• 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 an adsorber (1a, 1b) for purifying an exhaust gas containing at least SOX and NOX, comprising: - a gas distributor bottom (2) for supplying the exhaust gas; a bulk material region (4) arranged above the gas distributor bottom (2) and filled with adsorption and / or absorption medium, the bulk material region (4) having a lower (9) and an upper (10) section, the lower section ( 9) is arranged above the gas distributor base (2) and the upper section (10) is arranged above the lower section (9); - A above the bulk material region (4) arranged withdrawal device (5) for removing the flowing from bottom to top exhaust gas; - A discharge device (3) for discharging the adsorbent and / or absorbent; - a bunker (6) arranged above the take-off device (5) for feeding the adsorption and / or absorption medium through the bulk material region (4) from top to bottom; a lance (7) having at least one opening (25) projecting into the bulk material region (4) in a transition region between the lower (9) and the upper (10) section of the bulk material region (4) for direct injection of an ammonia-containing gas into the Bulk goods area (4). Furthermore, a method for purifying the exhaust gas is disclosed.
    公开号:AT520926A4
    申请号:T50700/2018
    申请日:2018-08-17
    公开日:2019-09-15
    发明作者:
    申请人:Integral Eng Und Umwelttechnik Gmbh；
    IPC主号:
    专利说明:

    The invention relates to an adsorber and a method for purifying an exhaust gas, which contains at least SO x and NO x .
    The requirements for the purity of waste gases from industrial process processes are constantly growing. In the exhaust gases, the concentrations of pollutants such as NOx, SOx, HCl, dioxins, furans, heavy metals and dust are subject to specified maximum limits, which are specified by legislation. Desulphurization and denitrification of the exhaust gas are particularly important in exhaust gas cleaning. The desulfurization is a separation of the sulfur dioxide (SO 2 ) and sulfur trioxide (SO 3 ) from the exhaust gas and the denitrification is a reduction of nitrogen oxides (NOx) from the exhaust gas. NOx is a collective term for the two nitrogen oxides nitrogen oxide (NO) and nitrogen dioxide (NO2) and SOx is a collective term for sulfur dioxide (SO2) and sulfur trioxide (SO3).
    WO 2008/071446 A1 describes a method and a device for cleaning exhaust gases from a sintering process of ores in the production of metals, the sintered exhaust gas containing at least NOx and SO2. The device has an adsorber filled with a lower and an upper activated carbon layer with a lower horizontal gas inflow and bulk material discharge floor, the adsorber being designed as a moving bed reactor. The exhaust gas is fed into the adsorber from below via the lower gas inflow and bulk material discharge floor and flows from below through the lower activated carbon layer, the main amount of SO2 being adsorbed by the activated carbon. The sintered exhaust gas then leaves the lower activated carbon layer on an upper free surface and is discharged from the reactor at a lateral deflection point and mixed intensively with ammonia (NH3) in an elongated gap, the ammonia at least partially forming nitrogen (NOx) N2) and water (H2O) reacts. The sintered exhaust gas then passes into the adsorber under an upper horizontal gas inflow and bulk material discharge floor, which is arranged above the lower activated carbon layer, and above it back into the upper activated carbon layer for denitrification. Desulfurization is of great importance before the addition of ammonia to the sintered exhaust gas, since SO2 can react with NH3 to form ammonium bisulfate crystals / 28, which can cause the activated carbon to expand in the pores of the activated carbon. In the upper activated carbon layer, the sintered exhaust gas flows from bottom to top, at least the main amount of NOx components from the sintered exhaust gas and / or their reaction products being adsorbed on the surface of the activated carbon. The cleaned sintered exhaust gas leaves the adsorber on the free surface of the upper activated carbon layer. The activated carbon is fed evenly distributed from above from a storage bunker via a bulk material distribution floor at the upper end of the adsorber to the upper free surface of the upper activated carbon layer, migrates from top to bottom through the adsorber and is via the lower gas inflow and bulk material extraction floor discharged from the adsorber. The lower and the upper gas inflow and bulk material discharge floor, which can be designed, for example, according to WO 88/08746 A1, are used to draw off the activated carbon moving from top to bottom via funnels and to feed the sintered exhaust gas flowing from bottom to top between the Funnels, with further funnels projecting into the funnels being arranged above the funnels, so that the sintered exhaust gas flows between the funnels and the further funnels through the activated carbon migrating into the funnels from above. The disadvantage here is that there is no contact between the sintered exhaust gas and the activated carbon in the area of the upper horizontal gas inflow and bulk material discharge floor, in which the sintered exhaust gas is discharged from the adsorber at the lateral deflection point, so that an adsorber with an upper gas inflow occurs - and bulk goods discharge floor must be built higher than an adsorber without this floor to ensure the same height of the activated carbon bed. Another disadvantage of the upper gas flow and bulk material discharge floor is the more complex maintenance of the adsorber, since this floor divides the adsorber into two activated carbon layers. Emptying and maintaining the adsorber is therefore associated with additional effort due to the upper gas flow and bulk material discharge floor. Another disadvantage is that when the sintered exhaust gas is mixed intensively with the ammonia, components of the sintered exhaust gas, such as hydrogen chloride (HCl) and sulfur oxides (SOx), can react with the ammonia to form solids. These solids, in the form of particles, can agglomerate (deposits) at the lateral deflection point and in the gas inflow and bulk material discharge floor and / 28 lead to business interruptions. These deposits cannot be removed during operation and can only be removed with great effort in the course of a business interruption. Another disadvantage as a result of the agglomerations is the constant increase in the pressure loss since these deposits adhere to the surface of the device in the area of the gas inflow floor and cannot be removed during operation. As a result, this leads to an uneven gas inflow.
