EP1927666B1 - A smelting process of ferronickel with nickel oxide ore containing of crystal water in a blast furnace - Google Patents

A smelting process of ferronickel with nickel oxide ore containing of crystal water in a blast furnace Download PDF

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Publication number
EP1927666B1
EP1927666B1 EP05801995.1A EP05801995A EP1927666B1 EP 1927666 B1 EP1927666 B1 EP 1927666B1 EP 05801995 A EP05801995 A EP 05801995A EP 1927666 B1 EP1927666 B1 EP 1927666B1
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Prior art keywords
ore
limestone
blast
fluorite
nickel
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German (de)
French (fr)
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EP1927666A4 (en
EP1927666A1 (en
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Shenjie Liu
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Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/002Ferrous alloys, e.g. steel alloys containing In, Mg, or other elements not provided for in one single group C22C38/001 - C22C38/60
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/02Making special pig-iron, e.g. by applying additives, e.g. oxides of other metals
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B3/00General features in the manufacture of pig-iron
    • C21B3/02General features in the manufacture of pig-iron by applying additives, e.g. fluxing agents
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B5/00Making pig-iron in the blast furnace
    • C21B5/008Composition or distribution of the charge
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/16Sintering; Agglomerating
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/005Preliminary treatment of ores, e.g. by roasting or by the Krupp-Renn process
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B23/00Obtaining nickel or cobalt
    • C22B23/02Obtaining nickel or cobalt by dry processes
    • C22B23/023Obtaining nickel or cobalt by dry processes with formation of ferro-nickel or ferro-cobalt
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/06Ferrous alloys, e.g. steel alloys containing aluminium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/18Ferrous alloys, e.g. steel alloys containing chromium
    • C22C38/34Ferrous alloys, e.g. steel alloys containing chromium with more than 1.5% by weight of silicon
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/18Ferrous alloys, e.g. steel alloys containing chromium
    • C22C38/40Ferrous alloys, e.g. steel alloys containing chromium with nickel
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22CALLOYS
    • C22C38/00Ferrous alloys, e.g. steel alloys
    • C22C38/60Ferrous alloys, e.g. steel alloys containing lead, selenium, tellurium, or antimony, or more than 0.04% by weight of sulfur
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/24Binding; Briquetting ; Granulating
    • C22B1/2413Binding; Briquetting ; Granulating enduration of pellets

