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 PDFInfo
- 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
- Authority
- EP
- European Patent Office
- Prior art keywords
- ore
- limestone
- blast
- fluorite
- nickel
- 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.)
- Not-in-force
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/002—Ferrous alloys, e.g. steel alloys containing In, Mg, or other elements not provided for in one single group C22C38/001 - C22C38/60
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B5/00—Making pig-iron in the blast furnace
- C21B5/02—Making special pig-iron, e.g. by applying additives, e.g. oxides of other metals
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B3/00—General features in the manufacture of pig-iron
- C21B3/02—General features in the manufacture of pig-iron by applying additives, e.g. fluxing agents
-
- 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
-
- 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
- C22B1/16—Sintering; Agglomerating
-
- 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
- C22B23/00—Obtaining nickel or cobalt
- C22B23/005—Preliminary treatment of ores, e.g. by roasting or by the Krupp-Renn process
-
- 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
- C22B23/00—Obtaining nickel or cobalt
- C22B23/02—Obtaining nickel or cobalt by dry processes
- C22B23/023—Obtaining nickel or cobalt by dry processes with formation of ferro-nickel or ferro-cobalt
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/06—Ferrous alloys, e.g. steel alloys containing aluminium
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/18—Ferrous alloys, e.g. steel alloys containing chromium
- C22C38/34—Ferrous alloys, e.g. steel alloys containing chromium with more than 1.5% by weight of silicon
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/18—Ferrous alloys, e.g. steel alloys containing chromium
- C22C38/40—Ferrous alloys, e.g. steel alloys containing chromium with nickel
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22C—ALLOYS
- C22C38/00—Ferrous alloys, e.g. steel alloys
- C22C38/60—Ferrous alloys, e.g. steel alloys containing lead, selenium, tellurium, or antimony, or more than 0.04% by weight of sulfur
-
- 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
- C22B1/2413—Binding; 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
Landscapes
- 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
- 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.
- 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 - Patent application
JP 58-213837 A - 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.
- 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.
- 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)
- 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%.
- 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.
- 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%.
- 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%.
- The metallurgical method according to Claim 1 or 2, wherein the content of Mg in the dolomite is higher than 10%.
- The metallurgical method according to Claim 1 or 2, wherein the content of CaF2 in the fluorite is bigger than 80%.
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 |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1927666A1 EP1927666A1 (en) | 2008-06-04 |
EP1927666A4 EP1927666A4 (en) | 2008-12-03 |
EP1927666B1 true EP1927666B1 (en) | 2013-04-24 |
Family
ID=36139000
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP05801995.1A Not-in-force EP1927666B1 (en) | 2005-09-16 | 2005-11-02 | A smelting process of ferronickel with nickel oxide ore containing of crystal water in a blast furnace |
Country Status (7)
Country | Link |
---|---|
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) |
Families Citing this family (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101020943A (en) * | 2006-07-12 | 2007-08-22 | 刘光火 | Phosphorus reducing method for process of smelting Ni-Cr pig iron with nickel oxide ore |
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 |
KR101322897B1 (en) | 2007-05-11 | 2013-10-29 | 주식회사 포스코 | Method for manufacturing molten irons comprising nickels |
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 |
KR101536745B1 (en) * | 2012-12-28 | 2015-07-15 | 재단법인 포항산업과학연구원 | Material for smelting magnesium |
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)
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 |
-
2005
- 2005-09-16 CN CNB200510102985XA patent/CN1300352C/en not_active Ceased
- 2005-11-02 KR KR1020067017163A patent/KR20070085068A/en active Application Filing
- 2005-11-02 KR KR1020107006683A patent/KR20100039907A/en not_active Application Discontinuation
- 2005-11-02 AU AU2005299184A patent/AU2005299184B2/en not_active Ceased
- 2005-11-02 JP JP2008530297A patent/JP4734415B2/en not_active Expired - Fee Related
- 2005-11-02 WO PCT/CN2005/001828 patent/WO2006045254A1/en active Application Filing
- 2005-11-02 EP EP05801995.1A patent/EP1927666B1/en not_active Not-in-force
-
2006
- 2006-10-10 MY MYPI20064303A patent/MY147763A/en unknown
Also Published As
Publication number | Publication date |
---|---|
EP1927666A4 (en) | 2008-12-03 |
CN1743476A (en) | 2006-03-08 |
EP1927666A1 (en) | 2008-06-04 |
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP1927666B1 (en) | A smelting process of ferronickel with nickel oxide ore containing of crystal water in a blast furnace | |
EP1927667B1 (en) | A smelting process of ferronickel with nickel oxide ore free of crystal water in a blast furnace | |
CN102352423B (en) | Method for selecting and smelting titanium from vanadium titanomagnetite at low temperature | |
