Classifications

• • C—CHEMISTRY; METALLURGY
  • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
  • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
  • C22B1/00—Preliminary treatment of ores or scrap
  • C22B1/14—Agglomerating; Briquetting; Binding; Granulating
  • C22B1/24—Binding; Briquetting ; Granulating
  • C22B1/242—Binding; Briquetting ; Granulating with binders
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B13/00—Making spongy iron or liquid steel, by direct processes
  • C21B13/0046—Making spongy iron or liquid steel, by direct processes making metallised agglomerates or iron oxide
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B13/00—Making spongy iron or liquid steel, by direct processes
  • C21B13/006—Starting from ores containing non ferrous metallic oxides
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B13/00—Making spongy iron or liquid steel, by direct processes
  • C21B13/0066—Preliminary conditioning of the solid carbonaceous reductant
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B13/00—Making spongy iron or liquid steel, by direct processes
  • C21B13/0086—Conditioning, transformation of reduced iron ores
  • C21B13/0093—Protecting against oxidation
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B13/00—Making spongy iron or liquid steel, by direct processes
  • C21B13/06—Making spongy iron or liquid steel, by direct processes in multi-storied furnaces
• • C—CHEMISTRY; METALLURGY
  • C21—METALLURGY OF IRON
  • C21B—MANUFACTURE OF IRON OR STEEL
  • C21B13/00—Making spongy iron or liquid steel, by direct processes
  • C21B13/10—Making spongy iron or liquid steel, by direct processes in hearth-type furnaces
  • C21B13/105—Rotary hearth-type furnaces
• • C—CHEMISTRY; METALLURGY
  • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
  • C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
  • C22B1/00—Preliminary treatment of ores or scrap
  • C22B1/14—Agglomerating; Briquetting; Binding; Granulating
  • C22B1/24—Binding; Briquetting ; Granulating
  • C22B1/242—Binding; Briquetting ; Granulating with binders
  • C22B1/244—Binding; Briquetting ; Granulating with binders organic
  • C22B1/245—Binding; Briquetting ; Granulating with binders organic with carbonaceous material for the production of coked agglomerates
• • 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
  • C22B19/00—Obtaining zinc or zinc oxide
  • C22B19/30—Obtaining zinc or zinc oxide from metallic residues or scraps
• • 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
  • C22B5/00—General methods of reducing to metals
  • C22B5/02—Dry methods smelting of sulfides or formation of mattes
  • C22B5/16—Dry methods smelting of sulfides or formation of mattes with volatilisation or condensation of the metal being produced
• • 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
  • C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
  • C22B7/02—Working-up flue dust
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
  • Y02P10/00—Technologies related to metal processing
  • Y02P10/20—Recycling

