• 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 a device for controlling process gases (11) in a plant for producing direct-reduced metal ores (8). This plant (8) has at least one reduction unit (10) (eg fluidized-bed reactor system, fixed-bed reduction shaft, etc.), a device (18) connected upstream of the reduction unit (10) for separating gas mixtures (18) with an associated compressor device (17) and a reduction unit (10 ) downstream gas cleaning device (13). The process gases (11) necessary for the production of directly reduced metal ores are partially recovered by recycling from the production process itself and partly from a plant via a supply line (16) which opens into a return line (14) for the process gases (11) for raw iron production (1) such as a smelting reduction plant (1) supplied. In this case, the gas purification device (13) of the device for a flow control of the process gases (11) is equipped. Furthermore, the device has a pressure control device (15) which is mounted in front of a confluence of the feed line (16) in the return line (14) for the process gases (11) such that a pressure level for the device for the separation of gas mixtures (18) associated compressor device (17) is kept constant. By means of the device according to the invention, the process gases (9, 11) in a plant for the production of directly reduced metal ores (8) can be optimally regulated such that often expensive compressors in the return line (14) are eliminated and investment and operating costs, in particular electricity, are lower can.
    公开号:AT510565A4
    申请号:T906/2011
    申请日:2011-06-21
    公开日:2012-05-15
    发明作者:Norbert Dipl Ing Rein；Gerald Dipl Ing Rosenfellner；Robert Dipl Ing Mba Millner；Jan Friedemann Dipl Ing Dr Plaul
    申请人:Siemens Vai Metals Tech Gmbh；
    IPC主号:
    专利说明:

    5 201103315 «♦ • + 1 • t ··································································· t * t *
    description
    Device for controlling process gases in a plant for the production of directly reduced metal ores
    Technical field 10 15 20
    The invention relates to apparatus for controlling process gases in a plant for the production of directly reduced metal ores. In this case, a plant for the production of directly reduced metal ores, in particular iron, at least one reduction unit (eg fluidized bed reactor system, fixed bed reduction shaft or eg MIDREX® reduction shaft, etc.), a reduction unit upstream means for the separation of gas mixtures with an associated compressor device and a gas purification device downstream of the reduction unit. The process gases necessary for the production of directly reduced metal ores are partly obtained by recycling from the production process itself and partly from a plant for the production of pig iron, such as a feed line, which leads into a return line for the process gases. fed to a smelting reduction plant. 25
    State of the art
    A so-called direct reduction of metal ores or metals, in particular iron ore or iron oxide, for example, in its own facility, a so-called
    Direct reduction plant, done. Such a plant for the production of directly reduced metals or sponge iron, which is also referred to as directly reduced iron (DRI "Direct Reduced Iron), usually comprises at least one reduction aggregate such as e.g. a fixed-bed reduction well, a fluidized-bed reactor system, etc., depending on whether the metal to be reduced is present, for example, in particulate or fine-particulate form or for 201103315 ♦ · 2 ·················································································· Further processing to pig iron, pig iron-like products or for steel production, etc. is required.
    In the case of direct reduction of metal ores or iron ore, the material to be reduced (for example, metal ore, iron ore, iron oxide, etc.) is introduced in lump form - for example as lump or pellets - or in fine particle form into the at least one reduction unit of the plant. Then, the material in the reduction unit under the counter 10 flow principle of a process gas - the so-called reducing gas - flows through. In this way the material, e.g. Iron oxide from the reducing gas to e.g. Wholly or partially reduced so-called sponge iron and the reducing gas thereby oxidized. The reduced material, such as sponge iron, then exhibits e.g. a degree of metallization of about 45 to more than 95%.