Definitions

  • the present invention relates to a method of blast-furnace smelting, more particularly to a metallurgical method of ferronickel production by blast-furnace smelting nickel oxide ore with crystal water.
  • Blast-furnace smelting may also be used, however, because Cr 2 O 3 as concomitant commonly exists in laterite nickel ore, extremely high melting point of its own can lead to large viscosity of molten iron so that molten iron containing nickel and chrome can't flow out successfully and cause severe results such as frozen furnace and damaged furnace.
  • ferronickel nickel iron
  • Patent application JP 58-213837 A discloses a metallurgical method to obtain sintering of chrome in short-time, by blending fine chrome ore, coke breeze and return ore as principal starting materials with suitable amounts of secondary starting materials such as powdered limestone and silica sand, and possibly fluorite, to prepare a starting material to be sintered.
  • the present invention provides a metallurgical method of ferronickel by blast-furnace smelting nickel oxide ore containing crystal water in one-step way.
  • the invention provides a metallurgical method of ferronickel production according to claim 1.
  • the metallurgical method of ferronickel production by blast-furnace smelting nickel oxide ore with crystal water in the present invention further includes the following steps:
  • the preferable weight ratio of the additives to the sintered ore is: fluorite 0.3 ⁇ 10% dolomite 0.5 ⁇ 5% limestone/calcium lime 8 ⁇ 20%.
  • the content of CaO in limestone is greater than 50%, while that of CaO in calcium lime is greater than 80%; the content of Mg in the dolomite is higher than 10% and that of CaF 2 in fluorite is bigger than 80%.
  • furnace temperature can reach up to about 1700 °C in the conventional blast-furnace smelting technology
  • chrome contained in nickel oxide ore mainly exists in the form of Cr 2 O 3 whose melting point is about 2300° C, consequently, the reduction degree of chrome in nickel oxide ore is limited to cause bad fluidity of the obtained molten iron and easily to produce phenomenon of frozen furnace, and even result in accidents.
  • the metallurgical method of one-step blast-furnace smelting provided by the present invention is characterized by short technical process, high yield of continuous production, total extraction of nickel, chrome and iron in laterite nickel ore once for all, high ratio of resource utilization.
  • the slag obtained by smelting is an excellent raw material to produce concrete, except the exhaustion of a given mass of CO 2 gas, no other solid or liquid wastes are produced and there is no pollution.
  • the metallurgical technology of blast-furnace smelting provided by the present invention has some advantages, for example low cost.
  • Blast furnace in the technology provided by the present invention can consume 150-200 kilowatt-hours per ton iron, while the conventional ore smelting technology need consume 2000-4000 kilowatt-hours and coke of 0.5 ton per ton iron;
  • high yield namely the mean yield of blast furnace is bigger than that of ore-smelting furnace; such as little pollution, little dust, high recovery rate of the raw materials which are respectively 97 ⁇ 98% for iron, 99% for nickel and 40 ⁇ 50% for chrome.
  • Raw ores in examples are selected from nickel and chrome iron ores imported form Bulgaria.
  • the main components in used nickel and chrome iron ore and its content are: components Fe Ni Cr Ca Si Mg Al Series code 1 7.18 4.37 11.93 18.14 21.08 0.84 6.17 2 17.81 3.21 9.26 16.25 18.27 1.18 5.77 3 26.28 2.68 8.10 14.36 17.35 1.45 4.69 4 36.54 2.30 6.32 11.87 16.09 1.64 3.14 5 43.51 1.83 4.71 8.29 15.14 1.94 2.84 6 54.26 0.57 0.35 4.57 5.88 2.11 2.11
  • the main components in obtained sintered ore and its content are: components Fe Ni Cr Ca Si Series code 1 9.01 4.23 10.29 16.17 19.14 2 23.14 3.60 7.39 14.19 16.32 3 33.83 2.97 7.10 13.24 16.10 4 46.83 2.51 5.48 12.31 14.26 5 55.59 2.13 3.62 7.25 4.77 6 65.51 0.63 0.33 3.67 2.59
  • Metallurgical technology parameters of blast furnace items Crucible diameter Vent diameter fan Wind pressure Type code Capacity of blast furnace 36 m 3 2.1 m 75 mm 230 m/s 559.95 kPa (4200 mmHg) Capacity of blast furnace 90 m 3 2.9 m 100 mm 380 m/s 613.28 kPa (4600 mmHg)
  • the main components in the obtained nickel iron by smelting and its content are: components Fe Ni Cr S P Series code 1 48.26 15.10 33.11 0.060 0.061 2 52.31 10.59 23.10 0.059 0.060 3 64.58 8.32 22.38 0.058 0.059 4 75.51 5.98 13.36 0.059 0.062 5 85.29 3.24 7.09 0.057 0.057 6 93.46 0.92 0.63 0.061 0.058