    The object of the present invention is to alleviate or eliminate at least individual disadvantages of known adsorbers for cleaning exhaust gases. The invention has in particular the aim of creating an adsorber and a method for efficient cleaning of an exhaust gas, increasing the availability and simplifying the maintenance of the adsorber.
    The present invention provides an adsorber for purifying an exhaust gas, which contains at least SOx and NOx. The adsorber has at least:
    a gas distributor base for supplying the exhaust gas which is substantially uniformly distributed over a horizontal cross section of the adsorber;
    - A bulk material area arranged above the gas distributor floor, which is filled with adsorbent and / or absorbent, the bulk material area having a lower section and an upper section, the lower section being arranged above the gas distributor floor and the upper section being arranged above the lower section ;
    - An extraction device arranged above the bulk material area for drawing off the exhaust gas flowing from the gas distributor base from bottom to top through the bulk material area;
    - a discharge device for discharging the adsorbent and / or absorbent;
    / 28
    - A bunker arranged above the discharge device for supplying the adsorbent and / or absorbent which passes through the bulk material area from top to bottom and is discharged from the adsorber via the discharge device; and
    - A lance protruding in a transition area between the lower and the upper section of the bulk goods area into the bulk goods area and having at least one opening for direct injection of an ammonia-containing gas into the bulk goods area.
    This accomplishes the stated task.
    Accordingly, the invention also provides a method for purifying an exhaust gas which contains at least SOx and NOx, the exhaust gas being fed from below into an adsorber, essentially uniformly distributed over a horizontal cross section of the adsorber, the adsorber having an adsorption and / or absorbent filled bulk material area, wherein the adsorbent and / or absorbent is fed above the bulk material area, the bulk material area travels from top to bottom and then discharged from the adsorber, the exhaust gas flowing from bottom to top through the bulk material area of the adsorber , wherein in a first process step in a lower section of the bulk material area at least the SOx contained in the exhaust gas is at least partially adsorbed or absorbed by the adsorbent and / or absorbent and arranged in a second process step in an above the lower section In the upper section of the bulk material area, the NOx contained in the exhaust gas is at least partially brought into contact with an ammonia-containing gas, after the first and the second process step, the cleaned exhaust gas is withdrawn from the adsorber via an extraction device arranged above the bulk material area, the ammonia-containing gas being without to be mixed beforehand with the exhaust gas / 28 is injected directly into a transition region between the lower and the upper section of the bulk material region into the bulk material region, preferably uniformly distributed over one or more horizontal cross sections of the bulk material region.
    This also achieves the stated object.
    With the method according to the invention, a large part of the SOx and the NOx as well as the solid particles formed from side reactions can be removed from the exhaust gas.
    The exhaust gas, which contains at least SOx and NOx, is fed to a single adsorber or adsorbers arranged in parallel from below via a gas distributor base. Gas distributor bases for uniform distribution of an inflowing gas over a horizontal cross section of the adsorber are known, for example, from WO 88/08746 A1. Above the gas distributor floor, a bulk material area is arranged in the adsorber, which is filled with adsorbent and / or absorbent. The exhaust gas flows from below through the bulk material area, whereby it is brought into contact with the adsorbent and / or absorbent. Above the bulk material area, the exhaust gas is drawn off via an extraction device or gas collection chamber of the adsorber. In the countercurrent process to the exhaust gas, the adsorbent and / or absorbent, which is preferably a carbon-containing adsorbent and / or absorbent, particularly preferably activated carbon, moves from the top to the bottom of the bulk material. For this purpose, the adsorbent and / or absorbent is fed to a bunker, which is arranged above the extraction device or gas collection chamber, for storing the adsorbent and / or absorbent. Adsorption and / or absorption medium is fed from the bunker to the bulk material area, which passes through the bulk material area from top to bottom and is discharged from the adsorber under the bulk material area via a discharge device. Discharge devices for the continuous or discontinuous discharge of the adsorbent and / or absorbent are shown, for example, in WO 88/08746 A1.
    The bulk material area consists of a single layer and / 28 has a lower section and an upper section arranged above the lower section. In the lower section, the exhaust gas is brought into contact with the adsorbent and / or absorbent, the SOx contained in the exhaust gas being at least partially adsorbed or absorbed by the adsorbent and / or absorbent. The exhaust gas, which is thereby at least partially cleaned of SOx, flows further into a transition area between the lower and upper section of the bulk material area. In this transition area, ammonia-containing gas, preferably carrier gas with ammonia, is injected into the bulk goods area via at least one lance projecting into the bulk goods area with at least one opening, which can be designed, for example, as a nozzle, hole or slot. The ammonia-containing gas can be injected into the bulk material area in the cocurrent and / or countercurrent and / or cross-flow process. Direct injection of the ammonia-containing gas mixes it with the exhaust gas in the bulk material area of the adsorber, as a result of which the NOx contained in the exhaust gas is at least partially brought into contact with the ammonia-containing gas due to the flow of the exhaust gas in the transition area and / or in the upper section of the bulk material area. In the presence of the adsorbent and / or absorbent, the NOx at least partially reacts with the ammonia of the ammonia-containing gas to nitrogen and water, the adsorbent and / or absorbent serving as a catalyst. The exhaust gas, at least partially cleaned of SOx and NOx, flows from the upper section of the bulk material area to the extraction device and leaves the adsorber.
