• 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 present invention relates to a process for charging material comprising lumped carbonaceous material and, preferably hot, iron carrier material into a melter gasifier of a melt reduction plant. The particulate carbonaceous material and the, preferably hot, iron carrier material are combined before and / or while they enter the melter gasifier. The ratio of the combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material is variable. The process is characterized in that the combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material are distributed across the cross section of the melter gasifier by means of a dynamic distributor, and the ratio of the combined amounts of, preferably hot, iron carrier material and of particulate carbonaceous material is adjusted depending on the position of the dynamic distribution device.
    公开号:AT511206A4
    申请号:T723/2011
    申请日:2011-05-19
    公开日:2012-10-15
    发明作者:Georg Dipl Ing Dr Aichinger；Franz Dipl Ing Berner；Thomas Ing Eder；Robert Dipl Ing Millner；Jan-Friedemann Dipl Ing Dr Plaul；Norbert Dipl Ing Rein；Andreas Scherney；Kurt Dipl Ing Wieder；Johann Dipl Ing Wurm
    申请人:Siemens Vai Metals Tech Gmbh；
    IPC主号:
    专利说明:

    May 19, 2011 14:53 Siemens CIO P
    No. 4141 S, 5
    201009550 1
    description
    Description of the Invention 5
    FIELD OF THE INVENTION The present invention relates to a process for charging material comprising lumped carbonaceous material and, preferably, hot, iron carrier material, into a smelting gasifier of a smelting reduction plant. 15
    State of the art
    In smelting reduction processes for producing pig iron in a melter gasifier, such as COREX® or FINEX®, for example, material comprising carbonaceous material and carrier material and aggregates is charged to the melter gasifier. The carbonaceous material is gasified with oxygen to a reducing gas, releasing the heat needed to melt the iron carrier material.
    Charcoal-containing material is, for example, chunky coal or carbonaceous briquettes; it is stored in a carbonaceous material storage tank at ambient temperature from which it is fed into the meltdown gasifier. For example, in the case of FIMEX®, the iron carrier material is hot briquetted iron (HBI) or hot compacted iron (HCl). 19/05/2011 14:55
    No .: R601 P.005 / 048 May 19th, 2011 14:53
    Siemens CIO P
    * »E« • ♦ ·
    No. 4141 p. 6 201009550 2
    Hfil is a hot pressed material with a very high content of metallic iron - often over 90% metallization - and a density of about 5 g / cm3, which allows transport by ship, for example. The material is in 5 briquette form, mostly > 25 mms isolated, so it is lumpy. HCl is hot pressed iron with aggregates and lower in metallic iron compared to HBI. Its density is just under 4 g / cm3. HCl is further processed directly in the process of 10 pig iron production after its production, wherein it is crushed by means of crusher used in advantageous form for a meltdown gasifier. In this case, HCl has a temperature of about 550-650 ° C. In the case of COREX®, the iron carrier material is, for example, hot reduced direct iron (DRI).
    Pyrolysis of coal or carbonaceous briquettes at elevated temperatures leads to the formation and release of volatile hydrocarbons and tar. Therefore, the carbonaceous material can not be stored together with hot iron carrier material in a storage container, because caused by the contact with the hot iron carrier material 25 generation and release of volatile
    Hydrocarbons and tar would lead to sticking and clogging in the reservoir and in the lines leading the material to the melter gasifier. 30 The charging of carbonaceous material and iron carrier material in a melter gasifier so far is usually separated.
    Charcoal containing material, for example, from a reservoir for carbonaceous material on 19/05/2011 14:56
    No .: R601 P.006 / 048 19.May 2011 14:54
    Siemens CIC P • * • ** a
    No. 4141 S, 7
    201009550 3 conveying screw supplied to a centrally mounted in the dome of the melter gasifier distributor, of which the carbonaceous material is distributed in the input to the melter gasifier over the 5 cross section of the melter gasifier. Iron carrier material is introduced into the melter gasifier, for example, via a plurality of falling legs arranged over the circumference of the dome of the melter gasifier. 10
    The separate addition of carbonaceous material and iron carrier material in the melter gasifier causes a lot of effort in the construction and the hardening of necessary for the separate 15 addition system components. Moreover, in a separate addition, carbonaceous material and iron carrier material in the material bed in the melter gasifier are not sufficiently well distributed - for example, 20 vertical islands of iron carrier material may form - which adversely affects the meltdown gasification process.
    From EP0299231A1 it is known to charge the carbonaceous material and the iron carrier material centrally through the same opening into the melter gasifier. In such a central charging according to EP0299231A1, it is disadvantageous that just the area of the material bed is supplied with fresh material in which a so-called "dead man". at the 30 meltdown gasification process preheating and
    Reduction processes run less well than in the edge region of the EinschmelzVergasers. In addition, fine and heavy material remains concentrated due to segregation processes in the central area of the material bed. 19/05/2011 14:56
    No .: R601 P.007 / 048 May 19th, 2011 14:54
    Siemens CIO P • · ♦ · • 9 · · · 9 «· • * • ···« 99 • ♦ • »
    No. 4141 p. 8 201009550 4 while coarser and lighter material migrates towards the edge area. Accordingly, the mixture charged onto the material bed is partially and uncontrollably separated again. 5
    Summary of the Invention Technical Fields It is the object of the present invention to provide, in comparison to the prior art, both less build-up and maintenance-related and controlled distribution enabling methods and apparatus for charging material comprising carbonaceous material and, preferably, hot material To provide iron carrier material.
    Technical solution 20
    This object is achieved by a method for charging material comprising lumped carbonaceous material and, preferably hot, biscuit material into a melter gasifier of a smelting reduction plant, wherein the lumped carbonaceous material and the, preferably hot, iron carrier material are combined before and / or as they enter the melter gasifier and the ratio of the combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material is changeable, characterized in that the combined amounts of, preferably hot, iron carrier material and lumpy carbonaceous material by means of a 19/05/2011 14:56
    No .: R601 P.008 / 048 May 19th, 2011 14:54
    Siemens C1C P
    Nr, 4141 S, 9 • · * · · · t · a · * ♦ · ··· ······················································································································································································································· are distributed over the cross section of the melter gasifier / and the ratio of the combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material 5 depending on the position of the dynamic distribution device is adjusted.
