin, Chen Banglie and others applied for the Chinese invention patent "a kind of waste cans surface paint removal agent" (Application No. 200910069633.7), which disclosed a method for removing the surface of the cans at the same time. Agent, which is composed of formic acid, dichloromethane and water. The two patents use a chemical stripping process and have a heavy environmental burden.
2008年 1 月 25 日加拿大 Befesa Aluminio Bilbao公司申请了
Process for Recycling Spent Pot Linings (SPL) From Primary Aluminium Production欧洲专利(申请号 EP08380016.9), 并通过 PCT申请了国际 专禾 l」(PCT/EP2009/000189)。 公开了一种酸解法回收废旧铝质罐产品。 经过破碎、 酸洗、 磁选得到工业广泛应用的铝原料。 2001年 11月 14 曰,俄罗其? Abdurakhmanov A D申请了 Method and Plant for Reworking Aluminium Tins (申请号 2001131605/02), 公开了一种处理废铝罐的方 法, 包括破碎、 磁选、 有机物脱除等工序, 最后得到废铝碎片。 2003 年 1月 8曰荷兰 Azrat Abdurakhmanov te Den Haag申请了 Methode en installatie voor de verwerking van aluminium blikjes,公开了废,吕罐的破 碎、分选和洗涤技术。 1995年 11月 28日, Fry申请了美国专利 Collector for empty used recyclable beverage cans(USP5,469,783) , 公开了——禾中饮 料罐的回收装置,可区分铁罐、有色金属罐、塑料罐,进行自动分类, 具备光电传感器可提供回收装置内的数量信息等。 On January 25, 2008, Befesa Aluminio Bilbao of Canada applied for Process for Recycling Spent Pot Linings (SPL) From Primary Aluminium Production European Patent (Application No. EP08380016.9), and applied for International Specialties through PCT (PCT/EP2009/000189). An acid hydrolysis method for recycling waste aluminum can products is disclosed. After crushing, pickling, and magnetic separation, aluminum raw materials widely used in the industry are obtained. On November 14, 2001, Russian, Abdurakhmanov AD applied for Method and Plant for Reworking Aluminium Tins (Application No. 2001131605/02), which discloses a method for treating waste aluminum cans, including crushing, magnetic separation, and organic removal. After the process, the scrap aluminum scrap is finally obtained. On January 8, 2003, Azrat Abdurakhmanov te Den Haag of the Netherlands applied for Methode en installatie voor de verwerking van aluminium blikjes, which disclosed the technology of crushing, sorting and washing of waste, cans. On November 28, 1995, Fry applied for the US patent Collector for empty used recyclable beverage cans (USP 5,469,783), which disclosed that the recycling device for the beverage cans in Hezhong can distinguish between iron cans, non-ferrous metal cans, and plastic cans. Automatic classification, with photoelectric sensors to provide quantitative information in the recycling device.
由此可见,现有回收处理废铝易拉罐的专利技术涉及的均为一个 工序的技术, 有些技术还有严重二次污染, 得到的铝合金产品降级实 用。 因此, 急需开发废铝易拉罐绿色循环再利用于易拉罐铝合金。 发明内容 It can be seen that the existing patented technology for recycling and processing waste aluminum cans is a process technology, and some technologies have serious secondary pollution, and the obtained aluminum alloy products are degraded. Therefore, there is an urgent need to develop green recycling of waste aluminum cans for use in cans of aluminum alloys. Summary of the invention
本发明针对废铝易拉罐成分比较复杂、 内外表面带有机物涂层、 来源复杂等特点, 采用破碎、 磁选除铁、 预处理脱漆、 熔炼、 熔液成 分快速检测、 成分调整、 变质处理、 过滤、 浇铸等, 最终得到易拉罐 用铝合金。 为实现达标排放, 采用烟气二次燃烧将二噁英分解、烟气 急冷, 经布袋除尘、 活性炭吸附、 脱硫 (硝)等技术。 The invention aims at the complex composition of the waste aluminum can, the organic coating on the inner and outer surfaces, and the complicated source. The crushing, magnetic separation and iron removal, pretreatment stripping, smelting, rapid detection of melt components, composition adjustment, modification treatment, filtration , casting, etc., and finally get aluminum alloy for cans. In order to achieve the standard discharge, the dioxin is decomposed by the secondary combustion of flue gas, the flue gas is quenched, and the technology is such as bag dust removal, activated carbon adsorption, and desulfurization (nitrogen).
(1)破碎: 回收到的废易拉罐的形态已经被破坏, 打成包块, 因 此, 在脱漆之前, 需进行打散和破碎到一定粒度, 有利于后续磁选除 铁和脱漆的进行。 (1) Crushing: The form of the recycled cans has been destroyed and broken into blocks. Therefore, before stripping, it is necessary to break up and crush to a certain particle size, which is conducive to the subsequent magnetic separation and stripping. .
