• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    The invention relates to fluxes for the agglomeration process based on secondary metallurgy slag, the use of these fluxes in the agglomeration process in the production of the agglomerate for use as a metal charge in blast furnaces and a process for the production of secondary metallurgy based slag fluxes or based on a Mixture of slag from secondary metallurgy with other materials.
    公开号:AT516369A2
    申请号:T9263/2014
    申请日:2014-07-02
    公开日:2016-04-15
    发明作者:
    申请人:Ecofer S R O；
    IPC主号:
    专利说明:

    Flux, process for its preparation, agglomeration mixture and use of slag from the secondary metallurgy
    Technical area
    The invention relates to: fluxes for an agglomeration process based on secondary metallurgy slag, agglomeration mixtures with fluxes for the production of an agglomerate, use of fluxes in the agglomeration process in the production of an agglomerate intended for a metal charge in high furnaces, processes for the production of Slag from secondary metallurgy or based on a mixture of slag from secondary metallurgy with other materials.
    Description of the Prior Art
    Steel is mainly produced in converters and electric arc furnaces. The main batch for the production of steel includes pig iron and steel scrap. Pig iron is produced in blast furnaces, where the main batch is iron ore, iron ore pellets, flux and coke. Before processing in a blast furnace, the iron ore is modified in an agglomeration process. The aim of the agglomeration process is to treat the ore to be suitable as a charge in a blast furnace. During the
    Agglomeration process takes place the setting of Erz-Granulometrie and the change of its chemical composition, in particular as regards the ratio of the content of the oxides CaO and Si02.
    Manufactured pig iron is treated in converters by a refining process in which the removal of carbon, silicon and phosphorus from the pig iron occurs through the action of oxygen. The treatment product is referred to as crude steel, which in most cases is similar to the raw steel from electric arc furnaces. This carbon steel is characterized by a low carbon content and a high oxygen activity of greater than 200 ppm, typically about 600 ppm oxygen. During the tapping, crude steel is deoxidized with aluminum, silicon, manganese, chromium or other elements. Deoxidized steel is used in secondary metallurgy in equipment such as LF (ladle furnace), VD, RH, DH, VAD, VD / VOD (various types of vacuum steel processing equipment ) and the like. In the secondary metallurgy facilities, steel in the final stage is treated under reducing conditions. This treatment also affects the composition of the slag. Slags have low oxygen activity and a low FeO content. For steels that have been deoxidized with aluminum, this value is up to 5 wt%, optimally up to 1 wt%. For paints that have been deoxidized with silicon and manganese, it is up to 10% by weight, optimally up to 5% by weight. These slags are capable of binding substantial amounts of sulfur. According to the deoxidation process, there are slags from steelmaking where the dominant deoxidizer is aluminum and slags from steelmaking where the dominant deoxidizer is silicon or manganese or their mixture. Deoxidation products are the oxide of these elements, which are typically attached to lime. Consequently, oxide-melt slags are produced whose chemical composition is shown in the following table:
    Table of approximate proportions of the composition of slags in secondary metallurgy (weight percent)
    The properties of these slags, such as crumbling, dusting, instability, make their use much more difficult. According to the BAT (best available techniques) leaflets, up to 80% of these slags are deposited. Their use is difficult.
    Use of slag from secondary metallurgy
    Slags produced in secondary metallurgy are difficult to use. The most common and widespread method of recycling these slags is to mix them with other steel slags used in the construction industry after prolonged exposure to air and rain, after aging. On solidification, they usually disintegrate into a fine dust which, in addition, significantly increases its volume as a result of the presence of free lime during hydration. The aftermath of this approach is a particularly difficult controllable expansion of slags, manifested for example by bulging of built roads and highways. This negative feature prevents their wider use in construction. A large portion of the slag is therefore dumped on slag heaps without further use.
    The problem of using slag was further addressed in the FI-IM5 / 133 project in the Czech Republic, Italy and Poland. The project uses the positive properties of these slags, especially low temperature melts, which enables rapid production of homogeneous steel slags in a steel aggregate. The use of slag from secondary metallurgy has also been explored within the scope of European Research Project No. 7210-PR / 203, which is directed to the use of
    Slag in an electric arc furnace (EAF) counts, solved. This method is suitable for the recycling of slag directly in a steelmaking plant equipped with the EAF, but requires a so-called slag formation which is costly. The use of slag from integrated smelters is not possible for capacity reasons and because of the additional transport costs.