    Advantageous Effects of the Invention 10 In such a process, the melter gasifier must have fewer parts and openings for charging than when particulate carbonaceous material and iron carrier material enter the melter gasifier separately from one another
    Hot iron carrier material is iron carrier material having a temperature of over 100 ° C, preferably above 2009C, more preferably above 300 ° C to understand. The iron carrier material contains 20 elemental iron and / or iron oxide. The iron carrier material is present either in lumpy form or lumpy with a proportion of undersize or as a fine grain preferably less than 10 mm, 25 The carbonaceous material is lumpy. The proportion of coal in the lumped carbonaceous material is at least 50 weight%, preferably 70 weight%, particularly preferably 90 weight%. Thus, the weight fraction based on the weight of the components of the 30-piece carbonaceous material to the
    Time at which the components are charged to the reservoir. In addition to coal, for example, coke may also be present in the particulate carbonaceous material. 19/05/2011 14:57
    No .: R601 P.009 / 048 May 19th, 2011 14:55
    Siemtns CIC P • * # * * * ♦ «« φ · I «··· · I · · Φ * ·« * · * · · ··· • * * »«
    No. 4141 5. 10 201009550 6
    In the case of a process according to the invention also in the melter gasifier - preferably via the iron carrier route - charged aggregates such as limestone and / or dolomite and / or quartz are not discussed in detail in the context of this application.
    Preferably, the lumped carbonaceous material and the, preferably hot, iron carrier material are combined into the melter gasifier shortly before and / or during the entry of the mixture obtained by the combination. In this case, lumpy carbonaceous material and, preferably hot, 15 iron carrier material in the feed to
    Melt carburetor - merged together without prior joint storage in a bunker - for example in a chute to the time during which both materials are present outside the melter gasifier 20 together in plant parts, low, preferably below a few seconds, for example up to 10 seconds. This minimizes the risk of pyrolysis of the particulate carbonaceous material caused by contact with hot iron carrier material leading to sticking and clogging of the equipment obtained by combining into the melter gasifier leading equipment.
    The pyrolysis and gasification of lumpy carbonaceous material thus takes place only in the melter gasifier.
    The term melter gasifier does not include a blast furnace. In a blast furnace are mainly layers of coke and iron carriers with aggregates at 19/05/2011 14:57
    No .: R601 P.010 / 048
    May 19, 2011 14:55 Siemens CIC P
    No. 4141 p. 11
    * · * · · ··· ··· 201009550 7 Conditions for the top of the tower. Pyrolysis and degassing of coal does not occur in the blast furnace, but already in the production of the coke, which is charged into the blast furnace, the temperatures in the blast furnace 5 are about 80 to 250 ° C,
    In a meltdown gasification process in a melter gasifier according to the invention, by contrast, not coke is charged, but carbonaceous material, and the charged carbonaceous material is pyrolyzed in the melter gasifier. The in the
    Melting carburetor cup, in the range of material is charged into the melter gasifier, prevailing temperatures are about 1000 ° C. By co-charging particulate carbonaceous material and, preferably hot, iron carrier material, the problem of uncontrolled and undesired inhomogeneous distribution, such as the formation of vertical islands of iron carrier material in the melter gasifier, arising from separate charging can be avoided. In addition, there is no expense associated with the construction and maintenance of the parts required for separate charging. A dynamic distribution device is to be understood as a distribution device which can be moved in a controlled manner during the distribution process. As a result, an outlet opening of the dynamic distribution device can be brought into various positions. Accordingly, the combined amounts of, preferably hot, iron carrier material and lumped carbonaceous material may be directed to different locations of the material bed in the melter gasifier. 19/05/2011 14:57
    No .: R601 P. 011/048 19.May 2011 14:55
    Sitmm C1C P • ♦ ♦ ♦ * • «· · ··· • · · * ·
    No. 4141 p. 12 201009550 8
    The dynamic distribution device can be, for example, a rotary chute or a cardanically suspended chute, which can be moved in such a way that its outlet opening describes, for example, circular or spiral paths or arbitrarily predeterminable paths, whereby different distribution tracks can also be selected.
    Advantageously, the movement pattern of the dynamic distribution device is changeable. 10
    The charged material forms a material bed in the melter gasifier.
    The combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material are distributed across the cross section of the melter gasifier by means of a dynamic distributor, and the ratio of combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material becomes 20 depending on the position of the dynamic
    Distributor set. Because the position of the dynamic distribution device in the melter gasifier dictates the range in which the material to be distributed impinges on the material bed in the melter gasifier, this can control the distribution of, preferably hot, iron carrier material and particulate carbonaceous material on the material bed of the melter gasifier be adjusted according to the requirements of the melter gasification process. As a result, certain distribution patterns of, preferably hot, iron carrier material and lumpy carbonaceous material can be adjusted in the melter gasifier. For example, with phased-wise charging of carbonaceous material with little 19/05/2011 14:58
    No .: R601 P.012 / 048 19. May 201 1 14:56 Siemens CIC P ................ No. 4141 p. 13 ·· «· * ··· • · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · · ·
    Elsenträger material in the melter gasifier targeted to build a dead man of predominantly carbonaceous material. The setting of certain distribution patterns of iron carrier material and carbonaceous material in the meltdown gasifier allows better control of the processes occurring in the melter gasifier by reacting iron carrier material and carbonaceous material. This results in a more stable guidance and a better yield of these processes. 10
    In which area the charging of material onto the material bed in the melter gasifier is particularly conducive to the meltdown gasification process, it can be derived from the properties of the surface. Under the surface of the material bed, the vertically upper layer of the material bed must also be understood. The upper layer is to be understood as meaning a layer with a layer thickness of up to 20 cm. 20
    According to one embodiment of the method according to the invention, the ratio of the combined amounts of, preferably hot, iron carrier material and lumped carbonaceous material is adjusted depending on the properties of the surface of the material bed.
    According to an embodiment of the method according to the invention, the property of the surface of the material bed is the height level and / or the height profile of the material bed,
    According to a further embodiment of the method according to the invention, the property of 19/05/2011 is 14:58
    No .: R601 P.013 / 048
    May 19, 201 1 14:56 Siemens CIO P • · · · · · · · · · «· · ·« · · · · · ·
    No. 4141 p. 14 * * • ···
    201009550 10
    Surface of the material bed the temperature profile on the surface of the material bed.
    Pig iron and slag are tapped at intervals approximately evenly throughout the day from a melter gasifier so that the level of liquid around the melter gasifier does not rise above the level of the oxygen feed nozzles. In operation, it comes, triggered by the tapping, always 10 back to inhomogeneous gasification and
    Reduction ratios. Negative effects of such inhomogeneities on the smelting reduction process can be counteracted by targeted charging to affected areas of the scale. Accordingly, according to an embodiment of the method according to the invention, the ratio of the combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material is set as a function of the tapping sequence followed during operation of the melter gasifier.
    Not only the ratio of the combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material, but also the particle size distribution and the nature of the materials have an influence on the meltdown gasification process. In this case, grain size distribution for the lumpy carbonaceous material is understood to mean the lump size of the lumpy carbonaceous material. Different types of, preferably hot, iron carrier material have, for example, different proportions of metallic iron and iron oxide or other constituents. For example, various types of particulate carbonaceous material have 19/05/2011 14:58
    No .: R601 P. 014/048 19. May 2011 14:56 Siemens CIC P ................ No. 4141 p. 15 ···· # · · · · • · · ································································································································································································································· Shares of coke or other ingredients. Various types of, preferably hot, iron carrier material and particulate carbonaceous material result, for example, from their extraction from different sources. After a
    Embodiment of the method according to the invention, the particle size distribution of, preferably hot, iron carrier material and / or the piece size of the lumpy carbonaceous material is selected depending on the position of the dynamic distribution device. According to a further embodiment of the method according to the invention, the type of charged, preferably hot, elastomeric material and / or the nature of the particulate carbonaceous material 15 is selected as a function of the position of the dynamic distributor.
