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RU2000110625A - DIRECT MELTING METHOD FOR PRODUCING METAL FROM METAL OXIDES - Google Patents

DIRECT MELTING METHOD FOR PRODUCING METAL FROM METAL OXIDES

Info

Publication number
RU2000110625A
RU2000110625A RU2000110625/02A RU2000110625A RU2000110625A RU 2000110625 A RU2000110625 A RU 2000110625A RU 2000110625/02 A RU2000110625/02 A RU 2000110625/02A RU 2000110625 A RU2000110625 A RU 2000110625A RU 2000110625 A RU2000110625 A RU 2000110625A
Authority
RU
Russia
Prior art keywords
metal
carbon
metal layer
layer
weight
Prior art date
Application number
RU2000110625/02A
Other languages
Russian (ru)
Other versions
RU2199591C2 (en
Inventor
Родни Джеймс Драй
Original Assignee
Текнолоджикал Ресорсиз Пти. Лтд.
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Priority claimed from AUPO9446A external-priority patent/AUPO944697A0/en
Application filed by Текнолоджикал Ресорсиз Пти. Лтд. filed Critical Текнолоджикал Ресорсиз Пти. Лтд.
Publication of RU2000110625A publication Critical patent/RU2000110625A/en
Application granted granted Critical
Publication of RU2199591C2 publication Critical patent/RU2199591C2/en

Links

Claims (10)