    The company Harsco invented a method according to the patent WO 2007/136914 A3, using secondary metallurgy slags by mixing them with refractory linings residues to give fresh slag-forming materials suitable for further use. A limitation of this method is given only by economic aspects.
    From US Patent No. 2009/0049955 there is also known a process for recycling slag based on the use of slag from secondary metallurgy in an electric arc furnace (EAF). Slag is added to the EAF as a flux and as a CaO source. This method is also not used for capacity reasons and because of additional transport costs.
    The solution according to the patent WO 2004/101828 uses slag for the production of binders and synthetic slag. However, the disadvantage of this solution is the requirement for a narrow range and stability of the chemical and phase composition of the slag. Mäkelä; I. Välimäki; R. Pöykiö; H. Nurmesniemi; 0. Dahl in the article "Evaluation of trace element availability from secondary metallurgicalslag generated in steel making by sequential chemical extraction"; The International Journal of Environmental Science and Technology; available online February 26, 2013, citing that - in contrast to the slag from blast furnaces and converters - the slag from secondary metallurgy is mainly deposited on dumps.
    Recycling slag in agglomeration
    A method of recycling a portion of converter slag having a higher iron content is known. Although this process is widely used, its major drawback is the re-reduction of phosphorus contained in this slag into the pig iron.
    Pelletizing and agglomeration process
    The agglomeration is used to make a batch for a blast furnace, and this process is not used to recycle other slags than those from the converter process. Raw materials for the agglomeration process are the following raw materials: • iron ore, bark, metallic waste, etc., • flux (mostly slag-forming parts of a batch) - limestone, lime, dolomite, overburden, etc. • Fuels and reducing agents - coke, natural gas etc.
    These raw materials are mixed and homogenized in several steps. The first step is the creation of homogenization piles, and the final step is, for example, in a pelletizing drum. In new, modern plants, all batches of batch preparation can be integrated into a single device capable of satisfying all stages of homogenization and pelletization.
    In the course of the agglomeration, a mixture of the homogenized material placed on an agglomeration belt is heated to a temperature higher than 1000 ° C. At these temperatures, the melting and aggregation of the individual granules of the feedstocks take place. As a result of the aggregation process, portions of the agglomerates suitable for use as a batch in the blast furnace are formed.
    To improve the agglomeration process, water-glass based materials are added, as described in US Pat. No. 6,683,583. Both methods improve the pelletization of raw materials in the agglomeration process, but on the other hand, they affect the heat and material balance of a furnace process.
    Summary of the invention
    The above-mentioned problems with the use of slag from secondary metallurgy, the improvement of the pelleting process and the improvement of the melt process are in large part solved by a process for producing an agglomerate according to the invention in which the agglomerate is intended for use as a charge in blast furnaces and the process of sieved, refracted slagging secondary metallurgy as flux, or mixtures of this slag with other materials, the object of the invention in blending these slags with other charge materials of the agglomeration process
    Homogenization heaps or in bunkers, so that the total content of the slag from the secondary metallurgy is less than 10 wt .-% of the total charge in the agglomeration process.
    After casting steel, slags from the secondary metallurgy are poured together with the metal residues from a ladle into flake boxes. After cooling, large pieces of metal, called iron scrap, are removed. Subsequently, the slag is sorted by size and optionally even crushed to a fraction of less than 100 mm. For later use, the fractions of sorted slag having a size of less than 100 mm, preferably less than 10 mm, appear optimal. When demetallization of the slag is required, it is possible to perform magnetic separation of iron from the slag. Slag or slag mixtures thus processed are added to the charge of the agglomeration process at the latest in a pelletizing drum or in a device having the same function.
    The best solution seems to be to mix slag or slag mixture in a homogenizing drum or in homogenisation piles or by silos onto a belt, such slag or the like
    Slag mixture is mixed with other charge materials in amounts of less than 10 wt .-% of the total charge in the agglomeration process, optimally in amounts of 0.5 to 1.5 Gew.-I, wherein at least 90 wt .-% of slag below a grain size 100 mm and optimally below 10 mm.