    A further subject of the present application is a device for charging material comprising lumped carbonaceous material and, preferably hot, iron carrier material into a meltdown gasifier of a smelting reduction plant, with at least one storage container for particulate carbonaceous material, and with at least one storage container for , preferably hot, iron carrier material, wherein from the at least one reservoir for particulate carbonaceous material, a first discharge line for lumped carbonaceous material emanating comprising a first conveyor for controlling the discharge of particulate carbonaceous material, and wherein at least one reservoir for , 19/05/2011 14:59
    No.: R601 P. 015/048 May 19, 2011 14:57
    Siemens CIC P
    No. 4141 p. 16
    201009550 12 preferably hot, iron carrier material, a second discharge line for, preferably hot, iron carrier material emanates, which comprises a second conveyor for controlling the discharge of, preferably hot, 5 iron carrier material, and with an input device for input of material in the Meltdown carburetor wherein the first lumped carbonaceous material discharge line and the second, preferably hot, iron carrier material discharge line 10 enter the input device for inputting material to the meltdown gasifier, characterized in that the input device for inputting material to the melter gasifier is a dynamic one Distributor device for distributing the material in the input comprises, and a device for controlling at least one of the conveying devices from the group - first conveying device for controlling the discharge 20 of lumped carbonaceous material - second conveying device to the Rege tion of the discharge of, preferably hot, iron carrier material depending on the position of the dynamic distribution device 25 is present.
    With such a device, the implementation of the method according to the invention is possible. Carbonaceous material and, preferably, hot iron carrier material 30 may be combined prior to and / or during entry into the melter gasifier.
    The input device for inputting material into the melter gasifier may, for example, be screw conveyors. 19/05/2011 14:59
    No .: R601 P.016 / 048 May 19th, 2011 14:57
    Siemens CIC P
    No. 4141 p. 17
    • · ♦ • ♦ ···· »201009550 13
    Such a device may be operated so that particulate carbonaceous material and, preferably hot, iron carrier material are continuously combined. It may also be operated to intermittently add iron carrier material, preferably hot iron carrier material, into a continuous stream of carbonaceous material. It may also be operated so that intermittently particulate carbonaceous material is added to a continuous stream 10 of iron carrier material, preferably hot iron carrier material.
    It may also be operated by alternating a stream of particulate carbonaceous material and a stream of, preferably hot, iron-carrying material via the input device to input material into the material
    Melt carburetor is entered.
    The input device for inputting material into the melter gasifier comprises a dynamic one
    Distribution device for the distribution of the material when entering. Here, a distribution of the material over the horizontal cross-section of the interior of the EinschmelzVergasers is meant. As a result, certain distribution patterns of, preferably hot, iron carrier material and lumpy carbonaceous material can be set in the melter gasifier. The input device for inputting material into the melter gasifier with dynamic distributor 30 may be, for example, a gimbal-mounted chute or a rotary chute, preferably driven via two axles. 19/05/2011 14:59
    No .: R601 P.017 / 048 19, May 2011 14:57
    Siemens C1C P
    No. 4141 p. 18 »· Φ
    201009550 14
    According to one embodiment of the device according to the invention, two storage containers for, preferably hot, iron carrier material and / or two storage containers for particulate carbonaceous material 5 are present. As a result, a more uniform charging can be ensured, because it is possible to resort to the second, filled reservoir when completely emptying a first reservoir. During the emptying of the second storage container, the first storage container can be refilled to stand by for complete emptying of the second storage container again for the charging. Furthermore, it is thereby possible to charge different types of, preferably hot, iron carrier material and / or different types of lumped carbonaceous material, or to charge different grain sizes of, preferably hot, iron carrier material and / or different piece sizes of lumped carbonaceous material, if 20, the two reservoirs are filled accordingly.
    There may also be more than two storage containers for iron carrier material, preferably hot iron carrier material, and / or more than two storage containers for particulate carbonaceous material. 25
    Wach one embodiment of the device according to the invention, the first conveyor for controlling the discharge of particulate carbonaceous material and / or the second conveyor for controlling the discharge of, preferably hot, iron carrier material comprises one or more material flow flaps. 19/05/2011 15:00
    No .: R601 P.018 / 048 19. May 2011 14:58
    Siemens CIO P
    No. 4141 8. 19 201009550 15
    According to one embodiment of the device according to the invention, the first conveying device for controlling the discharge of particulate carbonaceous material and / or the second conveying device comprises the control of the discharge of, preferably hot,
    Iron carrier material one or more screw conveyors. Screw conveyors allow better flow control than material flow flaps, and the material can be conveyed horizontally, thus making it possible to arrange several reservoirs side by side and convey the materials to the common input device into the melter gasifier.
    According to one embodiment of the device according to the invention, the first delivery device for controlling the discharge of particulate carbonaceous material and / or the second delivery device for regulating the discharge of, preferably hot, iron carrier material comprises one or more 20 rotary valves.
    Rotary valves allow better flow control than material flow flaps and can minimize unwanted gas flow in the presence of a pressure difference across the rotary valve 25 compared to screw conveyors.
    There are also mixed forms possible, for example, a device in which in the first discharge line a screw conveyor for controlling the discharge of particulate 30 carbonaceous material is present, and in the second discharge a material flow flap for controlling the discharge of, preferably hot, iron carrier material available is. Such a mixed form is advantageous, for example, if a 19/05/2011 15:00
    No .: R601 P.019 / 048
    May 9, 2011 14:58 Siemens CIC P
    No. 4141 p. 20 201009550
    * «· 16 continuous stream of particulate carbonaceous material is to be produced.
    According to a preferred embodiment, there is a device for controlling the distribution track realized by the dynamic distribution device for distributing the material during the input. The dynamic distribution device has an exit opening from which the material exits the dynamic distribution device. The distribution track is to be understood as meaning the track that leaves the outlet opening when projecting on a horizontal plane on this plane.
    By a variation of the distribution track over the 15 horizontal cross section of the interior of the
    Melting gasifier can be set in Einschmelzvergaser certain distribution patterns of, preferably hot, iron carrier material and lumpy carbonaceous material. 20
    According to a particularly preferred embodiment, a device for controlling the first conveying device for controlling the discharge of lumped carbonaceous material and / or the second 25 conveying device for controlling the discharge of, preferably hot, iron carrier material as a function of the dynamic distribution device 2ur distribution of Materials available when entering realized distribution track. As a result, a setting 30 of a certain distribution pattern of, preferably hot, iron carrier material and carbonaceous material in the melter gasifier is possible.
