EP3578672A1 - Charge for producing iron-ore pellets (variants) - Google Patents
Charge for producing iron-ore pellets (variants) Download PDFInfo
- Publication number
- EP3578672A1 EP3578672A1 EP17868869.3A EP17868869A EP3578672A1 EP 3578672 A1 EP3578672 A1 EP 3578672A1 EP 17868869 A EP17868869 A EP 17868869A EP 3578672 A1 EP3578672 A1 EP 3578672A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- charge
- pellets
- iron
- limestone
- manganese
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 239000008188 pellet Substances 0.000 title claims abstract description 59
- LIKBJVNGSGBSGK-UHFFFAOYSA-N iron(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[Fe+3].[Fe+3] LIKBJVNGSGBSGK-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 235000019738 Limestone Nutrition 0.000 claims abstract description 39
- 239000006028 limestone Substances 0.000 claims abstract description 39
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000012141 concentrate Substances 0.000 claims abstract description 19
- 229910001570 bauxite Inorganic materials 0.000 claims abstract description 13
- 239000011230 binding agent Substances 0.000 claims abstract description 13
- 230000004907 flux Effects 0.000 claims abstract description 13
- 229910052742 iron Inorganic materials 0.000 claims abstract description 12
- 230000000051 modifying effect Effects 0.000 claims abstract description 8
- 239000000654 additive Substances 0.000 claims abstract description 6
- 230000000996 additive effect Effects 0.000 claims abstract description 5
- 239000011572 manganese Substances 0.000 claims description 36
- 229910052748 manganese Inorganic materials 0.000 claims description 36
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 claims description 33
- 239000000203 mixture Substances 0.000 claims description 9
- 238000002844 melting Methods 0.000 abstract description 16
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000003723 Smelting Methods 0.000 abstract description 3
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 230000007423 decrease Effects 0.000 description 11
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 10
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 10
- 239000000440 bentonite Substances 0.000 description 6
- 229910000278 bentonite Inorganic materials 0.000 description 6
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 230000008018 melting Effects 0.000 description 5
- 239000000377 silicon dioxide Substances 0.000 description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 229910052681 coesite Inorganic materials 0.000 description 4
- 229910052593 corundum Inorganic materials 0.000 description 4
- 229910052906 cristobalite Inorganic materials 0.000 description 4
- 239000011521 glass Substances 0.000 description 4
- 229910052682 stishovite Inorganic materials 0.000 description 4
- 229910052905 tridymite Inorganic materials 0.000 description 4
- 229910001845 yogo sapphire Inorganic materials 0.000 description 4
- 239000000395 magnesium oxide Substances 0.000 description 3
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 1
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 description 1
- 238000001465 metallisation Methods 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000011435 rock Substances 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
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/24—Binding; Briquetting ; Granulating
- C22B1/242—Binding; Briquetting ; Granulating with binders
- C22B1/243—Binding; Briquetting ; Granulating with binders inorganic
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/008—Composition or distribution of the charge
Definitions
- the invention relates to the field of producing iron-ore pellets for blast-furnace smelting.
- the charge consists of iron-ore concentrate, bentonite and fluxing additives - limestone, chalk or dolomite.
- the disadvantage of this solution is the high SiO 2 content in marl, which reduces the iron content in the pellets, the low strength of the raw pellets and the wide temperature range of softening-melting of the pellets in the blast furnace.
- the closest technical solution to the technical essence and the achieved result (the closest analogue is the prototype in the second variant) with respect to the claimed charge in the second variant is the charge for producing pellets for metallization in the shaft units followed by hot briquetting according to the patent of the Russian Federation No. 2202632 for the invention containing iron-ore material, bentonite, limestone and bauxite in the following ratio of components, wt.%: the sum of bentonite and limestone is 0.5-1.0; bauxite - 0.4-1.1; iron-ore material - the rest.
- the disadvantage of this charge composition is the low value of the basicity of the pellets, which determines the wide softening-melting interval in the blast furnace.
- the objective of the invention is to develop a charge for the production of iron-ore pellets, which eliminated the disadvantages of the known charges.
- the charge contains manganese limestone, intended for use as a binder, and flux, while the ratio of the components of the charge is, wt%:
- the manganese content in manganese limestone is at least 6%.
- the charge for producing iron-ore pellets in the second variant, containing iron-ore concentrate, flux and binder contains bauxite, intended for use as a modifying additive, and manganese limestone, intended for use both as a binder and flux, while the ratio of the components of the charge is, wt%:
- the manganese content in manganese limestone is at least 6%.