(2)脱漆: 松散的废易拉罐 (含经过破碎的废易拉罐) 直接进入 脱漆窑进行脱漆。脱漆采用旋转式脱漆窑处理, 开始时需要加一定的 热能, 达到一定温度之后, 热能主要依靠易拉罐表面漆炭化过程的放 热。在旋转式的脱漆窑中, 易拉罐的漆层被炭化, 依靠旋转过程的自 身震动,漆层脱落,最后还要经过专门的震动设备,使炭粒全部脱落。
为防止铝片碎料的氧化烧损和过热熔化,需严格控制窑内温度和氧含 烟气二次燃烧:旋转式脱漆窑出来的气体和炭粒通入高温炉进行 二次燃烧, 一段燃烧处于缺氧还原区, 温度控制在 850°C左右, 烟气 继续送入二次燃烧室内彻底氧化分解, 二次燃烧室内温度较高, 通常 在 1000°C以上。 烟气经二次燃烧室高温燃烧后, 二噁英类物质已经 基本被消除, 研究表明, 二噁英去除率可达 99.999%。 烟气从二次燃 烧室出口进入控制设备时, 利用急冷技术, 通过热交换器将烟气温度 迅速冷却至 90-130°C,快速越过易产生二噁英类的温度区,从而抑制 其再次合成。冷却后的烟气经布袋除尘、活性炭吸附净化燃烧后的烟 气, 可吸收新生成的二噁英, 降低排放烟气中二噁英的含量, 最后通 过脱硫脱硝塔处理后达到环保要求排放。 (2) Stripping: Loose waste cans (including broken waste cans) directly enter the paint stripping kiln for stripping. The stripping paint is treated by a rotary paint stripping kiln. At the beginning, a certain amount of heat energy needs to be added. After reaching a certain temperature, the heat energy mainly depends on the exothermic heat of the surface paint of the can. In the rotary paint stripping kiln, the paint layer of the can is carbonized, relies on the vibration of the rotating process, the paint layer falls off, and finally the special vibration equipment is used to make the carbon particles fall off. In order to prevent the oxidation loss and overheating of the aluminum flakes, it is necessary to strictly control the temperature in the kiln and the secondary combustion of the flue gas containing oxygen: the gas from the rotary paint stripping kiln and the carbon particles are passed into the high temperature furnace for secondary combustion. The combustion is in the anoxic reduction zone, the temperature is controlled at about 850 °C, the flue gas continues to be sent to the secondary combustion chamber for complete oxidative decomposition, and the temperature in the secondary combustion chamber is relatively high, usually above 1000 °C. After the flue gas is burned at high temperature in the secondary combustion chamber, the dioxin-like substances have been basically eliminated. Studies have shown that the dioxin removal rate can reach 99.999%. When the flue gas enters the control equipment from the outlet of the secondary combustion chamber, the quenching technology is used to rapidly cool the flue gas temperature to 90-130 °C through the heat exchanger, and quickly pass over the temperature zone which is easy to generate dioxin, thereby suppressing it again. synthesis. The cooled flue gas is dedusted by bag, activated carbon adsorption and purification of flue gas after combustion, can absorb newly formed dioxins, reduce the content of dioxins in the flue gas, and finally reach the environmental protection requirements through the treatment of desulfurization and denitration tower.
(3)熔炼: 经过预处理脱漆的废易拉罐进入熔炼炉进行熔炼。 采 用先进的蓄热式双室反射炉。双室反射炉分为内外室, 熔融的铝液在 内室被加热, 流入外室, 与固体的废铝接触, 并使其熔化, 温度随之 降低, 然后再进入内室加热, 循环依靠特制的陶瓷泵进行。 由于废铝 不与火焰直接接触, 直接加入熔融的铝液中, 避免了废铝的烧损, 使 金属回收率提高。 (3) Smelting: The waste cans which have been pretreated and stripped are fed into a melting furnace for smelting. An advanced regenerative double chamber reverberatory furnace is used. The double-chamber reverberatory furnace is divided into inner and outer chambers, and the molten aluminum liquid is heated in the inner chamber, flows into the outer chamber, contacts the solid waste aluminum, and melts it, and the temperature is lowered, and then enters the inner chamber for heating, and the circulation is specially made. The ceramic pump is carried out. Since the waste aluminum is not in direct contact with the flame, it is directly added to the molten aluminum liquid, thereby avoiding the burning of the waste aluminum and improving the metal recovery rate.
(4)合金成分调整: 控制铝合金化学成分是保证废铝易拉罐保级 利用的关键。 要严格控制控制杂质 Si、 Fe、 Cu、 Mn、 Zn、 Cr禾 Π Mg 含量, 抑制元素 Na引起的脆性。 采用直读光谱仪迅速检测铝合金熔 液成分, 并根据监测数据调整熔液成分, 最终满足易拉罐用铝合金要 求。 (4) Adjustment of alloy composition: Controlling the chemical composition of aluminum alloy is the key to ensuring the reutilization of waste aluminum cans. It is necessary to strictly control the content of impurities Si, Fe, Cu, Mn, Zn, Cr, and Mg to suppress the brittleness caused by the element Na. The direct reading spectrometer is used to quickly detect the composition of the aluminum alloy melt, and the melt composition is adjusted according to the monitoring data, and finally meets the requirements for the aluminum alloy for the can.
(5)除气除杂: 除气主要是除去熔融铝液中的氢气和钠、 钙等, 决定再生铝合金产品质量的关键工序之一。采用高温氮气或者氩气作 为除气剂。除气剂在熔融的铝液中形成细小的气泡, 气泡与铝液的接 触,吸附了周围的氢气和钙、钠等的氧化物,然后飘逸到铝液的上方。 (5) Degassing and removing impurities: Degassing is mainly one of the key processes for determining the quality of recycled aluminum alloys by removing hydrogen, sodium and calcium from molten aluminum. High temperature nitrogen or argon is used as the deaerator. The deaerator forms fine bubbles in the molten aluminum solution, and the bubbles contact the aluminum liquid, adsorbing the surrounding hydrogen and oxides such as calcium and sodium, and then flowing over the aluminum liquid.
(6)变质与细化晶粒处理: 为改善共晶硅形貌和尺寸, 阻止粗大 的针、板状共晶硅生成, 使合金的组织细化, 添加 Al-Ti-B或 Al-Ti-C 晶粒细化剂, 防止铸锭裂纹。 (6) Metamorphism and refinement of grain treatment: In order to improve the morphology and size of the eutectic silicon, the formation of coarse needles and plate-like eutectic silicon is prevented, and the microstructure of the alloy is refined, and Al-Ti-B or Al-Ti is added. -C grain refiner to prevent cracking of ingots.
(7)静置保温: 精炼后的铝液在保持炉中静置一定时间, 其目的
一是便于精炼载体上浮将铝液中的气体和细小的非金属夹杂物带出 铝液上表面而去除, 二是便于大块的非金属夹杂物下沉至炉底。 (7) Static insulation: The refined aluminum liquid is allowed to stand in the furnace for a certain period of time. First, it is convenient for the refining carrier to float and remove the gas and fine non-metallic inclusions in the aluminum liquid from the upper surface of the aluminum liquid, and the second is to facilitate the sinking of large non-metallic inclusions to the bottom of the furnace.
(8)过滤: 采用泡沬陶瓷过滤器对铝合金熔液进行过滤, 去除夹 杂物。 (8) Filtration: The aluminum alloy melt is filtered using a foam ceramic filter to remove inclusions.
(9)浇铸: 采用先进的半连续性铸锭机连续平稳浇铸, 润滑油与 铸造气体通过石墨环渗透到结晶器表面,在铝合金熔液和结晶器之间 形成一层油气膜, 使得铸锭的晶粒细小均匀, 表面光滑。 (9) Casting: Continuously and smoothly casting with advanced semi-continuous ingot casting machine. Lubricating oil and casting gas permeate through the graphite ring to the surface of the crystallizer, forming a layer of oil and gas film between the aluminum alloy melt and the crystallizer, making casting The crystal grains of the ingot are fine and uniform, and the surface is smooth.