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Description

    Technical field
  • The present invention relates to a method of blast-furnace smelting, more particularly to a metallurgical method of ferronickel production by blast-furnace smelting nickel oxide ore with crystal water.
  • Background of the invention
  • Global extensive uses of stainless steel and special steel lead to supply shortage and rapid rise in price of nickel metal, a main element used to smelt stainless steel and special steel. Conventional technology is mature that nickel metal is produced by mainly extracting from nickel sulfide ore, which covers 30% of the nickel resources on the earth. But at present, reserves are in shortage and resources are in crises after continuous exploitation for nearly one century. People have to pay more attention to the extraction of nickel metal from laterite nickel ore (nickel oxide ore) covering 70% of nickel resources on the earth. The main reason that laterite nickel ore hasn't been exploited on a large scale for a long time is that the technology extracting Ni from such mineral resources is characterized by high cost, technological complexity, low yield, severe pollution. At present, for high-grade laterite nickel ore (nickel content above 2.0%), ore-smelting furnace is generally used to smelt on the international, however, this method is provided with disadvantages such as high power consumption, severe environmental pollution and low yield of intermittent production. For low-grade laterite nickel ore, hydrometallurgy is commonly used, namely, a method of vitriol soaking, i.e. converting solid-state nickel oxide, chromic oxide, ferric oxide or the like in the laterite nickel ore to mixed solution of liquid-state nickel sulfate, chrome sulfate, iron sulfate (Fe2+) and the like, then separating nickel sulfate thereby, forming nickel metal only accounting for 1-2% of the gross by electrolysis with all the other components wasted. The process equipment is characterized by large one-off investment, complex process, long periodicity, severe environmental pollution. Blast-furnace smelting may also be used, however, because Cr2O3 as concomitant commonly exists in laterite nickel ore, extremely high melting point of its own can lead to large viscosity of molten iron so that molten iron containing nickel and chrome can't flow out successfully and cause severe results such as frozen furnace and damaged furnace. Many corporations and research organizations at home and abroad have studied the technology for a long time that ferronickel (nickel iron) can be obtained by blast-furnace smelting laterite nickel ore in one-step way, but hitherto no success is reported.
  • Patent RU 2,157,412 C1 discloses a metallurgical method of ferronickel production by blast-furnace including the preparation of ore, production of sinter and its charging into furnace together with coke, supply of heated air blast and discharge of heat products; in this method, prior to sintering, ore is mixed with hot nickel sinter and fluxed up to basicity CaO/SiO2=0.4-0.6, and Fe/Ni ratio is maintained within 6-12; fluorite is not used in the method of this document.
  • Patent application JP 58-213837 A discloses a metallurgical method to obtain sintering of chrome in short-time, by blending fine chrome ore, coke breeze and return ore as principal starting materials with suitable amounts of secondary starting materials such as powdered limestone and silica sand, and possibly fluorite, to prepare a starting material to be sintered.
  • Consequently, it is urgent problem to be solved in this business to find an industrial method that nickel iron is smelted directly from laterite nickel ore, which is characterized by high efficiency, low consumption, high yield, low cost and no pollution or little pollution.
  • Summary of the invention
  • To solve the above problem, the present invention provides a metallurgical method of ferronickel by blast-furnace smelting nickel oxide ore containing crystal water in one-step way.
  • The above inventive object is achieved by the following technical proposal.
  • The invention provides a metallurgical method of ferronickel production according to claim 1.
  • The metallurgical method of ferronickel production by blast-furnace smelting nickel oxide ore with crystal water in the present invention further includes the following steps:
    • Crushing and sieving the sintered blocks obtained by first sintering by means of a sieve with openings in the range between 25 and 53 µm (300-500 meshes), and then producing refined ore powder by magnetic sorting;
    • Mixing the feed of the refined ore powder with coke powder, calcium lime/limestone and sintering to obtain sintered ore blocks;
    • Mixing the sintered ore blocks obtained by second sintering with coke, lime/limestone, dolomite and fluorite, and then blast-furnace smelting to obtain ferronickel.
  • Wherein the preferable weight ratio of the additives to the sintered ore is:
    fluorite 0.3 ∼ 10%
    dolomite 0.5 ∼ 5%
    limestone/calcium lime 8 ∼ 20%.