    For example, this device serves to control the material flow flaps and / or the screw conveyors. P.020 / 048 19/05/2011 15:00 No .: R601 May 19th, 2011 14:58
    Siemens C1C P
    No. 4141 p. 21 • * • · · »• ♦ · ·
    «♦ •« M
    201009550 17
    Advantageously, at least one device is present for detecting properties of the surface of the material bed formed in the melter gasifier. Such a device can be, for example, a microwave measurement or a radar measurement for determining the height and / or profile and / or temperature and / or the composition of the gas escaping from the material bed or a thermometer for determining the temperature or the temperature profile at the surface of the material bed be. There may also be several such devices.
    According to one embodiment of the invention, a device for controlling the first conveying device for controlling the discharge of lumped carbonaceous material and / or the second conveying device for controlling the discharge of, preferably hot, iron carrier material in dependence of 20 of the device 'for detecting Properties detected on the surface of the material bed formed in the melter gasifier.
    In this Heise the ratio of the combined amounts of, preferably hot, iron carrier material and 25-piece carbonaceous material depending on properties of the surface of the material bed can be adjusted.
    According to one embodiment of the device according to the invention there are at least two reservoirs for lumped carbonaceous material which are filled with lumpy carbonaceous material of different piece size. For example, a first reservoir for particulate carbonaceous material is 19/05/2011 15:01
    No .: R601 P.021 / 048 19th May 2011 14:59
    Siemens CIO P
    No. 4141 p. 22 with a piece size A, and a second storage container for lumped carbonaceous material with a piece size B, the piece sizes A and B being different. A possibly existing third storage container for lumped carbonaceous material is filled with a piece size C, the piece size C being different from the piece sizes A and B. 10 According to one embodiment of the invention
    Device, there are at least two reservoirs for particulate carbonaceous material, which are filled with lumpy carbonaceous material of different types. For example, a first reservoir for 15-piece carbonaceous material is filled with a type A, and a second reservoir for particulate carbonaceous material is filled with a type B, the types A and B being different. An optional third Vortatsbehälter for lumpy 20 carbonaceous material is filled with a type C, the type C is different from the types A and B.
    According to one embodiment of the device according to the invention, there are at least two storage containers for, preferably hot, iron carrier material which with
    Iron carrier material, preferably hot iron carrier material, different grain size are filled. For example, a first reservoir for, preferably hot, carrier material having a grain size A is filled, and a second reservoir for, preferably hot, iron carrier material having a grain size B is filled, wherein the grain sizes A and B are different. An optional third reservoir for, preferably hot, 19/05/2011 15:01
    No .: R601 P.022 / 048 19th May 2011 14:59
    Siemens CIC P
    No. 4141 p. 23 • · i * · ··· * • · * ·········································································································································································································
    Iron carrier material is filled with a grain size C, the grain size C is different from the grain sizes A and B. 5 According to an embodiment of the invention
    Device, there are at least two storage containers for, preferably hot, iron carrier material, which are filled with iron carrier material, preferably hot iron carrier material, different types. For example, a first reservoir for, preferably hot, iron carrier material filled with a type A, and a second reservoir for, preferably hot, iron carrier material filled with a type B, wherein the types A and B are different. A possibly existing third storage container for, preferably hot, iron carrier material is filled with a type C, the type C is different from the types A and B. 20 Description of the execution forms
    With reference to the following schematic exemplary figures, the present invention will be explained with reference to embodiments. 25
    FIG. 1 shows an embodiment of the device according to the invention with material flow flaps. FIG. 2 shows an embodiment of the device according to the invention with screw conveyors. 30
    Figure 1 shows an apparatus for charging material comprising lumped carbonaceous material 1, represented by circles, and hot iron carrier material 2, represented by squares, in a 19/05/2011 15:01
    No .: R601 P.023 / 048 19. May 2011 14:59 Siemens CIC P ................ No. 4141 $ · 24 «·« # · * «« * 201009550 20
    Meltdown gasifier 3 of a smelting reduction plant. The device has a reservoir for particulate carbonaceous material 4 and a reservoir for hot iron carrier-5 material 5. From the reservoir for particulate carbonaceous material 4 is a first discharge line 6 for lumped carbonaceous material goes out, which a first conveyor 7 2ur control of the discharge of lumped carbonaceous material 1 comprises. From the storage container for hot iron carrier material 5 is a second Austragsleitung 0 for hot iron carrier material from which comprises a second conveyor 9 for controlling the discharge of hot iron carrier material 2. The first feeder device 7 for controlling the discharge of particulate carbonaceous material 1 and the second conveying device 9 for controlling the discharge of hot iron carrier material 2 are designed as material flow flaps. These 20 material flow flaps are displaceable, which is represented by straight double arrows; the material flow flaps in a state where they do not narrow the first particulate carbonaceous material discharge line 6 and the second hot iron carrier material discharge line 8, respectively, are shown in Fig. 1; auf die'Darstellung a state in which they are partially inserted and therefore constrict the first discharge line 6 for particulate carbonaceous material or the second 30 Austragsleitung 8 for hot iron carrier material was omitted for reasons of clarity. The lumped carbonaceous material 1 and the hot iron carrier material 2 are combined before they enter the melter gasifier 3, to 19/05/2011 15:02
    No .: R601 P.024 / 048
    May 19, 2011 15:00 Siemens CIC P
    No. 4141 p. 25 ♦
    The first discharge line 6 for particulate carbonaceous material and the second discharge line 8 for hot iron carrier material open into an input device 10 for inputting material into the meltdown gasifier 3. Via the input device 10 for introducing material into the melter gasifier, lumped carbonaceous material is introduced 1 and hot iron carrier material 2 entered into the melter gasifier. The input device 10 for inputting material into the melter gasifier 3 comprises a dynamic distribution device 11 for distributing the material during the input, in the illustrated case a cardan-type suspended chute. The possible rotation of the gimballed chute is indicated by a curved double arrow, which wraps around the dashed line indicated axis of rotation of the rotary motion. The pivoting of the gimbal-mounted chute is indicated by a curved double arrow. By means of 20 gimbaled chute lumpy carbonaceous material 1 and hot iron carrier material 2 are distributed controlled on the material bed 12 in the melter gasifier 3.
    The ratio of the combined amounts of hot iron carrier material 2 and lumped carbonaceous material 1 is changeable. For this purpose, at least one of the conveying devices from the group - first feeder device 7 for controlling the discharge of particulate carbonaceous material - second conveying device 9 for controlling the discharge of hot iron carrier material as a function of the position of the dynamic distribution device 10 controlled. P.025 / 048 19/05/2011 15:02 No .: R601 19, May 2011 15:00 Siemens C1C P ................ No. 4141 p 26 * · «··· * · · • * * · ♦ · * · ·»! ··· • · · · # ♦ * 4
    * * * * # · Ft · I 201009550 22
    Device connected to the controller 13 via the signal line 14 to the dynamic distribution device 11 connected for the purpose of transmitting information about the position of the dynamic distribution device 11. 5 For example, it can be ascertained / at which point of the circular arc described by the movement of the cardanych-suspended chute the gimballed chute is located. The signal line 15 controls the first 10 conveying device 7 designed as a material flow flap for regulating the discharge of lumped carbonaceous material 1 according to the invention as a function of the position of the dynamic distribution device 10.