    The advantage of eliminating the mixing area outside the bulk material area is that no solid deposits caused by the reaction of ammonia and HCL and SO 2 clog the inflow floor. The adsorber can be made more compact and the pressure loss of the adsorber can be reduced. Due to the lack of a mixing area, the availability of the system is higher, which can save time and costs.
    It is expedient for the ammonia-containing gas to be injected into the bulk material area in a countercurrent and / or crossflow process, preferably in a countercurrent and crossflow process, based on the exhaust gas flowing from bottom to top. This results in a longer residence time of the ammonia-containing gas in the bulk material area and particularly good mixing of the ammonia-containing gas with the exhaust gas, possibly favored by the bulk material.
    According to a preferred embodiment, at least two lances projecting into the bulk material area and having at least one opening are provided for direct injection of an ammonia-containing gas into the bulk material area, which is uniformly distributed over a horizontal cross section of the bulk material area. Because of the uniform distribution of the ammonia-containing gas, the exhaust gas is mixed particularly well with the ammonia-containing gas in order to reduce the largest possible amount of NOx to nitrogen and water.
    According to a further preferred embodiment, the lances projecting into the bulk material region are arranged horizontally and parallel to one another, the lances extending from a first side to a second side of the bulk material region, the second side being opposite the first side, with at least one outside the bulk material region connected to the lances supply line for supplying the ammonia-containing gas is arranged. With this arrangement, the feed lines do not reduce the flow cross section of the exhaust gas in the adsorber, which enables a particularly uniform flow profile. The horizontal and parallel arrangement of the lances leads to a distribution of the ammonia-containing gas that is as uniform as possible over the cross section of the adsorber. The two lances can also be connected in the bed with webs to form a grid.
    According to a preferred embodiment, the adsorber has at least two further lances arranged horizontally and parallel to one another, the further lances being arranged above and / or below the lances and parallel to the lances. As a result, the ammonia-containing gas is injected in a uniformly distributed manner over a further horizontal cross section of the bulk material area, as a result of which the contact of the exhaust gas with the ammonia-containing gas is increased. The further lances are preferably not arranged directly above or below the lances, but offset in the horizontal direction, so that the further lances are positioned above the / 28
    Gaps between the lances are arranged. This results in better mixing of the exhaust gas with the ammonia-containing gas.
    Furthermore, it is favorable if the lance or the lances is / are divided into sections, the sections having separating devices for preventing gas transport between the sections, each section having at least one separate feed line for supplying variable amounts of gas to each section. The sections can be used to react to irregular process conditions distributed over the cross section of the bulk material area, such as unevenly distributed flow velocities of the exhaust gas, by supplying different gas quantities to the sections. The targeted supply of variable gas quantities can also respond better to disturbances in the flow behavior of the exhaust gas.
    According to a preferred embodiment, a tube, preferably a round tube or square shaped tube, is provided to form the lance or lances. In this embodiment of the lance, advantageously no adsorbent and / or absorbent collects on the lance, as a result of which the entire bed of adsorbent and / or absorbent migrates through the adsorber from top to bottom.
    According to a further preferred embodiment, the lance has injection nozzles, preferably pipe sections with at least one nozzle opening at their respective free ends, for injecting the ammonia-containing gas into the bulk material area, the injection nozzles preferably being arranged in a plane transverse to a longitudinal extension of the lance. Advantageously, the injection nozzles enable a particularly uniform injection of the ammonia-containing gas over a cross section of the bulk material area for intensive mixing with the exhaust gas. The injection nozzles, which are smaller in cross section than the lances, enable a larger flow cross section for the exhaust gas.
    In order to further increase the mixing of the exhaust gas with the ammonia-containing gas, it is expedient if the injection nozzles are downward, preferably based on a horizontal plane, between / 28
    30 ° and 60 ° downwards, particularly preferably, are inclined with respect to a horizontal plane at 45 ° downwards.
    To improve the mixing of the exhaust gas with the ammonia-containing gas, it is favorable if the ammonia-containing gas injected into the bulk material area has a turbulent flow. Due to the free jet effect, the exhaust gas surrounding the injected ammonia-containing gas is advantageously sucked in and carried away by the free jet of the ammonia-containing gas, as a result of which the two gases are thoroughly mixed.
    According to a further preferred embodiment, the opening of the lance is inclined upwards and at least one deflection plate, preferably a gable roof-shaped deflection plate, is arranged above the lance to protect the opening from the adsorbent and / or absorption medium. Advantageously, the migrating adsorbent and / or absorbent is deflected over the lance by the baffle plate past the lance, so that the opening of the lance is not blocked by the adsorbent and / or absorbent.
    To stabilize the lance, it is advantageous if at least one stabilizer, preferably a plate, particularly preferably a vertical plate, is arranged below the lance in the direction of the lance. Advantageously, the stabilizer is intended to prevent the lance from bending due to the temperatures in the adsorber and / or the weight of the adsorbent and / or absorbent which is loaded on the lance.
