EP1927667A1 - Verhüttungsverfahren für ferronickel mit kristallwasserfreiem nickeloxiderz in einem hochofen - Google Patents
Verhüttungsverfahren für ferronickel mit kristallwasserfreiem nickeloxiderz in einem hochofen Download PDFInfo
- Publication number
- EP1927667A1 EP1927667A1 EP05803616A EP05803616A EP1927667A1 EP 1927667 A1 EP1927667 A1 EP 1927667A1 EP 05803616 A EP05803616 A EP 05803616A EP 05803616 A EP05803616 A EP 05803616A EP 1927667 A1 EP1927667 A1 EP 1927667A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- ore
- limestone
- dolomite
- ferronickel
- sintered ore
- 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.)
- Granted
Links
Classifications
-
- 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
- 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
-
- 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
- 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
- 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
Definitions
- the present invention relates to a method of blast-furnace smelting, more particularly to a metallurgical method of ferronickel by blast-furnace smelting nickel oxide ore without crystal water.
- hydrometallurgy For low-grade laterite nickel ore, hydrometallurgy is commonly used, namely, a method of vitriol soaking, ie 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, ferrite sulfate (Fe 2+ ) 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 use, however, because Cr 2 0 3 as concomitant commonly exists in laterite nickel ore, extremely high melting point of its own can lead to large viscosity of molten iron water so that iron water containing nickel and chrome can't flow out successfully and cause severe results such as frozen furnace and damaged furnace.
- ferronickel nickel iron
- the present invention provides a metallurgical method of ferronickel by blast-furnace smelting nickel oxide ore containing no crystal water in one-step way.
- the invention provides a metallurgical method of ferronickel by blast-furnace smelting nickel oxide ore containing no crystal water, mainly comprising the steps as follows:
- the raw ore block may not be added as metallurgical raw material in smelting steps.
- nickel oxide ore and the weight ratio of its own are: Nickel: 0.5 ⁇ 4.5%; Chrome: 0.3 ⁇ 12%; iron: 38 ⁇ 55%.
- the preferable weight ratio of the additives to the sintered ore is: fluorite 0.3 ⁇ 5% dolomite 0.5 ⁇ 5% limestone/calcium lime 8 ⁇ 15%.
- 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 in dolomite 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 iron water 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.
- Sintered ore and other raw materials can be mixed and smelted, wherein the sintered ore and raw ore may be combined in any proportions and also used in total sintered ore or total raw ore.
- the ratio of ore stone to coke is 1.9-2.1:1, when sintered ore is used as the total, that ratio of ore to coke is 2.2-2.4:1.
- the main component in used nickel and chrome iron ore and its content (wt.%) are:
- the main component in obtained sintered ore and its content (wt.%) are:
- the main component in the obtained nickel iron by smelting and its content (wt.%) are:
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (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)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2005101029845A CN1306049C (zh) | 2005-09-16 | 2005-09-16 | 不含结晶水的氧化镍矿经高炉冶炼镍铁工艺 |