    According to the invention, the second conveying device 9 designed to regulate the discharge of hot iron carrier material 2 is controlled by the signal line 16 according to the invention as a function of the position of the dynamic distributing device 10. 20 It is also a device for detecting properties of the surface 17 of the material bed formed in melter gasifier present, which is formed in the illustrated case as Radarmesseinrichtung with integrated temperature measuring device. 25 The radar measuring device collects information on height level and height profile of the material bed 12 lm melter gasifier 3. The temperature measuring device collects information about the Teroperaturprofil on the surface of the material bed. This information about 30 properties of the surface of the bed of material formed in the melter gasifier are transmitted via the signal line 18 to the device 13 for controlling the first conveyor for controlling the discharge of particulate carbonaceous material and / or the second 19/05/2011 15:02
    No.: R601 P.026 / 048 19.May 2011 15:00
    Sitmins CIO P
    No. 4141 p. 27 conveyed where they are used to control the discharge of hot iron carrier material depending on the characteristics detected. In this way, the ratio of the combined amounts of hot iron carrier material 2 and lumped carbonaceous material 1 can be adjusted depending on properties of the surface of the material bed. About a 10 information input device 19, the over
    Signal line 20 is connected to the device 13 for controlling the first conveyor for controlling the discharge of particulate carbonaceous material and / or the second conveyor for data transmission 15, information about the following in operation of the melter gasket Abstichfolge to the device for controlling the first conveyor 13 for controlling the discharge of particulate carbonaceous material and / or the second 20 conveying device are transmitted. Thereby, the ratio of the combined amounts of hot iron carrier material and lumped carbonaceous material can be adjusted depending on the Abstachabfolge 25 followed in the operation of the EinschmelzVergasers. The said signal lines may physically be present as a cable, but the possibility for wireless transmission of signals is also included. FIG. 2 shows a device for charging
    Material comprising lumped carbonaceous material 1, represented by circles, and hot iron carrier material 2, represented by squares, in a meltdown gasifier 3 of a smelting reduction plant. The 19/05/2011 15:03
    No .: R601 P.027 / 048 19. May 2011 15:01 Siemens CIC P ................ No. 4141 p. 28 * »* ·· * * * · • * · · * «CI ··· # ·»
    »* * I · * · · I • · · · · · · · · 201009550 24
    Device has two reservoirs for lumped carbonaceous material, a reservoir for particulate carbonaceous material 4a and a reservoir for particulate carbonaceous material 5 4b. In the storage container for lumped carbonaceous
    Material 4a is lumped carbonaceous material la stored with a piece size A, in the reservoir for lumped carbonaceous material 4b lumpy carbonaceous material la with a piece size B 10 is stored. The piece sizes A and B are different, which is represented by different sized circles. The device for the charging of material also has a reservoir for hot iron carrier material 5. Of the two reservoirs 15 for lumped carbonaceous material 4a / 4b goes from a first discharge line 6 for particulate carbonaceous material, which is a first conveyor 7 for controlling the discharge of lumped carbonaceous material 1 includes. From the reservoir for hot 20 iron carrier material 5 is a second Austragsleitung 8 for hot iron carrier material from which comprises a second conveyor 9 for controlling the discharge of hot iron carrier material 2. The first conveyor 7 for controlling the discharge of 25 pieces of carbonaceous material 1 and the second conveyor 9 for controlling the discharge of hot iron carrier material 2 are designed as screw conveyors. 30 The lumped carbonaceous material la / lb and the hot iron carrier material 2 are combined before they enter the melter gasifier 3. To this end, the first discharge line 6 for lumped carbonaceous material and the second discharge line 8 for hot 19/05/2011 15:03
    No .: R6Q1 P.028 / 048
    May 19, 2011 15:01 Siemens C1C P
    Nr, 4141 p. 29 • · · · · * * * * - · m ψ η * * · · ·
    201009550 25
    Iron carrier material in an input device 10 for input of material into the melter gasifier. 3
    By way of the input device 10 for introducing material into the melter gasifier, lumped carbonaceous material 1a / 1b and hot iron carrier material 2 are introduced into the melter gasifier 3. The input device 10 for input of material into the Einachmelzvergaser 3 comprises a dynamic distribution device 11 for distributing the material at 10 of the input, in the illustrated Pall a gimballed Schurre - Details of the gimbal are not shown for reasons of clarity. The gimbal-mounted chute is rotatable about an axis of rotation and adjustable in its inclination. 15 The possible rotation of gimbaled
    Schurre is indicated by a curved double arrow, which wraps around the dashed line indicated axis of rotation of the rotary motion. The adjustability of the inclination is indicated by the fact that the outlines of the gimbal 20 suspended chute are shown pulled through for a position and dashed lines for another position. In addition, the adjustability of the inclination is indicated by a curved double arrow. By means of the gimbal-mounted chute lumpy carbonaceous material la / lb and hot iron carrier material 2 are distributed in a controlled manner on the material bed 12 in the melter gasifier 3. The movement pattern of the gimbal-mounted chute can be changed, for example, it can describe circular or elliptical orbits with different inclinations and thus different resulting distributions on the material bed 12. 19/05/2011 15:03
    No .: R601 P.029 / 048
    May 19, 2011 15:01 Siemens CIC P
    No. 4141 p. 30
    201009550 26
    As already shown analogously in FIG. 1, the ratio of the combined amounts of hot iron carrier material 2 and lumped carbonaceous material 1 a / 1 b is variable. For this purpose, at least one of the conveying devices from the group - first conveying device 7 for regulating the discharge of lumped carbonaceous material - second conveying device 9 for regulating the discharge of hot iron carrier material in dependence on the position of the dynamic distribution device 10 controlled. For this purpose, the device is connected to the controller 13 via the signal line 14 to the dynamic distribution device 11 15 for the purpose of transmitting information about the position of the dynamic distribution device 11 connected. For example, it can be determined at which point of its rotation path the cardanically suspended chute is located and what inclination it has. According to the present invention, the first conveyor device 7 for controlling the discharge of particulate carbonaceous material 1a / 1b is controlled via the signal line 15. The control of the discharge can be achieved, for example, by changing the rotational speed of the conveyor screw respectively.
