• 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:

    公开号:AT510177A1
    申请号:T0122410
    申请日:2010-07-20
    公开日:2012-02-15
    发明作者:Robert Dipl Ing Millner
    申请人:Siemens Vai Metals Tech Gmbh；
    IPC主号:
    专利说明:

    200821822AT; ;; ; *. *. * * ♦ · · * «· · · · · · ·« * * · * ·· -1-
    Process for cleaning a dust-laden gas stream
    The invention relates to a process for purifying a gas stream laden with dusts and / or with finely particulate solids from top gas and / or offgas and / or export gas from a direct reduction plant or smelting reduction plant for reduction, and optionally for melting, of particulate or particulate, in particular fine particulate, Solids, wherein the gas stream is first subjected to dry cleaning by means of at least one dry filter, wherein dusts and / or fine particulate starting materials are separated from the gas stream, and this purified gas stream is at least partially supplied to a CO 2 separation device for CO 2 separation, CO 2 and optionally water to form a substantially C02-free product gas and a CO2-rich tail gas
    A smelting reduction plant is operated in a two-stage process, wherein in a first step metal-containing solid raw materials are reduced by means of reducing gas and this pre-reduced material is melted in a second step to liquid metal with simultaneous addition of energy carriers, in particular coal, coke, etc. Smelting reduction plants in the context of this application are understood to mean a blast furnace (operated with hot blast and / or oxygen), a plant according to the COREX® or FINEX® process and other available smelting reduction processes.
    It is known from the prior art that dry filters are used to clean, in particular hot, process gases, e.g. Blast furnace gas from blast furnaces or top gas from reduction plants, can be used. It is advantageous that, in contrast to the wet cleaning no sludge or wastewater incurred, which in turn would have to be fed to a complex post-treatment. Furthermore, it is known to clean the dry filter by rewinding with purge gases, the filter cake from the filter
    200821822AT * fr · ♦ fr * * * · ·
    fr *** · fr «I · **« «« «I t • · ·« fr «« fr -2-. For this purpose, in the prior art, especially compressed air but also nitrogen application. The disadvantage here is that additional process gases are required in considerable quantities.
    From JP 05-076803 A, it is known to arrange a filter in a cyclone, wherein after a coarse separation in the cyclone, a fine separation takes place in the filter. The deposited material can be further processed.
    Likewise, WO 94/11283 shows separating dusts from a conveying gas and supplying the dusts separated to an open vessel or cleaning the conveying gas in the cyclone and a bag filter.
    It is therefore an object of the invention to provide a method which enables the cleaning of a dry filter safely and inexpensively.
    This object is achieved by the method according to claim 1.
    By the method according to the invention, a product gas which is almost free of CO 2 is used for rewinding the at least one dry filter. Product gas is passed through adsorption systems, e.g. (Vacuum) Pressure swing adsorption (PSA Pressure Swing Adsorption or VPSA Vacuum Pressure Swing Adsorption), prepared, with C02 and moisture are separated from a gas. This produces a CO and H2 enriched gas which has no moisture (dewpoint <-100eC). This dry and pure product gas is ideal for backwashing the dry filter or for removing the filter cake, due to the
    Composition of the product gas this as a high-quality gas e.g. together with export gas further uses can be supplied. A pressure range of, in particular, 1.5 to 12 barg and particularly preferably 2 to 6 barg has proven to be advantageous for rewinding. When using e.g. Nitrogen as gas to rewind the dry filter leads to an unwanted accumulation of nitrogen in the
    200821822AT • · »· k * -3-
    Process gas or export gas. In addition, according to the prior art, relatively large amounts of purge gas such as e.g. Nitrogen can be used. In addition to the gases mentioned, the top gases of direct reduction plants based on reformed natural gas or of MIDREX® plants, which work in conjunction with coal gas plants or whose products are also processed by oxygen blast furnaces.
    According to a particular embodiment of the method according to the invention, the product gas used for backwashing is again passed through the dry filter after backwashing and thereby cleaned. Due to the composition comparable to the reducing gas, the product gas can be reused and e.g. be mixed with process gases from the direct reduction plant.