- Increasing the strength of the sintered pellets in the charge in the first variant is achieved by increasing the content of manganese oxide.
- the lower limit of the content of manganese limestone in the charge in the first variant is due to its minimum amount capable of providing high strength of green and sintered pellets. With less than 1.0% content of manganese limestone in the charge, the strength of green and sintered pellets decreases below the level that provides strength when using chalky marl. When the content of manganese limestone in the charge is less than 1 %, the effect of manganese oxide on the softening and melting temperatures is weak.
- the upper limit of the content of manganese limestone in the charge in the first variant is due to a decrease in the iron content in the pellets and the strength of the sintered pellets.
- 5% The upper limit of the content of manganese limestone in the charge in the first variant, that is, 5%, is due to a decrease in the iron content in the pellets and the strength of the sintered pellets.
- the strength of the sintered pellets is reduced due to the formation of glass in their structure. Glass formation also leads to a decrease in the softening temperature and an increase in the softening-melting range.
- the decrease in the temperature range of softening-melting of the pellets is achieved due to the influence of manganese oxide (when the manganous limestone content is within the stated limits in the charge according to the first variant) on the softening and melting temperatures of the pellets in the blast furnace.
- the reduction in the softening-melting range of pellets in the blast furnace in the charge according to the second variant is achieved due to the higher content of Al 2 O 3 in the pellets and the influence of manganese oxide on the softening temperatures and melting of the pellets in the blast furnace.
- the increase in the strength of green pellets in the charge according to the second variant is due to the increased water-physical properties of manganese limestone, and the strength increase of the sintered pellets (when the content of manganese limestone is within the limit stated according to the second variant) is simultaneously due to an increase in the content of manganese oxide, and also due to the formation of the structure of the brownmillerite mineral in the interaction of manganese limestone with aluminum oxide Al 2 O 3 .
- the lower limit of the content of manganese limestone in the charge in the second variant is due to its minimum amount capable of providing high strength of green and sintered pellets. With less than 1.0% content of manganese limestone in the charge, the strength of green and sintered pellets decreases below the level that provides strength when using bentonite.
- the upper limit of the content of manganese limestone in the charge in the second variant is due to a decrease in the iron content in the pellets and the strength of the sintered pellets.
- the lower limit of the bauxite content in the charge according to the second variant that is 1.2%, is due to its minimum amount, at which the modifying effect on the softening and melting temperatures in the blast furnace occurs. With less than 1.2% bauxite content in the mixture, the effect of Al 2 O 3 on the decrease in softening and melting temperatures is weak.
- the upper limit of the bauxite content in the charge in the second variant is due to a decrease in the iron content in the pellets. With a greater than 1.5% bauxite content in the charge, the iron content in the pellets decreases.
- the test charge for iron-ore pellets was performed in laboratory conditions.
- the iron-ore concentrate was used as the iron-ore material, the chemical composition of which is given in table. 1.
- Raw pellets were tested for strength by dropping from a height of 30 cm.
- the sintering was performed in a muffle furnace with a programmable heat treatment mode at a maximum temperature of 1300 °C. After firing and cooling, the pellets were tested for crushing strength according to GOST 24765-81, the chemical composition and softening-melting temperatures were determined according to GOST 26517-85.
- Simplification of the charge is due to the fact that manganese limestone is intended for use as a flux and binder (i.e., such a component of the charge as a binder is not required separately).
- manganese limestone use natural raw materials (manganese ore), characterized by a manganese content of at least 6%.
- Table 1 The chemical composition of the charge components, % Components Fe FeO Fe 2 O 3 CaO MgO SiO 2 AL 2 O3 MnO LOI Iron-ore concentrate 67.49 28.70 64.52 0.22 0.51 5.50 0.19 0.03 0.27 Bentonite - - 1.50 1.00 0.50 60.00 36.90 - - Manganese limestone 0.84 - 1.20 40.50 0.77 8.70 3.10 9.91 35.75 Bauxite 14.04 - 20.06 0.79 0.75 8.70 40.87 - 24.90 Chalky marl 1.12 - 1.60 44.40 0.70 14.50 3.50 - 35.40 Limestone 0.18 - 0.26 54.2 0.71 1.28 0.34 0.01 42.50 LOI - loss on ignition
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Metallurgy (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Environmental & Geological Engineering (AREA)
- Geology (AREA)
- Geochemistry & Mineralogy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Inorganic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
- The invention relates to the field of producing iron-ore pellets for blast-furnace smelting.
