EP2438203A1 - Procédé de préparation d'un aggloméré à partir de fines contenant des oxydes métalliques, destiné à être utilisé en tant que charge pour haut-fourneau - Google Patents

Procédé de préparation d'un aggloméré à partir de fines contenant des oxydes métalliques, destiné à être utilisé en tant que charge pour haut-fourneau

Info

Publication number
EP2438203A1
EP2438203A1 EP10722706A EP10722706A EP2438203A1 EP 2438203 A1 EP2438203 A1 EP 2438203A1 EP 10722706 A EP10722706 A EP 10722706A EP 10722706 A EP10722706 A EP 10722706A EP 2438203 A1 EP2438203 A1 EP 2438203A1
Authority
EP
European Patent Office
Prior art keywords
raw material
mineral
weight
fines
lime
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
Application number
EP10722706A
Other languages
German (de)
English (en)
Other versions
EP2438203B1 (fr
Inventor
Theo GÜNTHER
Matthias BLÖSER
Denise Alfenas Moreira
Arnd Pickbrenner
Christopher Pust
Wolfgang RÜCKERT
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Rheinkalk GmbH
Original Assignee
Rheinkalk GmbH
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
Application filed by Rheinkalk GmbH filed Critical Rheinkalk GmbH
Priority to PL10722706T priority Critical patent/PL2438203T3/pl
Publication of EP2438203A1 publication Critical patent/EP2438203A1/fr
Application granted granted Critical
Publication of EP2438203B1 publication Critical patent/EP2438203B1/fr
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • C22B1/16—Sintering; Agglomerating
    • C22B1/20—Sintering; Agglomerating in sintering machines with movable grates
    • 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
    • C21B5/00—Making pig-iron in the blast furnace
    • 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
    • C22B1/00—Preliminary treatment of ores or scrap
    • C22B1/14—Agglomerating; Briquetting; Binding; Granulating
    • C22B1/16—Sintering; Agglomerating
    • C22B1/20—Sintering; Agglomerating in sintering machines with movable grates
    • C22B1/205—Sintering; Agglomerating in sintering machines with movable grates regulation of the sintering 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
    • C22B1/00—Preliminary treatment of ores or scrap
    • C22B1/14—Agglomerating; Briquetting; Binding; Granulating
    • C22B1/24—Binding; Briquetting ; Granulating
    • 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
    • C22B1/2406—Binding; Briquetting ; Granulating pelletizing
    • 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
    • C22B1/243—Binding; Briquetting ; Granulating with binders inorganic