    The process gases necessary for the reduction, such as e.g. For example, the reducing gas is used in a melted carburettor, e.g. obtained in a smelting reduction process (for example COREX®, FINEX®, etc.) or coal gasifier and preferably in the middle to lower fourth of the reduction unit or, in the case of fluidized bed reactors, preferably introduced into the first fluidized bed reactor. The e.g. Reduction gas produced in a melted gasifier is preferably 750 to 1000 ° C hot, dusty, as well as carbon monoxide and hydrogen (e.g., 70 to 90% CO and H2). The reducing gas rises in the reduction unit upwards or in the case of a fluidized-bed reactor from reactor to reactor and thereby reduces the material (for example metal ore, iron ore,
    Iron oxide, etc.) preferably in countercurrent. Then, the reducing gas is discharged as so-called off-gas from the reduction unit. By means of a gas purifier downstream of the reduction unit (eg gas scrubber) and at least partially treated as so-called recycle gas for treatment in a device preceding the reduction unit. * ♦ · · · · · ♦ ····· • ·· ♦ · * t · t · · · ·
    Separation of gas mixtures, in particular CO 2 removal device (for example, pressure swing adsorption or vacuum pressure swing adsorption, etc.) / forwarded with associated compressor device. After the treatment in the device for separating gas mixtures, the gas can be introduced again as a reducing gas in the reduction unit, wherein a pressure necessary for the device for separating gas mixtures, which is built up with the aid of the associated compressor device (eg compressor), is reduced again or has to be reduced.
    In addition to the e.g. partial recycling of the process gases used in the plant is called export gas, which is e.g. from the process of pig iron production or from a smelting reduction process such as withdrawn from the COREX® or FINEX® process because it can no longer be used there, used for the reduction process in the reduction unit. The term "export gas" serves in particular as a name for that part of the so-called top gas, which 20 withdrawn from the smelting reduction process or the production of pig iron, usually cooled and dedusted, in particular dry dedusted, and optionally other process gases such as excess gas from the melter gasifier. The top gas is usually the used reducing gas from a
    Blast furnace, a melter gasifier or a reduction shaft / fluidized bed reactor called.
    If the export gas is from one or more smelting reduction plants, e.g. deducted on the basis of COREX® and / or FINEX® process for the production of directly reduced metal, such a system is referred to as a so-called composite system. The export gas is introduced via a feed line into the plant for the production of directly reduced metal or iron and used in the respective reduction unit (eg fluidized bed reactor system, reduction shaft furnace, MIDREX® reduction shaft, etc.), wherein the supplied export gas with the recycle gas of Appendix 35 201103315 4
    for the production of directly reduced metal ores or iron can mix.
    However, pressure differences usually occur between the supplied export gas and the process gases of the plant for the production of directly reduced metal, or pressure values may occur at the inlet of the export gas, which provide a pressure of approximately 0.8 to approximately 2 bar overpressure can have. In addition, the amount of export gas supplied from one or more smelting reduction plants may fluctuate up to 10%, for example, which may cause variations in the flow rate of process gases in the reduction process. 15 For an optimal functioning of the reduction process in the plant for the production of directly reduced metal or iron, however, an approximately constant inlet pressure in the device for the separation of gas mixtures or at the associated compressor device is necessary. Usually, the inlet pressure at the compressor device should be e.g. constant at about 2 bar overpressure or the inlet pressure level for the means for separating gas mixtures e.g. constant at approx. 3 to 8 bar overpressure, in order to achieve an efficient and economical CO 2 removal from the 25 process gases.
    In addition, an approximately constant amount of reducing gas is assumed in the reduction unit. This approximately constant amount of gas or a ratio of the amount of reduction gas and directly reduced material (metal, iron (DRI), etc.) determines, for example, the product quality of the directly reduced metal or iron. Therefore, depending on the desired product quality, a specifically selected, approximately constant amount of reducing gas in the reduction unit is necessary. Usually, therefore, for example, in a complex system for regulating the export gas pressure or for a 201103315 5
    * · »· · · ♦
    constant input pressure at the device for the separation of gas mixtures associated compressor device one or more compressors used. This compressor or compressors are e.g. mounted in a return line for the recycle gas or before a junction of the feed line of the export gas. In addition, the flow control for adjusting the specific, desired reduction gas amount for the reduction process via a complex and complex valve station, which is mounted between the means for separating gas mixtures and a reduction unit upstream of the heater for the reducing gas.