PCT/CN2005/001827 WO2006050658A1 (fr) | 2005-09-16 | 2005-11-02 | Procede de preparation de ferronickel par fusion en haut fourneau de minerai d’oxyde de nickel depourvu d’eau cristalline |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1927667A1 true EP1927667A1 (de) | 2008-06-04 |
EP1927667A4 EP1927667A4 (de) | 2008-11-05 |
EP1927667B1 EP1927667B1 (de) | 2013-06-19 |
Family
ID=36076566
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP05803616.1A Not-in-force EP1927667B1 (de) | 2005-09-16 | 2005-11-02 | Verhüttungsverfahren für ferronickel mit kristallwasserfreiem nickeloxiderz in einem hochofen |
Country Status (7)
Country | Link |
---|---|
EP (1) | EP1927667B1 (de) |
JP (1) | JP4734414B2 (de) |
KR (2) | KR20070085069A (de) |
CN (1) | CN1306049C (de) |
AU (1) | AU2005304190B2 (de) |
MY (1) | MY140939A (de) |
WO (1) | WO2006050658A1 (de) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009052580A1 (en) * | 2007-10-26 | 2009-04-30 | Bhp Billiton Innovation Pty Ltd | Production of nickel |
WO2012172168A1 (en) * | 2011-06-13 | 2012-12-20 | Outokumpu Oyj | Method for improving the reduction degree in the smelting of ferroalloy |
WO2015092132A1 (en) * | 2013-12-17 | 2015-06-25 | Outotec (Finland) Oy | Method for exploiting dusts generated in a ferronickel process and sintered pellets produced by the method |
NO20170743A1 (en) * | 2017-05-05 | 2018-11-06 | Knut Henriksen | Method for converting a waste material from sulphide ore based nickel refining into nickel pig iron |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100595290C (zh) * | 2006-09-06 | 2010-03-24 | 刘光火 | 氧化镍矿经电炉冶炼镍铬钴铁工艺 |
KR101322898B1 (ko) * | 2007-05-11 | 2013-10-29 | 주식회사 포스코 | 니켈 함유 용철의 제조 방법 |
KR101322897B1 (ko) | 2007-05-11 | 2013-10-29 | 주식회사 포스코 | 니켈 함유 용철의 제조 방법 |
KR100948926B1 (ko) | 2007-07-23 | 2010-03-24 | 주식회사 포스코 | 니켈 함유 용철의 제조 방법 |
WO2008140226A1 (en) * | 2007-05-11 | 2008-11-20 | Posco | Method for manufacturing molten iron comprising nickel |
CN101353708B (zh) * | 2008-09-11 | 2010-06-02 | 张家港浦项不锈钢有限公司 | 以氧化镍矿和不锈钢生产废弃物为原料的镍铁冶炼工艺 |
KR101009034B1 (ko) * | 2008-09-19 | 2011-01-17 | 주식회사 포스코 | 페로니켈의 제조 방법 |
CN101392331B (zh) * | 2008-10-10 | 2010-08-25 | 建德市新安江镍合金有限公司 | 回转窑处理镍矿的冶炼工艺 |
CN102212681B (zh) * | 2010-12-27 | 2013-03-27 | 池州市润鹏冶金科技有限公司 | 烧结增效剂及其使用方法 |
CN102650002A (zh) * | 2011-02-25 | 2012-08-29 | 云南锡业集团(控股)有限责任公司 | 改进的红土镍矿冶炼镍铁或镍锍的方法 |
CN102965521B (zh) * | 2012-11-26 | 2013-11-20 | 罕王实业集团有限公司 | 一种采用湿球入炉低温还原方式冶炼红土镍矿的方法 |
CN103131872B (zh) * | 2013-02-20 | 2015-06-03 | 罕王实业集团有限公司 | 一种铝热法控制节能环保红土镍矿冶炼竖炉温度的方法 |
CN103773948B (zh) * | 2014-01-30 | 2015-08-26 | 首钢总公司 | 一种在炼铁系统中使用铁矿粉的方法 |
CN104060084A (zh) * | 2014-05-08 | 2014-09-24 | 无锡市阳泰冶金炉料有限公司 | 含镍贫铬铁矿分离富集冶炼方法 |
CN104911288B (zh) * | 2015-04-14 | 2017-09-29 | 四川金广实业(集团)股份有限公司 | 降低炉渣氧化镁含量的高炉冶炼红土镍矿方法 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1290436A (de) * | 1969-04-30 | 1972-09-27 | ||
GB1400505A (en) * | 1971-07-16 | 1975-07-16 | Avesta Jernverks Ab | Process for treatment of oxidic nickel ores |
JPS62290843A (ja) * | 1986-06-10 | 1987-12-17 | Nippon Kokan Kk <Nkk> | フェロニッケルの製造方法 |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62290842A (ja) * | 1986-06-10 | 1987-12-17 | Nippon Kokan Kk <Nkk> | フェロニッケルの製造方法 |
AUPN639995A0 (en) * | 1995-11-03 | 1995-11-30 | Technological Resources Pty Limited | A method and an apparatus for producing metals and metal alloys |