    The product gas temporarily increases the pressure on the clean gas side in the filter element (for example, a bag filter, ceramic filter candle, etc.), which results in a cleaning of the filter cake on the outside of the filter element. The product gas mixes with the process gas after backwashing and is therefore either reused in the process via the gas recirculation and / or used with the export gas (for example, thermal utilization in the power plant, etc.). The product gas may have approximately the following composition:
    Gas component Typical proportions: Typical range: CO 52 vol% 45 - 60 vol% oo ro 3 vol% 2-3 vol% h 2 25 vol% 20 - 35% vol 2 vol 0 vol% 0 vol% ch 4 2 vol% 1 - 2 vol% n2 18 vol% 5-25 vol%
    A special embodiment of the method according to the invention provides that at least a portion of the purified product gas again the direct reduction plant or
    200821822AT ·· «·« · · · »
    The smelting reduction plant and / or a further reduction plant operating in conjunction with at least one of these plants or a coal gasification plant is supplied as reducing gas. The purified and dry product gas, which was used to rinse the dry filter, is suitable for use in the direct reduction plant, in the smelting reduction plant or for use in other reduction plants, which are operated in conjunction with the direct reduction or smelting reduction plant. The operation of a direct reduction plant together with a blast furnace is an advantageous embodiment. For example, the purified product gas can also be supplied to the export gas from the direct reduction plant.
    An alternative embodiment of the inventive method provides that at least a portion of the product gas after its use in the dry filter again the direct reduction plant or the smelting reduction plant and / or a working in conjunction with at least one of these plants or a coal gasification plant further reduction plant is fed as a reducing gas. By using the product gas, the process efficiency can be increased, whereby this can also be done in combination with a direct reduction plant with a further reduction plant.
    According to a special embodiment of the method according to the invention, nitrogen is used for backwashing the dry filter during the startup and / or shutdown operating state as an alternative to product gas.
    A suitable embodiment of the method according to the invention provides that the smelting reduction plant is operated by a COREX® or FINEX® process or is a blast furnace. COREX® and FINEX® are well-known smelting reduction processes for the reduction of particulate or fine particulate feedstocks. Top gas from the COREX® process or off-gas from the FINEX® process or blast furnace gas from a blast furnace can thus be supplied to the inventive use, wherein the product gas can in turn be used further, 200821822at ::::. *. *
    «*« * · I · I ♦ * * · · »··· ♦ ♦ * * * *» * · » This can therefore be e.g. be used together with export gas further uses. For example, thermal utilization of the export gas for power generation in an attached power plant, e.g. conceivable in a gas and steam power plant.
    According to a special embodiment of the process according to the invention, the particulate starting materials are oxidic, iron-containing solids, in particular iron ores, and optionally additives.
    According to a further special embodiment of the method according to the invention, the filter cake is fed for further use of a compacting device, in particular an agglomerating device, or a metallurgical aggregate, in particular a melting aggregate, for processing the particulate solids. Thus, in addition to the product gas for rewinding the dry filter and the filter cake is recycled. In addition, further utilization of the filter cake is possible.
    Due to the large amounts of dusts and fine particulate solids that result in process gases of the reduction metallurgy, cleaning equipment for process gases must be designed so that these large quantities can be safely processed. In order to ensure a safe function of the dry filter, the dry filter has backwashing devices for separating the filter cake from the dry filter. In most cases, the dry filter with a container having a cone-shaped lower part, in such a way that the filter cake passes during backwashing in the lower part of the container. By backwashing the filter device, the filter is cleaned and returned to the initial operating state. The solids deposited on the filter as filter cake are removed from the dry filter and placed in the •.
    200821822AT
    Container introduced. From the container, the filter cake may e.g. be fed to an agglomerator or other processing.