CN100532579C (en) | Method for smelting base material of low phosphorous stainless steel by using low-grade limonite containing nickel-chromium | |
CN100507013C (en) | Method for directly producing ferrochromium from chrome ore powder and coal | |
CN100485071C (en) | Electric furnace smelting recovery method for chronium-nickel alloy element in stainless steel dedusting ash | |
CN101748298B (en) | Method for treating laterite nickel ore and producing ferronickel by combining tunnel kiln prereduction and melting furnace final reduction | |
CN1847440A (en) | Nickel-chromium-iron alloy and production method thereof | |
CN110669980B (en) | Preparation method of stainless steel 3D printing powder and product thereof | |
CN102337408B (en) | Two-step reduction method for recycling stainless steel scales | |
CN103556068A (en) | Method for producing weather-resisting steel by using low-grade nickel ores | |
CN101875987A (en) | Method for smelting low chromium pig iron by utilizing chromium slag | |
CN1312307C (en) | Mangan-alloy production | |
CN101886231A (en) | Method for manufacturing nickel iron alloy | |
CN105821281B (en) | A kind of direct steelmaking metal of alloying oxide core-spun yarn and preparation method thereof | |
CN109971948B (en) | Method for recovering iron, copper and manganese by co-reduction of copper smelting slag and ferromanganese ore | |
TW201400624A (en) | Method for producing austenitic stainless steel with nickel and chromium ore | |
CN109457117A (en) | A kind of method of valuable constituent element comprehensive reutilization in steel slag | |
CN108796236A (en) | A kind of method of valuable constituent element comprehensive reutilization in copper ashes | |
CN101338373B (en) | Method for producing smelting copper-cobalt oxidation ore by blast furnace | |
CN107262731A (en) | A kind of method that stocking/component of machine product is forged in powdery iron ore DRI hot pressing | |
CN100352949C (en) | Smelting technology of weather resistant steel | |
CN1313407A (en) | Process for preparing Cr-contained sintered ore of blast furnace from powdered chromium ore and Fe-contained raw material | |
CN107881399A (en) | A kind of system and method for producing high phosphorus weathering steel | |
CN207877839U (en) | A kind of system producing high phosphorus weathering steel |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20080411 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR |
|
A4 | Supplementary search report drawn up and despatched |
Effective date: 20081103 |
|
17Q | First examination report despatched |
Effective date: 20090220 |
|
DAX | Request for extension of the european patent (deleted) | ||
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU LV MC NL PL PT RO SE SI SK TR |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: REF Ref document number: 608700 Country of ref document: AT Kind code of ref document: T Effective date: 20130515 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R096 Ref document number: 602005039291 Country of ref document: DE Effective date: 20130627 |
|
REG | Reference to a national code |
Ref country code: AT Ref legal event code: MK05 Ref document number: 608700 Country of ref document: AT Kind code of ref document: T Effective date: 20130424 |
|
REG | Reference to a national code |
Ref country code: LT Ref legal event code: MG4D |
|
REG | Reference to a national code |
Ref country code: NL Ref legal event code: VDEP Effective date: 20130424 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IS Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130824 Ref country code: LT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: BE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: AT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130804 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130826 Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: SI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130725 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BG Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130724 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: PL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: LV Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: EE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: CZ Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: SK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: RO Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 Ref country code: NL Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed |
Effective date: 20140127 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R097 Ref document number: 602005039291 Country of ref document: DE Effective date: 20140127 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20131102 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131130 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131130 Ref country code: MC Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20140731 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: MM4A |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R119 Ref document number: 602005039291 Country of ref document: DE Effective date: 20140603 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20140603 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131102 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131102 Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131202 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: TR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20130424 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20131102 Ref country code: HU Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO Effective date: 20051102 |