本发明的优点在于:实现了废铝易拉罐内外表面脱漆处理和后续 的烟气处理, 消除了回收再利用过程的环境污染; 实现了以废铝易拉 罐为原料生产易拉罐用铝合金, 达到了保级循环再利用; 易于工业化 生产, 具有显著的经济、 环境和社会效益。 附图说明 The invention has the advantages that the stripping treatment of the inner and outer surfaces of the waste aluminum can and the subsequent flue gas treatment are realized, and the environmental pollution of the recycling process is eliminated; the aluminum alloy for the cans is produced by using the waste aluminum cans as the raw material, and the relegation is achieved. Recycling; easy to industrialize, with significant economic, environmental and social benefits. DRAWINGS
图 1为本发明方法的整体工艺流程图。 具体实施方式 Figure 1 is a flow chart showing the overall process of the method of the present invention. detailed description
下面结合实施例对本发明作进一歩的描述,但本发明不仅仅局限 于以下实施例。 The present invention will be further described in conjunction with the embodiments, but the present invention is not limited to the following embodiments.
实施例 1 Example 1
将废铝易拉罐包进行机械打散、 撕碎得到零散的碎片, 然后经过 磁选机将混杂在易拉罐碎片中的铁磁性金属分离出来,避免混入后续 工序。 The scrap aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
易拉罐碎片在氧分压为 8%、 温度为 450°C下热脱漆 120min。 热 脱漆过程中产生的烟气经烟气管道送入燃烧炉, 1000 °C以上高温燃烧 后,二噁英类物质被消除。通过热交换器将烟气温度迅速冷却至 130°C 以下, 抑制二噁英类物质再次合成。冷却后的烟气经布袋除尘、 活性 炭吸附、 脱硫脱硝塔处理, 达到环保要求后排放。热脱漆后的易拉罐 碎片经振动筛震动脱除粘附的炭粒,防止在熔炼过程中炭粒燃烧产生 二次污染。 The cans were hot stripped for 120 min at an oxygen partial pressure of 8% and a temperature of 450 °C. The flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a temperature of 1000 ° C or higher. The temperature of the flue gas is rapidly cooled to below 130 ° C by a heat exchanger to suppress the re-synthesis of dioxins. The cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitration tower treatment, and discharges after meeting environmental protection requirements. The hot-drawn paint cans are shaken to remove the adhered carbon particles by vibrating the sieve to prevent secondary pollution caused by the combustion of the carbon particles during the smelting process.
脱漆后的铝片打包后压入蓄热式双室反射炉外室熔融的铝液中 进行熔化, 避免火焰直接接触到铝片降低回收率。外室铝液温度控制
在 700°C左右, 内室铝液的温度控制在 850°C左右。 内室和外室熔融 的铝液依靠陶瓷泵循环。 After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate. Outer chamber aluminum liquid temperature control At about 700 ° C, the temperature of the aluminum liquid in the inner chamber is controlled at about 850 ° C. The molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
反射炉中铝片完全熔化并且铝液循环搅拌均匀后, 在线提取铝合 金成分分析样, 采用直读光谱仪分析铝液中 Si、 Fe、 Cu、 Mn、 Mg、 Zn和 Ti含量和杂质含量, 要求 Si、 Fe、 Cu、 Mn、 Mg、 Zn禾 Π Ti合 金元素达到易拉罐用铝合金要求的范围内, 单个杂质元素含量低于 0.05% , 杂质总含量低于 0.15%。 采用 500°C的氮气作为除气剂, 均 匀通入铝合金熔液中, 形成细小的气泡, 吸附铝液中的氢气和钙、钠 等的氧化物, 然后飘逸到铝液的上方。 After the aluminum sheet in the reverberatory furnace is completely melted and the aluminum liquid is evenly stirred, the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Zn and Ti in the aluminum liquid and the impurity content are analyzed by a direct reading spectrometer. The Si, Fe, Cu, Mn, Mg, Zn and Zn alloy elements reach the range required for the aluminum alloy for cans, and the content of the single impurity element is less than 0.05%, and the total impurity content is less than 0.15%. Using 500 ° C nitrogen as a deaerator, it is evenly introduced into the aluminum alloy melt to form fine bubbles, which absorb hydrogen and calcium, sodium and other oxides in the aluminum liquid, and then float above the aluminum liquid.
在铝合金熔液中加入 0.5%的 Α1ΤΪ5Β1进行变质处理, 改善共晶 硅形貌和尺寸,阻止粗大的针、板状共晶硅生成,使合金的组织细化。 添加晶粒细化剂, 防止铸锭裂纹。经变质处理后且成分和杂质含量满 足 3104铝合金要求的熔液在保持炉中静置一段时间, 使精炼载体上 浮, 将铝液中的气体和细小的非金属夹杂物带出铝液上表面而去除, 大块的非金属夹杂物下沉至炉底;然后采用泡沬陶瓷过滤器对铝合金 熔液进行过滤, 进一歩去除夹杂物; 过滤后的铝合金流进半连续性铸 锭机连续平稳浇铸,润滑油与铸造气体通过石墨环渗透到结晶器表面, 在铝合金熔液和结晶器之间形成一层油气膜,使得铸锭的晶粒细小均 匀, 表面光滑。 表 2 为本实施例制备的铝合金的成分, 符合 "GB/T3190-2008变形铝及铝合金化学成分" 中规定的 3104铝合金 成分要求。 Add 0.5% Α1ΤΪ5Β1 to the aluminum alloy melt for modification, improve the morphology and size of the eutectic silicon, prevent the formation of coarse needles and plate-like eutectic silicon, and refine the microstructure of the alloy. A grain refiner is added to prevent cracking of the ingot. After the metamorphism treatment, the composition and the impurity content satisfying the requirements of the 3104 aluminum alloy are allowed to stand in the holding furnace for a period of time, the refining carrier is floated, and the gas and the fine non-metallic inclusions in the aluminum liquid are taken out of the upper surface of the aluminum liquid. And removing, the large non-metallic inclusions sink to the bottom of the furnace; then the aluminum alloy melt is filtered by a ceramic filter to remove inclusions; the filtered aluminum alloy flows into the semi-continuous casting machine Continuous continuous casting, lubricating oil and casting gas penetrate into the surface of the crystallizer through the graphite ring, forming a layer of oil and gas film between the aluminum alloy melt and the crystallizer, so that the crystal grains of the ingot are fine and uniform, and the surface is smooth. Table 2 shows the composition of the aluminum alloy prepared in this example, which meets the requirements of the 3104 aluminum alloy composition specified in "GB/T3190-2008 Chemical composition of deformed aluminum and aluminum alloy".