    When operating conventional COREX® systems, approximately 380,000 Nm3 / h are required. Top gas at a temperature of about 300 ° C, which must be cleaned before using the top gas. This is done by a dry filtration. For a safe operation of the dry filter is about 300 Nm3 / hr. Purge gas, specifically so product gas needed. Accordingly, by the invention, this amount of nitrogen, which is used as purge gas can be saved. When operating FINEX® plants, the export gas accumulates at a temperature of about 450 ° C, with about 330,000 Nm3 / hr having to be cleaned through the dry filter. Usual Spülgasmengen are about 500 Nm3 / hr. The purge gas is introduced at a pressure of 4 to 8 barg, in particular about 5.5 barg. Typical purging durations per filter element group are fractions of a second, with the individual filter element groups or even individual filters being cleaned up cyclically (for example due to a limit value for the differential pressure or after the lapse of a period of time).
    As a dry filter sintered porous metal filter, ceramic filter or bag or bag filter can be used. Such filters are characterized by high operating temperatures, with bag or bag filters, it may be necessary to subject the gas to a cooling before.
    Fig. 1: Example of a dry filter with backwashing for top gas or offgas
    Figure 1 shows a possible embodiment of a dry filter with filter elements 1, which are arranged in a housing 2. Under the housing 2, a cone-shaped container 3 is arranged. The cone-shaped container 3 can, for example, be connected to an agglomerating device, not shown, and / or to a melting unit (also not shown), so that the filter cake is formed from the cone-shaped element. 200821822AT ::::. · · · · · · «· *»
    * * * * «« # T t I ** ** · · M * · -7-
    Container 3 can be removed. Via a transport line 4 a laden with dusts and / or with fine particulate solids gas stream 5 is introduced from top gas and / or export gas from a direct reduction plant in the housing 2.
    The inflowing gas stream 5 and the particulate solids partially separate in the housing 2, wherein a portion of the finely particulate solids 6a and 6b falls into the container 3 due to gravity. Dust and the remaining fine particulate solids are transported with the gas stream 7a, 7b in the dry filter and deposit on the filter elements 1 from. The purified gas stream is discharged via pipes 8 of one or more discharge lines 9 from the dry filter and fed to a CO 2 separation device, not shown, wherein a substantially CO 2 -free and dry product gas and a CO 2 -rich tail gas are formed. Alternatively, a portion of the purified gas stream may be discharged prior to the CO 2 separation device.
    The dry filter has backwashing devices 10a, with which, as required, a portion of the product gas can be introduced as purge gas under overpressure of about 6.5 bar counter to the flow direction of the gas stream in the dry filter, wherein the separated dusts and fine particulate solids that form the filter cake FK , in turn, can be removed from the filter elements 1 and placed in the container 3. Alternatively, nitrogen can also be introduced via a backwashing device 10b.
    The backwashing device can be designed as a loop with a large number of discharges and corresponding shut-off valves. Usually, the supply of the loaded with dusts and / or with fine particulate solids gas stream 5 is interrupted in the dry filter during purging with product gas through valves. -8- -8-
    200821822AT
    The dry filter can directly process the hot top gas when using ceramic filter elements. When using bag filters or bag filters, it is necessary to cool the top gas before filtering. In any case, the waste heat of the hot top gas can be used before or after the dry filtration to generate steam and relaxes the purified top gas in a turbine and fed to other external uses.
    200821822AT * * * * * «* * I · · * * *« · «·· +« »· ι» ···· · i «I 4 • * * * * * *» * * -9-
    REFERENCE SIGNS LIST 1 filter elements 2 housing 3 cone-shaped container 4 transport line 5 gas stream 6a, 6b fine particulate solids 7a, 7b dusts and residual fine particulate solids 8 tubes 9 discharge lines 10a, 10b backwashing 11 tubes
    权利要求:
    Claims (8)
    [1]
    200821822AT ••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••• with gas and / or with finely particulate solids laden gas stream of top gas and / or offgas and / or export gas from a direct reduction plant or smelting reduction plant, and optionally for melting, of particulate or particulate, in particular fine particulate, solids, the gas stream first by means of at least one Dry cleaning is subjected to a dry cleaning, wherein dusts and / or fine particulate starting materials are separated from the gas stream, and this purified gas stream is at least partially fed to a CO 2 separation device for COr deposition, CO 2 and optionally water are deposited, to form a substantially CO 2 -free product gas and a C02-rich Taiigases, characterized in that at least ei n part of the product gas under pressure, in particular from 1.5 to 12 barg, more preferably 2 to 6 barg, for backwashing the at least one dry filter and for removing the filter cake, is introduced into the dry filter.