    According to a preferred embodiment, the adsorber has at least one additional supply line for supplying the ammonia-containing gas at the level of the extraction device and / or the gas distributor base, the at least one further supply line being connected to the lance via at least one vertical line. The pressure line in the lance can be reduced via the additional feed line, thus enabling a more uniform flow profile in the lance and, subsequently, a more uniform injection of the ammonia-containing gas into the bulk material area.
    In order to ensure the stability and long life of the lance, it is advantageous if the lance is made of steel, for example structural steel. The lance can be made of stainless steel to increase the corrosion resistance.
    According to a preferred embodiment, the ratio of the height of the lower section of the bulk material area to the height of the upper section of the bulk material area 2 to 3 or 2 to 4 depends on the adsorbent and / or absorbent and maximum NOX concentrations. This ratio enables efficient separation of the SOx from the exhaust gas and efficient separation of the NOx from the exhaust gas.
    Furthermore, it is favorable if the exhaust gas additionally contains at least one pollutant which reacts with ammonia to form a solid, for example hydrogen chloride or sulfur dioxide, the at least one pollutant at least partially reacting with the injected ammonia-containing gas to form a solid, the solid being separated from the adsorption and / or absorbent is at least partially adsorbed or agglomerated on the surface. Due to the direct injection of the ammonia-containing gas into the bulk material area, the solids are advantageously not deposited on the walls of the adsorber, but are at least partially adsorbed or absorbed by the adsorbent and / or absorbent. Deposits at the opening of the lance are removed by rubbing the adsorbent and / or absorbent at the opening and are removed from the adsorber via the adsorbent and / or absorbent.
    To fight fire as a result of self-ignition of the bulk material, it is advantageous if nitrogen is injected directly into the bulk material area, uniformly distributed over the horizontal cross section of the bulk material area, for inerting the bulk material area. As a result, when the exhaust gas flow is stopped, the oxygen supply to the bulk material area is interrupted and the oxygen present in the bulk material area is consumed by the injection of nitrogen. The fire in the adsorber is thus inhibited or completely extinguished.
    The invention is illustrated below with reference to the non-restrictive exemplary embodiments shown in the drawings.
    Fig. 1 shows a section of the adsorber according to the invention along a vertical sectional plane.
    FIG. 1a shows a section of an adsorber according to the invention similar to FIG. 1, which is of two-tier design.
    Fig. 2 shows a section of a further adsorber according to the invention along a vertical sectional plane.
    Fig. 2a shows a section of an inventive adsorber similar to Fig. 2, which is designed in two stories.
    3 shows a section along line a-a in FIG. 2 above lances of the further inventive adsorber according to FIG. 2.
    FIG. 4 shows a section of a lance of the adsorber according to the invention according to FIG. 1 along a vertical sectional plane.
    5 shows a section of a further lance of an adsorber according to the invention along a vertical sectional plane.
    1 shows an adsorber 1a according to the invention for cleaning an exhaust gas, which has a gas distributor base 2, a discharge device 3, a bulk material area 4 arranged above the gas distributor base 2, a discharge device 5 arranged above the bulk material region 4, a bunker 6 arranged above the exhaust device 5 and in the horizontally and parallel lances 7 projecting the bulk material area 4 and having at least one opening. The exhaust gas, which contains among other things SOx, NOx, possibly also HCl, dioxins, furans, heavy metals and dust, is fed from below into the adsorber 1a essentially uniformly via the gas distributor base 2 of the adsorber 1a and flows through the bottom from the top Bulk material area 4 of the adsorber 1a. The bulk material area 4 is filled with activated carbon 8 as an adsorbent and / or absorbent and has a lower 9 and an upper 10 section, the lower section 9 being arranged above the gas distributor body 12/28 and the upper section 10 above the lower section 9 is arranged. The activated carbon 8 is fed into the bunker 6 via two feed nozzles 11a, 11b and, starting from the bunker 6, traverses the bulk material area 4 from top to bottom and is then discharged from the bulk material area 4 via the discharge device 3 and subsequently via a discharge funnel 12 from the Adsorber 1a removed. Due to the migration of the activated carbon 8 from top to bottom and the flow of the exhaust gas from bottom to top, the loading of the activated carbon 8 with pollutants from the exhaust gas increases from top to bottom. The activated carbon 8 discharged from the adsorber 1a via the discharge funnel 12 can be regenerated by removing the pollutants adsorbed by the activated carbon 8 from the activated carbon 8 by known methods. The activated carbon 8 thus regenerated can be returned to the bunker 6 of the adsorber 1a.
    In the embodiment shown in FIG. 1, the gas distributor base 2 and the discharge device 3 are the same device, this device as the inflow floor according to FIG
    WO 88/08746 A1 is executed. The exhaust gas flowing into the adsorber 1a via the gas distributor base 2 flows evenly distributed from bottom to top in a countercurrent process to the activated carbon 8 through the adsorber 1a, the SOx contained in the exhaust gas being at least partially removed from the bottom section 9 of the bulk material area 4 in a first process step Activated carbon 8 is adsorbed or absorbed. In a second process step in the upper section 10 of the bulk material area 4, the NOx contained in the exhaust gas is at least partially removed from the lances with an ammonia-containing gas, which is a carrier air with ammonia, and in a transition area between the lower 9 and the upper 10 section of the bulk material area 4 7 is sprayed over a horizontal cross section of the bulk material area 4, evenly distributed, directly into the bulk material area 4 and mixed with the exhaust gas, in the presence of the activated carbon 8. Due to the catalytic effect of the activated carbon 8, the NOx of the exhaust gas in the upper section 10 of the bulk material area 4 is at least partially reduced to N2 and H2O. Subsequently, the cleaned exhaust gas is drawn off from the adsorber 1 a via the extraction device 5 after the first and the second process step. The extraction / extraction device 5 has funnels 13 and a separating plate 14, so that the activated carbon 8 can migrate from the bunker 6 into the bulk material area 4, but the exhaust gas cannot flow into the bunker 6.