表 2 本实施例制备的铝合金与 3104铝合金的成分对比表 (重量百分比) Table 2 Comparison Table of Compositions of Aluminum Alloy and 3104 Aluminum Alloy Prepared in This Example (% by Weight)
实施例 2 Example 2
将废铝易拉罐包进行机械打散、 撕碎得到零散的碎片, 然后经过 磁选机将混杂在易拉罐碎片中的铁磁性金属分离出来,避免混入后续 工序。
易拉罐碎片在氧分压为 0、温度为 500 °C下热脱漆 80min。热脱漆 过程中产生的烟气经烟气管道送入燃烧炉, 1000°C以上高温燃烧后, 二噁英类物质被消除。 通过热交换器将烟气温度迅速冷却至 130°C以 下, 抑制二噁英类物质再次生成。冷却后的烟气经布袋除尘、 活性炭 吸附、 脱硫脱硝塔处理, 达到环保要求后排放。热脱漆后的易拉罐碎 片经振动筛震动脱除粘附的炭粒,防止在熔炼过程中炭粒燃烧产生二 次污染。 The waste aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes. The cans were hot stripped for 80 min at a partial pressure of oxygen of 0 and a temperature of 500 °C. The flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a high temperature of 1000 ° C or higher. The temperature of the flue gas is rapidly cooled to below 130 ° C by a heat exchanger to suppress the re-generation of dioxins. The cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitrification tower, and discharged after meeting environmental protection requirements. The cans of the cans after hot stripping are shaken to remove the adhered carbon particles by the vibrating screen to prevent secondary pollution caused by the combustion of the carbon particles during the smelting process.
脱漆后的铝片打包后压入蓄热式双室反射炉外室熔融的铝液中 进行熔化, 避免火焰直接接触到铝片降低回收率。外室铝液温度控制 在 750°C左右, 内室铝液的温度控制在 900 °C左右。 内室和外室熔融 的铝液依靠陶瓷泵循环。 After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate. The temperature of the aluminum liquid in the outer chamber is controlled at about 750 °C, and the temperature of the aluminum liquid in the inner chamber is controlled at about 900 °C. The molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
反射炉中铝片完全熔化并且铝液循环搅拌均匀后, 在线提取铝合 金成分分析样, 采用直读光谱仪分析铝液中 Si、 Fe、 Cu、 Mn、 Mg、 Zn和杂质含量, 要求 Si、 Fe、 Cu、 Mn、 Mg和 Zn合金元素达到易 拉罐用铝合金要求的范围内, 单个杂质元素含量低于 0.05%, 杂质总 含量低于 0.15%。 采用 600 °C的氮气作为除气剂, 均匀通入的铝合金 熔液中, 形成细小的气泡, 吸附铝液中的氢气和钙、 钠等的氧化物, 然后飘逸到铝液的上方。 After the aluminum sheet in the reverberatory furnace is completely melted and the aluminum liquid is evenly stirred, the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Zn and impurities in the aluminum liquid is analyzed by a direct reading spectrometer, and Si, Fe is required. The Cu, Mn, Mg, and Zn alloy elements are within the range required for the aluminum alloy for cans, and the content of the single impurity element is less than 0.05%, and the total impurity content is less than 0.15%. Using 600 °C nitrogen as a deaerator, the aluminum alloy melt is uniformly introduced to form fine bubbles, which adsorb hydrogen and calcium, sodium and other oxides in the aluminum liquid, and then float above the aluminum liquid.
在铝合金熔液中加入 0.1%的 ΑΓΠ5Β1进行变质处理, 改善共晶 硅形貌和尺寸,阻止粗大的针、板状共晶硅生成,使合金的组织细化。 添加晶粒细化剂, 防止铸锭裂纹。经变质处理后且成分和杂质含量满 足 3004铝合金要求的熔液在保持炉中静置一段时间, 使精炼载体上 浮, 将铝液中的气体和细小的非金属夹杂物带出铝液上表面而去除, 大块的非金属夹杂物下沉至炉底;然后采用泡沬陶瓷过滤器对铝合金 熔液进行过滤, 进一歩去除夹杂物; 过滤后的铝合金流进半连续性铸 锭机连续平稳浇铸,润滑油与铸造气体通过石墨环渗透到结晶器表面, 在铝合金熔液和结晶器之间形成一层油气膜,使得铸锭的晶粒细小均 匀, 表面光滑。 表 3 为本实施例制备的铝合金的成分, 符合 "GB/T3190-2008变形铝及铝合金化学成分" 中规定的 3004铝合金 成分要求。 0.1% ΑΓΠ5Β1 was added to the molten aluminum alloy for modification, which improved the morphology and size of the eutectic silicon, prevented the formation of coarse needles and plate-like eutectic silicon, and refined the microstructure of the alloy. A grain refiner is added to prevent cracking of the ingot. After the metamorphism treatment, the composition and the impurity content satisfying the requirements of the 3004 aluminum alloy are allowed to stand in the holding furnace for a period of time, the refining carrier is floated, and the gas and the fine non-metallic inclusions in the aluminum liquid are carried out of the upper surface of the aluminum liquid. And removing, the large non-metallic inclusions sink to the bottom of the furnace; then the aluminum alloy melt is filtered by a ceramic filter to remove inclusions; the filtered aluminum alloy flows into the semi-continuous casting machine Continuous continuous casting, lubricating oil and casting gas penetrate into the surface of the crystallizer through the graphite ring, forming a layer of oil and gas film between the aluminum alloy melt and the crystallizer, so that the crystal grains of the ingot are fine and uniform, and the surface is smooth. Table 3 shows the composition of the aluminum alloy prepared in this example, which meets the composition requirements of the 3004 aluminum alloy specified in "Chemical Composition of Modified Aluminum and Aluminum Alloys of GB/T3190-2008".
