CN101831555B - Method for producing artificial rich iron ore by using nickel smelting waste slag through sintering process - Google Patents
Method for producing artificial rich iron ore by using nickel smelting waste slag through sintering process Download PDFInfo
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- CN101831555B CN101831555B CN2010101778430A CN201010177843A CN101831555B CN 101831555 B CN101831555 B CN 101831555B CN 2010101778430 A CN2010101778430 A CN 2010101778430A CN 201010177843 A CN201010177843 A CN 201010177843A CN 101831555 B CN101831555 B CN 101831555B
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- iron
- waste
- slag
- warm sludge
- nickel smelting
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- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 159
- 239000002699 waste material Substances 0.000 title claims abstract description 90
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 79
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title claims abstract description 66
- 239000002893 slag Substances 0.000 title claims abstract description 58
- 238000000034 method Methods 0.000 title claims abstract description 36
- 238000003723 Smelting Methods 0.000 title claims abstract description 33
- 229910052759 nickel Inorganic materials 0.000 title claims abstract description 33
- 230000008569 process Effects 0.000 title claims abstract description 16
- 238000005245 sintering Methods 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title abstract description 9
- 238000001816 cooling Methods 0.000 claims abstract description 8
- 239000010802 sludge Substances 0.000 claims description 41
- 239000000463 material Substances 0.000 claims description 25
- 239000000843 powder Substances 0.000 claims description 17
- 238000012216 screening Methods 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 3
- 239000012467 final product Substances 0.000 claims description 2
- 238000004064 recycling Methods 0.000 claims description 2
- 238000013467 fragmentation Methods 0.000 claims 1
- 238000006062 fragmentation reaction Methods 0.000 claims 1
- 239000002994 raw material Substances 0.000 abstract description 11
- 239000012535 impurity Substances 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 9
- 229910000831 Steel Inorganic materials 0.000 description 7
- 239000002184 metal Substances 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- 239000010959 steel Substances 0.000 description 7
- CWYNVVGOOAEACU-UHFFFAOYSA-N Fe2+ Chemical compound [Fe+2] CWYNVVGOOAEACU-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 238000007599 discharging Methods 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 229910000640 Fe alloy Inorganic materials 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000004568 cement Substances 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910000604 Ferrochrome Inorganic materials 0.000 description 1
- 229910000616 Ferromanganese Inorganic materials 0.000 description 1
- 229910000519 Ferrosilicon Inorganic materials 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 229910000870 Weathering steel Inorganic materials 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- 238000009770 conventional sintering Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000003113 dilution method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000009851 ferrous metallurgy Methods 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- DALUDRGQOYMVLD-UHFFFAOYSA-N iron manganese Chemical compound [Mn].[Fe] DALUDRGQOYMVLD-UHFFFAOYSA-N 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 239000012256 powdered iron Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000001698 pyrogenic effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 229960001866 silicon dioxide Drugs 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000011701 zinc Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Classifications
-
- 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
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- Manufacture And Refinement Of Metals (AREA)
Abstract
The invention relates to a method for producing artificial rich iron ore for ironmaking by using nickel smelting waste slag, in particular to a method for producing artificial rich iron ore by using nickel smelting waste slag through a sintering process, which is characterized by comprising the following steps: a. pouring the nickel smelting waste slag with the temperature of 1100-1300 ℃ into a hot slag ladle, shaking the ladle for 5-15 minutes, and standing for 10-20 minutes; b. transferring the rest of the waste slag in the hot slag ladle to another hot slag ladle; c. adding an iron-containing raw material into the hot slag ladle filled with most of the waste slag, wherein the dosage of the iron-containing raw material is 30-100% of the total weight of the waste slag in the hot slag ladle; d. and pouring out the waste slag added with the iron-containing raw material and then cooling. The method of the invention fully utilizes the sensible heat when the nickel smelting waste slag is discharged, purifies and removes impurities from the waste slag, recovers iron metal, and saves heat energy, thereby obtaining a novel artificial iron-rich ore product.
Description
Technical field
The present invention relates to a kind ofly, especially utilize nickel smelting waste slag to pass through the method that sintering process is produced artificial high-grad iron ore deposit with the get rich method of iron ore of nickel smelting waste slag production ironmaking personnel selection.
Background technology
Nickel smelting waste slag is a kind of solid slag of discharging during the Metal smelting of non-ferrous metallurgical enterprise nickel is produced, a kind of iron and steel resource of uniqueness especially.Not only contain a large amount of ferrous metal (about 34%-45%), silicon-dioxide, quicklime, Natural manganese dioxide in the nickel smelting waste slag; And also have metal such as minor amount of nickel, copper, cobalt, lead, zinc and non-metallic element sulphur etc.; The nickel smelting waste slag of enormous amount is except that additive replacement iron ore is made in a small amount of confession cement mill at present, and all the other are all fully developed.Temperature was at 1100 ℃-1300 ℃ when the pyrogenic process nickel smelting waste slag discharged in addition, and the sensible heat after the slag discharging is not utilized effectively, and has caused the great amount of heat energy waste.