1. Способ прямого плавления для получения металлов из оксидов металлов (включая частично восстановленные оксиды металлов), содержащий следующие стадии: (a) образование ванны расплава, имеющей слой металла и слой шлака над слоем металла в металлургической емкости; (b) введение содержащего металл исходного сырья в слой металла через один или несколько каналов/фурм и плавление содержащего металл сырья до получения металла преимущественно, по меньшей мере, в виде слоя металла; (c) введение твердого углеродсодержащего материала в слой металла через один или несколько каналов/фурм в количестве, необходимом, чтобы уровень растворенного в металле углерода составлял, по меньшей мере, 3% по отношению к суммарному весу углерода и металла; (d) обеспечение выброса кверху брызг, капель и струй расплавленного материала из слоя металла ванны расплава, который: (i) позволяет получить интенсивное подмешивание металла в слой шлака ванны расплава, чтобы поддерживать в слое шлака условия активного восстановления, приводящие к достижению уровня FeO ниже 8% по отношению к полному весу шлака в слое шлака; и (ii) распространяет их в пространстве над номинально спокойной поверхностью ванны расплава для образования переходной зоны; и (е) введение содержащего кислород газа в емкость через один или несколько каналов/фурм для дожигания реакционных газов, выходящих из ванны расплава, благодаря чему происходит выброс вверх, а затем падение вниз брызг, капель и струй расплавленного материала в переходной зоне, что облегчает передачу тепла в ванну расплава и снижает потери тепла из емкости через боковые стенки в контакте с переходной зоной.1. A direct melting method for producing metals from metal oxides (including partially reduced metal oxides), comprising the following steps: (a) forming a molten bath having a metal layer and a slag layer above the metal layer in a metallurgical vessel; (b) introducing the metal-containing feedstock into the metal layer through one or more channels / tuyeres and melting the metal-containing raw material to obtain the metal, preferably at least as a metal layer; (c) introducing solid carbon-containing material into the metal layer through one or more channels / tuyeres in an amount necessary for the level of carbon dissolved in the metal to be at least 3% with respect to the total weight of carbon and metal; (d) providing upward discharge of splashes, drops and jets of molten material from the melt bath metal layer, which: (i) allows intensive mixing of the metal into the melt bath slag layer in order to maintain active reduction conditions in the slag layer, leading to lower FeO levels 8% with respect to the total weight of the slag in the slag layer; and (ii) distributes them in the space above the nominally calm surface of the melt pool to form a transition zone; and (e) introducing oxygen-containing gas into the vessel through one or more channels / tuyeres for burning off the reaction gases leaving the melt pool, whereby upward discharge and then downward spraying, droplets and jets of molten material in the transition zone occur, which facilitates heat transfer to the molten bath and reduces heat loss from the tank through the side walls in contact with the transition zone. 2. Способ по п. 1, отличающийся тем, что уровень растворенного в металле углерода составляет более 4 вес. %. 2. The method according to p. 1, characterized in that the level of carbon dissolved in the metal is more than 4 weight. % 3. Способ по пп. 1 или 2, отличающийся тем, что концентрация FeO в шлаке слоя шлака составляет менее 6 вес. %. 3. The method according to PP. 1 or 2, characterized in that the concentration of FeO in the slag of the slag layer is less than 6 weight. % 4. Способ по п. 3, отличающийся тем, что концентрация FeO составляет менее 5 вес. %. 4. The method according to p. 3, characterized in that the concentration of FeO is less than 5 weight. % 5. Способ по любому из пп. 1-4, включающий выбор количества твердого углеродсодержащего материала, вводимого в слой металла, для того чтобы пылевидное вещество, захватываемое отходящим из емкости газом, содержало, по меньшей мере, некоторое количество углерода. 5. The method according to any one of paragraphs. 1-4, including the selection of the amount of solid carbon-containing material introduced into the metal layer, so that the dusty substance captured by the exhaust gas from the tank contains at least some carbon. 6. Способ по п. 5, отличающийся тем, что концентрация твердого углерода в отходящем из емкости газе находится в диапазоне от 5 до 90 вес. % от веса пылевидного вещества в отходящем газе, который соответствует скорости образования пылевидного вещества в отходящем газе 10-50 г/норм. м3.6. The method according to p. 5, characterized in that the concentration of solid carbon in the exhaust gas from the tank is in the range from 5 to 90 weight. % of the weight of the pulverulent substance in the exhaust gas, which corresponds to the rate of formation of the pulverulent substance in the exhaust gas 10-50 g / normal. m 3 . 7. Способ по любому из пп. 1-6, включающий функционирование процесса при уровнях первичного дожигания более 40%. 7. The method according to any one of paragraphs. 1-6, including the functioning of the process with primary afterburning levels of more than 40%. 8. Способ по п. 7, включающий функционирование процесса при уровнях первичного дожигания более 50%. 8. The method according to p. 7, including the functioning of the process at levels of primary afterburning of more than 50%. 9. Способ по любому из пп. 1-8, отличающийся тем, что стадия (d) включает введение содержащего металл исходного сырья и углеродсодержащего материала в газ-носитель через один или несколько каналов/фурм, которые расположены книзу в направлении слоя металла и тем самым вызывают выброс вверх брызг, капель и струй расплавленного материала в пространство над номинальной спокойной поверхностью для образования переходной зоны. 9. The method according to any one of paragraphs. 1-8, characterized in that stage (d) comprises introducing a metal-containing feedstock and a carbon-containing material into the carrier gas through one or more channels / tuyeres, which are located downward in the direction of the metal layer and thereby cause upward spatter, droplets and jets of molten material into the space above the nominal calm surface to form a transition zone. 10. Способ по любому из пп. 1-8, отличающийся тем, что стадия (d) включает введение содержащего металл исходного сырья и углеродсодержащего материала через одну или несколько фурм в донной части емкости или в боковых стенках емкости, чтобы обеспечить контакт со слоем металла и вызвать выброс вверх брызг, капель и струй расплавленного материала в пространство над номинальной спокойной поверхностью для образования переходной зоны. 10. The method according to any one of paragraphs. 1-8, characterized in that stage (d) includes the introduction of a metal-containing feedstock and carbon-containing material through one or more tuyeres in the bottom of the vessel or in the side walls of the vessel to ensure contact with the metal layer and cause upward discharge of sprays, drops and jets of molten material into the space above the nominal calm surface to form a transition zone.
RU2000110625/02A 1997-09-26 1998-09-23 Method of direct melting for obtaining metals from their oxides RU2199591C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
AUPO9446 1997-09-26
AUPO9446A AUPO944697A0 (en) 1997-09-26 1997-09-26 A method of producing metals and metal alloys

Publications (2)

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RU2000110625A true RU2000110625A (en) 2002-05-10
RU2199591C2 RU2199591C2 (en) 2003-02-27

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US (1) US6143054A (en)
EP (1) EP1034311B1 (en)
JP (2) JP2001518557A (en)
KR (1) KR100573818B1 (en)
CN (1) CN1083489C (en)
AR (1) AR017761A1 (en)
AT (1) ATE299952T1 (en)
AU (1) AUPO944697A0 (en)
BR (1) BR9813016A (en)
CA (1) CA2304618C (en)
CZ (1) CZ299875B6 (en)
DE (1) DE69830924T2 (en)
ES (1) ES2243006T3 (en)
ID (1) ID24572A (en)
MY (1) MY127877A (en)
RU (1) RU2199591C2 (en)
TW (1) TW514668B (en)
WO (1) WO1999016911A1 (en)
ZA (1) ZA988707B (en)

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