  • Wherein the content of CaO in limestone is greater than 50%, while that of CaO in calcium lime is greater than 80%; the content of Mg in the dolomite is higher than 10% and that of CaF2 in fluorite is bigger than 80%.
  • Compared with the prior art, furnace temperature can reach up to about 1700 °C in the conventional blast-furnace smelting technology, chrome contained in nickel oxide ore mainly exists in the form of Cr2O3 whose melting point is about 2300° C, consequently, the reduction degree of chrome in nickel oxide ore is limited to cause bad fluidity of the obtained molten iron and easily to produce phenomenon of frozen furnace, and even result in accidents. In metallurgical method of ferronickel production by smelting nickel and chrome iron ore provided by the present invention, the addition of fluorite can lower the influence of chrome on furnace temperature effectively and raise the fluidity of molten iron, meanwhile, because the addition quantity of fluorite in metallurgical method provided by the present invention is strictly calculated, the accidents, such as burnout of the crucible, caused by too high addition quantity of fluorite, can be effectively avoided. In the metallurgical method provided by the present invention, meanwhile, magnesium contained in dolomite may also be helpful to solve the problem on bad fluidity of molten iron caused by chrome in nickel and chrome ores. Limestone can not only provide alkalinity, but also can balance the above two additives. The metallurgical method of one-step blast-furnace smelting provided by the present invention is characterized by short technical process, high yield of continuous production, total extraction of nickel, chrome and iron in laterite nickel ore once for all, high ratio of resource utilization. The slag obtained by smelting is an excellent raw material to produce concrete, except the exhaustion of a given mass of CO2 gas, no other solid or liquid wastes are produced and there is no pollution.
  • By contrast, the metallurgical technology of blast-furnace smelting provided by the present invention has some advantages, for example low cost. Blast furnace in the technology provided by the present invention can consume 150-200 kilowatt-hours per ton iron, while the conventional ore smelting technology need consume 2000-4000 kilowatt-hours and coke of 0.5 ton per ton iron; For example economic resources, high yield, namely the mean yield of blast furnace is bigger than that of ore-smelting furnace; such as little pollution, little dust, high recovery rate of the raw materials which are respectively 97 ∼ 98% for iron, 99% for nickel and 40 ∼ 50% for chrome.
  • Specific embodiment:
  • The present invention can further be explained and described in combination with specific examples below.
  • Raw ores in examples are selected from nickel and chrome iron ores imported form Albania.
  • Crushing and sieving raw ores, mixing the feed of ore powder in grain diameter smaller than 2 mm thereof with coke powder, calcium lime/limestone and sintering to obtain sintered ore blocks;
  • Crushing and sieving the sintered blocks obtained by first sintering by means of a sieve with openings in the range between 25 and 53 µm (300-500 meshes) and then magnetic sorting to obtain refined ore powder.
  • Mixing the feed of the refined ore powder with coke powder, calcium lime/limestone and sintering to obtain sintered ore blocks.
  • Mixing sintered ore of the sintered ore blocks in particulate diameter of 10-50 mm with other raw materials and smelting to obtain ferronickel.
  • The main components in used nickel and chrome iron ore and its content (wt.%) are:
    components Fe Ni Cr Ca Si Mg Al
    Series code
    1 7.18 4.37 11.93 18.14 21.08 0.84 6.17
    2 17.81 3.21 9.26 16.25 18.27 1.18 5.77
    3 26.28 2.68 8.10 14.36 17.35 1.45 4.69
    4 36.54 2.30 6.32 11.87 16.09 1.64 3.14
    5 43.51 1.83 4.71 8.29 15.14 1.94 2.84
    6 54.26 0.57 0.35 4.57 5.88 2.11 2.11
  • The main components in obtained sintered ore and its content (wt.%) are:
    components Fe Ni Cr Ca Si
    Series code
    1 9.01 4.23 10.29 16.17 19.14
    2 23.14 3.60 7.39 14.19 16.32
    3 33.83 2.97 7.10 13.24 16.10
    4 46.83 2.51 5.48 12.31 14.26
    5 55.59 2.13 3.62 7.25 4.77
    6 65.51 0.63 0.33 3.67 2.59
  • Constitution of the furnace materials (Weight: Kg) is shown in following table.
    Components Sintered ore coke fluorite dolomite limestone/ calcium lime
    Series code
    1 1000 455 200 80 350
    2 1000 415 170 70 300
    3 1500 680 240 90 300
    4 1500 625 150 75 150
    5 2000 920 100 20 160
    6 2000 830 6 - 80
  • Metallurgical technology parameters of blast furnace:
    items Crucible diameter Vent diameter fan Wind pressure
    Type code
    Capacity of blast furnace 36 m3 2.1 m 75 mm 230 m/s 559.95 kPa (4200 mmHg)
    Capacity of blast furnace 90 m3 2.9 m 100 mm 380 m/s 613.28 kPa (4600 mmHg)
  • The main components in the obtained nickel iron by smelting and its content (wt.%) are:
    components Fe Ni Cr S P
    Series code
    1 48.26 15.10 33.11 0.060 0.061
    2 52.31 10.59 23.10 0.059 0.060
    3 64.58 8.32 22.38 0.058 0.059
    4 75.51 5.98 13.36 0.059 0.062
    5 85.29 3.24 7.09 0.057 0.057
    6 93.46 0.92 0.63 0.061 0.058