- There are various compositions of the charge of pellets for blast-furnace smelting. In the production of fluxed pellets, the charge consists of iron-ore concentrate, bentonite and fluxing additives - limestone, chalk or dolomite.
- For example, from the USSR Author's Certificate No.
692879 , a method is known for producing pellets from concentrates containing 4-10% silica in barren rock, and fluxing the charge to a CaO/SiO2 ratio of 0.5-1.3 is produced with the introduction of magnesium oxide in the amount of providing a ratio of CaO:MgO = 1.5-3.9. After sintering, cooling to a temperature of 700-900 °C is conducted at a speed of 120-240 ° C/min. - The disadvantage of this composition of the charge is high basicity, accompanied by a decrease in the iron content in the pellets, and the formation of glass in the structure of the pellets, reducing their strength.
- The closest technical solution to the technical essence and the achieved result (the closest analogue is the prototype in the first variant) with respect to the claimed charge in the first variant is the charge for producing pellets according to the USSR Inventor's Certificate No.
800200 containing iron-ore concentrate and a binder in the form of lime-containing material. In order to reduce the cost of metallurgical processing, the charge contains chalky marl with a particle content of 2-0 microns 20-80% as a lime-containing material with the following ratio of ingredients, %: chalky marl 3-7, iron-ore concentrate - the rest. - The disadvantage of this solution is the high SiO2 content in marl, which reduces the iron content in the pellets, the low strength of the raw pellets and the wide temperature range of softening-melting of the pellets in the blast furnace.
- The closest technical solution to the technical essence and the achieved result (the closest analogue is the prototype in the second variant) with respect to the claimed charge in the second variant is the charge for producing pellets for metallization in the shaft units followed by hot briquetting according to the patent of the Russian Federation No.
for the invention containing iron-ore material, bentonite, limestone and bauxite in the following ratio of components, wt.%: the sum of bentonite and limestone is 0.5-1.0; bauxite - 0.4-1.1; iron-ore material - the rest.2202632 - The disadvantage of this charge composition is the low value of the basicity of the pellets, which determines the wide softening-melting interval in the blast furnace.
- The objective of the invention is to develop a charge for the production of iron-ore pellets, which eliminated the disadvantages of the known charges.
- The technical result achieved by the invention increase the strength of green and sintered pellets while maintaining a high iron content, reducing the softening-melting interval of the pellets in the blast furnace, and simplifies the production of iron-ore pellets.
- The technical result is achieved due to the fact that in the charge to obtain iron-ore pellets in the first variant, containing iron-ore concentrate, flux and binder, according to the invention, the charge contains manganese limestone, intended for use as a binder, and flux, while the ratio of the components of the charge is, wt%:
- manganese limestone - (1.0-5.0);
- iron-ore concentrate - the rest.
- The manganese content in manganese limestone is at least 6%.
- In the charge for producing iron-ore pellets in the second variant, containing iron-ore concentrate, flux and binder, according to the invention, the charge contains bauxite, intended for use as a modifying additive, and manganese limestone, intended for use both as a binder and flux, while the ratio of the components of the charge is, wt%:
- manganese limestone - (1.0-3.5);
- modifying additive - (1,2 - 1,5);
- iron-ore concentrate - the rest.
- The manganese content in manganese limestone is at least 6%.
- While using charge in both variants, the preservation of a high iron content in the pellets is achieved due to a lower SiO2 content in manganese limestone.
- The increase in the strength of raw pellets in the charge in both variants is due to the increased water-physical properties of manganese limestone.
- Increasing the strength of the sintered pellets in the charge in the first variant (when the content of manganese limestone is within the limits stated in the first embodiment) is achieved by increasing the content of manganese oxide.
- The lower limit of the content of manganese limestone in the charge in the first variant, that is, 1.0%, is due to its minimum amount capable of providing high strength of green and sintered pellets. With less than 1.0% content of manganese limestone in the charge, the strength of green and sintered pellets decreases below the level that provides strength when using chalky marl. When the content of manganese limestone in the charge is less than 1%, the effect of manganese oxide on the softening and melting temperatures is weak.
- The upper limit of the content of manganese limestone in the charge in the first variant, that is, 5%, is due to a decrease in the iron content in the pellets and the strength of the sintered pellets. With a greater than 5.0% content of manganese limestone in the charge, the strength of the sintered pellets is reduced due to the formation of glass in their structure. Glass formation also leads to a decrease in the softening temperature and an increase in the softening-melting range.
- In the charge according to the first variant, the decrease in the temperature range of softening-melting of the pellets is achieved due to the influence of manganese oxide (when the manganous limestone content is within the stated limits in the charge according to the first variant) on the softening and melting temperatures of the pellets in the blast furnace.