    Prior to use in agglomeration, other materials such as limestone, limestone, dolomite, dolomitic limestone, undersize coke, and waste or by-products of the metallurgical or cement industries may be added to these slags or slag mixtures.
    The main advantage of this method according to the invention is the possibility of reducing the energy demand of the
    Agglomeration process by up to 10% along with the improvement of the mechanical properties of the agglomerates produced as well as a reduction of the fines of the agglomerate, which would otherwise be attributed to the agglomeration process. Another advantage is the use of a residual metal, the increase in MnO content in the agglomerate, particularly in the recycling of slag from the manufacture of manganese and silicon killed steel. A side effect is a reduction in C02 emissions from fuel and carbonates, especially limestone and dolomite.
    Another favorable property of secondary metallurgy slags useful in agglomeration is their self-disaggregation and the formation of particulate matter fractions. The fine dust fractions produce large reaction surfaces, help with pelleting, and the slag need not be broken. Since the paints do not contain CO 2, the release of which requires a considerable amount of heat, their use influences the
    Overall heat balance of the agglomeration process positive. Using slags from secondary metallurgy as a flux and as a replacement or partial replacement for limestone, lime, dolomite or other materials, there is a substantial reduction in the melting temperature at the grain boundaries. The
    Melting temperature of lime is 2612 ° C, while the slag eutectics from secondary metallurgy show a melting temperature of about 1300 ° C.
    In this way it is possible to recycle both the total slag from secondary metallurgy of integrated steelworks and slag from steelworks producing steel in electric arc furnaces. The invention solves, in a practical and cost effective manner, the use of secondary metallurgy slag and its use in the agglomeration process.
    Brief description of the drawings
    Explanation of the invention requires no figures.
    Detailed description of the invention
    The process for producing the agglomerate intended for use as a batch furnace may be used in accordance with the invention for various types of secondary metallurgy slag or slag mixtures as a substitute or partial substitute for limestone, lime and dolomite or other steel or metal aggregates.
    The invention is explained in more detail in the following embodiments of the invention:
    Example 1:
    Steel from a converter or electric arc furnaces or similar devices, such as the CONARC hybrid furnace, is tapped into a pan and deoxidized by aluminum, silicon, manganese or other deoxidizing elements. Such modified steel is processed in a secondary metallurgy apparatus and, after processing, is ready for casting, for example in a continuous casting plant or in the form of a block casting. After casting, the remaining slag and the remainder of the steel in the pan are poured into a skim bucket and, after it is filled, transported to a skimming bunker. After cooling and solidifying, coarse pieces of the remaining steel are mechanically removed. Slag decomposes spontaneously to a fine dust mass. Slag disintegrates when the cooling rate is less than 200 ° C per hour. The
    Slag that does not spontaneously disintegrate is mechanically crushed to granulometry below 100 mm or otherwise used. Slag modified in this way is ready for further use as a raw material for the agglomeration process. Slips with lower levels of SiO 2 (below 15%) are more suitable for the above use.
    Slag and slag forming materials are mixed into an agglomeration mixture, thus preventing the generation of unnecessary amount of slag in the blast furnace process. The composition of the flux in the agglomerate is conducted so that the resulting ratio of CaO / SiO 2 in the agglomerate is higher than 0.5 and optimally around 0.8-1.5. Also, the total content of A1203 is limited by the value of 8%. For example, ores and ore concentrates have 4 to 10% of SiO 2, with the content of CaO being about 2%, and therefore, it is necessary to add the corresponding amount of CaO so that the ratio of CaO to SiO 2 is 0.8 to 2.5 in accordance with the operation of a particular furnace, advantageously in the range of 0.8 to 1.5. From these ratios, and from the composition of the slag from secondary metallurgy or from its mixture with other materials, it is easily possible to derive the necessary additions of the slag or slag mixture. The particular slag from secondary metallurgy forms a flux useful in the agglomeration process.