At present, from nickel smelting waste slag, reclaiming metal has several different methods, and wherein commonly used have the hot method of charcoal, fuming process, electric dilution method, a flotation process etc., utilizes nickel smelting waste slag to reclaim ferrous metal, and also existing abroad proven technique technology is used for reference.But, to end up till now, these technical matters processing costs are generally too high, cause its economic benefit too poor, and especially aspect saving energy and reduce the cost, various economic targets are very poor, and therefore, these technology seldom are employed so far.
Iron and steel enterprise is the energy consumption rich and influential family, with traditional SINTERING PRODUCTION technology powdered iron ore carried out agglomeration and become an indispensable important production process in the ferrous metallurgy industry, and specifically be with various powdery iron-containing raw materials; Allocate an amount of fuel and flux into, add an amount of water, on agglomerating plant, make material that a series of physicochemical change take place through mixing with after making ball; Mineral powder granular is cohered caked process; Wherein the sintering circuit energy consumption accounts for 10% in ton steel comprehensive energy consumption, is only second to the ironmaking operation, therefore; Reduce the sintering circuit energy consumption, can effectively reduce a ton steel comprehensive energy consumption.
Summary of the invention
The purpose of this invention is to provide a kind of nickel smelting waste slag that utilizes and pass through the method that sintering process is produced artificial high-grad iron ore deposit; Can a kind of approach that effectively utilizes be provided to nickel smelting waste slag; The sensible heat that can also make full use of nickel smelting waste slag replaces conventional sintering fuel to carry out sintering process; Thereby effectively practiced thrift the required energy consumption of sintering process, also avoided environmental pollution.
For realizing above-mentioned purpose, the technical scheme that the present invention adopts is:
A kind of nickel smelting waste slag that utilizes passes through the method that sintering process is produced artificial high-grad iron ore deposit, it is characterized in that, comprises the steps:
A, temperature is poured in the warm sludge bag at 1100-1300 ℃ nickel smelting waste slag, through leaving standstill 10-20 minute after 5-15 minute the shaking ladle vibration;
B, the showy slag that the waste the superiors in the warm sludge bag are accounted for waste TV 3-8% are partly removed, and keep the bottom slag part that waste orlop in the warm sludge bag accounts for waste TV 3-8%, and the rest part of waste in the warm sludge bag is transferred in another warm sludge bag;
C, in the above-mentioned warm sludge bag that most of waste is housed, add iron-bearing material, the consumption of iron-bearing material is the 30-100% of waste gross weight in this warm sludge bag, stirs afterwards, and iron-bearing material is evenly melted in waste;
D, the waste that will add iron-bearing material are again poured out postcooling and are got final product.
Thereby remainder added recycling in the waste among the step a after the bottom slag that wherein the warm sludge bag orlop that keeps among the step b is accounted for waste TV 3-8% partly carried out the secondary ore dressing.
Utilize its heat energy that iron-bearing material for use is carried out heating, drying to reduce moisture content and to increase temperature when wherein waste cools off in the steps d.
Wherein the iron-holder of iron-bearing material is 60-65%, and iron-bearing material is at least a in the smart powder of iron, iron scale and the high-grad iron ore deposit powder.
The waste that wherein will add iron-bearing material in the steps d pour into the mould internal cooling, or cylinder iron machine carry out broken again after the ingot bar cooling, screening and finishing can be used.
The product of the inventive method can directly be used for iron-smelting raw material, the irony material in producing as iron alloy, and alternative agglomerate, oxide pellet, steel cuttings, iron scale, production cost is lower, and more energy-conserving and environment-protective are a kind of new ferriferous raw materials;
Sensible heat when the inventive method has made full use of the nickel smelting waste slag discharging to the waste purification and impurity removal, reclaims ferrous metal, practices thrift heat energy; Thereby obtained a kind of novel artificial high-grad iron ore deposit product, the nickel smelting waste slag of serious environment pollution has been turned waste into wealth, turned harm into good; Fully utilize resource to greatest extent, not only met national industrial policies and save energy; Reduce and pollute, for energy-saving and emission-reduction, developing a circular economy has very big meaning.Through experiment showed, that the enriched ore ferrous grade that the inventive method is produced can reach 49-55%, the requirement of National standard; Because wherein contain the minor amount of nickel metallic element and ordinary sinter ore deposit, acid pellet are compared, this product physical strength is high; Anti-knocking property are good; Good permeability is particularly suitable for the raw material as ironmaking, stainless steel and weathering steel, and the working of a furnace of blast furnace, electric furnace is more smooth and easy, stable when using this raw material.Simultaneously, also can be used as the ferriferous raw material in the iron alloy production, result of use is better, more energy-conservation than effects such as ordinary oxygen pellet, steel cuttings, iron scales in ferrosilicon, ferromanganese, ferrochrome production, cost is lower.