Definitions

• This invention relates to a two stage method for removal of zinc, reduction of iron ores and production of liquid metal using iron ores and process dust containing high zinc.
• the invention further relates to a selection of binders in agglomeration and thermal profile of the furnace through sequencial adjustment of porosity which accelerates the removal of zinc vapors at high temperatures during reduction reaction.
• first stage non-shaft furnaces are used for zinc removal and direct reduction of iron ores and dust.
• electric furnace is used to produce liquid metal and remove the remaining zinc from reduced metal by using innovative the slag chemistry.
• Blast Furnace process is used worldwide for production of hot iron metal. using variety of iron ores.
• the volatile impurities such as alkalis, zinc, lead, etc. creates various operational problems in Blast furnace process. Therefore blast furnace process is not convenient route for processing iron ores with high zinc content.
• Alternative processes developed for iron and steel making, where shaft furnaces are used, are also not suitable for treatment of these high zinc ores.
• the boiling point of zinc metal is -910C and in oxidizing conditions it forms stable zinc oxide (solid phase). In furnaces where various temperature zones and oxidizing conditions exist, zinc recycles / accumulates inside the furnace.
• Another object of the invention is to propose a combination of binders in the improved method of agglomeration process for rapid removal of zinc vapor during reduction reaction, through sequential adjustment of porosity.
• a further object of the invention is select a suitable combination of processes for production of iron and steel using product of first stage i.e.' direct reduced iron.
• a still further object of the invention is to propose a process for recovery of Zn values from waste gas stream for extraction of Zn metal.
• an improved method for processing high zinc iron ores for production of iron and steel comprising the steps of; producing of agglomerate comprising a mixture of iron oxides, carbonaceous materials, and fluxes with mean-particle size respectively of 35 to 70, 25 to 60, and 45-85 microns, to form agglomerates of 8 to 15 mm size using combination of organic and inorganic binders and moisture to achieve the desired properties of the agglomerates; dezincificating and metallising of agglomerates in a furnace; smelting the reduced agglomerates, in hot / cold charging condition, to form hot metal (iron) in a furnace leading to producing steel; recovering zinc values from waste gas stream of the furnace by carrying - out conventional zinc extraction process.
• Figure 1 shows the plot of free energy change Vs temperature for reduction reactions of Zn & Fe oxides, which is used for development of the present invention.
• Figure 2 presents the ZnFe2U4 - O2 phase diagram used for controlling the gaseous atmosphere inside various zones in Furnace and for separation of zinc from waste gas strem.
• ZnS Common zinc mineral is sphalerite, ZnS.
• zinc also found in the form of Franklinite [(Zn 1 Fe, Mn) [Fe, MnfeO/ij.a oxide mineral.
• Franklinite (Zn 1 Fe, Mn) [Fe, MnfeO/ij.a oxide mineral.
• Zn 2+ can replace Fe 2+ cations forming stable (Fe3U4 - ZnF2U4) solid solution phase.
• the Zn 2+ cation is smaller in size than Fe 2+ so replacement of Fe 2+ by Zn 2+ reduces the lattice dilation and strain energy. Therefore dissolution of ZnO in magnetite increases thermodynamic and structural stability.
• HCP hematite
• structure can accommodate partial replacement of Fe 3+ by Zn 2+ cations by vacancy formation and lattice dilation. Therefore, high zinc concentration is detected in hematite minerals (as in case of oxidized ores of Thach Khe, Vietnam). It is not possible to remove this lattice zinc in iron ores by conventional beneficiation techniques such as magnetic separation, gravity separation, etc. Therefore present invention provides a method capable of removing zinc locked in the iron mineral lattice and also produces reduced iron, which can be integrated with conventional iron & steel making process.
• phase diagram of ZnFe2 ⁇ 4 - O2 computed using FACT-Sage program is shown in Figure 2, which shows the boundary lines for thermodynamic stability of various phase (solid, liquid and gas) Zn - Fe - 0 compounds. Therefore solid state reduction above 750C temperature and below 10 16 oxygen partial pressure, are the critical thermodynamic conditions for removal of zinc from magnetite lattice.
• Zn 2+ and Fe 3+ cations have zero octahedral site preferential energy therefore the site occupancy of cations is mainly decided on basis of cationic radii and charge.
• smaller Zn 2+ and Fe 3+ cations occupy both tetrahedral & octahedral sites, whereas large Fe 2+ cations preferentially occupy octahedral sites in magnetite lattice.
• the imposed oxygen chemical potential promotes the diffusion of Fe and Zn cations through oxygen anions on CCP lattice in the magnetite, toward the reaction interface on the surface of the grain.
• iron ores with high Zn content are mixed with carbonaceous materials, as a reductant and other fluxes.
• the mixture is then agglomerated in the form of pellets or briquettes. Desired properties of the agglomerates comprises wet-drop number, dry-drop number, green crushing strength and dry-crushing strength which respectively ranges 6 to 8, 10 to 15, 1.5 kg pellet, and 15kg /pellet.
• the green agglomerates are dried to remove the moisture.
• a non shaft furnaces such as rotary hearth furnace is used for solid state reduction and dezincification, However present invention does not exclude operation in the other type of furnaces. In the rotary hearth furnace the agglomerated feed is charged continuously in layers to maintained appropriate height of the burden on the hearth.
• the agglomerates are heated in different zones of furnace.
• the heat required for endothermic reduction reactions is supplied by the combustion products and radiation energy from the furnace heaters / burners.
• the air : fuel ratio of the furnace burners is kept at appropriate levels in different zones to maintain at desired reducing conditions in various zones of furnace.
• the carbonaceous material in the agglomerate acts as reductant and also maintain reducing atmosphere close to reaction interface.
• the ratio of ore to carbonaceous materials is adjusted to provide to C required for reduction and for maintaining reducing atmosphere at reaction interface.
• Temperature profile of the furnace is maintained as desired to form a molten slag at appropriate time and also allow coalesce of reduced metal.
• the reduced pellets are cooled to 800 0 C to 1000 0 C required for subsequent processes.
• the DRI are agglomerated by hot briquetting process.
• the atmosphere of cooling zone and subsequent hot process is controlled to minimize the reoxidation of newly formed metallic iron.
• 70 - 95 % degree of metallization with 80 - 95 % dezincification can be achieved in the temperature range from 1100 to 1400 C and 10 - 60 minutes heating cycle.