表 3 本实施例制备的铝合金与 3004铝合金的成分对比表 (重量百分比)
合金成分 Si Fe Cu Mn Mg Zn Ti Al 本实施例 0.22 0.55 0.21 1.24 1.08 0.18 0.008 佘量Table 3 Comparison Table of Components of Aluminum Alloy and 3004 Aluminum Alloy Prepared in the Present Example (% by Weight) Alloy composition Si Fe Cu Mn Mg Zn Ti Al This example 0.22 0.55 0.21 1.24 1.08 0.18 0.008
3004罐体 0.30 0.70 0.25 1.00-1.50 0.80-1.30 0.25 1 佘量 实施例 3 3004 can body 0.30 0.70 0.25 1.00-1.50 0.80-1.30 0.25 1 佘 quantity Example 3
将废铝易拉罐包进行机械打散、 撕碎得到零散的碎片, 然后经过 磁选机将混杂在易拉罐碎片中的铁磁性金属分离出来,避免混入后续 工序。 The scrap aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
易拉罐碎片在氧分压为 4%、 温度为 550°C下热脱漆 60min。 热脱 漆过程中产生的烟气经烟气管道送入燃烧炉, 1000 °C以上高温燃烧后, 二噁英类物质被消除。 通过热交换器将烟气温度迅速冷却至 130°C以 下, 抑制二噁英类物质再次生成。冷却后的烟气经布袋除尘、 活性炭 吸附、 脱硫脱硝塔处理, 达到环保要求后排放。热脱漆后的易拉罐碎 片经振动筛震动脱除粘附的炭粒,防止在熔炼过程中炭粒燃烧产生二 次污染。 The cans were hot stripped for 60 min at an oxygen partial pressure of 4% and a temperature of 550 °C. The flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a high temperature of 1000 ° C or higher. The temperature of the flue gas is rapidly cooled to below 130 °C by a heat exchanger to suppress the re-generation of dioxins. The cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitrification tower, and discharged after meeting environmental protection requirements. The hot-painted cans of the cans are vibrated by vibrating screen to remove the adhered carbon particles to prevent secondary contamination of the carbon particles during the smelting process.
脱漆后的铝片打包后压入蓄热式双室反射炉外室熔融的铝液中 进行熔化, 避免火焰直接接触到铝片降低回收率。外室铝液温度控制 在 800°C左右, 内室铝液的温度控制在 900 °C左右。 内室和外室熔融 的铝液依靠陶瓷泵循环。 After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate. The temperature of the aluminum liquid in the outer chamber is controlled at about 800 °C, and the temperature of the aluminum liquid in the inner chamber is controlled at about 900 °C. The molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
反射炉中铝片完全熔化并且铝液循环搅拌均匀后, 在线提取铝合 金成分分析样, 采用直读光谱仪分析铝液中 Si、 Fe、 Cu、 Mn、 Mg、 Cr、 Zn和 Ti含量和杂质含量, 要求 Si、 Fe、 Cu、 Mn、 Mg、 Cr、 Zn 和 Ti合金元素达到易拉罐用铝合金要求的范围内, 单个杂质元素含 量低于 0.05%, 杂质总含量低于 0.15%。 采用 650°C的氩气作为除气 剂, 均匀通入的铝合金熔液中, 形成细小的气泡, 吸附铝液中的氢气 和钙、 钠等的氧化物, 然后飘逸到铝液的上方。 After the aluminum sheet in the reverberatory furnace is completely melted and the aluminum liquid is evenly stirred, the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Cr, Zn and Ti and the impurity content in the aluminum liquid are analyzed by a direct reading spectrometer. It is required that the Si, Fe, Cu, Mn, Mg, Cr, Zn and Ti alloy elements reach the required range of the aluminum alloy for cans, the content of the single impurity element is less than 0.05%, and the total impurity content is less than 0.15%. Argon gas at 650 ° C is used as a deaerator, and fine aluminum bubbles are uniformly introduced into the aluminum alloy melt to adsorb hydrogen and calcium, sodium and the like in the aluminum liquid, and then float above the aluminum liquid.
在铝合金熔液中加入 0.25%的 AlTi5Cl进行变质处理, 改善共晶 硅形貌和尺寸,阻止粗大的针、板状共晶硅生成,使合金的组织细化。 添加晶粒细化剂, 防止铸锭裂纹。经变质处理后且成分和杂质含量满 足 5182铝合金要求的熔液在保持炉中静置一段时间, 使精炼载体上 浮将铝液中的气体和细小的非金属夹杂物带出铝液上表面而去除,大
块的非金属夹杂物下沉至炉底;然后采用泡沬陶瓷过滤器对铝合金熔 液进行过滤, 进一歩去除夹杂物; 过滤后的铝合金流进半连续性铸锭 机连续平稳浇铸, 润滑油与铸造气体通过石墨环渗透到结晶器表面, 在铝合金熔液和结晶器之间形成一层油气膜,使得铸锭的晶粒细小均 匀, 表面光滑。 表 4 为本实施例制备的铝合金的成分, 符合 "GB/T3190-2008变形铝及铝合金化学成分" 中规定的 5182铝合金 成分要求。 Adding 0.25% AlTi5Cl to the aluminum alloy melt for modification, improving the morphology and size of the eutectic silicon, preventing the formation of coarse needles and plate-like eutectic silicon, and refining the microstructure of the alloy. A grain refiner is added to prevent cracking of the ingot. After the metamorphism treatment, the composition and the impurity content satisfying the requirement of the 5182 aluminum alloy are allowed to stand in the holding furnace for a certain period of time, and the refining carrier is floated to bring the gas and the fine non-metallic inclusions in the aluminum liquid out of the upper surface of the aluminum liquid. Remove, big The non-metallic inclusions of the block sink to the bottom of the furnace; then the aluminum alloy melt is filtered by a ceramic filter to remove inclusions; the filtered aluminum alloy flows into the semi-continuous casting machine for continuous smooth casting. The lubricating oil and the casting gas permeate through the graphite ring to the surface of the crystallizer, and a gas film is formed between the aluminum alloy melt and the crystallizer, so that the crystal grains of the ingot are fine and uniform, and the surface is smooth. Table 4 The composition of the aluminum alloy prepared in the present example meets the composition requirements of the 5182 aluminum alloy specified in "GB/T3190-2008 Modified Aluminum and Aluminum Alloy Chemical Composition".