    Via the signal line 16, designed as a screw conveyor second conveyor 9 is controlled to control the discharge 30 of hot iron carrier material 2, according to the invention in dependence on the position of the dynamic distribution device 10th
    It is also a device for detecting properties of the surface 17 of the in the P.030 / 048 19/05/2011 15:04 No .: R601 19.May 2011 15:02
    Siemens CIO P
    No. 4141 p. 31 • * * · · · · »• * * * • • • • ** ··· - * · · · · 201009550 27
    Melt carburetor material bed formed formed, which is formed in the illustrated Pall as Radarmesseinrichtung with integrated temperature measuring device. The radar measuring device collects information about 5 height level and height profile of the material bed 12 in the melter gasifier 3. The temperature measuring device collects information about the temperature profile on the surface of the material bed. This information about properties of the surface of the material bed formed in the melter gasifier 10 are transmitted via the signal line 18 to the device 13 for controlling the first conveyor for controlling the discharge of particulate carbonaceous material and / or the second conveyor, where they are used to control the discharge of 15 hot iron carrier material in
    Be used depending on the detected properties. In this way, the ratio of the combined amounts of hot iron carrier material 2 and lumped carbonaceous material 1 can be adjusted depending on properties of the surface of the material bed. Through the signal line 21, the opening mechanism of the reservoir for particulate carbonaceous material 4 a, and via the signal line 22 of the opening mechanism of the reservoir for 25-piece carbonaceous material 4 b through the
    Device 2ur control 13 are controlled. By this control, it is possible to choose the piece sizes of the lumped carbonaceous material depending on the position of the dynamic distribution device 30. Of course, the opening mechanism of the reservoir of hot iron carrier material 5 can also be controlled by the device to the controller 13, for reasons the clarity is not shown. The mentioned signal lines can 19/05/2011 15:04
    No .: R601 P.031 / 048
    t9. May 201 1 15:02 Siemens CIC P
    No. 4141 S, 32 • ♦ ♦ ·
    9 0 9 * 900 9 * 0 201009550 28 physically available as a cable, but the possibility of wireless transmission of signals is also included.
    Analogous to the possibility shown, to select the piece size 5 of the lumped carbonaceous material depending on the position of the dynamic distribution device, the type of lumped carbonaceous material may be selected depending on the position of the dynamic distribution device, if 10 lumped carbonaceous material la and lb different are of different kinds.
    If, in an analogous manner, two storage containers for hot iron carrier material 5 were present, each with different hot iron carrier material
    Particle size distribution and / or different nature are filled, can be selected analogous to the lumpy carbonaceous material depending on the position of the dynamic distribution device, the grain size distribution 20 and / or the type of hot iron carrier material.
    A device for controlling the distribution track 23 realized by the dynamic distribution device for distributing the material at the input is present. This is shown schematically; it acts by influencing the drive of the dynamic distribution device 11 or by influencing the system parts which are responsible for the inclination of the distribution device 11,
    By varying the distribution track over the horizontal cross-section of the interior of the melter gasifier, certain distribution patterns of hot iron carriers can be determined in the melter gasifier 19/05/2011 15:04
    No .: R601 P.032 / 048
    May 19, 2011 15:02 Siemens CIO P
    No. 4141 p. 33 5 10 15 20 25 201009550 29 • M • Φ · • ·% • · ·
    «• •« M • «·« · • *
    Adjust material and lumpy carbonaceous material. Via the signal line 24, the device for controlling the distribution track 23 realized by the dynamic distribution device for distributing the material during the input with the device 13 for controlling at least one of the conveying devices from the group - first conveying device for regulating the discharge of lumped carbonaceous material - second Conveying device for controlling the discharge of hot iron carrier material as a function of the position of the dynamic distribution device connected. Since the realized distribution track is determined by the position of the dynamic distribution device, the device for controlling 13 also includes a device for controlling the first conveying device for controlling the discharge of particulate carbonaceous material and / or the second conveying device for regulating the discharge of hot iron carrier. Material depending on the realized from the dynamic distribution device for distributing the material in the input distribution track 23 available. This makes it possible to adjust a certain distribution pattern of hot iron carrier material and carbonaceous material in the melter gasifier. For example, this device is used to control material flow flaps and / or augers. Although the invention has been further illustrated and described in detail by the preferred embodiments, the invention is not limited to those disclosed in US Pat
    No .: R601 P.033 / 048 30 19.May 2011 15:03
    Siemens CIC P
    No. 4141 p. 34
    201009550 30
    Examples are limited and other variations can be deduced therefrom by one skilled in the art without departing from the scope of the invention. 5 19/05/2011 15:05
    No .: R601 P.034 / 048 19.May 2011 15:03
    Siemens (HC • t «* · · · t * t» · · · · · e »♦ · ··· • e * e * · * · ·» * e e · e »v *
    No. 4141 p. 35 201009550 31
    Liata's quotations
    Patent Literature EP0299231A1 19/05/2011 15:05
    No .: R601 P.035 / 048 9th May 2011 15:03
    Siemens CIO P
    No. 4141 p. 36 201009550 32
    Reference material 1 lumped carbonaceous material lumped carbonaceous material 1b lumped carbonaceous material 2 hot iron carrier material 3 melter gasifier 4 lumped carbonaceous material reservoir 4a lumped carbonaceous material reservoir 4b lumped carbonaceous material reservoir 5 hot iron carrier material reservoir 6 first Discharge line (for particulate carbonaceous material) 7 first conveyor (for controlling the discharge of particulate carbonaceous material) 8 second discharge line (for hot iron carrier material) 9 second conveyor 9 for controlling the discharge of hot iron carrier material 2 10 input device for input of material in the melter gasifier 11 dynamic distributor 19/05/2011 15:05
    No .: R601 P.036 / 048 19. May 2011 15:03 Siemens C1C P _ No. 4141 S, 3 / • ·· * · · 4 * · «« · · ··· 4 # ·· 4 «4 Material bed Device for controlling (at least one of the conveying devices from the group - first conveying device for controlling the discharge of lumped carbonaceous material). 4 4 4 4 4 4 4 4 4 4 4 4 201009550 33 12 13 second conveying device for controlling the discharge of hot iron carrier material in dependence on the position of the dynamic distribution device) 14 signal line 15 16 signal line signal line 17 device for detecting properties (the surface of the material bed formed in the melter gasifier) 18 19 20 21 signal line information input device signal line signal line 22 23 Signal line Device for the regulation of the dynamic distribution device for distribution of the material at 19/05/2011 15:05
    No .: R601 P.037 / 048 19. May 201 1 15:03 Siemens CIC P .............. No. 4141 p. 38 * · ♦♦ «· * · · • * * * * ·· »*** ················································································································································································
    No .: R601 P.038 / 048
    权利要求:
    Claims (19)
    [1]
    May 19th, 2011 15:04 Siemens CH! P < • e ··············································

    A process for charging material comprising lumped carbonaceous material and, preferably, hot bisulphide material into a melter gasifier of a smelting reduction plant, wherein the lumped carbonaceous material and the, preferably hot, iron carrier material Material before and / or during entering the melter gasifier 10, and the ratio of the combined amounts of, preferably hot, iron carrier material and particulate carbonaceous material is variable, characterized in that the combined amounts of, preferably hot, Iron carrier material and 15 pieces of carbonaceous material are distributed over the cross section of the melter gasifier by means of a dynamic distributor, and the ratio of the combined amounts of, preferably hot, iron carrier material and lumped carbonaceous material depending on the position of the dynamic n distribution device is set.