    In the embodiment shown in FIG. 1, two feed lines 15a, 15b connected to the lances 7 for supplying the ammonia-containing gas to the adsorber 1a are arranged outside the bulk material area 4. The ammonia-containing gas is injected into the bulk material area 4 at a temperature similar to the temperature of the exhaust gas, based on the exhaust gas flowing from the bottom upwards, in the countercurrent and crossflow processes. This results in a particularly good mixing of the ammonia-containing gas with the exhaust gas and a long residence time of the ammonia-containing gas in the bulk material area 4. The lances 7 have injection nozzles 16, which are designed as pipe sections, with a nozzle opening 17 (FIG. 4) at their free end, for injecting the ammonia-containing gas into the bulk material area 4, the injection nozzles 16 being arranged in planes transverse to a longitudinal extension the lance 7 are arranged. The injection nozzles 16 are, relative to a horizontal plane, at any angle, preferably inclined downwards by 45 °. Below the lances 7, vertical sheets 18 are arranged in the direction of the lances 7 in order to stabilize the lances 7 and to prevent deformation of the lances 7.
    In the embodiment shown in FIG. 1, in the event of a fire in the activated carbon 8, nitrogen can be supplied to the lances 7 via the feed lines 15a, 15b in order to inject the nitrogen directly into the bulk material area 4, evenly distributed over the horizontal cross section of the bulk material area 4. As a result, the bulk material area 4 is rendered inert and the fire is prevented from spreading or the fire suffocates.
    Fig. 1a shows a further embodiment according to the invention, which is designed in two stories. Here, two adsorbers 1 a, which essentially correspond to the exemplary embodiment according to FIG. 1, are arranged one above the other. For the simple supply of the activated carbon 8 provided as adsorbent and / or absorbent, a further feed nozzle 11c is provided on the upper adsorber 1a, to which conveyor pipes 12a adjoin / 28. The conveyor pipes 12 pass through the upper adsorber 1a completely, so that the activated carbon 8 is fed to the bunker 6 of the lower adsorber 1a. The two adsorbers 1a are completely separated from one another by an intermediate base 12b. The loaded adsorbent and / or absorbent discharged from the upper adsorber 1a is conveyed through conveyor pipes 12a through the lower adsorber 1a and through separate pipes into or through the discharge hopper 12.
    2 shows a further adsorber 1b according to the invention in a sectional view, which comprises a gas distributor base 2, a discharge device 3, a bulk material area 4 arranged above the gas distributor base 2, a discharge device 5 arranged above the bulk material region 4, and a bunker 6 arranged above the exhaust device 5 and has lances 7 that project horizontally and parallel to the bulk material area 4 and have at least one opening. The adsorber 1b is configured in the same way as the adsorber 1a, the adsorber 1b, in contrast to the adsorber 1a, having a further feed line 19 for supplying the ammonia-containing gas at the level of the extraction device 5, the further feed line 19 with the lances 7 via vertical lines 20 connected is. This has the advantage that the pressure gradient in the lances 7 is lower and thus the injection of the ammonia-containing gas into the bulk material area 4 is more uniform. Of course, two adsorbers 1a, 1b of the same type can be installed one above the other and would then form a so-called double-deck adsorber.
    FIG. 2a shows a further two-story exemplary embodiment in which two adsorbers 1b, which essentially correspond to the exemplary embodiment according to FIG. 2, are arranged one above the other. For the simple supply of the activated carbon 8 provided as adsorbent and / or absorbent to the lower adsorber 1b, delivery tubes 12a are provided, as already described in connection with FIG. 1a. To avoid repetitions, reference is made to the explanations in connection with FIG.
    FIG. 3 shows a section aa above the lances 7 of the adsorber 1b according to the invention according to FIG. 2. The lances 7 are arranged horizontally and parallel to one another in the bulk material area 4 of the adsorber 1b, the lances 7 extending from a first side 21 to extend to a second side 22 of the bulk material area 4, the second side 22 lying opposite the first side 21. The two feed lines 15a, 15b connected to the lances 7 for supplying the ammonia-containing gas are arranged outside the bulk material area 4. Each of the lances 7 is connected to the feed line 19 (FIG. 2) via one of the vertical lines 20. In addition, each of the lances 7 is divided into at least three sections, the gas transport between the sections being prevented with the aid of separating devices 23. Each section of each lance 7 can be supplied with a gas quantity of the ammonia-containing gas defined for the respective section with the aid of one of the two feed lines 15a, 15b or one vertical line. With the help of the sections, different amounts of the ammonia-containing gas can thus be supplied to the at least three different sections of each lance 7.