    Example 2:
    Slag from secondary metallurgy with granulometry below 100 mm is mixed with other slag-forming materials such as lime, limestone, dolomite, dolomitic limestone, magnesite, optionally with a fuel in the form of fine-grained coke. The mixture prepared in such a way is ready for subsequent use as a flux for the agglomeration process.
    Example 3:
    The slag from the production of aluminum killed steel is mixed with the slag of the steel calmed by silicon or manganese. After mixing and adjusting the granulometry, the slag is ready for subsequent use as a flux for the agglomeration process.
    Example 4:
    In the agglomeration process, some or all of the slag is recovered from the secondary metallurgy produced in the respective steelworks, and in the case of low transportation costs, it is also possible to mix this slag with secondary metallurgy slag from nearby steel plants, particularly from electric steelworks. The respective slag from the secondary metallurgy forms a flux usable in the agglomeration process.
    Example 5:
    After cooling, coarse scrap metal from the secondary metallurgy slag is first removed from the production of aluminum killed steel, and then the slag is sorted into individual fractions on sorters. For direct use in the agglomeration process, the slag fractions with granulometry below 100 mm, suitably below 20 mm are used. The remaining coarse slag pieces are comminuted to finer fractions for use in the agglomeration process, or are used in a different manner. The slag mixture processed in this way is evenly distributed on slag heaps, preferably in quantities of 10 tons.
    Slag may be added to the batch in a single portion or in multiple portions at individual stages of homogenization, at the latest in a pelletizing drum or apparatus having the same function, such that the total content of slags in the batch of the agglomeration process is a maximum of 10% of the total batch in the Agglomeration corresponds.
    Example 6:
    The slag produced according to Example 1 is further enriched with materials such as lime, limestone, dolomite, dolomitic limestone, undersize coke, waste or by-products of the metallurgical or cement industries. Slag or slag-forming mixtures with recycled materials may be added singly or in any mixtures, and added to the metal batch at any stage of homogenization in a single portion or in several consecutive steps, but at the latest in a pelletizing drum or in a device having the same function. The amount of secondary metallurgy slag is always less than 10% by weight of the total weight of the charge material of the agglomeration process.
    Example 7:
    This example consists in the use of slags from the production of silicon and manganese-killed steel, of which the total content of SiO 2 + MnO + FeO is higher than 15% by weight. These slips can also be used to prepare agglomeration mixtures or can be added directly to such mixtures. Similar to Examples 1 and 2, these slags are cleared of coarse scrap metal, then sorted, optionally also crushed and prepared for use. The fractions below 100 mm, advantageously below 20 mm are used. These slags may be used directly or mixed with other materials in a similar manner as described in Example 2.
    Example 8:
    Secondary metallurgy slags from the production of aluminum or, if applicable, manganese and silicon killed steels are mixed and used in a similar manner as described in Examples 1-7.
    Example 9:
    A special case is the use of secondary metallurgy slags produced only by deoxidizing by silicon and manganese. These slags contain a higher concentration of SiO 2, but at the same time they also contain high concentrations of MnO. In any case, it is necessary that lime or limestone or, if appropriate, dolomite be added to these slags, either directly to the slags or subsequently to the agglomeration mixtures.
    Industrial applicability
    Slags from secondary metallurgy can be used as fluxes in the agglomeration process for the batch of a blast furnace process. These fluxes are characterized by the presence of low melting eutectics that facilitate the agglomeration process. The reduced content of carbonates leads to energy savings.
    权利要求:
    Claims (6)
    [1]
    Claims 1. A sintered slag based on secondary metallurgy, characterized in that it contains remelted mixtures of oxides CaO, Al 2 O 3, SiO 2, MgO, MnO, FeO and other compounds forming eutectics of which the melting temperature is lower than 1600 ° Cist and wherein the total content of these oxides is greater than 75 wt .-%, wherein the content of CaO is higher than 40 wt .-% and the content of sulfur less than 2.5 wt .-%, wherein at least 90 wt. % of the flux shows a particle size below 100 mm and preferably below 10 mm.
    [2]
    Secondary metallurgy-based flux according to claim 1, characterized in that the flux further contains lime, limestone, dolomite, dolomitic limestone, magnesite, undersize coke, waste or by-products from the metallurgical or cement industry, and the ratio of CaO / SiO 2 and Ca0 / Al 2 O 3 of the resulting flux is higher than 1.25.