Claims (6)

  1. A metallurgical method of ferronickel production by blast-furnace smelting nickel oxide ore with crystal water containing from 0.5% to 4% by weight of nickel, from 0.3% to 12% by weight of chromium, and from 7% to 55% by weight of iron, wherein the said method of blast- furnace smelting mainly comprising the following steps:
    Crushing and sieving raw ores, mixing the feed of ore powder in grain diameter smaller than 2 mm thereof with coke powder, calcium lime/limestone and sintering to obtain sintered ore blocks;
    Mixing sintered ore blocks, coke, limestone/calcium lime, dolomite and fluorite and blast-furnace smelting to obtain ferronickel; wherein the weight ratio of the following additives to sintered ore is:
    fluorite 0.3∼20%
    dolomite 0.5∼8%
    limestone/calcium lime 4∼35%.
  2. The metallurgical method according to Claim 1, wherein the blast furnace smelting further comprising the following steps:
    Crushing and sieving the sintered blocks obtained by first sintering by means of a sieve with openings in the range between 25 an 53 µm (in 300-500 meshes) and then producing refined ore powder by magnetic sorting; Mixing the feed of the refined ore powder with coke powder, calcium lime/limestone and sintering to obtain sintered ore blocks;
    Mixing the sintered ore blocks obtained by second sintering with coke, lime/limestone, dolomite and fluorite, and then blast-furnace smelting to obtain ferronickel.
  3. The metallurgical method according to Claim 1 or 2, wherein the preferable weight ratio of the said additives to the sintered ore is:
    fluorite 0.3∼10%
    dolomite 0.5∼5%
    limestone/calcium lime 8∼20%.
  4. The metallurgical method according to Claim 1 or 2, wherein the content of CaO in the limestone is greater than 50% ,while that of CaO in calcium lime is greater than 80%.
  5. The metallurgical method according to Claim 1 or 2, wherein the content of Mg in the dolomite is higher than 10%.
  6. The metallurgical method according to Claim 1 or 2, wherein the content of CaF2 in the fluorite is bigger than 80%.
EP05801995.1A 2005-09-16 2005-11-02 A smelting process of ferronickel with nickel oxide ore containing of crystal water in a blast furnace Not-in-force EP1927666B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CNB200510102985XA CN1300352C (en) 2005-09-16 2005-09-16 Nickel-iron smelting process from nickel oxide ore containing crystal water through blast furnace
PCT/CN2005/001828 WO2006045254A1 (en) 2005-09-16 2005-11-02 A smelting process of ferronickel with nickel oxide ore containing of crystal water in a blast furnace

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EP1927666A1 EP1927666A1 (en) 2008-06-04
EP1927666A4 EP1927666A4 (en) 2008-12-03
EP1927666B1 true EP1927666B1 (en) 2013-04-24

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EP (1) EP1927666B1 (en)
JP (1) JP4734415B2 (en)
KR (2) KR20070085068A (en)
CN (1) CN1300352C (en)
AU (1) AU2005299184B2 (en)
MY (1) MY147763A (en)
WO (1) WO2006045254A1 (en)