Definitions

  • the invention relates to a method for producing an agglomerate comprising a metal and / or metal oxide-containing fines and a mineral binder.
  • the invention further relates to a blast furnace feed which can be produced by the process according to the invention, and to a premix for the production of the blast furnace feed.
  • Finely divided iron ore-containing substances are obtained, for example, during sieving of the lump or by other treatment methods.
  • the use of these finely divided ores has the advantage that these ores are readily available and inexpensive. It is common to agglomerate the finely divided ores prior to their use. In this way, dust formation in the blast furnace can be kept low.
  • the agglomeration has the additional advantage that the agglomerates formed can be easily melted and have a good gas permeability. Thus, the reducing gases can be sucked through the ores without much effort. Finally, the use of agglomerates can reduce rust diarrhea.
  • pelletization A common form of agglomeration of finely divided ores is pelletization.
  • a smelting furnace such as a blast furnace
  • the pellets often do not have sufficient mechanical strength. This has a detrimental effect in particular during transport and handling of the pellets.
  • the known pellets are often not sufficiently permeable to hot
  • sintering Another common form of processing of not immediately usable fine ores is sintering.
  • This also fine ores can be used, which are difficult to agglomerate due to their grain size and properties.
  • difficult to agglomerate fine ores typically have mean grain diameters of up to 2 mm, more typically from 0.2 to 0.7 mm, in particular from 0.2 mm to 0.5 mm (inter-particle sizes).
  • the binder used is usually lime-based products. Lime-based products increase the cohesion of fine ores. Nevertheless, the proportion of fine ores which are difficult to agglomerate remains limited since a high proportion of these grain sizes weaken the cohesion of the sintered product and can also lead to a high dust discharge from the sintering belt. In addition, a high proportion of intermediate grain sizes also deteriorates the gas flowability of the sintered product and leads to a high proportion of recycled material in the sintering treatment.
  • an aggregate for the production of autoclave-hardened building materials comprising a mineral filler with a silica content of at least 60 wt.%, Preferably 75 wt.% And a
  • the invention has for its object to provide a method for producing an agglomerate, as
  • Blast furnace feed can be used, and with which the aforementioned problems in the prior art can be overcome.
  • a method is to be provided in which fine ore can be used with a high proportion of intermediate grain sizes and yet a sintered good having a high cohesion and a good gas permeability can be obtained.
  • the sintered material should have a low dust discharge.
  • a small amount of return material should be obtained.
  • a method is to be provided in which fine ore can be used with a high proportion of inter-particle sizes and yet pellets with a high mechanical strength can be obtained.
  • This object is achieved by a method for producing an agglomerate, as
  • Blast furnace feed is used by mixing a metal and / or metal oxide-containing fines, a mineral binder having a mineral raw material and a lime-based material, and optionally conventional additives to a mass and solidifying the mass to an agglomerate, wherein as a mineral raw material is used, which has a silica content of at least 40 wt.% And a Feinstkornanteil of less than 4 microns of at least 20 wt.%, Wherein the particle size fraction of less than 1 .mu.m is at least 10 wt.%.
  • ore containing ore sizes metal and / or metal oxide-containing fines having a mean grain diameter of less than 1 mm, preferably from 0.05 mm to 1 mm, more preferably from 0.2 to 0.7 mm, in particular of 0.1 to 0.5 mm understood.
  • agglomerates in the form of a sintered product are to be produced by the process according to the invention, it is possible according to the invention to use fines with a proportion of ore of greater than 30% by weight containing ore grains while nevertheless obtaining sintered material having an excellent cohesion.
  • agglomerates in the form of pellets are to be produced by the process according to the invention, it is possible according to the invention to use fines having a proportion of ore of greater than 30% by weight of ore grain sizes and still obtain pellets having a high mechanical strength.
  • An essential process step of the method according to the invention is the use of a lime-based material together with a mineral raw material as a binder.
  • a mineral raw material can be used in principle a variety of substances that have a silica content of at least 40 wt.%, And a Feinstkornanteil of less than 4 microns of at least 20 wt.% And a particle size fraction of less than 1 micron of at least 10 wt. % exhibit.
  • Obtained raw material having a silica content of at least 60 wt.%, Preferably at least 75 wt.%, And a Feinstkornanteil of less than 2 microns of at least 40 wt.%, The particle size fraction of less than 0.5 microns at least 25 wt. % is.
  • clay mineral-containing raw material preferably an unfired two- and / or three-layer clay mineral containing raw material has proved to be particularly favorable.
  • the lean clay has, which consists of at least 60 wt.% Fine quartz and 20 to 40 wt.% Kaolinit and optionally subordinate micas.
  • Excellent is a mineral raw material, the 70 to 90 wt.%, Preferably about 83 wt.% Of silica, 5 to 20 wt.%, Preferably about 13 wt.% Of alumina, 0.2 to 1.5 wt.%, Preferably about 0.7 wt% Fe 2 O 3 and 0.1 to 1 wt%, preferably about 0.4 wt% potassium oxide.
  • Calexor ® Q HP is a mineral binder.
  • the mineral raw material with a substantially continuous particle size distribution.
  • the metal and / or metal oxide-containing fines and the mineral binder are mixed together.
  • the mixing of fines and binders can be carried out in a variety of ways known to those skilled in the art.