    As a result, a high pressure drop is usually caused by a required, relatively high operating pressure of the device for separating gas mixtures, in particular when using a vacuum pressure swing adsorption (VPSA), and a relatively low operating pressure of the reduction unit. Thus, for example, when using a pressure swing system and a so-called MIDREX® reduction shaft as a reduction unit due to the respectively required operating pressure about 1 to 5 bar destroyed. In addition to a significant pressure drop due to the flow control by the valve station, the use of one or more compressors in the recycle gas line has the disadvantage that both the investment and the maintenance costs for the system are relatively high.
    Presentation of the invention
    The invention is therefore based on the object to find a simple device for controlling process gases in a plant for the production of directly reduced metal ores or iron, which reduces pressure losses within the system or avoided in a simple manner and costs are reduced. 6 201103315 ♦ · • ♦ »·
    The solution of this object is achieved by a device of the type specified, wherein the gas cleaning device, which is connected downstream of the at least one reduction unit, is equipped for a flow control of the process gases 5. In addition, the device comprises a pressure control device, which is mounted before a confluence of the feed line in a return line for the process gases, in particular the so-called off-gas, such that a pressure level for the means for separating gas mixtures with 10 associated compressor device is kept constant.
    The main aspect of the proposed solution according to the invention is that a pressure control of the process gases, in particular for a mixture of recycle gas (= off-gas in the recirculation or recycle gas line of the plant) and supplied export gas from a plant for pig iron production, in particular a smelting reduction plant, for example on the basis of the COREX® and / or FINEX® method, via a pressure control device, e.g. Pressure holding valves, expansion turbine, 20 etc. takes place. This is despite pressure fluctuations - especially in the supply of the export gas - for a constant pressure level of about 2 bar overpressure at the entrance of the device for the separation of gas mixtures associated compression device (eg compressor) or for a constant pressure level 25 for the device for separation of gas mixtures {eg (V) PSA, etc.). As a result, the compressors in the recirculation or recycle gas line are eliminated and both investment and maintenance costs for the plant for the production of directly reduced metal or iron are reduced. Also sink by a low power consumption of the system, the ongoing operating costs. For a regulation or adjustment of the amount of process gases, in particular reducing gas, which is finally fed to the reduction unit, the gas purification device downstream of the reduction unit (for example gas scrubber, etc.) is used. For this purpose, the gas cleaning device has a flow control device, such as a flow control device. 201103315 »*« · · · ♦ »ι β ·« * · «• I · · · ·« «· 7
    a through valve, adjustable Venturi throat, etc. on. By means of this flow control device, that amount of process gases is then defined which is purified in the gas purification device and flows through it. 5 Thus, a complex and complex valve station, which is mounted between the means for separating gas mixtures and a reduction unit upstream heating means for the reducing gas can be saved for the flow control. In addition to the cost savings are reduced or avoided 10 by a flow or volume control by means of the gas cleaning device pressure losses within the plant for the production of directly reduced metal ores or iron. Ideally, the device according to the invention can also be used with different reduction units - such as e.g. Fluidized bed reactor systems, a fixed bed reduction or MIDREX® reduction well.
    Furthermore, it is also advantageous if the quantity control of the 20 process gases of the gas purification device is configured such that a quantity of process gases supplied to the reduction unit is set and kept constant. By provided in the gas cleaning device device for flow control can be set in a very simple manner, a 25 amount of reducing gas for each reduction unit used. In addition, the flow control in the gas purifier downstream of the reduction unit has the advantage that a differential pressure (e.g., typically between 0.3 to 0.5 bar) 30 for the gas scrubber can be optimized for scrubbing action.