    [2]
    2. The method according to claim 1, wherein the charged material in the melter gasifier forms a material bed 25, characterized in that the ratio of the combined amounts of, preferably hot, iron carrier material and lumpy carbonaceous material is adjusted depending on properties of the surface of the material bed. 30
    [3]
    3. The method according to claim 2, characterized in that the property of the surface of the material bed is the height level and / or the height profile of the material bed. 19/05/2011 15:06 No .: R601 P.039 / 048
    [4]
    4. The method according to claim 2, characterized in that the property of the surface of the material bed is the temperature profile on the surface of the material bed.
    [5]
    5. The method according to any one of claims 1 to 4, characterized in that the ratio of the combined amounts of, preferably hot, iron carrier material and 10-piece carbonaceous material is adjusted depending on the sequence of tappings during operation of the melter gasifier.
    [6]
    6. The method according to any one of claims 1 to 5, characterized 15 characterized in that the movement pattern of the dynamic distribution device is changeable.
    [7]
    7. The method according to any one of claims 1 to 6, characterized in that the grain size distribution of, 20 preferably hot, iron carrier material and / or the piece size of the lumpy carbonaceous material is selected in dependence on the position of the dynamic distribution device.
    [8]
    8. The method according to any one of claims 1 to 7, characterized in that the type of charged, preferably hot, iron carrier material and / or the type of particulate carbonaceous material is selected depending on the position of the dynamic distribution device 30.
    [9]
    9. An apparatus for charging material comprising lumped carbonaceous material and, preferably, hot, iron carrier material in a melter gasifier of a 19/05/2011 15:06 No .: R601 P.040 / 048
    May 19, 2011 15:04 Siemens CJC P, ............. ····· * * * * • · · · · · · · · ························ I 37 smelting reduction plant, with at least one storage container for lumped carbonaceous material, and with at least one supply container for, preferably 5 hot, iron carrier material, wherein.. from the at least one reservoir for lumped carbonaceous material, a first discharge line for lumped carbonaceous material emanates, which is a first conveying device for
    [10]
    10 control of the discharge of particulate carbonaceous material comprises, and wherein from the at least one reservoir for, preferably hot, iron carrier material, a second discharge line for, preferably hot, iron carrier material emanates from a second feeder device for regulating the Auetrages of, preferably hot, iron carrier material, and with an input device for inputting material into the melter gasifier 20 wherein the first particulate carbonaceous material discharge line and the second, preferably hot, iron carrier material discharge line enter the input device for inputting material to the melter gasifier 25, characterized in that the input device for inputting material into the fusing device comprises a dynamic distribution device for distributing the material in the input, and a device for controlling at least one of the 30 conveying devices from the group - ers te conveyor for controlling the discharge of particulate carbonaceous material 19/05/2011 15:07 No .: R601 P.041 / 048
    19 May 201 1 15:05 Siemens C ^ C P. Nr. 4141 p. 42 ♦ »· · · · · · · · ·» · ·

    10. The device according to claim 9, characterized in that two storage containers for, preferably hot, iron carrier material and / or two reservoirs for lumped carbonaceous material are present.
    [11]
    11. The device according to claim 9 or 10, characterized in that the first conveying device for controlling the discharge of particulate carbonaceous material and / or the second conveying device for regulating the discharge of, preferably hot, iron carrier material one or more material flow flaps and / or Conveying screws and / or 20 rotary valves includes.
    May 9, 2011 3:04 pm Siemens CIC P No. 4141 p. 40 • · • ·· «201009550 36
    [12]
    12. Device according to one of claims 9 to 11, characterized in that a device for controlling the realized by the dynamic distribution device for distributing the material in the input distribution track is present.
    [13]
    13. Device according to one of claims 9 to 12, characterized in that a device for controlling the first conveying device for regulating the discharge of particulate carbonaceous material and / or the second conveying device for regulating the discharge of, preferably hot, iron carrier material 19th / 05/2011 15:07 No .: R601 P. 042/048
    May 19, 2011 15:05 Siemens C. ^ C P .............. ································································································································································· (· *. ······································································································································································) according to the distribution pattern realized by the dynamic distribution device for distributing the material upon input.
    [14]
    14. Device according to one of claims 9 to 13, characterized in that a device for detecting properties of the surface of the material bed formed in the melter gasifier is present. 10
    [15]
    15, Device according to one of claims 9 to 14, characterized in that for controlling the first conveying device for controlling the discharge of particulate carbonaceous material and / or the second conveyor 15 for regulating the discharge of, preferably hot, iron carrier material in dependence is provided by the device for detecting properties of the surface of the material bed formed in the melter gasifier 20 detected properties.
    [16]
    16. Device according to one of claims 9 to 15, 25, characterized in that there are at least 2wei reservoir for particulate carbonaceous material, which are filled with lumpy carbonaceous material of different piece size.
    [17]
    17. Device according to one of claims 9 to 15, characterized in that there are at least two reservoirs for lumped carbonaceous material, which are filled with lumpy carbonaceous material of different kinds. 19/05/2011 15:07 No .: R601 P.043 / 048
    May 19, 2011 15:05 Siemens C. ^ CP, Nr, 4141 p. 44 - - * ·· · • * I · *. · · ··· *** • t · · · · · * * * * · · · '· · · · * · ···· ··· ·· • * 201009550 40
    [18]
    18. Device according to one of claims 9 to 15, characterized in that there are at least two storage containers for, preferably hot, Eisenträger- 5 material which are filled with iron carrier material, preferably hot, iron carrier material of different particle size.