  • the mixing of fines and binders in a mixing unit is particularly simple.
  • the ratio of metal and / or metal oxide-containing fines and mineral binder can vary within a wide range and is suitably adapted to the type and grain size structure of the fine material used and the binder. Practical experiments have shown that usually with a quantitative ratio between metal and / or metal oxide-containing fines and mineral binder of 5 to 1 to 1000 to 1, preferably from 10 to 1 to 100 to 1, agglomerates with particularly good strength properties can be obtained. It has been found that in some cases agglomeration can be facilitated by the fact that the mass containing the fine material and the binder has a certain mass moisture content. Depending on the intrinsic moisture content of fines and binders, the
  • Mass moisture can be adjusted by withdrawal or addition of water.
  • the height of the mass moisture is expediently set as a function of various factors, for example composition and grain size distribution of the fine material and binder used. Another important factor is the way in which the agglomeration is carried out. Usually, good results are achieved with mass moistures in the range from 2 to 20% by weight, preferably from 4 to 10% by weight.
  • metal and / or metal oxide-containing fines the most diverse fines can be used.
  • the term "metal and / or metal oxide-containing fines" are understood according to the invention as powdery to finer materials. These preferably have average particle sizes of 0.01 to 10 mm. The use of materials having average particle sizes of from 0.05 to 3 mm, in particular from 0.1 to 2 mm, has proven particularly suitable. Preferably, up to 50 wt.% Of the particle sizes of the fine material in the grain size range between 0.1 and 2 mm.
  • the binder contains a lime-based material.
  • Lime, limestone, quicklime, slaked lime, hydrated lime, dolomite, dolomitic lime, dolomitic lime, dolomitic lime hydrate and mixtures thereof are particularly suitable according to the invention.
  • additional solidifying substances preferably inorganic thickening agents, in particular waterglass, sugar solution, aluminum chromate and / or phosphate.
  • inorganic thickening agents in particular waterglass, sugar solution, aluminum chromate and / or phosphate.
  • the amount of additional strengthens depends on the degree of solidification to be achieved. Usually, even with the addition of 0.3 to 1.5% by weight of additional solidification substances, based on the mixture of fine material and binder, good results are achieved.
  • offset additives for lowering the hardening temperature such as, for example, low-melting silicatic substances, in particular a glass powder and / or phonolite, can be added to the mixture.
  • Invention is used as fines intermediate grain sizes containing ore in admixture with sintered feed.
  • the proportion of ore containing intermediate grain sizes in the fine material is particularly preferably greater than 30% by weight, preferably greater than 50% by weight, more preferably greater than 70% by weight, and in particular greater than 90% by weight, based in each case on the total amount Fines.
  • agglomerates produced by a sintering process have proven to be particularly suitable.
  • the production of a sintered product constitutes a particularly preferred embodiment of the invention.
  • the advantages of sintering include the fact that the agglomerates can be pre-reduced and losses in the furnace can be avoided.
  • the course of the sintering process is known to the person skilled in the art and may, for example, be as follows. It is first produced a mix containing fine ores, KreislaufStoffe, fuel, especially coke breeze, mineral binder and Sintereigenabsiebung. This mix is mixed with water and layered on a sintered belt. The fuel contained in the mixture is ignited, for example, by natural gas and / or blast gas flames. The induced draft fan located under the sintering belt now pulls the firing front through the mixture, so that the sinter cake is completely burnt out at the discharge of the belt. Due to the heat generated in the process, the fine ores melt superficially so that their grains form a firm connection. After breaking the sinter cake, it is cooled and classified. So-called grate and sintered material can remain in the sintering plant. The finished sinter is fed to the blast furnace.
  • the solidification of the mass to the agglomerate is carried out by a sintering process.
  • a mixture containing the fine material and the mineral binder is preferably mixed with water, customary blast furnace circulating materials, preferably pan outbreak and / or slag, fuel, preferably coke breeze, mixed and optionally compressed.
  • the resulting mixture is then subjected to a heat treatment at a temperature which is below the melting temperature of the mixture, forming a sinter cake.
  • a heat treatment at a temperature which is below the melting temperature of the mixture, forming a sinter cake.
  • the starting materials are chosen such that at least a minimum cohesion of the individual particles is given.
  • the fines used contain fractions having a particle size of less than 2 mm, preferably from 0.05 mm to 1 mm, preferably in an amount of at least 30% by weight.
  • An essential process step of sintering is the thermal treatment of the starting materials.
  • the mass of fines and binder is cured.
  • the curing is preferably based on a sintering process to form a silicate sintered matrix, which has a glass phase and optionally a crystalline phase, in particular a mullitic phase.
  • the silicate sintered matrix is preferably a glassy matrix in which crystalline particles are embedded. These are preferably a primary zero.
  • the curing process is preferably carried out by means of a thermal treatment at temperatures between 800 and
  • the mineral raw material form a melting phase, which preferably gives a glassy solidified sintered matrix with a crystalline content, in particular granular mullite or Primärärmullit, in which the metal and / or metal oxide-containing fines is embedded. If a high porosity of the sintered products is desired, this can be effected in a simple manner by subjecting a mass with a higher water content to the sintering process.