    An advantageous development of the device according to the invention additionally has a derivative for the pressure control upstream of the pressure control device, via which excess amounts of process gas, in particular as export gas of the plant for the production of directly reduced metals or iron can be derived. In this case, it is more advantageous to obtain the following: ## EQU1 ##
    Way provided in the derivative for excess amounts of process gas a control valve. On the one hand, the pressure level for the device for separating gas mixtures can be optimally adjusted via the discharge. In addition, 5 excess amounts of gas, in particular excess recycle gas, as so-called export gas of the plant for the production of directly reduced metal ores are derived. Thus, in addition, the amount of gas for the reduction unit can be set even more accurately and it will be compensated in a simple way 10 variations in the supplied export gas quantity from the plant for pig iron production.
    It is favorable if the device for the separation of gas mixtures is arranged as a device for pressure swing adsorption (PSA) 15 or as a device for vacuum pressure swing adsorption (VPSA). Pressure swing adsorption usually refers to a physical process for separating gas mixtures under pressure by means of so-called adsorption (= retention of, for example, certain gas components of the gas mixture, such as H 2 O, CO 2, etc. on a substance or so-called adsorbent). In the production of directly reduced metal ores or iron C02 is removed from the process gases by means of the device for pressure swing adsorption so that they can be used again for the reduction process 25 in the reduction unit and can be oxidized.
    In a device for pressure swing adsorption or pressure swing adsorption (PSA), the 30 to be separated gas mixture under elevated pressure (eg, about 6 to 10 bar) into the device, which is filled with an adsorbent, introduced so that it is flowed through and to adsorb one or more components to be removed (eg H 2 O, CO 2). The remaining gas mixture leaves the device via the outlet. If the adsorbent is loaded, the process is e.g. switched over valves and under pressure reduction so that the adsorbed component or components are desorbed again and this component and this component 201103315 9 • * «· ** · * * I ft * * · # • φ · · *« «* * · · · Or components are desorbed from the adsorbent. A precise adjustment of a switching time usually depends on a desired purity of the gases or component. If pressure is operated at at least one pressure below atmospheric pressure, the method also becomes a vacuum
    Pressure Swing Adsorption (VPSA), which usually requires one or more additional vacuum pumps. The input pressure of the process gas for the PSA or VPSA is thereby generated via at least one of the PSA 10 or VPSA upstream compression device, in particular a compressor.
    In the case of the device according to the invention, however, there is the advantage that a higher so-called feed gas pressure for the compression for the separation of gas mixtures can be achieved by means of the quantity control via the gas cleaning device and / or the pressure control device. There is thus the possibility of using a PSA device, whereby costs for a VPSA device or for vacuum pumps 20 can be saved.
    An expedient development of the device according to the invention is characterized in that the pressure control device consists of at least one pressure-holding valve 25, which upstream of an inlet of the supply line for the so-called export gas from a plant for pig iron production such. a smelting reduction plant or between the first and second compressor stage is mounted. Via a pressure-maintaining valve, the pressure of the process gases, in particular the supplied export gas from the plant for the production of pig iron, can be adjusted to a constant and desired pressure level for the device for separating gas mixtures or CO 2 removal in a simple and cost-effective manner. In this case, the export gas from 35 of the supply line specifically off-gas or recycle gas from the
    Recycle gas line, which has a slightly higher pressure, added to a desired pressure level at the inlet 201103315 »» «* · · · · · · * * f« »· * * * * * · · · * * + ································································································
    Depending on the selected pressure level for the device for separating gas mixtures and the reduction unit used in each case (solidified reduction shaft, fluidized bed reactor system, etc.), the pressure control device can also be designed advantageously as expansion turbine, which is mounted in front of the mouth of the supply line for export gas. Not only is the pressure controlled by an expansion turbine, but electrical energy can also be generated at the same time, or at least part of the mechanical energy of the compressor (eg compressor) associated with the device for separating gas mixtures can be substituted, for example via mechanical coupling. In this way, in addition, the power requirement of the plant for the production of directly reduced metal ores or iron can be reduced.