RU2132400C1 (ru) * | 1998-09-03 | 1999-06-27 | Открытое акционерное общество "Серовский металлургический завод" | Способ переработки окисленных никелевых руд |
RU2157412C1 (ru) * | 1999-04-19 | 2000-10-10 | ЗАО "Научно-производственное предприятие ФАН" | Способ получения доменного ферроникеля |
CN1237641A (zh) * | 1999-06-15 | 1999-12-08 | 吉林省冶金研究院 | 由硫化镍精矿中提取镍、铜、钴、镁及制造镍铁的工艺 |
JP2001303113A (ja) * | 2000-04-26 | 2001-10-31 | Mitsui Matsushima Co Ltd | 燃焼灰成分においてCaO成分とFe2O3成分とが多い石炭の利用方法 |
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 (zh) * | 2004-11-15 | 2006-05-24 | 四川川投峨眉铁合金(集团)有限责任公司 | 一种火法提取镍的生产方法 |
-
2005
- 2005-09-16 CN CNB2005101029845A patent/CN1306049C/zh not_active Expired - Fee Related
- 2005-11-02 JP JP2008530296A patent/JP4734414B2/ja not_active Expired - Fee Related
- 2005-11-02 KR KR1020067017169A patent/KR20070085069A/ko active Application Filing
- 2005-11-02 KR KR1020107006684A patent/KR20100039908A/ko not_active Application Discontinuation
- 2005-11-02 WO PCT/CN2005/001827 patent/WO2006050658A1/zh active Application Filing
- 2005-11-02 EP EP05803616.1A patent/EP1927667B1/de not_active Not-in-force
- 2005-11-02 AU AU2005304190A patent/AU2005304190B2/en not_active Ceased
-
2006
- 2006-10-10 MY MYPI20064302A patent/MY140939A/en unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1290436A (de) * | 1969-04-30 | 1972-09-27 | ||
GB1400505A (en) * | 1971-07-16 | 1975-07-16 | Avesta Jernverks Ab | Process for treatment of oxidic nickel ores |
JPS62290843A (ja) * | 1986-06-10 | 1987-12-17 | Nippon Kokan Kk <Nkk> | フェロニッケルの製造方法 |
Non-Patent Citations (1)
Title |
---|
See also references of WO2006050658A1 * |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009052580A1 (en) * | 2007-10-26 | 2009-04-30 | Bhp Billiton Innovation Pty Ltd | Production of nickel |
AU2008316326B2 (en) * | 2007-10-26 | 2013-06-20 | Bhp Billiton Innovation Pty Ltd | Production of nickel |
WO2012172168A1 (en) * | 2011-06-13 | 2012-12-20 | Outokumpu Oyj | Method for improving the reduction degree in the smelting of ferroalloy |
WO2015092132A1 (en) * | 2013-12-17 | 2015-06-25 | Outotec (Finland) Oy | Method for exploiting dusts generated in a ferronickel process and sintered pellets produced by the method |
CN105829552A (zh) * | 2013-12-17 | 2016-08-03 | 奥图泰(芬兰)公司 | 利用在镍铁合金工艺中产生的粉尘的方法以及通过该方法生产的烧结球团 |
EA032170B1 (ru) * | 2013-12-17 | 2019-04-30 | Оутотек (Финлэнд) Ой | Способ применения пыли, образованной в процессе получения ферроникеля, и спеченные окатыши, полученные данным способом |
NO20170743A1 (en) * | 2017-05-05 | 2018-11-06 | Knut Henriksen | Method for converting a waste material from sulphide ore based nickel refining into nickel pig iron |
NO346383B1 (en) * | 2017-05-05 | 2022-07-04 | Knut Henriksen | Method for converting a waste material from sulphide ore based nickel refining into nickel pig iron |
Also Published As
Publication number | Publication date |
---|---|
JP4734414B2 (ja) | 2011-07-27 |
EP1927667A4 (de) | 2008-11-05 |
AU2005304190B2 (en) | 2009-09-17 |
EP1927667B1 (de) | 2013-06-19 |
CN1306049C (zh) | 2007-03-21 |
KR20100039908A (ko) | 2010-04-16 |
KR20070085069A (ko) | 2007-08-27 |
AU2005304190A1 (en) | 2006-05-18 |
MY140939A (en) | 2010-02-12 |
JP2009508004A (ja) | 2009-02-26 |
CN1733950A (zh) | 2006-02-15 |
WO2006050658A1 (fr) | 2006-05-18 |
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