  • Sintered material is ideal for use as a blast furnace feed.
  • the mixture of fines and binders can be mixed with water and conventional pelletizing additives, the resultant mixture is shaped into green pellets and the green pellets are cured in one firing operation.
  • the hardening of the pellets can also be carried out hydraulically.
  • a mixture of fine material, binder and water is additionally added with a hydraulic solidification substance, the resulting mixture is shaped into green pellets and the green pellets are hardened.
  • hydraulic consolidation materials can also be used in the production of sintered material.
  • Cement in particular Portland cement, Portland cement clinker, aluminum oxide cement, alumina cement clinker, cement mixed with blast furnace slag, cement mixed with fly ash, cement mixed with borazon and / or bentonite are preferably used as the hydraulic binder.
  • the hydraulic binder can also be mixed with various additives.
  • An advantage of the use of a hydraulic binder is that it is possible to dispense with firing the green pellets. In this way, the manufacturing costs for the blast furnace charge can be reduced and the release of harmful gases such as SO x and NO x can be avoided during the firing process.
  • the preparation of the pellets can be carried out in a manner known to those skilled in a shaft furnace, a traveling grate furnace or a traveling grate / rotary kiln.
  • the pellets may be provided with a coating before curing.
  • Suitable coating materials are preferably inorganic substances, for example iron ore powder.
  • the thickness of the coating is preferably not greater than 0.5 mm.
  • the size of the pellets can vary widely. Pellets with a diameter of 1 to 20 mm, preferably of 3 to 10 mm, have proven to be particularly suitable for the blast furnace process.
  • the invention further relates to a blast furnace feed which can be prepared by the process according to the invention.
  • the blast furnace feed can be fed as the only metal and / or metal oxide-containing material to the blast furnace. According to the invention, it is preferable that the blast furnace feedstock together with other metal and / or metal oxide-containing
  • the blast furnace charge according to the invention accounts for a share of 30 to 80 wt.%, Preferably from 40 to 70 wt.% And in particular from 55 to 65 wt.% Of the total carrier for the blast furnace operation.
  • Another object of the invention is a premix for the production of blast furnace feedstock according to the invention containing a metal and / or metal oxide-containing fines and a mineral binder having a mineral raw material and a kalkstämmiges material, wherein the metal and / or metal oxide-containing fines a proportion of fines having a mean grain diameter of less than 1 mm, preferably from 0.05 mm to 0.9 mm and in particular from 0.1 to 0.5 mm of more than 30 wt.%, Each based on the total amount of the fine material.
  • the mineral raw material used is preferably a raw material as described in relation to the process according to the invention.
  • the premix contains 50 to 99 wt.%, Preferably 60 to 90 wt.%, In particular 70 to 85 wt.% Of metal and / or metal oxide-containing fines and 1 to 20 wt.%, Preferably 1 to 15% by weight, conventional additives and mineral binder.
  • the proportion of mineral binder in the premix should not exceed 15% by weight.
  • the amount of slag produced in the blast furnace can be kept low.
  • the mineral binder comprises 30 to 98% by weight lime-based material and 2 to 70% by weight, preferably 10 to 60% by weight, of mineral raw material.
  • the premix contains 0 to 30% by weight.
  • Additives preferably coke breeze, pan breakout and / or slags.
  • a further subject of the invention is a premix for the production of the blast furnace feedstock according to the invention comprising a metal and / or metal oxide-containing fines and a mineral binder which comprises a mineral raw material and a lime-based material, wherein a raw material is used as the mineral raw material which contains a silicon oxide.
  • a premix for the production of the blast furnace feedstock according to the invention comprising a metal and / or metal oxide-containing fines and a mineral binder which comprises a mineral raw material and a lime-based material, wherein a raw material is used as the mineral raw material which contains a silicon oxide.
  • the invention further relates to the use of a mineral binder comprising a mineral raw material and a lime-based material and optionally conventional additives, for the production of an agglomerate, the is used as a blast furnace feedstock, being used as a mineral raw material, a silicon oxide content of at least 40 wt.%, And a Feinstkornanteil of less than 4 microns of at least 20 wt.% And a particle size fraction of less than 1 micron of at least 10% by weight.
  • the use according to the invention comprises both the joint and the separate addition of mineral raw material and lime-based material.
  • Mix 1, 2, 3, 3a, 3b there are five different Sinterbandmischungen (mix 1, 2, 3, 3a, 3b) produced.
  • the mixed material 3a and 3b fine material, which has a defined proportion of intermediate grain sizes, mixed with the respective binder and conventional sintering aids and adjusted the mass moisture.
  • a mineral raw material is used as a binder having a silica content of at least 40 wt.%, And a Feinstkornanteil of less than 4 microns of at least 20 wt.% And a particle size fraction of less than 1 micron of at least 10 % By weight.
  • the mix 1, 2 and 3 is prepared without the addition of binder. Subsequently, the mix is mixed with water and layered on a sintered belt.
  • the mix has a specific Gas shealek, which can be measured by the pressure loss of a compressed air flow through the mixture. A low pressure loss indicates good gas flowability. A good Gas sheströmiana is desirable in the sintering process, since it leads to a good burn through of the sinter cake.