表 4 本实施例制备的铝合金与 5182铝合金的成分对比表 (重量百分比) Table 4 Comparison Table of Compositions of Aluminum Alloy and 5182 Aluminum Alloy Prepared in This Example (% by Weight)
实施例 4 Example 4
将废铝易拉罐包进行机械打散、 撕碎得到零散的碎片, 然后经过 磁选机将混杂在易拉罐碎片中的铁磁性金属分离出来,避免混入后续 工序。 The scrap aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
易拉罐碎片在氧分压为 4%、 温度为 640°C下热脱漆 20min。 热脱 漆过程中产生的烟气经烟气管道送入燃烧炉, 1000 °C以上高温燃烧后, 二噁英类物质被消除。 通过热交换器将烟气温度迅速冷却至 130°C以 下, 抑制二噁英类物质再次生成。冷却后的烟气经布袋除尘、 活性炭 吸附、 脱硫脱硝塔处理, 达到环保要求后排放。热脱漆后的易拉罐碎 片经振动筛震动脱除粘附的炭粒,防止在熔炼过程中炭粒燃烧产生二 次污染。 The cans were hot stripped for 20 min at an oxygen partial pressure of 4% and a temperature of 640 °C. The flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a high temperature of 1000 ° C or higher. The temperature of the flue gas is rapidly cooled to below 130 °C by a heat exchanger to suppress the re-generation of dioxins. The cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitrification tower, and discharged after meeting environmental protection requirements. The hot-painted cans of the cans are vibrated by vibrating screen to remove the adhered carbon particles to prevent secondary contamination of the carbon particles during the smelting process.
脱漆后的铝片打包后压入蓄热式双室反射炉外室熔融的铝液中 进行熔化, 避免火焰直接接触到铝片降低回收率。外室铝液温度控制 在 850°C左右, 内室铝液的温度控制在 950°C左右。 内室和外室熔融 的铝液依靠陶瓷泵循环。 After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate. The temperature of the aluminum liquid in the outer chamber is controlled at about 850 °C, and the temperature of the aluminum liquid in the inner chamber is controlled at about 950 °C. The molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
反射炉中铝片完全熔化并且铝液循环搅拌均匀后, 在线提取铝合 金成分分析样, 采用直读光谱仪分析铝液中 Si、 Fe、 Cu、 Mn、 Mg、 Cr、 Zn和 Ti含量和杂质含量, 要求 Si、 Fe、 Cu、 Mn、 Mg、 Cr、 Zn 和 Ti合金元素达到易拉罐用铝合金要求的范围内, 单个杂质元素含
量低于 0.05%, 杂质总含量低于 0.15%。 采用 700 °C的氩气作为除气 剂, 均匀通入的铝合金熔液中, 形成细小的气泡, 吸附铝液中的氢气 和钙、 钠等的氧化物, 然后飘逸到铝液的上方。 After the aluminum sheet in the reverberatory furnace is completely melted and the aluminum liquid is evenly stirred, the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Cr, Zn and Ti and the impurity content in the aluminum liquid are analyzed by a direct reading spectrometer. , requires Si, Fe, Cu, Mn, Mg, Cr, Zn, and Ti alloy elements to reach the required range of aluminum alloy for cans, and a single impurity element The amount is less than 0.05%, and the total impurity content is less than 0.15%. Argon gas at 700 °C is used as a deaerator, and fine aluminum bubbles are uniformly introduced into the aluminum alloy melt to adsorb hydrogen and calcium, sodium and the like in the aluminum liquid, and then float above the aluminum liquid.
在铝合金熔液中加入 0.75%的 AlTi5Cl进行变质处理, 改善共晶 硅形貌和尺寸,阻止粗大的针、板状共晶硅生成,使合金的组织细化。 添加晶粒细化剂, 防止铸锭裂纹。经变质处理后且成分和杂质含量满 足 5042铝合金要求的熔液在保持炉中静置一段时间, 使精炼载体上 浮将铝液中的气体和细小的非金属夹杂物带出铝液上表面而去除,大 块的非金属夹杂物下沉至炉底;然后采用泡沬陶瓷过滤器对铝合金熔 液进行过滤, 进一歩去除夹杂物; 过滤后的铝合金流进半连续性铸锭 机连续平稳浇铸, 润滑油与铸造气体通过石墨环渗透到结晶器表面, 在铝合金熔液和结晶器之间形成一层油气膜,使得铸锭的晶粒细小均 匀, 表面光滑。 表 5 为本实施例制备的铝合金的成分, 符合 "GB/T3190-2008变形铝及铝合金化学成分" 中规定的 5042铝合金 成分要求。 0.75% AlTi5Cl was added to the molten aluminum alloy for modification, which improved the morphology and size of the eutectic silicon, prevented the formation of coarse needles and plate-like eutectic silicon, and refined the microstructure of the alloy. A grain refiner is added to prevent cracking of the ingot. After the metamorphism treatment, the composition and the impurity content satisfying the requirements of the 5042 aluminum alloy are allowed to stand in the holding furnace for a period of time, and the refining carrier is floated to bring the gas and the fine non-metallic inclusions in the aluminum liquid out of the upper surface of the aluminum liquid. Remove, the large non-metallic inclusions sink to the bottom of the furnace; then use the foam ceramic filter to filter the aluminum alloy melt, and remove the inclusions; the filtered aluminum alloy flows into the semi-continuous casting machine continuously Smooth casting, lubricating oil and casting gas penetrate into the surface of the crystallizer through the graphite ring, forming a layer of oil and gas film between the aluminum alloy melt and the crystallizer, so that the crystal grains of the ingot are fine and uniform, and the surface is smooth. Table 5 shows the composition of the aluminum alloy prepared in this example, which meets the composition requirements of the 5042 aluminum alloy specified in "Chemical Composition of Modified Aluminum and Aluminum Alloys of GB/T3190-2008".
表 5 本实施例制备的铝合金与 5042铝合金的成分对比表 (重量百分比) Table 5 Comparison Table of Compositions of Aluminum Alloy and 5042 Aluminum Alloy Prepared in This Example (% by Weight)
实施例 5 Example 5
将废铝易拉罐包进行机械打散、 撕碎得到零散的碎片, 然后经过 磁选机将混杂在易拉罐碎片中的铁磁性金属分离出来,避免混入后续 工序。 The scrap aluminum cans are mechanically broken up and shredded to obtain scattered pieces, and then the ferromagnetic metal mixed in the cans is separated by a magnetic separator to avoid mixing into subsequent processes.