    [3]
    A process for the production of a flux based on secondary metallurgy slag, characterized in that slags from the secondary metallurgy are cooled to a temperature below the solidification point, and after this cooling, the granulometry of the flux obtained is adjusted so that at least 90% by weight has a particle size below 100 mm and preferably less than 10 mm.
    [4]
    4. A process for the production of a flux based on secondary metallurgy slag according to claim 3, characterized in that the flux is mixed with other fluxes, such as lime, limestone, dolomite, dolomitic limestone, magnesite, undersize coke, waste or by-products of the metallurgical or cementitious process. So that the resulting flux has a ratio of CaO / SiO 2 and CaO / Al 2 C> 3 higher than 1.25.
    [5]
    An agglomeration mixture for the production of an agglomerate for use as a charge in blast furnaces, characterized in that it comprises a metal charge of the agglomeration which contains a flux for the agglomeration process in an amount of less than 10% by weight of the total charge, preferably 0.5 to 1.5 At least 90% by weight of the flux has a particle size below 100 mm and preferably below 10 mm, the resulting agglomeration mixture having a ratio of CaO / SiO 2 higher than 1.25 and CaO / Al 2 C> 3 higher than 1, Has 25 and less than 5 wt .-% A1203.
    6. Use of slags from secondary metallurgy as flux to produce an agglomeration mixture for the production of the agglomerates for use as charge in blast furnaces. Amended claims, received by the International Bureau on December 1, 2014 (01.12.2014) 1. flux for agglomeration based on slags from the secondary metallurgy, characterized in that it again melted mixtures of oxides CaO, A1203, SiO 2, MgO, MnO, FeO and other compounds containing eutecticides of which the melting temperature is lower than 1600 ° C and the total content of said oxide is higher than 75% by weight, the content of CaO being higher than 40% by weight and the content of sulfur being less than 2% 5% by weight, with at least 90% by weight of the flux showing a particle size below 100 mm, and preferably below 10 mm. Secondary metallurgy slag agglomeration flux according to claim 1, characterized in that the flux further contains lime, limestone, dolomite, dolomitic limestone, magnesite, undersize coke, waste or by-products from the metallurgical or cement industry, and the ratio of CaO / SiO 2 and CaO / Al 2 O 3 of the resulting flux is higher than 1.25. A process for the production of a slag based secondary slag agglomeration catalyst, characterized in that slag from the secondary metallurgy is gradually cooled at a cooling rate of up to 200 degrees Celsius per hour to a temperature below the solidification point where the slag spontaneously disintegrates and optionally the remaining portion the slag is adjusted to a granulometry such that at least 90% by weight of the resulting flux has a particle size below 100 mm and preferably below 10 mm. A process for the production of secondary metallurgy slag agglomeration slurries according to claim 3, characterized in that the flux is impregnated with other fluxes such as limestone, limestone, dolomite, dolomitic limestone, magnesite, undersize coke, waste or metallurgical by-products or cement industry, so that the resulting flux has a ratio of CaO / SiO 2 and CaO / Al 2 O 3 higher than 1.25. An agglomeration mixture for producing an agglomerate for use as a charge in blast furnaces, characterized in that it comprises, from the metal charge agglomeration and to less than 10% by weight, preferably 0.5 to 1.5% by weight, of the total charge from the flux Claim 1 and / or 2, wherein the resulting agglomeration contains less than 5 wt .-% A1203.
    [6]
    6. Use of slags from secondary metallurgy as flux to produce an agglomeration mixture for the production of the agglomerates for use as charge in blast furnaces.