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

Abstract

L'invention porte sur un procédé de fabrication d'un aggloméré qui est utilisé en tant que charge pour un haut-fourneau, par mélange de fines contenant des métaux et/ou des oxydes métalliques, d'un liant minéral, qui comprend une matière brute minérale et un matériau dérivé de la chaux, et, le cas échéant, d'additifs usuels, pour former une matière, et solidification de ladite matière pour former un aggloméré. La matière brute minérale utilisée est une matière brute comprenant une proportion d'oxyde de silicium d'au moins 40 % en poids et une proportion de grains à très fine granulométrie, inférieure à 4 µm, d'au moins 20 % en poids, ainsi qu'une proportion de grains ayant une granulométrie inférieure à 1 µm d'au moins 10 % en poids. L'invention porte en outre sur une charge pour haut-fourneau, qui peut être fabriquée par le procédé selon l'invention, ainsi que sur un prémélange destiné à la fabrication de la charge pour haut-fourneau.
EP10722706.8A 2009-06-04 2010-06-04 Procédé de préparation d'agglomérats à partir de matières granulaires fines d' oxydes de métaux pour charge de haut-fourneau Active EP2438203B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL10722706T PL2438203T3 (pl) 2009-06-04 2010-06-04 Sposób wytwarzania aglomeratu z drobnego materiału zawierającego tlenek metalu do zastosowania jako materiał wsadowy

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102009023928A DE102009023928A1 (de) 2009-06-04 2009-06-04 Verfahren zur Herstellung eines Agglomerats
PCT/EP2010/057842 WO2010139789A1 (fr) 2009-06-04 2010-06-04 Procédé de préparation d'un aggloméré à partir de fines contenant des oxydes métalliques, destiné à être utilisé en tant que charge pour haut-fourneau

Publications (2)