    [2]
    2. The method according to claim 1, characterized in that the product gas used for backwashing is in turn passed through the dry filter after rewinding and thereby cleaned.
    [3]
    3. The method according to claim 2, characterized in that at least a portion of the pure product gas is again the direct reduction plant or the smelting reduction plant and / or a working in conjunction with at least one of these plants or a coal gasification plant further reduction plant fed as a reducing gas.
    [4]
    4. The method according to any one of claims 1 to 3, characterized in that at least a portion of the product gas after its use in the dry filter again * * Φ 200821822AT * · «· t ι t« »« ·· »« ··· ·· The direct reduction plant or the smelting reduction plant and / or a further reduction plant operating in conjunction with at least one of these plants or a coal gasification plant is supplied as reducing gas.
    [5]
    5. The method according to any one of claims 1 to 4, characterized in that is used for backwashing the dry filter during the startup and / or Abfahrbetriebszustandes as an alternative to product gas nitrogen.
    [6]
    6. The method according to any one of claims 1 to 5, characterized in that the smelting reduction plant is operated by a method of the type COREX® or FINEX® or a blast furnace.
    [7]
    7. The method according to any one of claims 1 to 6, characterized in that the particulate starting materials are oxidic, iron-containing solids, in particular iron ores, and optionally additives.
    [8]
    8. The method according to any one of claims 1 to 7, characterized in that the filter cake for further use of a compacting device, in particular an agglomerating device, or a metallurgical unit, in particular a melting unit, for processing the particulate solids is supplied.
    类似技术:
    公开号 | 公开日 | 专利标题
    AT507525B1|2010-09-15|METHOD AND DEVICE FOR OPERATING A MELT REDUCTION PROCESS
    AT510177B1|2012-05-15|METHOD FOR CLEANING A DYED GAS STREAM
    AT507524B1|2010-10-15|METHOD AND DEVICE FOR REMOVING PARTICULATE SOLIDS FROM A GASSTROM
    AT506837B1|2010-03-15|METHOD AND DEVICE FOR PRODUCING RAW STEEL OR LIQUID STEEL PREPARATIONS
    DE212009000108U1|2012-02-02|Device for the dry cleaning of gas produced during pig iron / iron production
    DE3340204A1|1985-05-15|METHOD AND DEVICE FOR PURIFYING HOT GAS WITH HEAT RECOVERY
    AT507713B1|2010-10-15|METHOD AND DEVICE FOR PRODUCING RAW STEEL OR LIQUID STEEL PREPARATIONS
    AT511892B1|2013-07-15|METHOD FOR THE TREATMENT OF EXHAUST GASES FROM PLANTS FOR THE PRODUCTION OF RAW CHEMISTRY AND / OR SYNTHESEGAS
    DE102007046260A1|2009-04-09|Process for purifying the raw gas from a solid gasification
    AT507823B1|2011-01-15|METHOD AND APPARATUS FOR PRODUCING RAW IRONS OR LIQUID STEEL PREPARED PRODUCTS
    DE102008049579A1|2010-04-01|Hot gas cleaning
    AT508250B1|2010-12-15|METHOD FOR REMOVING CO2 FROM EXHAUST GASES SUCH AS EXHAUST GASES FROM PLANTS FOR THE PRODUCTION OF REFRIGERATED STEEL OR EXTRACTIONS FROM SYNTHESEGAS PLANTS
    WO2013037634A1|2013-03-21|System for energy optimization in a plant for producing direct-reduced metal ores
    EP2524061A1|2012-11-21|Method and device for reducing iron ore-containing feed materials or for producing pig iron or liquid steel pre-products
    AT506640B1|2010-07-15|METHOD AND DEVICE FOR PRODUCING LIQUID RAW IRONS OR LIQUID STEEL PREPARED PRODUCTS
    AT506949B1|2010-01-15|METHOD FOR PRODUCING LIQUID METALS
    AT510565A4|2012-05-15|DEVICE FOR REGULATING PROCESS GASES IN A PLANT FOR PRODUCING DIRECTLY REDUCED METAL ORCHES
    AT509865B1|2011-12-15|METHOD FOR THE PRODUCTION OF RAW IRONS OR LIQUID STEEL PREPARED PRODUCTS
    AT509735B1|2012-03-15|METHOD AND DEVICE FOR PRODUCING AT LEAST PARTIALLY REDUCED METAL ORCES AND / OR METALS
    CH701016A2|2010-11-15|to form A process for removing nitrogen from the blast furnace gas to provide an additional feed to a gas turbine engine.