• the process also generates DRI with very low silicon (0.1 - 0.9%) and carbon (0.3 - 1.5%) content.
• the gas flow follows the charge / heart movement so that hot gas will not come in contact with low temperature charge, on which Zn vapors can deposit and recirculate / accumulate inside the furnace.
• Other option used in this innovative process is to collect the gas from high temperature zone and cool to temperatures below .900C to separate the Zn vapors and then recycle in the furnace to maintain the reducing atmosphere.
• other applications of hot furnace gas are not excluded in this invention.
• the porosity of dry carbon composite pellets is preferred to enhance the vaporization of zinc near reaction interface and rapid transport of Zn vapor to outlet gas stream.
• This is achieved by using combination of the hybrid binders and moisture in the agglomeration.
• the inorganic binders doses ranges between 0.5 to 2%, and wherein the organic binders are used in the doses between 1 to 5%.
• the volume ratios of iron ore, coal, binder and moisture are adjusted in innovative way to generate porosity within agglomerate as reduction and dezincification reaction proceeds.
• the binder vaporization and coal utilization is sequenced in such a way to compensate the shrinkage of the agglomerate during reduction reaction and also to achieve the required strength in reduced pellets.
• the composite pellets are dried in the temperature range from 110 to 300 0 C to remove the moisture and thereby generate the porosity (primary pores).
• the combination of organic and inorganic binders is used so that the organic binder enhances the strength of dry pellets / briquettes whereas inorganic binder provides strength at high temperature inside the furnace during reduction reactions.
• the organic binder vaporizes in the early stages of reduction reaction which increases 5 - 10 % porosity (secondary pores) of the pellets / briquettes.
• porous channels primary and secondary pores generated at lower temperature enhance the rapid transport of Zn vapors formed during solid state reduction of magnetite and zinc ferrite solid solution phase above 800 0 C temperature.
• carbon / reductant gets consumed which also maintains pore channels i.e. the high porosity for rapid gas phase transport from reaction interface to furnace atmosphere.
• particle size and size distribution of feed (iron ore, reductant, flux and binders) used for agglomeration process are adjusted to achieve the required green and dry pellet strength, to generate the pore channels for rapid transport of gaseous products and to enhance the rate of reduction reaction (topochemical).
• Iron oxides, carbonaceous materials, and fluxes are prepared to achieve mean-particle size respectively of 35 to 70, 25 to 60, and 45-85 microns, to form agglomerates of 8 to 15 mm size.
• high productivity (tones / hour / m 2 ) is achieved in this short time reduction process (heating and cooling cycle).
• a combination of fluxes is used to form slag with desired liquidus.
• the rate of reduction reaction is also adjusted in innovative way to produce desired amount of FeO oxide in the charge during reduction reaction which forms molten slag.
• the fluxes used in the charge impart desired physico - chemical properties in molten slag and also control loss of Fe in the slag phase.
• the slag properties are adjusted to dissolve gangue phases and also maintain desired viscosity so that molten slag will not block the pores and thereby hinder the flow of Zn vapors and product gases.
• the designed slag chemistry forms fluid slag which accelerate coalesce of reduced metallic particles and better separation of slag and metal.
• rapid dezincification and better slag-metal separation is achieved by innovative flux chemistry and heating cycle / rate.
• the higher degree of metallization and dezincification was also achieved by using appropriate grade of iron ore concentrate.
• the increase in Fe content of iron ore enhances the degree of metallization and removal of gangue components help to reduce the flux requirement.
• the higher % metallization and lower slag content decrease the cold crushing strength of the reduced pellets. Therefore heating cycle, porosity, feed size, and slag chemistry are adjusted to achieve the desired properties of reduced pellets / briquettes.
• the process described in this invention was used for processing Iron ore containing ⁇ 0.07 % Zinc.
• the agglomerates were prepared using anthracite coal, iron ore fines and flux, using combination of binders as discussed in the invention.
• the agglomerates were reduced in a furnace using desired heating profile in the temperature range from 1100 to 1400 C.
• the DRI with metallization in the range of 70 - 95% and zinc less than 0.01 % were produced by the process.
• the DRI was used to produce liquid metal in electric furnace.
• the hot DRI is directly melted in electric furnace to form either a) hot metal, which can be used of BOF steel making, by adjusting the C, Si, S, P levels, or b) directly steel by using double slag practice. Production process options will be dictated by local economics.
• One of the embodiments of the present invention is recovery of zinc.
• the zinc vaporized during reduction in the furnace is carried away by the waste gas stream.
• the zinc vapors are condensed by reducing the temperature below 900C and by readjusting the oxygen partial pressure of the gas stream, if required.
• the waste gas stream from arc furnace used for iron and steel making is also treated in similar way to recover the zinc values.
• the zinc oxide condensed in the condenser is collected. Since, coal is used as a reductant, the zinc oxides dust also contents many impurities which needs to be removed. When the concentration of the zinc in the dust is > 40 % then dust is used directly for zinc extraction.
• carbo-thermic reduction of zinc oxide is carried out to extract metallic zinc which, is then purified by conventional electrolysis technique.

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• Chemical & Material Sciences (AREA)
• Engineering & Computer Science (AREA)
• Manufacturing & Machinery (AREA)
• Organic Chemistry (AREA)
• Metallurgy (AREA)
• Materials Engineering (AREA)
• Mechanical Engineering (AREA)
• Geology (AREA)
• Geochemistry & Mineralogy (AREA)
• Life Sciences & Earth Sciences (AREA)
• General Life Sciences & Earth Sciences (AREA)
• Environmental & Geological Engineering (AREA)
• Manufacture And Refinement Of Metals (AREA)
• Manufacture Of Iron (AREA)
• Refinement Of Pig-Iron, Manufacture Of Cast Iron, And Steel Manufacture Other Than In Revolving Furnaces (AREA)

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• 2009
  • 2009-08-28 KR KR1020107007396A patent/KR101619169B1/ko not_active Expired - Fee Related
  • 2009-08-28 CN CN200980100973XA patent/CN101970699B/zh not_active Expired - Fee Related
  • 2009-08-28 JP JP2011524530A patent/JP5380536B2/ja not_active Expired - Fee Related
  • 2009-08-28 WO PCT/IN2009/000472 patent/WO2010023691A1/en active Application Filing

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