    类似技术:
    公开号 | 公开日 | 专利标题
    AT516369B1|2019-03-15|Flux, process for its preparation, agglomeration mixture and use of slag from the secondary metallurgy
    EP0770149B1|1999-01-20|Process for producing hydraulic binders and/or alloys, e.g. ferrochromium or ferrovanadium
    DE2926482C2|1983-03-03|Process for the recovery and utilization of useful substances from a metal melt
    DE2719743A1|1977-11-17|BINDER COMPOSITION AND ITS USE
    DE2645155A1|1977-04-14|FLOWS AND CONDITIONERS FOR SLAGGING AND METHODS FOR IMPROVING FLOW PROPERTIES AND CONDITIONING MELTS
    EP2843063B1|2016-07-13|A method for treating a steel slag and a hydraulic mineral binder
    EP0061012A1|1982-09-29|Process for producing desulfurizing agents for pig iron and steel melts
    DE2255234A1|1973-05-17|LIME COMPOSITION
    DE3347685C1|1985-04-04|Process for the production of ferromanganese
    DE3341154C2|1988-09-22|
    EP2892860B1|2020-08-19|Method for the treatment of steelwork slag
    EP0235291B1|1990-02-07|Method for obtaining vanadium slag
    EP0031552B1|1984-11-21|Desulphurising composition and process for its production
    DE1758799B1|1971-12-23|PROCESS FOR THE MELT METALLURGICAL PRODUCTION OF VANADIUM ALLOYS
    DE3347686C1|1985-04-18|Process for producing ferrochromium
    EP3074540B1|2020-05-06|Method for treating desulfurization slag
    DE2545340B2|1978-02-16|METHOD OF DESULFURIZING MOLTEN STEEL
    DE102016007030B4|2018-03-22|Process for the complete metallurgical processing of Manfeld copper slags by production of polymineral mass products
    DE896561C|1953-11-12|Method of treating slag
    DE202014100884U1|2014-03-13|Slag conditioner for desulfurization in secondary metallurgy of steel
    DE4331156C1|1995-05-18|Electroplating sludge use in mfr. of additives for metal casting industries
    DE941392C|1956-04-12|Process for the extraction of zinc from oxidic zinc-containing material with carbon-containing reducing agents in an electric arc furnace
    DE1646432C3|1976-04-29|Basic refractory mass
    JP4772290B2|2011-09-14|Method for producing sintered ore and sintered ore
    AT360570B|1981-01-26|MEASUREMENT FOR THE DESULFURATION OF IRON METAL MELT
    同族专利:
    公开号 | 公开日
    RU2016103760A3|2018-04-27|
    WO2015003669A1|2015-01-15|
    US10435760B2|2019-10-08|
    CZ2013531A3|2015-02-04|
    AT516369B1|2019-03-15|
    PL232186B1|2019-05-31|
    AT516369A3|2019-03-15|
    RO131333A2|2016-08-30|
    SK50492015A3|2016-04-01|
    CZ304951B6|2015-02-04|
    PL415845A1|2016-08-01|
    CN105431557A|2016-03-23|
    DE112014003176T5|2016-03-31|
    UA117753C2|2018-09-25|
    RU2016103760A|2017-08-11|
    SK288758B6|2020-06-02|
    US20160160302A1|2016-06-09|
    RO131333B1|2021-04-29|
    RU2671781C2|2018-11-06|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    SU783355A1|1978-12-29|1980-11-30|Грузинский Ордена Ленина И Ордена Трудового Красного Знамени Политехнический Институт Им. В.И.Ленина|Method of preparing agglomeration charge for sintering|
    CS222330B1|1981-01-30|1983-06-24|Libor Odstrcil|Method of preparation of the steelmaker slag for its reutilization as the charge in the metallurgical aggregates|
    RU2064508C1|1993-03-15|1996-07-27|Гурьевский металлургический завод им.М.К.Курако|Exothermic briquette for deoxidation and alloying of killed steel|
    US5397379A|1993-09-22|1995-03-14|Oglebay Norton Company|Process and additive for the ladle refining of steel|
    JP3455287B2|1994-06-16|2003-10-14|セイレイ工業株式会社|Rotary padding of ridge coater|
    RU2092587C1|1995-03-17|1997-10-10|Акционерное общество открытого типа "Комбинат Южуралникель"|Method of processing oxidized nickel-containing materials|