    DE3003000A1|1981-07-30|Filter for removing dust from hot gases - has layer of material resistant to temp. exceeding 800 degrees C., esp. for treating gas from metallurgical reactors, coal gasifiers etc.
    同族专利:
    公开号 | 公开日
    EP2595724A1|2013-05-29|
    MX2013000723A|2013-06-05|
    EP2595724B1|2014-06-25|
    UA106669C2|2014-09-25|
    WO2012010430A1|2012-01-26|
    CN103002967B|2016-01-20|
    KR101895882B1|2018-09-07|
    RU2546724C2|2015-04-10|
    CA2805971A1|2012-01-26|
    US8882893B2|2014-11-11|
    AT510177B1|2012-05-15|
    KR20130141444A|2013-12-26|
    US20130112075A1|2013-05-09|
    BR112013001527A2|2016-05-10|
    CN103002967A|2013-03-27|
    RU2013107406A|2014-08-27|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    GB761999A|1953-12-10|1956-11-21|Sueddeutsche Kalkstickstoff|Process for the separation of solids from gases|
    DE1607694C3|1967-02-11|1974-08-29|Deutsche Gold- Und Silber-Scheideanstalt Vormals Roessler, 6000 Frankfurt|Plant for the separation of solids from aerosols|
    SU430871A1|1972-11-29|1974-06-05|А. Д. Мальгин|SLEEVE FILTER FOR GAS CLEANING|
    DK18878A|1978-01-16|1979-07-17|K V Frederiksen|CLEANING DEVICE FOR HOSE FILTERS|
    DE3114068A1|1981-04-08|1982-11-04|Hölter, Heinz, Dipl.-Ing., 4390 Gladbeck|Process for purifying high-temperature and high-pressure gases|
    AT377511B|1981-06-23|1985-03-25|Glaxo Group Ltd|METHOD FOR PRODUCING NEW INDOL-5-CARBOXAMIDE DERIVATIVES, THEIR SALTS AND HYDRATES|
    DE3505729A1|1985-02-15|1986-08-21|Deutsche Filterbau GmbH, 4000 Düsseldorf|METHOD FOR CLEANING FILTER ELEMENTS|
    FR2617735B1|1987-07-07|1990-12-07|Dimate|AUTOMATIC DECOLMATION PROCESS OF SLEEVE AIR FILTER AND DEVICE FOR IMPLEMENTING SAME|
    SU1584980A1|1988-04-05|1990-08-15|Научно-Исследовательский Институт С Опытным Машиностроительным Заводом Научно-Производственного Объединения "Спектр"|Bag filter|
    DE3925818C2|1989-08-04|1993-06-09|Intensiv-Filter Gmbh & Co Kg, 5620 Velbert, De|
    JPH0576803A|1991-09-18|1993-03-30|Daihen Corp|Cyclone type dust collector and dust collecting method|
    US5269835A|1992-10-13|1993-12-14|Jensen Robert M|Baghouse floater purge system|
    EP0668839A4|1992-11-18|1997-09-03|Dengel Carl A|Dust-free powder substance delivery and filter system.|
    DE10126048B4|2001-05-29|2004-01-29|Norbert Fleckenstein|Device for cleaning dust-laden raw gases|
    US6562103B2|2001-07-27|2003-05-13|Uop Llc|Process for removal of carbon dioxide for use in producing direct reduced iron|
    DE10223335B4|2002-05-25|2004-08-26|Döhler, Andreas|Cleaning device for a particulate filter element with filter bags|