易拉罐碎片在氧分压为 6%、 温度为 600°C下热脱漆 100min。 热 脱漆过程中产生的烟气经烟气管道送入燃烧炉, 1000 °C以上高温燃烧 后,二噁英类物质被消除。通过热交换器将烟气温度迅速冷却至 130°C 以下, 抑制二噁英类物质再次生成。冷却后的烟气经布袋除尘、 活性 炭吸附、 脱硫脱硝塔处理, 达到环保要求后排放。热脱漆后的易拉罐 碎片经振动筛震动脱除粘附的炭粒,防止在熔炼过程中炭粒燃烧产生 二次污染。
脱漆后的铝片打包后压入蓄热式双室反射炉外室熔融的铝液中 进行熔化, 避免火焰直接接触到铝片降低回收率。外室铝液温度控制 在 800°C左右, 内室铝液的温度控制在 880°C左右。 内室和外室熔融 的铝液依靠陶瓷泵循环。 The cans were hot stripped for 100 min at an oxygen partial pressure of 6% and a temperature of 600 °C. The flue gas generated during the hot stripping process is sent to the combustion furnace through the flue gas pipeline, and the dioxin-like substance is eliminated after burning at a high temperature of 1000 ° C or higher. The temperature of the flue gas is rapidly cooled to below 130 ° C by a heat exchanger to suppress the re-generation of dioxins. The cooled flue gas is treated by bag dust removal, activated carbon adsorption, desulfurization and denitrification tower, and discharged after meeting environmental protection requirements. The cans of the cans after hot stripping are shaken to remove the adhered carbon particles by the vibrating screen to prevent secondary pollution caused by the combustion of the carbon particles during the smelting process. After the stripping of the aluminum sheet is packed, it is pressed into the molten aluminum liquid in the outer chamber of the regenerative double chamber reverberating furnace to be melted, so as to avoid direct contact of the flame with the aluminum sheet to reduce the recovery rate. The temperature of the aluminum liquid in the outer chamber is controlled at about 800 °C, and the temperature of the aluminum liquid in the inner chamber is controlled at about 880 °C. The molten aluminum in the inner and outer chambers is circulated by means of a ceramic pump.
反射炉中铝片完全熔化并且铝液循环搅拌均匀后, 在线提取铝合 金成分分析样, 采用直读光谱仪分析铝液中 Si、 Fe、 Cu、 Mn、 Mg、 Zn、 Ti和杂质含量, 要求 Si、 Fe、 Cu、 Mn、 Mg、 Zn和 Ti合金元素 达到易拉罐用铝合金要求的范围内, 单个杂质元素含量低于 0.05%, 杂质总含量低于 0.15%。 采用 600°C的氮气作为除气剂, 均匀通入的 铝合金熔液中, 形成细小的气泡, 吸附铝液中的氢气和钙、 钠等的氧 化物, 然后飘逸到铝液的上方。 After the aluminum sheet in the reverberatory furnace is completely melted and the aluminum liquid is evenly stirred, the aluminum alloy composition sample is extracted on-line, and the content of Si, Fe, Cu, Mn, Mg, Zn, Ti and impurities in the aluminum liquid is analyzed by a direct reading spectrometer, and Si is required. The Fe, Cu, Mn, Mg, Zn and Ti alloy elements are within the range required for the aluminum alloy for cans, the content of the single impurity element is less than 0.05%, and the total impurity content is less than 0.15%. Using 600 ° C of nitrogen as a deaerator, the aluminum alloy melt is uniformly introduced to form fine bubbles, which adsorb hydrogen in the aluminum liquid and oxygen such as calcium and sodium, and then float above the aluminum liquid.
在铝合金熔液中加入 1.0%的 ΑΓΠ5Β1进行变质处理, 改善共晶 硅形貌和尺寸,阻止粗大的针、板状共晶硅生成,使合金的组织细化。 添加晶粒细化剂, 防止铸锭裂纹。经变质处理后且成分和杂质含量满 足 3104铝合金要求的熔液在保持炉中静置一定时间, 使精炼载体上 浮将铝液中的气体和细小的非金属夹杂物带出铝液上表面而去除,大 块的非金属夹杂物下沉至炉底;然后采用泡沬陶瓷过滤器对铝合金熔 液进行过滤, 进一歩去除夹杂物; 过滤后的铝合金流进半连续性铸锭 机连续平稳浇铸, 润滑油与铸造气体通过石墨环渗透到结晶器表面, 在铝合金熔液和结晶器之间形成一层油气膜,使得铸锭的晶粒细小均 匀, 表面光滑。 表 6 为本实施例制备的铝合金的成分, 符合 "GB/T3190-2008变形铝及铝合金化学成分" 中规定的 3104铝合金 成分要求。 Adding 1.0% ΑΓΠ5Β1 to the aluminum alloy melt for modification, improving the morphology and size of the eutectic silicon, preventing the formation of coarse needles and plate-like eutectic silicon, and refining the microstructure of the alloy. A grain refiner is added to prevent cracking of the ingot. After the metamorphism treatment, the composition and the impurity content satisfying the requirements of the 3104 aluminum alloy are allowed to stand in the holding furnace for a certain period of time, so that the refining carrier floats to bring the gas and the fine non-metallic inclusions in the aluminum liquid out of the upper surface of the aluminum liquid. Remove, the large non-metallic inclusions sink to the bottom of the furnace; then use the foam ceramic filter to filter the aluminum alloy melt, and remove the inclusions; the filtered aluminum alloy flows into the semi-continuous casting machine continuously Smooth casting, lubricating oil and casting gas penetrate into the surface of the crystallizer through the graphite ring, forming a layer of oil and gas film between the aluminum alloy melt and the crystallizer, so that the crystal grains of the ingot are fine and uniform, and the surface is smooth. Table 6 shows the composition of the aluminum alloy prepared in this example, which meets the composition requirements of 3104 aluminum alloy specified in "Chemical Composition of Modified Aluminum and Aluminum Alloys of GB/T3190-2008".