    Brief description of the drawing
    The invention will now be described by way of example with reference to the accompanying figure. FIG. 1 shows, by way of example and schematically, a design of the device according to the invention for controlling process gases in a plant for producing directly reduced metals, in particular iron.
    Embodiment of the invention
    FIG. 1 shows, schematically and by way of example, a construction of a so-called composite installation for producing directly reduced metal ores, in particular iron, which comprises the device according to the invention. In a combined plant, an export gas 7 is usually a plant for pig iron production 1, in particular a smelting reduction plant, as a reducing gas 9 for a reduction of 201103315 • «• · fe 4 • · • · Μ« «
    «B 11
    Metal ores, iron ore, etc. used in a plant for the production of directly reduced metal ores, iron, etc.
    A plant for pig iron production 1 such as the smelting reduction plant 1 exemplified in Figure 1 5 based on the so-called COREX® process comprises at least one reduction shaft 3, in which the carrier of the metal ore, in particular iron ore (lump, pellets, sinter) with a reducing gas. 5 the smelting reduction plant 1 is reduced. The reducing gas 5 of the smelting reduction plant 1 is thereby produced in a melter gasifier 4 by gasification of coal from a coal / fine ore tank 2 (and possibly a small proportion of coke) with oxygen (90% or more). 15 The reducing gas 5 is partially introduced from the melter gasifier 4 in the reduction shaft 3 in the lower part and above as so-called top gas 6 again derived. The top gas 6 is then freed from coarse dust in a dust collector or cyclone, cooled in a chiller and cleaned in a gas scrubber or scrubber. In the line of the top gas 6 of the smelting reduction plant also opens a line which diverts a portion of the reducing gas 5 (so-called excess gas). Also, the reducing gas 5 is cooled and cleaned in a gas scrubber 25. The top gas 6 and the supplied reducing gas 5 are then discharged as so-called export gas 7 of the smelting reduction plant 1 and the COREX® plant and fed via a supply line 16 of the plant for the production of directly reduced metal ores 8. 30
    In addition to the COREX® process, in which a two-stage smelting reduction process (= combination of a direct reduction process (prereduction of, for example, iron ore to sponge iron) with a smelting process (main reduction)), a pulp ore (e.g., iron ore) in particulate form, e.g. Lump ore, pellet, etc. is introduced, the export gas 7 can also be withdrawn from a smelting reduction plant 1 based on the FINEX® process or from a coal gasification plant. In the FINEX® process, the metal ore or
    Iron ore introduced as fine ore and the prereduction takes place for example in a fluidized bed reactor system.
    The export gas 7 passes as process gas via the Zuftihrleitung 16 in the plant for the production of directly reduced metal ores 8 or in the DR system 8. In this case, the feed line 16 opens into a return line 14, in which the so-called off-gas or recycle gas 11 of the DR plant 8 is recycled again for the reduction process and returned.
    The export gas 7 and the recycle gas 11 are sent to a compactor 17 - e.g. a compressor-fed. It should be noted that there is a pressure difference between the export gas 7 and the recycle gas 11. The export gas has, for example, a pressure of 1 to 2 bar overpressure. The recycle gas 11 has e.g. a pressure of approx. 2.5 bar overpressure. In addition, the supplied export gas 7 also fluctuates in quantity (for example, by 10%). In order to reduce the pressure at the inlet of the compressor 17 and thus also for a downstream device for separating gas mixtures 18, which has a constant pressure level of e.g. 6 bar pressure required to keep constant, a pressure control device 15 is provided in the return line 14 before the confluence of the supply line 16. As a pressure control device 15, for example, a pressure-holding valve 15 may be provided. The recycle gas 11, which is not necessary for pressure regulation and quantity compensation, can be removed, for example via a discharge line 19, as a so-called export gas of the DR plant 8. This derivative 19 also has a valve for pressure control.