    [19]
    19. Device according to one of claims 9 to 15, characterized in that there are at least two storage containers for, preferably hot, iron carrier material which are filled with iron carrier material, preferably hot iron carrier material, of different types. 15 19/05/2011 15:07 No .: R601 P.044 / 048
    类似技术:
    公开号 | 公开日 | 专利标题
    DE69922144T2|2005-11-10|METHOD FOR OPERATING A REDUCING OVEN WITH A MOVABLE STOVE
    DE60125669T2|2007-11-08|Process for the production of metallic iron
    DE60116009T2|2006-08-03|METHOD FOR PRODUCING REDUCED IRON
    EP0111176B1|1986-05-07|Process and device for the instant production of reduced iron pellets and liquid iron from iron oxide pellets
    DE69838246T2|2008-01-10|METHOD FOR OPERATING A MOVABLE OVEN FOR REDUCING OXIDES
    DE102007006981B4|2009-01-29|Process, gasification reactor and plant for entrained flow gasification of solid fuels under pressure
    AT506837A1|2009-12-15|METHOD AND DEVICE FOR PRODUCING RAW STEEL OR LIQUID STEEL PREPARATIONS
    DE4240197C2|1996-04-18|Process for the production of pig iron from iron ore and device for the thermal and / or chemical treatment of a readily disintegrating material or for the production of pig iron by means of this process
    DE2851912A1|1979-12-06|METHOD FOR DIRECTLY REDUCING IRON ORE IN A FLOATING LAYER
    DE3026949A1|1981-02-12|METHOD AND DEVICE FOR REDUCING IRON OXIDE PARTICLES AND FOR PRODUCING MOLTEN IRON
    DE2401540A1|1975-07-17|METHOD OF MELTING IRON SPONGE
    AT511206B1|2012-10-15|METHOD AND DEVICE FOR CHARGING CARBONATED MATERIAL AND ICE CARRIER MATERIAL
    DE1909192A1|1971-04-22|Process for the simultaneous production of powdered iron and activated carbon
    EP1105541B1|2002-09-25|Method for producing liquid pig iron
    DE3347685C1|1985-04-04|Process for the production of ferromanganese
    EP3150729A1|2017-04-05|Method and device for feeding iron carrier material
    EP0493752A1|1992-07-08|Process and apparatus for reinjecting hot dusts
    EP2734649B1|2016-05-25|Melting reduction assembly and method for operating a melting reduction assembly
    EP0910671B1|2001-07-04|Process and device for charging a fusion gasifier with gasifying means and spongy iron
    DE2633025C2|1982-11-11|Process for modifying pig iron
    AT508953B1|2011-07-15|METHOD AND DEVICE FOR CHARGING IN A FILLING UNIT
    EP2427581B1|2018-07-11|Process for slag foaming a non-stainless steel melt in an electric arc furnace
    DE2842425A1|1980-04-17|METHOD AND DEVICE FOR PRODUCING HOT BRIQUETTES
    DE880636C|1953-06-22|Process and melting furnace for melting down light and bulky scrap
    DE2127847A1|1971-12-16|Iron smelting - using low-grade ores and coal in low-cost appts
    同族专利:
    公开号 | 公开日
    BR112013029560A2|2016-12-06|
    CN103562413B|2016-04-06|
    CA2836355A1|2012-11-22|
    BR112013029560B1|2018-10-23|
    ZA201308170B|2014-09-25|
    KR20140045947A|2014-04-17|
    RU2593808C2|2016-08-10|
    CA2836355C|2020-04-28|
    US9470456B2|2016-10-18|
    CN103562413A|2014-02-05|
    US20140110891A1|2014-04-24|
    KR101928453B1|2018-12-12|
    AU2012257876B2|2016-08-04|
    WO2012156243A1|2012-11-22|
    RU2013156411A|2015-06-27|
    UA111076C2|2016-03-25|
    AT511206B1|2012-10-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    US4412858A|1982-07-12|1983-11-01|Hylsa, S.A.|Method of converting iron ore into molten iron|
    WO1997047774A1|1996-06-10|1997-12-18|Voest-Alpine Industrieanlagenbau Gmbh|Method of charging metalliferous material into a smelting-gasification zone|
    JP2002256311A|2001-02-28|2002-09-11|Nkk Corp|Method for charging raw material for blast furnace into furnace|
    JP2011068926A|2009-09-24|2011-04-07|Nippon Steel Corp|Method for charging raw material into blast furnace|
    US4913406A|1986-08-26|1990-04-03|Kawasaki Steel Corp.|Shaft furnace having means for charging and adjusting a pre-mixture of ore and coke|
    DE3723137C1|1987-07-13|1989-03-16|Voest Alpine Ind Anlagen|Device for feeding a melter gasifier with gasifying agents and sponge iron|
    AT403696B|1996-06-20|1998-04-27|Voest Alpine Ind Anlagen|MELTING CARBURETTOR AND SYSTEM FOR THE PRODUCTION OF A METAL MELT|
    EP1662009A1|2004-11-26|2006-05-31|VAI Industries Ltd.|Device for distributing material into a furnace|
    AT506042A1|2007-11-13|2009-05-15|Siemens Vai Metals Tech Gmbh|METHOD FOR MELTING RAW IRONS AND STEEL PREPARED PRODUCTS IN A MELTING GASER|
    AT511206B1|2011-05-19|2012-10-15|Siemens Vai Metals Tech Gmbh|METHOD AND DEVICE FOR CHARGING CARBONATED MATERIAL AND ICE CARRIER MATERIAL|AT511206B1|2011-05-19|2012-10-15|Siemens Vai Metals Tech Gmbh|METHOD AND DEVICE FOR CHARGING CARBONATED MATERIAL AND ICE CARRIER MATERIAL|
    EP3150729A1|2015-10-02|2017-04-05|Primetals Technologies Austria GmbH|Method and device for feeding iron carrier material|
    法律状态:
    2016-06-15| PC| Change of the owner|Owner name: PRIMETALS TECHNOLOGIES AUSTRIA GMBH, AT Effective date: 20160415 |
    优先权:
    申请号 | 申请日 | 专利标题
    ATA723/2011A|AT511206B1|2011-05-19|2011-05-19|METHOD AND DEVICE FOR CHARGING CARBONATED MATERIAL AND ICE CARRIER MATERIAL|ATA723/2011A| AT511206B1|2011-05-19|2011-05-19|METHOD AND DEVICE FOR CHARGING CARBONATED MATERIAL AND ICE CARRIER MATERIAL|
    KR1020137033568A| KR101928453B1|2011-05-19|2012-05-09|Method and device for charging coal-containing material and iron carrier material|
    CN201280024194.8A| CN103562413B|2011-05-19|2012-05-09|For loading the method and apparatus of carbonaceous material and year iron material|
    RU2013156411/02A| RU2593808C2|2011-05-19|2012-05-09|Method and device for loading carbon containing material and iron-containing material|
    PCT/EP2012/058499| WO2012156243A1|2011-05-19|2012-05-09|Method and device for charging coal-containing material and iron carrier material|
    UAA201313426A| UA111076C2|2011-05-19|2012-05-09|METHOD AND DEVICE FOR charging coal-containing material and iron-containing material|
    CA2836355A| CA2836355C|2011-05-19|2012-05-09|Method and device for charging coal-containing material and iron carrier material|
    US14/118,849| US9470456B2|2011-05-19|2012-05-09|Method and device for charging coal-containing material and iron carrier material|
    AU2012257876A| AU2012257876B2|2011-05-19|2012-05-09|Method and device for charging coal-containing material and iron carrier material|
    BR112013029560-0A| BR112013029560B1|2011-05-19|2012-05-09|method and device for loading coal-containing material and iron-bearing material|
    ZA2013/08170A| ZA201308170B|2011-05-19|2013-10-31|Method and device for charging coal-containing material and iron carrier material|
    [返回顶部]