表 6 本实施例制备的铝合金与 3104铝合金的成分对比表 (重量百分比) Table 6 Comparison Table of Compositions of Aluminum Alloy and 3104 Aluminum Alloy Prepared in This Example (% by Weight)
Claims
1、一种废铝易拉罐绿色循环保级再利用的方法,具体歩骤如下:1. A method for green recycling, upgrading and reuse of scrap aluminum cans. The specific steps are as follows:
( 1 ) 破碎: 将废铝易拉罐进行打散和撕碎; (1) Crushing: Scatter and shred scrap aluminum cans;
( 2) 磁选除铁: 将经破碎的废铝易拉罐碎片经过磁选机将铁磁 性金属与易拉罐碎片分离; (2) Magnetic separation and iron removal: Pass the crushed scrap aluminum can fragments through a magnetic separator to separate the ferromagnetic metal from the can fragments;
(3 ) 预处理脱漆: 将易拉罐碎片进入脱漆窑进行脱漆, 漆层被 炭化, 再经过专门的震动设备, 使炭粒全部脱落; (3) Pretreatment paint removal: Put the can fragments into the paint removal kiln for paint removal, the paint layer will be carbonized, and then go through special vibration equipment to make all the carbon particles fall off;
(4) 熔炼: 采用蓄热式双室反射炉, 脱漆后的铝片经打包后, 在外室压入熔融的铝液进行熔化,熔融的铝液在内室被反射炉火焰加 热, 内室和外室熔融的铝液依靠陶瓷泵循环; 外室铝液温度为 700°C -850°C, 内室铝液的温度在 850°C-950°C ; (4) Melting: A regenerative double-chamber reverberatory furnace is used. After the stripped aluminum sheets are packed, molten aluminum is pressed into the outer chamber for melting. The molten aluminum is heated by the flame of the reverberatory furnace in the inner chamber. The molten aluminum liquid in the outer chamber is circulated by a ceramic pump; the temperature of the aluminum liquid in the outer chamber is 700°C-850°C, and the temperature of the aluminum liquid in the inner chamber is 850°C-950°C;
(5 ) 成分调整: 所述的成分调整是控制铝合金中 Si、 Fe、 Cu、 Mn、 Mg、 Cr、 Zn和 Ti含量达到易拉罐用铝合金的要求; 单个杂质 元素含量低于 0.05%, 杂质总含量低于 0.15%; (5) Composition adjustment: The described composition adjustment is to control the content of Si, Fe, Cu, Mn, Mg, Cr, Zn and Ti in the aluminum alloy to meet the requirements of aluminum alloy for cans; the content of a single impurity element is less than 0.05%, and the impurity The total content is less than 0.15%;
(6)变质处理:所述的变质处理是在熔融的铝液中加入 0.1%-1% 的 ΑΓΠ5Β1或 AlTi5Cl改善共晶硅形貌和尺寸, 阻止粗大的针、板状 共晶硅生成, 使合金的组织细化, 添加晶粒细化剂, 防止铸锭裂纹; (6) Modification treatment: The described modification treatment is to add 0.1%-1% AΓΠ5B1 or AlTi5Cl to the molten aluminum liquid to improve the morphology and size of the eutectic silicon, and prevent the formation of thick needles and plate-shaped eutectic silicon, so that The structure of the alloy is refined, and grain refiners are added to prevent ingot cracks;
(7 ) 过滤、 浇铸: 经变质处理后的铝液在保持炉中静置一定时 间,使精炼载体上浮将铝液中的气体和细小的非金属夹杂物带出铝液 上表面而去除, 大块的非金属夹杂物下沉至炉底; 然后采用泡沬陶瓷 过滤器对铝合金熔液进行过滤, 进一歩去除夹杂物; 过滤后的铝合金 流进半连续性铸锭机连续平稳浇铸,润滑油与铸造气体通过石墨环渗 透到结晶器表面, 在铝合金熔液和结晶器之间形成一层油气膜, 使得 铸锭的晶粒细小均匀, 表面光滑, 最终得到易拉罐用铝合金。 (7) Filtration and casting: The modified aluminum liquid is allowed to stand in the holding furnace for a certain period of time, so that the refining carrier floats and the gas and small non-metallic inclusions in the aluminum liquid are brought out of the upper surface of the aluminum liquid for removal. Large pieces of non-metallic inclusions sink to the bottom of the furnace; then a foam ceramic filter is used to filter the aluminum alloy melt to further remove the inclusions; the filtered aluminum alloy flows into the semi-continuous ingot casting machine for continuous and smooth casting. Lubricating oil and casting gas penetrate into the surface of the crystallizer through the graphite ring, forming an oil and gas film between the aluminum alloy melt and the crystallizer, making the grains of the ingot fine and uniform, and the surface smooth, and finally the aluminum alloy for cans is obtained.
2、 根据权利要求 1所述的方法, 其特征在于: 所述歩骤 (2) 的 预处理脱漆采用旋转式脱漆窑处理,氧分压不高于 8%、温度为 450°C -640 °C, 进行热脱漆 20min- 120min。 2. The method according to claim 1, characterized in that: the pretreatment paint removal in step (2) is performed by a rotary paint removal kiln, the oxygen partial pressure is not higher than 8%, and the temperature is 450°C - 640 °C, perform thermal paint removal for 20min-120min.
3、 根据权利要求 1所述的方法, 其特征在于: 所述歩骤 (2) 热 脱漆过程中产生的烟气在 1000°C以上进行高温燃烧后, 二噁英类物 质被消除, 通过热交换器将烟气温度迅速冷却至 130°C以下, 抑制二
噁英类物质再次合成; 冷却后的烟气经布袋除尘、 活性炭吸附后, 通 过脱硫脱硝塔处理后达到环保要求排放。 3. The method according to claim 1, characterized in that: after the flue gas generated during the thermal depainting process in step (2) is burned at a high temperature above 1000°C, the dioxin-like substances are eliminated. The heat exchanger quickly cools the flue gas temperature below 130°C, suppressing the Oxins are synthesized again; the cooled flue gas is bag dusted, activated carbon adsorbed, and processed through a desulfurization and denitrification tower before being discharged to meet environmental protection requirements.
4、 根据权利要求 1所述的方法, 其特征在于: 所述歩骤 (5 )成 分调整采用 500°C-700°C高温氮气或者氩气作为除气剂, 均匀通入的 铝液中形成细小的气泡, 吸附铝液中的氢气和钙、钠等的氧化物, 然 后飘逸到铝液的上方。
4. The method according to claim 1, characterized in that: the component adjustment in step (5) uses 500°C-700°C high-temperature nitrogen or argon as a degassing agent, and is formed in the aluminum liquid that is uniformly passed through The tiny bubbles absorb hydrogen and oxides such as calcium and sodium in the aluminum liquid, and then float to the top of the aluminum liquid.
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