    After the compressor 17, the process gas 7 is supplied to the device for separating gas mixtures 18 for CO 2 removal. This device 18 may, for example, at sufficiently high pressure level as a device for pressure swing adsorption (PSA) 18 201103315 • · Φ · »# · * »» Be executed. Is e.g. due to a reduction unit 10 used to select a lower pressure level for the means for the separation of gas mixtures 18, so can also a so-called vacuum pressure-swing adsorption-5 device 18 (VPSA) can be used. Then, the process gas freed from CO 2 is heated in a heater 20 for the reduction process and sent as a reducing gas 9 to the reduction unit 10. Part of the process gas is used thermally in the reduction gas furnace to heat the process gas which has largely been purified of the CO 2 and blown off as exhaust gas via an exhaust gas disposal 21.
    The reducing gas 9 can also oxygen O2 for the purpose of partial combustion and the associated increase in temperature-15 are supplied. Then the reducing gas 9 is introduced into the reduction unit 10, in which the material to be reduced fed via a material feed - e.g. Metal ore, iron ore, etc., introduced to countercurrently reduce this material. Depending on the material to be reduced (ore in particulate form, pellet, fine ore, etc.), a fixed-bed reduction shaft, MIDREX® reduction shaft or a fluidized-bed reactor system can be used as the reduction unit 20. The reducing gas 9 is then removed from the upper part of the
    Reduction unit 10 as off-gas, top-gas or recycle gas 11 derived and cooled in a cooling device 12. For the purification of the recycle gas 11, a reduction unit 10 downstream gas cleaning device 30 is provided 13. The gas purifier 13 has means for flow control, such as flow control. a through-valve or an annular gap washer, etc. on. By this valve in the gas cleaning device 13, that amount of process gases 7, 11 is set, which is necessary or desired for the flow or volume control for the reduction unit 10. The purified recycle gas 11 is then returned to the reduction process via the return line 14 and by the pressure control device 15. * 14 201103315
    Depending on the selected pressure level for the device for separating gas mixtures 18 or for CO 2 removal and for the reduction unit 10, it is also possible to use an expansion turbine instead of a 5 pressure holding valve 15 as a pressure control device 15 in the return line 14. At the same time, the pressure is controlled via the expansion turbine and, for example, electrical energy is generated, which in the DR system 8 is generated, for example. can be used for the compressor 17 10. In addition, at a higher selected pressure (e.g., 3 to 6 bar) for the reduction unit 10, it may, for example, have a small size and also be e.g. the size of the device for the separation of gas mixtures 18 are chosen to be smaller, since a hydraulic limit -15 decisive for this is usually an operating volume flow-for a capacity limit is crucial. 201103315 • * • ·· * 15 *
    • · ♦ ♦ φ · 4 | t t «·« ♦ I
    References «1 Plant for the production of pig iron, in particular smelting reduction plant 5 2 coal / fine ore tanks 3 reduction shaft 4 melter gasifier 5 reduction gas of smelting plant 6 top gas of smelting plant 10 7 export gas of smelting plant 8 plant for the production of directly reduced metal ore or iron (DR plant) 9 reducing gas 10 Reduction unit with material feed 15 11 Off-gas, top gas or recycle gas 12 Cooling device 13 Gas cleaning device with quantity control (eg annular gap scrubber) 14 Return line 20 15 Pressure control device 16 Feed line for export gas of smelting reduction plant 17 Compression device (eg compressor) 18 Device for separating gas mixtures - C02 removal 19 Discharge for export gas of the DR plant 20 Heating device for reducing gas (eg
    Reducing gas stove)
    Waste gas disposal 21 25
    权利要求:
    Claims (7)
    [1]
    201103315 ···························································································································································································································· Apparatus for controlling process gases in a plant for producing directly reduced metal ores (8) with at least one reduction unit (10), a device upstream of the reduction unit (10) for separating gas mixtures (18) with associated compressor device (17) and a reduction unit (10) downstream gas purification device (13), wherein at least a portion of the process gases (7) via a supply line (16) from a plant for pig iron production (1), in particular a smelting reduction plant, is supplied, characterized in that the gas cleaning device (13) for a flow control of the process gases (11) is equipped, and that the device comprises a pressure control device (15), which upstream of a confluence of the feed line (16) in a return line (14) for the Pr ozessgase (11), in particular the so-called off-gas (11), is mounted such that a pressure level for the means for separating gas mixtures (18) with associated compressor means (17) is kept constant.