    In the embodiment shown in FIG. 3, the injection nozzles 16 of the lances 7 are arranged in planes that are transverse to the longitudinal extent of the respective lance 7. Each of the injection nozzles 16 has a nozzle opening 17 at its free end for uniformly distributed injection of the ammonia-containing gas into the bulk material area 4.
    FIG. 4 shows a lance 7 of the adsorber 1b and 1a according to the invention according to FIGS. 1 and 2 in a section. The lance 7 is designed in cross section as a square shaped tube, one edge of the square pointing upwards and one edge of the square pointing downwards. Injection nozzles 16 are arranged on the two lower side surfaces 24a, 24b of the square shaped tube, the injection nozzles 16 each projecting perpendicularly from the side surface 24a or the side surface 24b, so that the injection nozzles 16 are preferably at an arbitrary angle with respect to a horizontal plane are inclined downwards by 45 °. At the free end of each injection nozzle 16 there is a nozzle opening 17 for injecting the ammonia-containing gas into the bulk material area 4. Below the lances 7, vertical sheets 18 are arranged in the direction of the lances 7/28 in order to stabilize the lances 7 and to prevent deformation of the lances. Pollutants reacting with ammonia to form a solid, such as chlorine-hydrogen (HCl) and sulfur oxides (SOx), can be contained in the exhaust gas and react with ammonia to form a solid in the area of the injection and mixing of the ammonia-containing gas with the exhaust gas in the transition area. The solid reaction products of these reactions agglomerate at least partially on the surface of the activated carbon 8 or are adsorbed and discharged from the adsorber 1a and 1b via the discharge device 3. At least in part, the solid reaction products can also be deposited on the nozzle openings 17 of the injection nozzles 16, these deposits being removed by the shear action of the activated carbon 8 moving past the nozzle openings 17. Thus, due to friction processes of the activated carbon 8 at the nozzle openings 17, the nozzle openings 17 are self-cleaning.
    5 shows a further lance 7 of an adsorber according to the invention in section. In this exemplary embodiment, in addition to the lances 7 arranged horizontally and parallel to one another, further lances arranged horizontally and parallel to one another are provided, the further lances being arranged above the lances 7 and parallel to the lances 7. As a result, the ammonia-containing gas can be injected in a uniformly distributed manner over a further horizontal cross section of the bulk material region 4.
    In the embodiment shown in FIG. 5, the lance 7 is designed as a round tube and has openings 25, the openings 25 being inclined upward. A gable roof-shaped deflection plate 26 is arranged above the lance 7 over the entire length of the lance 7, which extends from the first side 21 to the second side 22 of the bulk material area 4. The deflection plate 26 protects the openings 25 of the lance 7 from the activated carbon 8 migrating downward, in that the activated carbon 8, which is located above the lance 7, is deflected by means of the deflection plate 26 and is guided past the lance 7. Furthermore, the ammonia-containing gas injected from the opening 25 into the bulk material area 4 is deflected downward, so that the ammonia-containing gas, based on the exhaust gas flowing upward from below, is introduced into the bulk material area 4 in a countercurrent and cross-current process.
    权利要求:
    Claims (15)
    [1]
    1. Adsorber (1a, 1b) for cleaning an exhaust gas which contains at least SO x and NO x , which has the following:
    - A gas distributor floor (2) for a horizontal
    Cross section of the adsorber (1a, 1b) essentially uniformly distributed supply of the exhaust gas;
    - A bulk material region (4) which is arranged above the gas distributor base (2) and is filled with adsorbent and / or absorption medium, the bulk material region (4) having a lower section (9) and an upper section (10), the lower section (9) is arranged above the gas distributor base (2) and the upper section (10) is arranged above the lower section (9);
    - An extraction device (5) arranged above the bulk material region (4) for extracting the exhaust gas flowing from the gas distributor base (2) through the bulk material region (4) from bottom to top;
    - A discharge device (3) for discharging the adsorbent and / or absorbent;
    - One arranged above the trigger device (5)
    Bunker (6) for feeding the bulk material area (4) from top to bottom and discharged from the adsorber (1a, 1b) via the discharge device (3)
    Adsorbent and / or absorbent;
    marked by:
    - In a transition area between the lower (9) and the upper (10) section of the bulk material area (4) in the bulk material area (4) projecting, at least one opening (25) having a lance (7) for the direct injection of an ammonia-containing gas into the Bulk goods area (4).
    [2]
    2. Adsorber (1a, 1b) according to claim 1, characterized in that at least two projecting into the bulk material area (4), at least
    19/28 at least one lance (25) has lances (7) for direct injection of an ammonia-containing gas into the bulk material area (4), which is uniformly distributed over a horizontal cross section of the bulk material area (4).
    [3]
    3. Adsorber (1a, 1b) according to claim 2, characterized in that the lances (7) projecting into the bulk material region (4) are arranged horizontally and parallel to one another, the lances (7) extending from a first side (21) to extend to a second side (22) of the bulk material area (4), the second side (22) lying opposite the first side (21), with at least one supply line (15a, 15b) connected to the lances (7) outside the bulk material area (4) ) for feeding the ammonia
    Gases is arranged.
    [4]
    4. adsorber (1a, 1b) according to claim 3, characterized by at least two further horizontally and parallel to each other arranged lances, the further lances above and / or below the lances (7) and parallel to the lances (7) are arranged ,
    [5]
    5. Adsorber (1a, 1b) according to one of claims 1 to 4, characterized in that the lance (7) or the lances (7) is / are divided into sections, the sections separating devices (23) for preventing gas transport have between the sections, each section having at least one separate feed line for supplying variable amounts of gas to each section.