    SE532975C2|2008-10-06|2010-06-01|Luossavaara Kiirunavaara Ab|Process for the production of direct-reduced iron|
    AT507524B1|2008-10-23|2010-10-15|Siemens Vai Metals Tech Gmbh|METHOD AND DEVICE FOR REMOVING PARTICULATE SOLIDS FROM A GASSTROM|
    RU2378037C1|2008-10-23|2010-01-10|Вадим Анатольевич Егоров|Bag filter for dust trapping|
    CN101638702B|2009-08-14|2011-07-20|中冶赛迪工程技术股份有限公司|Recycling method of outlet gas in direct reduction process using gas as reducing gas|
    AT510177B1|2010-07-20|2012-05-15|Siemens Vai Metals Tech Gmbh|METHOD FOR CLEANING A DYED GAS STREAM|AT507524B1|2008-10-23|2010-10-15|Siemens Vai Metals Tech Gmbh|METHOD AND DEVICE FOR REMOVING PARTICULATE SOLIDS FROM A GASSTROM|
    AT510177B1|2010-07-20|2012-05-15|Siemens Vai Metals Tech Gmbh|METHOD FOR CLEANING A DYED GAS STREAM|
    SG194229A1|2011-04-25|2013-11-29|Ngk Insulators Ltd|Method for washing ceramic filter|
    CN104349830B|2012-04-05|2016-10-12|特诺恩派罗梅特私人有限公司|Method and apparatus for dry filtration process gas|
    EP3606637A1|2017-04-07|2020-02-12|H. Lundbeck A/S|Apparatus and method for isolation and/or preparation of particles|
    法律状态:
    2016-06-15| PC| Change of the owner|Owner name: PRIMETALS TECHNOLOGIES AUSTRIA GMBH, AT Effective date: 20160415 |
    2017-03-15| MM01| Lapse because of not paying annual fees|Effective date: 20160720 |
    优先权:
    申请号 | 申请日 | 专利标题
    ATA1224/2010A|AT510177B1|2010-07-20|2010-07-20|METHOD FOR CLEANING A DYED GAS STREAM|ATA1224/2010A| AT510177B1|2010-07-20|2010-07-20|METHOD FOR CLEANING A DYED GAS STREAM|
    RU2013107406/05A| RU2546724C2|2010-07-20|2011-07-07|Method of dusty gas flow cleaning|
    UAA201300643A| UA106669C2|2010-07-20|2011-07-07|Method for cleaning a gas flow loaded with dust|
    BR112013001527A| BR112013001527A2|2010-07-20|2011-07-07|method for cleaning a dust-laden gas stream|
    PCT/EP2011/061507| WO2012010430A1|2010-07-20|2011-07-07|Method for cleaning a gas flow loaded with dust|
    MX2013000723A| MX2013000723A|2010-07-20|2011-07-07|Method for cleaning a gas flow loaded with dust.|
    KR1020137004163A| KR101895882B1|2010-07-20|2011-07-07|Method for cleaning a gas flow loaded with dust|
    EP11739011.2A| EP2595724B1|2010-07-20|2011-07-07|Method for cleaning a gas flow loaded with dust|
    US13/811,433| US8882893B2|2010-07-20|2011-07-07|Method for cleaning a gas flow loaded with dust|
    CA2805971A| CA2805971A1|2010-07-20|2011-07-07|Method for cleaning a gas flow loaded with dust|
    CN201180035167.6A| CN103002967B|2010-07-20|2011-07-07|The purification method of dust-containing air stream|
    [返回顶部]