    [2]
    2. Apparatus according to claim 1, characterized in that the flow control of the process gases (11) of the gas cleaning device (13) is designed such that the reduction unit (10) supplied amount of process gases (7, 9, 11) is set and kept constant ,
    [3]
    3. Device according to one of claims 1 to 2, characterized in that in addition to the pressure control in front of the pressure control device (15) has a derivative (19) is provided, via which excess amounts of process gas (11) can be derived. 201103315 «* ··········································································································································································
    [4]
    4. Apparatus according to claim 3, characterized in that the discharge line (19) for excess amounts of process gas (11) has a control valve.
    [5]
    5. Device according to one of claims 1 to 4, characterized in that the means for separating gas mixtures (18) is arranged as a device for pressure swing adsorption or as a device for vacuum pressure swing adsorption.
    [6]
    6. Device according to one of claims 1 to 5, characterized in that the pressure control device (15) consists of at least one pressure-holding valve, which is mounted in front of a junction of the supply line (16).
    [7]
    7. Device according to one of claims 1 to 5, characterized in that the pressure control device (15) is designed as expansion turbine, which is mounted in front of a junction of the feed line (16).
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    同族专利:
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    UA110382C2|2015-12-25|
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    CN112522727B|2020-12-02|2021-11-12|上海毅镤新能源科技有限公司|Hydrogen production plant|
    法律状态:
    2016-06-15| PC| Change of the owner|Owner name: PRIMETALS TECHNOLOGIES AUSTRIA GMBH, AT Effective date: 20160415 |
    2020-02-15| MM01| Lapse because of not paying annual fees|Effective date: 20190621 |
    优先权:
    申请号 | 申请日 | 专利标题
    ATA906/2011A|AT510565B1|2011-06-21|2011-06-21|DEVICE FOR REGULATING PROCESS GASES IN A PLANT FOR PRODUCING DIRECTLY REDUCED METAL ORCHES|ATA906/2011A| AT510565B1|2011-06-21|2011-06-21|DEVICE FOR REGULATING PROCESS GASES IN A PLANT FOR PRODUCING DIRECTLY REDUCED METAL ORCHES|
    US14/128,103| US9400139B2|2011-06-21|2012-06-01|Device for the closed-loop control of process gases in a plant for producing directly reduced metal ores|
    PCT/EP2012/060355| WO2012175313A1|2011-06-21|2012-06-01|Device for the closed-loop control of process gases in a plant for producing directly reduced metal ores|
    RU2014101612/05A| RU2596253C2|2011-06-21|2012-06-01|Device for control of process gases in apparatus for producing metal by direct reduction of ore|
    UAA201314987A| UA110382C2|2011-06-21|2012-06-01|A device for close-loop control of process gases in a plant for producing directly reduced metal ores|
    CN201280030575.7A| CN103608089B|2011-06-21|2012-06-01|To the device that the process gas be used in the equipment of the metallic ore manufacturing direct-reduction regulates|
    BR112013032628A| BR112013032628A2|2011-06-21|2012-06-01|device for closed-loop control of process gases in a plant to produce directly reduced metal ores|
    KR1020147001663A| KR20140039315A|2011-06-21|2012-06-01|Device for the closed-loop control of process gases in a plant for producing directly reduced metal ores|
    CA2839975A| CA2839975A1|2011-06-21|2012-06-01|Device for the closed-loop control of process gases in a plant for producing directly reduced metal ores|
    ZA2013/09058A| ZA201309058B|2011-06-21|2013-12-03|Device for the closed-loop control of process gases in a plant for producing directly reduced metals ores|
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