    DE19522320C1|1995-06-20|1996-08-22|Joseph E Doumet|Cooling and solidifying red hot molten blast furnace slag in metallurgy|
    US6179895B1|1996-12-11|2001-01-30|Performix Technologies, Ltd.|Basic tundish flux composition for steelmaking processes|
    JPH10265827A|1997-03-25|1998-10-06|Kawasaki Steel Corp|Regenerating/utilizing method of refined slag in chromium-containing steel and regenerating/utilizing method of metallic component contained in the slag|
    JP4084906B2|1999-05-21|2008-04-30|株式会社神戸製鋼所|Method for producing sintered ore and sintered ore|
    WO2002038816A1|2000-11-13|2002-05-16|Demolizioni Industriali S.R.L.|Method and apparatus for treatment of metallurgical slag and the like|
    US6565623B2|2001-03-20|2003-05-20|Startec Iron Llc|Method and apparatus for curing self-reducing agglomerates|
    JP4669189B2|2001-06-18|2011-04-13|株式会社神戸製鋼所|Production of granular metallic iron|
    AT412283B|2003-05-16|2004-12-27|Voest Alpine Ind Anlagen|METHOD FOR RECYCLING SLAG|
    BE1016098A3|2004-06-24|2006-03-07|Lhoist Rech & Dev Sa|Mobile slag fine granulation.|
    ITMI20050538A1|2005-04-01|2006-10-02|Techint Spa|METHOD AND APPARATUS FOR THE RECOVERY OF SECONDARY METALLURGY-LF-AND RECYCLING RECYCLING IN THE STEEL PRODUCTION PROCESS THROUGH ELECTRIC ARC OVEN|
    US7727328B2|2006-05-16|2010-06-01|Harsco Corporation|Regenerated calcium aluminate product and process of manufacture|
    KR101259374B1|2007-12-31|2013-04-30|주식회사 포스코|Method for manufacturing high cleaness bearing steel|
    JP5420935B2|2008-04-09|2014-02-19|株式会社神戸製鋼所|Manufacturing method of granular metallic iron|
    CZ301924B6|2009-02-10|2010-08-04|Raclavský@Milan|Refining technology of and a device for treating metalline zinc-containing waste in revolving furnace|
    DE102009023928A1|2009-06-04|2010-12-09|Rheinkalk Gmbh|Process for producing an agglomerate|
    JP5699567B2|2010-11-29|2015-04-15|Ｊｆｅスチール株式会社|Method for producing sintered ore|
    US8523977B2|2011-01-14|2013-09-03|Nucor Corporation|Method of desulfurizing steel|
    FR2991693B1|2012-06-12|2014-08-08|Centre Nat Rech Scient|METHOD FOR PROCESSING CONVERSION STEEL LAYER|US20160333431A1|2014-01-31|2016-11-17|Saudi Basic Industries Corporation|Use of ladle furnace slag from al-killed steel in si-killed steelmaking as calcium aluminate flux|
    FI127031B|2015-02-05|2017-10-13|OutotecOy|PROCEDURE AND ARRANGEMENTS FOR PREPARING CHROMITE CONCENTRATE FOR PELLETING AND SINTERING AND FEED FOR PELLETING|
    BE1023884B1|2016-07-08|2017-09-04|Lhoist Rech Et Developpement Sa|PROCESS FOR PRODUCING BRIQUETTES CONTAINING ACTIVE IRON OXIDE AND BRIQUETTES THUS OBTAINED|
    KR101798846B1|2016-09-12|2017-11-17|주식회사 포스코|Blocking material and manufacturing method of alloy steel using the same|
    CN108611487A|2018-04-04|2018-10-02|首钢集团有限公司|A kind of resource utilization method of the solid waste containing magnesium|
    AU2020246810A1|2019-03-22|2021-07-08|Tata Steel Nederland Technology B.V.|Method of manufacturing iron in a metallurgical vessel|
    US10759697B1|2019-06-11|2020-09-01|MSB Global, Inc.|Curable formulations for structural and non-structural applications|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    CZ2013-531A|CZ2013531A3|2013-07-08|2013-07-08|Agglomeration slagging medium, process for preparing the slagging medium, agglomeration mixture for producing agglomerate and use of secondary metallurgy slags as slagging media for producing the agglomeration mixture um|
    PCT/CZ2014/000075|WO2015003669A1|2013-07-08|2014-07-02|Fluxing agent, process of its production, agglomeration mixture and use of slug from secondary metallurgy|
    [返回顶部]