- The reduction in the softening-melting range of pellets in the blast furnace in the charge according to the second variant is achieved due to the higher content of Al2O3 in the pellets and the influence of manganese oxide on the softening temperatures and melting of the pellets in the blast furnace.
- An additional decrease in the softening-melting range of pellets in the blast furnace is achieved by modifying Al2O3 with bauxite.
- The increase in the strength of green pellets in the charge according to the second variant is due to the increased water-physical properties of manganese limestone, and the strength increase of the sintered pellets (when the content of manganese limestone is within the limit stated according to the second variant) is simultaneously due to an increase in the content of manganese oxide, and also due to the formation of the structure of the brownmillerite mineral in the interaction of manganese limestone with aluminum oxide Al2O3.
- The lower limit of the content of manganese limestone in the charge in the second variant, that is, 1.0%, is due to its minimum amount capable of providing high strength of green and sintered pellets. With less than 1.0% content of manganese limestone in the charge, the strength of green and sintered pellets decreases below the level that provides strength when using bentonite.
- The upper limit of the content of manganese limestone in the charge in the second variant, that is, 3.5%, is due to a decrease in the iron content in the pellets and the strength of the sintered pellets.
- With a greater than 3.5% content of manganese limestone in the charge, the strength of the sintered pellets is reduced due to the formation of glass in their structure.
- The lower limit of the bauxite content in the charge according to the second variant, that is 1.2%, is due to its minimum amount, at which the modifying effect on the softening and melting temperatures in the blast furnace occurs. With less than 1.2% bauxite content in the mixture, the effect of Al2O3 on the decrease in softening and melting temperatures is weak.
- The upper limit of the bauxite content in the charge in the second variant, that is, 1.5%, is due to a decrease in the iron content in the pellets. With a greater than 1.5% bauxite content in the charge, the iron content in the pellets decreases.
- The test charge for iron-ore pellets was performed in laboratory conditions. The iron-ore concentrate was used as the iron-ore material, the chemical composition of which is given in table. 1. There are also compositions of fluxes and bauxite given there. Bentonite, fluxes and bauxite were ground in a ball mill to a particle size of less than 0.072 mm, injected into the concentrate in a predetermined amount, mixed, moistened, and then the pellets were produced in a drum granulator with a particle size of 10-15 mm. Raw pellets were tested for strength by dropping from a height of 30 cm. The sintering was performed in a muffle furnace with a programmable heat treatment mode at a maximum temperature of 1300 °C. After firing and cooling, the pellets were tested for crushing strength according to GOST 24765-81, the chemical composition and softening-melting temperatures were determined according to GOST 26517-85.
- For comparison, the tests were conducted on the charge of the prototypes, respectively, according to the first and second variant. The test results are presented in Table 2.
- Analysis of the obtained results shows that the claimed charge for producing iron-ore pellets in both variants ensures the achievement of the stated goal of increasing the strength of raw and sintered pellets while maintaining a high iron content and reducing the softening-melting interval in the blast furnace.
- The charge in both variants for obtaining iron-ore pellets compared to the corresponding prototypes increases the strength of raw pellets from 2.2 to 3.5-5.0 drops, the strength of sintered pellets from 250 to 313-510 kg/pellet, reduces the softening-melting temperature range from 320 to 240-290 °C, retains a high iron content in the pellets.
- The claimed technique can be implemented in industry with the achievement of the stated technical result.
- Simplification of the charge is due to the fact that manganese limestone is intended for use as a flux and binder (i.e., such a component of the charge as a binder is not required separately).
- As manganese limestone use natural raw materials (manganese ore), characterized by a manganese content of at least 6%.
Table 1. The chemical composition of the charge components, % Components Fe FeO Fe2O3 CaO MgO SiO2 AL2O3 MnO LOI Iron-ore concentrate 67.49 28.70 64.52 0.22 0.51 5.50 0.19 0.03 0.27 Bentonite - - 1.50 1.00 0.50 60.00 36.90 - - Manganese limestone 0.84 - 1.20 40.50 0.77 8.70 3.10 9.91 35.75 Bauxite 14.04 - 20.06 0.79 0.75 8.70 40.87 - 24.90 Chalky marl 1.12 - 1.60 44.40 0.70 14.50 3.50 - 35.40 Limestone 0.18 - 0.26 54.2 0.71 1.28 0.34 0.01 42.50 LOI - loss on ignition
Claims (4)
- The charge to obtain iron-ore pellets containing iron-ore concentrate, flux and a binder, characterized in that it contains manganese limestone intended for use as a binder and a flux, at that, the ratio of the components of the mixture is as follows, wt%:- manganese limestone - (1.0-5.0);- iron-ore concentrate - the rest.