Embodiment
The inventive method still is in molten state after being particularly suitable for smelting, and typical temperature is at 1100-1300 ℃ nickel smelting waste slag, if cooled waste then need reheat, its economic benefit obviously can obviously descend.After the showy slag that the warm sludge bag the superiors account for waste TV 3-8% among the step b is in addition partly removed, can supply the cement mill to make additive and replace iron ore to use.
Because the sintering circuit energy consumption accounts for 10% in ton steel comprehensive energy consumption, the inventive method has been saved this part energy consumption fully, the environmental pollutions such as flue dust of also having avoided this part operation to cause simultaneously.
In the inventive method iron-bearing material is added waste, the ferrous metasilicate alkalescence of molten state is increased relatively, acidity weakens, thus transition is a kind of people of hot-melting type (iron) mineral products of getting rich.
The iron-bearing material iron-holder of using in the inventive method is 60-65%; Iron-bearing material is at least a in the smart powder of iron, iron scale and the high-grad iron ore deposit powder; Following embodiment provides the example of independent use above-mentioned raw materials respectively; But through evidence, any two kinds or whole three kinds in the above-mentioned raw materials are mixed with arbitrary proportion and also to be suitable for.
Embodiment 1
A, temperature is poured in the warm sludge bag at 1200 ℃ nickel smelting waste slag, through leaving standstill 15 minutes after 10 minutes the shaking ladles vibration;
B, the showy slag that the warm sludge bag the superiors are accounted for waste TV 5% are partly removed, and keep the bottom slag part that warm sludge bag orlop accounts for waste TV 5%, and rest part in the warm sludge bag is transferred in another warm sludge bag;
C, in the above-mentioned warm sludge bag that most of waste is housed, to add iron-holder be 62% the smart powder of iron, the consumption of the smart powder of iron be in this warm sludge bag the waste gross weight 50%, stir afterwards, iron essence powder is evenly melted in waste;
That d, the waste that will add the smart powder of iron are again poured into is broken again after the mould internal cooling, screening and finishing promptly can be used as the qualified artificial high-grad iron ore deposit of finished product and use.
Iron-bearing material adopts the smart powder of iron in the present embodiment; Can the bottom slag that the warm sludge bag orlop that keep among the step b accounts for waste TV 5% partly be carried out the secondary ore dressing in addition; Obtain wherein more valuable metal; Reuse in the waste among the remainder adding step a; If this part noble metal content more also can be abandoned certainly, can also recycle its heat energy that distributes when waste cools off in steps d iron-bearing material for use is carried out heating, drying to reduce moisture content and to increase temperature, the cold water of can also heating is hot water etc.
Embodiment 2
A, temperature is poured in the warm sludge bag at 1100 ℃ nickel smelting waste slag, through leaving standstill 10 minutes after 5 minutes the shaking ladles vibration;
B, the showy slag that the warm sludge bag the superiors are accounted for waste TV 3% are partly removed, and keep the bottom slag part that warm sludge bag orlop accounts for waste TV 3%, and rest part in the warm sludge bag is transferred in another warm sludge bag;
C, in the above-mentioned warm sludge bag that most of waste is housed, to add iron-holder be 60% iron scale, and the consumption of iron scale be 30% of the interior waste gross weight of this warm sludge bag, stirs afterwards, and iron scale is evenly melted in waste;
D, will add iron scale again waste cylinder iron machine carry out broken again after the ingot bar cooling, screening and finishing and promptly can be used as the qualified artificial high-grad iron ore deposit of finished product and use.
Iron-bearing material adopts iron scale in the present embodiment, can the bottom slag that the warm sludge bag orlop that keep among the step b accounts for waste TV 3% partly be carried out the secondary ore dressing in addition, and rest part is identical with embodiment 1.