    [6]
    6. Adsorber (1a, 1b) according to one of claims 1 to 5, characterized in that a tube, preferably a round tube or square shaped tube, is provided to form the lance (7) or the lances (7).
    [7]
    7. Adsorber (1a, 1b) according to one of claims 1 to 6, characterized in that the lance (7) injection nozzles (16), preferably pipe pieces with at least one nozzle opening (17) at their free end, for injecting the ammonia-containing gas in the bulk material area (4), the injection nozzles (16) preferably being arranged in a plane transverse to a longitudinal extension of the lance (7).
    20/28
    [8]
    8. adsorber (1a, 1b) according to claim 7, characterized in that the injection nozzles (16) downwards, preferably, based on a horizontal plane, between 30 ° and 60 ° downwards, particularly preferably, based on a horizontal plane, are inclined downwards by 45 °.
    [9]
    9. adsorber (1a, 1b) according to any one of claims 1 to 6, characterized in that the opening (25) of the lance (7) is inclined upwards and above the lance (7) at least one baffle, preferably a gable roof-shaped Deflector (26) is arranged to protect the opening (25) from the adsorbent and / or absorbent.
    [10]
    10. adsorber (1a, 1b) according to one of claims 1 to 9, characterized in that below the lance (7) in the direction of the lance (7) at least one stabilizer, preferably a plate, particularly preferably a vertical plate (18), is arranged to stabilize the lance (7).
    [11]
    11. Adsorber (1a, 1b) according to one of claims 1 to 10, characterized by at least one additional feed line (19) for supplying the ammonia-containing gas at the level of the extraction device (5) and / or the gas distributor base (2), the further supply line (19) is connected to the lance (7) via at least one vertical line (20).
    [12]
    12. A method for purifying an exhaust gas which contains at least SOx and NOx, the exhaust gas being fed from below into an adsorber (1a, 1b) essentially uniformly distributed over a horizontal cross section of the adsorber (1a, 1b), the adsorber ( 1a, 1b) one with adsorption and / or
    Absorbent-filled bulk material area (4), wherein the adsorbent and / or absorbent is supplied above the bulk material area (4), the bulk material area (4) travels from top to bottom and then discharged from the adsorber (1a, 1b), which Exhaust gas flows from bottom to top through the bulk material area (4) of the adsorber (1a, 1b),
    21/28 whereby in a first process step in a lower section (9) of the bulk material area (4) at least the SO x contained in the exhaust gas is at least partially adsorbed or absorbed by the adsorbent and / or absorbent and in a second process step in an above the the lower section (9), the upper section (10) of the bulk material area (4), the NOx contained in the exhaust gas is at least partially brought into contact with an ammonia-containing gas, the cleaned exhaust gas after the first and the second process step via an above the bulk material area (4 ) arranged extraction device (5) is withdrawn from the adsorber (1a, 1b), characterized in that the ammonia-containing gas without being previously mixed with the exhaust gas directly in a transition region between the lower (9) and the upper (10) section of the Bulk material area (4) into the bulk material area (4), preferably over a horizontal cross section of the bulk material area (4) evenly distributed, injected.
    [13]
    13. The method according to claim 12, characterized in that the ammonia-containing gas is injected into the bulk material region (4) in a countercurrent and / or crossflow method, preferably in a countercurrent and crossflow method, based on the exhaust gas flowing from the bottom up.
    [14]
    14. The method according to claim 12 or 13, characterized in that the exhaust gas additionally contains at least one pollutant which reacts with ammonia to form a solid, for example chlorine-hydrogen or sulfur dioxide, the at least one pollutant at least partially reacting with the injected ammonia-containing gas to form a solid, the solid being at least partially adsorbed or absorbed by the adsorbent and / or absorbent.
    [15]
    15. The method according to any one of claims 12 to 14, characterized in that in the event of a fire of the adsorber (1a, 1b) nitrogen directly in the bulk material area (4), evenly distributed over the horizontal cross section of the bulk material area (4), for inerting the bulk material area (4) is injected.