Publication Number Publication Date
EP2438203A1 true EP2438203A1 (fr) 2012-04-11
EP2438203B1 EP2438203B1 (fr) 2015-02-25

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EP10722706.8A Active EP2438203B1 (fr) 2009-06-04 2010-06-04 Procédé de préparation d'agglomérats à partir de matières granulaires fines d' oxydes de métaux pour charge de haut-fourneau

Country Status (18)

Country Link
US (2) US9175363B2 (fr)
EP (1) EP2438203B1 (fr)
JP (1) JP5762403B2 (fr)
KR (1) KR101798162B1 (fr)
CN (1) CN102459658B (fr)
AU (1) AU2010255697B2 (fr)
BR (1) BRPI1010034B1 (fr)
CA (1) CA2764535A1 (fr)
CL (1) CL2011003071A1 (fr)
DE (1) DE102009023928A1 (fr)
EA (1) EA023830B1 (fr)
ES (1) ES2537209T3 (fr)
MX (1) MX2011012939A (fr)
PL (1) PL2438203T3 (fr)
RS (1) RS54006B1 (fr)
UA (1) UA103533C2 (fr)
WO (1) WO2010139789A1 (fr)
ZA (1) ZA201108924B (fr)

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DE102009023928A1 (de) 2009-06-04 2010-12-09 Rheinkalk Gmbh Verfahren zur Herstellung eines Agglomerats
BRPI1104742A2 (pt) * 2011-09-05 2013-08-13 Vale Sa mÉtodo de inibiÇço do envelhecimento (intemperismo) de pelotas de minÉrio de ferro durante estocagem
KR101291403B1 (ko) * 2012-09-05 2013-07-30 한호재 광석화 펠릿, 이의 제조방법, 첨가제 펠릿 및 이를 이용한 선철의 제조방법
US9228246B2 (en) 2013-01-11 2016-01-05 Alternative Charge Materials, Llc Method of agglomerating silicon/silicon carbide from wiresawing waste
CZ304951B6 (cs) * 2013-07-08 2015-02-04 Ecofer, S.R.O. Tavidlo pro aglomeraci, způsob výroby tavidla, aglomerační směs pro výrobu aglomerátu a použití strusek sekundární metalurgie jako tavidel pro přípravu aglomerační směsi
EP2848299B1 (fr) 2013-09-11 2019-08-14 Primetals Technologies Austria GmbH Procédé et dispositif destinés à la fabrication de granulés
EP3502284A1 (fr) * 2017-12-22 2019-06-26 Imertech Sas Procédé de traitement de minéraux
CN111733320A (zh) * 2020-07-29 2020-10-02 攀钢集团研究院有限公司 改善烧结混合料粒度的制粒方法

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EA201101700A8 (ru) 2014-05-30
JP2012528941A (ja) 2012-11-15
US9175363B2 (en) 2015-11-03
AU2010255697B2 (en) 2015-12-03
AU2010255697A1 (en) 2012-01-19
BRPI1010034A2 (pt) 2020-08-18
EA201101700A1 (ru) 2012-07-30
EA023830B1 (ru) 2016-07-29
JP5762403B2 (ja) 2015-08-12
CN102459658A (zh) 2012-05-16
KR101798162B1 (ko) 2017-11-15
US20160083809A1 (en) 2016-03-24
ZA201108924B (en) 2012-08-29
CN102459658B (zh) 2015-12-16
MX2011012939A (es) 2012-04-02
PL2438203T3 (pl) 2015-07-31
RS54006B1 (en) 2015-10-30
WO2010139789A1 (fr) 2010-12-09
US20120180599A1 (en) 2012-07-19
BRPI1010034B1 (pt) 2021-04-06
CA2764535A1 (fr) 2010-12-09
ES2537209T3 (es) 2015-06-03
US9988695B2 (en) 2018-06-05
EP2438203B1 (fr) 2015-02-25
CL2011003071A1 (es) 2012-05-04
DE102009023928A1 (de) 2010-12-09
UA103533C2 (ru) 2013-10-25
KR20120037447A (ko) 2012-04-19

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