- The charge of claim 1, characterized in that the manganese content in manganese limestone is at least 6%.
- The charge for producing iron-ore pellets containing iron ore concentrate, flux and binder, characterized in that the charge contains bauxite, intended for use as a modifying additive, and manganese limestone, intended for use both as a binder and flux, while the ratio of the components of the charge is, wt%:- manganese limestone - (1.0-3.5);- modifying additive - (1,2 - 1,5);- iron-ore concentrate - the rest.
- The charge of claim 3, characterized in that the manganese content in manganese limestone is at least 6%.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU2016144588A RU2637850C1 (en) | 2016-11-14 | 2016-11-14 | Charge for producing iron ore pellets (versions) |
| PCT/RU2017/000855 WO2018088941A1 (en) | 2016-11-14 | 2017-11-17 | Charge for producing iron-ore pellets (variants) |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP3578672A1 true EP3578672A1 (en) | 2019-12-11 |
| EP3578672A4 EP3578672A4 (en) | 2020-09-02 |
Family
ID=60581320
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP17868869.3A Withdrawn EP3578672A4 (en) | 2016-11-14 | 2017-11-17 | Charge for producing iron-ore pellets (variants) |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US20200010922A1 (en) |
| EP (1) | EP3578672A4 (en) |
| CN (1) | CN110199037A (en) |
| BR (1) | BR112019014466A2 (en) |
| RU (1) | RU2637850C1 (en) |
| WO (1) | WO2018088941A1 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112430731A (en) * | 2020-05-28 | 2021-03-02 | 王彩杰 | Method for preparing alkaline pellets from high-silicon iron powder |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| SU765383A2 (en) * | 1978-04-06 | 1980-09-23 | Научно-Исследовательский И Проектный Институт Обогащения И Механической Обработки Полезных Ископаемых "Уралмеханобр" | Method of producing oxidized pellets |
| SU800200A1 (en) * | 1978-12-26 | 1981-01-30 | Salykin Aleksej A | Charge for producing pellets |
| RU2202632C1 (en) * | 2001-08-08 | 2003-04-20 | Открытое акционерное общество "Лебединский горно-обогатительный комбинат" | Composition of burden to produce pellets for their metallization in plants of shaft type and subsequent hot briquetting of iron |
| RU2245930C1 (en) * | 2003-09-26 | 2005-02-10 | Научно-производственное внедренческое предприятие "ТОРЭКС" (НПВП "ТОРЭКС") | Batch for pellet production used in metallurgy |
| EP2325341A1 (en) * | 2008-01-30 | 2011-05-25 | Nu-Iron Technology, Inc | Methods and system für producing metallic ion nuggets |
| RU2410447C1 (en) * | 2009-04-28 | 2011-01-27 | Открытое акционерное общество "Высокогорский горно-обогатительный комбинат" | Mix material for production of manganese-containing staflux |
| RU2465350C2 (en) * | 2010-05-11 | 2012-10-27 | Открытое акционерное общество "ЕВРАЗ Нижнетагильский металлургический комбинат" (ОАО "ЕВРАЗ НТМК") | Agglomerated flux, charge, and method for its manufacture |
| CN106755653A (en) * | 2016-12-10 | 2017-05-31 | 东北大学 | A kind of method containing rare earth or the also original production of niobium slag metallurgy melting |
-
2016
- 2016-11-14 RU RU2016144588A patent/RU2637850C1/en active
-
2017
- 2017-11-17 EP EP17868869.3A patent/EP3578672A4/en not_active Withdrawn
- 2017-11-17 CN CN201780083142.0A patent/CN110199037A/en active Pending
- 2017-11-17 BR BR112019014466-8A patent/BR112019014466A2/en not_active Application Discontinuation
- 2017-11-17 WO PCT/RU2017/000855 patent/WO2018088941A1/en not_active Ceased
-
2019
- 2019-07-17 US US16/514,708 patent/US20200010922A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| CN110199037A (en) | 2019-09-03 |
| RU2637850C1 (en) | 2017-12-07 |
| BR112019014466A2 (en) | 2020-02-11 |
| US20200010922A1 (en) | 2020-01-09 |
| EP3578672A4 (en) | 2020-09-02 |
| WO2018088941A1 (en) | 2018-05-17 |
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