    类似技术:
    公开号 | 公开日 | 专利标题
    EP0863790B1|2001-03-14|Flue-gas cleaning installation
    DE1519962B2|1971-07-15|METHOD OF ADSORPTION OF SO DEEP 2 OR OTHER GAS-FORMED POLLUTIONS FROM EXHAUST GASES
    EP0232731B1|1991-08-07|Process and apparatus for purifying gases, particularly for desulfurizing and denitrating smoke
    EP0376356A1|1990-07-04|Method and apparatus for removing undesirable components from an exhaust gas
    DE2119061C3|1974-08-22|Device for carrying out catalytic vapor phase reactions
    EP0472565B1|1994-03-16|Moving bed reactor installation
    EP0270531B1|1989-11-08|Moving bed reactor
    AT520926B1|2019-09-15|Adsorber for purifying exhaust gases and method therefor
    EP0357653B1|1994-01-19|Feed inlet floor for mobile bed reactors
    EP3095505B1|2018-03-07|Process and system for the purification of waste gases charged with nitrogen oxides
    DE3039477A1|1982-05-06|Desulphurisation and denitrification of waste gas - by passing across two travelling beds of partly charged and then fresh carbonaceous adsorbent
    EP0354952B1|1992-07-01|Shaft with a moving bed of pourable material
    DD215477A5|1984-11-14|METHOD AND DEVICE FOR CARRYING OUT REACTIONS IN THE FLYBED SOLIDS SYSTEM
    EP3268114B1|2020-05-06|Flue gas cleaning installation and method for cleaning flue gas
    DE3013645A1|1980-10-23|METHOD AND DEVICE FOR INPUTING PARTICLES INTO A FLUIDIZED LAYER
    EP0193135A2|1986-09-03|Process for eliminating sulfur dioxide and nitrogen oxides from waste gases
    AT522436B1|2020-11-15|Container and method for loading an adsorbent and / or absorbent with ammonia
    DE19961691B4|2009-09-03|Process for cleaning flue gas
    DD232836A5|1986-02-12|METHOD AND APPARATUS FOR REDUCING THE CONTAMINANT CONTENT OF SMOKE GASES
    WO1996004065A1|1996-02-15|Adsorption reactor for separating undesirable components from a fluid
    DE69737187T2|2007-05-03|METHOD OF EXHAUST TREATMENT
    EP3299079B1|2019-12-04|Gas treatment system and method for operating a gas treatment system with an injection lance
    DD136927B1|1986-03-26|ANROASTIVE FLOOR FOR SWIVEL LAYER APPARATUS
    AT398709B|1995-01-25|Inflow plate for moving-bed reactors
    DE3427905C2|1987-10-29|
    同族专利:
    公开号 | 公开日
    CN110833743A|2020-02-25|
    WO2020033986A1|2020-02-20|
    AT520926B1|2019-09-15|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE3232544A1|1981-09-10|1983-06-30|Mitsui Mining Co., Ltd., Tokyo|Process for eliminating sulphur oxides and nitrogen oxides from an exhaust gas|
    WO2006084671A1|2005-02-08|2006-08-17|Horst Grochowski|Method for cleaning exhaust gases produced by a sintering process for ores and/or other metal-containing materials in metal production|
    WO2008071215A1|2006-12-14|2008-06-19|Horst Grochowski|Method and device for scrubbing effluent gases from a sintering process for ores or other metal-containing materials in metal production|
    CN102895839A|2012-10-17|2013-01-30|艾淑艳|Device and method for performing integrated purification on smoke|
    CN206240303U|2016-11-14|2017-06-13|一重集团大连工程建设有限公司|A kind of adverse current, the integrated activated coke smoke eliminator of cross-current type series connection|
    CN108479344A|2018-04-08|2018-09-04|中冶长天国际工程有限责任公司|A kind of desulphurization denitration removes ammonia system|WO2020215115A1|2019-04-26|2020-10-29|Integral Engineering Und Umwelttechnik Gmbh|Container and method for charging an adsorption and/or absorption medium with ammonia|DE3510671A1|1985-03-23|1986-09-25|Kernforschungsanlage Jülich GmbH, 5170 Jülich|Process and apparatus for carrying out adsorptive and/or catalytic reactions|
    DE3523417A1|1985-03-23|1987-01-08|Kernforschungsanlage Juelich|WALKING BED REACTOR FOR ADSORPTIVE AND / OR CATALYTIC REACTIONS|
    JPH0667454B2|1985-09-30|1994-08-31|三菱重工業株式会社|Comprehensive exhaust gas treatment method|
    DE3732567A1|1987-05-07|1988-11-24|Horst Dr Grochowski|ANSTROME FLOOR FOR WALKING BED REACTORS AND METHOD FOR OPERATING THIS DEVICE|
    US5766555A|1987-05-07|1998-06-16|Grochowski; Horst|Feed inlet floor for mobile bed reactors|
    JP2000102719A|1998-09-29|2000-04-11|Sumitomo Heavy Ind Ltd|Treatment of waste gas and device therefor|
    CN101279186B|2008-05-23|2011-05-11|清华大学|Flue gas dry-type method for simultaneously desulfurizing and denitrating|
    CN101450278B|2008-12-22|2011-04-06|西安热工研究院有限公司|Whole wing type current sharing and partition adjustable ammonia-gas spraying device|
    EP2575997B1|2010-05-28|2021-06-30|ExxonMobil Upstream Research Company|Integrated adsorber head and valve design and swing adsorption methods related thereto|
    CN202506301U|2012-03-23|2012-10-31|蓝天环保设备工程股份有限公司|Adverse-flow ammonia spraying device for selective catalytic reduction denitration device|
    CN203842500U|2014-05-23|2014-09-24|国家电网公司|Anti-blocking ammonia injection grid|
    CN105148681B|2015-09-29|2017-09-22|北京首钢国际工程技术有限公司|A kind of agglomerates of sintered pellets flue gas absorption and blanking device|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50700/2018A|AT520926B1|2018-08-17|2018-08-17|Adsorber for purifying exhaust gases and method therefor|ATA50700/2018A| AT520926B1|2018-08-17|2018-08-17|Adsorber for purifying exhaust gases and method therefor|
    CN201811027495.1A| CN110833743A|2018-08-17|2018-09-04|Adsorber and method for exhaust gas purification|
    PCT/AT2019/060261| WO2020033986A1|2018-08-17|2019-08-16|Adsorber for cleaning exhaust gases and associated method|
    [返回顶部]