Embodiment 3
A, temperature is poured in the warm sludge bag at 1300 ℃ nickel smelting waste slag, through leaving standstill 20 minutes after 15 minutes the shaking ladles vibration;
B, the showy slag that the warm sludge bag the superiors are accounted for waste TV 8% are partly removed, and keep the bottom slag part that warm sludge bag orlop accounts for waste TV 8%, and rest part in the warm sludge bag is transferred in another warm sludge bag;
C, in the above-mentioned warm sludge bag that most of waste is housed, to add iron-holder be 65% high-grad iron ore deposit powder, and the consumption of high-grad iron ore deposit powder be 100% of the interior waste gross weight of this warm sludge bag, stirs afterwards, and the high-grad iron ore deposit powder is evenly melted in waste;
D, will add the high-grad iron ore deposit powder again waste cylinder iron machine carry out broken again after the ingot bar cooling, screening and finishing and promptly can be used as the qualified artificial high-grad iron ore deposit of finished product and use.
Iron-bearing material adopts the high-grad iron ore deposit powder in the present embodiment, can the bottom slag that the warm sludge bag orlop that keep among the step b accounts for waste TV 8% partly be carried out the secondary ore dressing in addition, and rest part is identical with embodiment 1.
Claims (4)
1. one kind is utilized nickel smelting waste slag to pass through the method that sintering process is produced artificial high-grad iron ore deposit, it is characterized in that, comprises the steps:
A, temperature is poured in the warm sludge bag at 1100-1300 ℃ nickel smelting waste slag, through leaving standstill 10-20 minute after 5-15 minute the shaking ladle vibration;
B, the showy slag that the waste the superiors in the warm sludge bag are accounted for waste TV 3-8% are partly removed, and keep the bottom slag part that waste orlop in the warm sludge bag accounts for waste TV 3-8%, and the rest part of waste in the warm sludge bag is transferred in another warm sludge bag;
C, in the above-mentioned warm sludge bag that most of waste is housed, add iron-bearing material, the consumption of iron-bearing material is the 30-100% of waste gross weight in this warm sludge bag, stirs afterwards, and iron-bearing material is evenly melted in waste; Wherein the iron-holder of iron-bearing material is 60-65%, and iron-bearing material is at least a in the smart powder of iron, iron scale and the high-grad iron ore deposit powder;
D, the waste that will add iron-bearing material are again poured out postcooling and are got final product.
2. the nickel smelting waste slag that utilizes as claimed in claim 1 passes through the method that sintering process is produced artificial high-grad iron ore deposit, it is characterized in that: thus remainder added recycling in the waste among the step a after the bottom slag that the warm sludge bag orlop that keeps among the step b accounts for waste TV 3-8% partly carried out the secondary ore dressing.
3. the nickel smelting waste slag that utilizes as claimed in claim 1 passes through the method that sintering process is produced artificial high-grad iron ore deposit, it is characterized in that: utilize its heat energy that iron-bearing material for use is carried out heating, drying to reduce moisture content and to increase temperature when wherein waste cools off in the steps d.
4. the nickel smelting waste slag that utilizes as claimed in claim 1 passes through the method that sintering process is produced artificial high-grad iron ore deposit, it is characterized in that: fragmentation, screening and finishing can be used again after the waste that wherein will add iron-bearing material in the steps d was poured the mould internal cooling into, perhaps cylinder iron machine carries out the ingot bar cooling.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101778430A CN101831555B (en) | 2010-05-20 | 2010-05-20 | Method for producing artificial rich iron ore by using nickel smelting waste slag through sintering process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101778430A CN101831555B (en) | 2010-05-20 | 2010-05-20 | Method for producing artificial rich iron ore by using nickel smelting waste slag through sintering process |
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| Publication Number | Publication Date |
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| CN101831555A CN101831555A (en) | 2010-09-15 |
| CN101831555B true CN101831555B (en) | 2012-05-02 |
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| CN2010101778430A Expired - Fee Related CN101831555B (en) | 2010-05-20 | 2010-05-20 | Method for producing artificial rich iron ore by using nickel smelting waste slag through sintering process |
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| CN102212711B (en) * | 2011-06-08 | 2012-07-18 | 鞍山鑫普新材料有限公司 | Method for treating hydrogen storage alloy waste residues |
| CN103667684B (en) * | 2013-12-24 | 2016-04-20 | 云南文山斗南锰业股份有限公司 | Ore powder becomes block method |
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| JP3529317B2 (en) * | 2000-03-03 | 2004-05-24 | 日鉱金属株式会社 | Operating method of copper smelting furnace |
| JP4112523B2 (en) * | 2004-05-20 | 2008-07-02 | 日鉱金属株式会社 | Dissolution treatment method of hydrous fine iron-containing material in copper PS converter |
| JP4350711B2 (en) * | 2006-02-03 | 2009-10-21 | 日鉱金属株式会社 | Industrial waste melting process |
| CN101545042A (en) * | 2009-02-09 | 2009-09-30 | 牛庆君 | Method for producing microalloy ferro-silicon by using a ferrous metasilicate electric stove integral deoxidation and reduction |
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