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CN100532579C (en) * 2007-04-30 2009-08-26 郑州永通特钢有限公司 Method for smelting base material of low phosphorous stainless steel by using low-grade limonite containing nickel-chromium
JP5194111B2 (en) * 2007-05-11 2013-05-08 ポスコ Method for producing molten iron containing nickel
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KR101322898B1 (en) * 2007-05-11 2013-10-29 주식회사 포스코 Method for manufacturing molten irons comprising nickels
KR100948926B1 (en) 2007-07-23 2010-03-24 주식회사 포스코 Method for manufacturing molten iron comprising nickel
CN100478477C (en) * 2007-07-09 2009-04-15 贵研铂业股份有限公司 Method for extracting nickel iron alloy from laterite ore
CN101638730B (en) * 2008-07-31 2015-03-25 塔塔钢铁有限公司 Method for producing sponge chromium from metallurgical-grade chromite concentrate fine powder
CN101792866B (en) * 2010-03-26 2011-08-03 常州市兴昌盛合金制品有限公司 Method for refining ferronickel by utilizing waste alumina-based nickel accelerant
CN102212691A (en) * 2011-05-20 2011-10-12 营口宝成不锈钢有限公司 Method for producing chromium-nickel-iron alloy
KR101359970B1 (en) * 2011-12-20 2014-02-12 주식회사 포스코 Recycling method of ferro nickel slag
CN102719582B (en) * 2012-07-03 2014-10-29 刘光火 Process for smelting low-quality complex ore
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CN103103366B (en) * 2013-02-20 2014-07-16 罕王实业集团有限公司 Method for controlling energy saving and environment protecting laterite nickel ore smelting shaft furnace temperature by silicothermic process
JP5991290B2 (en) * 2013-09-13 2016-09-14 Jfeスチール株式会社 Method for producing sintered ore
CN103740933B (en) * 2014-01-24 2015-12-02 温德昌 A kind of method of nickel oxide material production Rhometal
CN105909679A (en) * 2016-06-18 2016-08-31 中山市盈科轴承制造有限公司 Multi-wedge pulley type double-row angular contact ball bearing with DLC coating
CN111663034B (en) * 2020-06-28 2022-10-14 宝钢德盛不锈钢有限公司 Low-cost blast furnace molten iron production process
CN111763823B (en) * 2020-08-26 2022-05-20 甘肃高能中色环保科技有限公司 Method for producing sintered cake from complex nickel-containing wet material
CN112573842B (en) * 2020-12-29 2022-04-22 中国水利水电第九工程局有限公司 Method for preparing ingredients for cement production by using limestone mine tailing dolomite

Family Cites Families (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
SE354297B (en) * 1971-07-16 1973-03-05 Avesta Jernverks Ab
US3746533A (en) * 1972-03-22 1973-07-17 L Moussoulos Process of producing ferro-nickel in a rotary furnace including pelletizing and pre-reducing ore
JPS597770B2 (en) 1983-05-12 1984-02-21 日新製鋼株式会社 Chrome ore sintering method
JPS62290842A (en) * 1986-06-10 1987-12-17 Nippon Kokan Kk <Nkk> Manufacture of ferronickel
JPS62290843A (en) * 1986-06-10 1987-12-17 Nippon Kokan Kk <Nkk> Production of ferronickel
AUPN639995A0 (en) * 1995-11-03 1995-11-30 Technological Resources Pty Limited A method and an apparatus for producing metals and metal alloys
RU2132400C1 (en) * 1998-09-03 1999-06-27 Открытое акционерное общество "Серовский металлургический завод" Method of processing oxidized nickel ores
RU2157412C1 (en) * 1999-04-19 2000-10-10 ЗАО "Научно-производственное предприятие ФАН" Method of production of blast-furnace ferronickel
CN1237641A (en) * 1999-06-15 1999-12-08 吉林省冶金研究院 Technological process for extracting Ni, Cu, Co and Mg from nickel sulfide preparation concentrate and making nickelferrite
JP2001303113A (en) * 2000-04-26 2001-10-31 Mitsui Matsushima Co Ltd METHOD FOR UTILIZING COAL HAVING MUCH CaO COMPONENT AND Fe2O3 COMPONENT IN BURNT ASH
US6903585B2 (en) * 2003-06-27 2005-06-07 Analog Devices, Inc. Pulse width modulated common mode feedback loop and method for differential charge pump
CN1257295C (en) * 2004-11-15 2006-05-24 四川川投峨眉铁合金(集团)有限责任公司 Production method for extracting nickel by pyrogenic process

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CN1743476A (en) 2006-03-08
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JP4734415B2 (en) 2011-07-27
KR20100039907A (en) 2010-04-16
AU2005299184B2 (en) 2009-06-04
MY147763A (en) 2013-01-31
WO2006045254A1 (en) 2006-05-04
KR20070085068A (en) 2007-08-27
CN1300352C (en) 2007-02-14
AU2005299184A1 (en) 2006-05-04
JP2009508005A (en) 2009-02-26

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