Abstract:
The invention relates to a filtering device for multiply polluted gasses, with an inclined bed with a filling of catalytic material, which bed has a retaining wall at its lower longer side, with a clean-gas exit positioned in the area of one front side of the bed, which ejects the gas which has passed through the filling, and with a flush-gas entrance also positioned in the area of one front side of the bed, the flush-gas entrance ( 40 ) and the clean-gas exit ( 36 ) being provided at the same front side ( 38 ), and beneath the bed ( 12 ), current-influencing devices ( 50 ) being positioned spread between the two front sides, which devices prevent or at least reduce current peaks in the flow of flush gas through the bed ( 12 ).

Description:
TECHNICAL FIELD 
       [0001]    The invention relates to a filtering devicefor multiply polluted gasses, with an inclined bed with a filling of catalytic material, which bed has a retaining wall at its lower longer side, with a clean-gas exit positioned in the area of one front side of the bed, which ejects the gas which has passed through the filling, and with a flush-gas entrance also positioned in the area of one front side of the bed. 
       BACKGROUND OF THE INVENTION 
       [0002]    Such a filtering device is known for instance from DE 10 2005 022 138 A1. This filtering device is characterized in that it is particularly suited for filtering out dust, dioxins, nitrogen oxides or the like, in particular from blast-furnace waste gasses or waste-incinerating plants. For this purpose, it has a number of inclined beds which are provided with a filling of catalytic material. At the lower longer side of the bed, the catalytic material borders a retaining wall each, and the bed is penetrated by a flow or current from top to bottom in order to achieve the desired filtering effect. 
         [0003]    If the catalytic material is clogged, in particular due to the resulting dust, a flush gas is supplied through the bed from bottom to top. As a result, the uppermost and compressed layer of catalytic material is slightly lifted and will slide off over the retaining wall. 
         [0004]    Obviously the angle of repose of the filling material must correspond to the angle of inclination of the bed in order to secure an optimal operation. 
         [0005]    For industrial use, such filtering devices are of considerable lengths. For example, a bed can be six meters or even ten meters long in the longitudinal direction, with the width then amounting to one meter, for instance. The bed which is inclined, perceived in a cross direction, is then underflushed over its entire length, i.e. over six or ten meters, by the flush gas, and the flush gas penetrates gradually through the bed from underneath. 
         [0006]    In order to guarantee a safe lifting of the compression layer, it has been suggested to work with flush-gas impulses. This results in a slightly more even removal of the compression layer, but the pressure wave thus created will cause also catalytic material which is not yet worn out to be catapulted off, such that the resulting losses are too high. 
         [0007]    In order to improve the cleaning of the filling, it has also been suggested to attach flush-gas entrances laterally, i.e. along the lower longer side of the bed, for instance. However, this is unfavourable in the process because such entrances are then easily polluted by the compression layer sliding downwards, and if the flush-gas impulse is kept very short, such that no flush gas is flowing any more when the compression layer slides down, parts of the compressed granules will inevitably enter the flush-gas apertures. In addition, a large number of flush-gas pipe connections at the outer side of the filter box makes it necessary to have a corresponding number of sealings, pipe diversions and branchings and is insofar unfavourable to put into practice. 
       OBJECTS AND SUMMARY OF THE INVENTION 
       [0008]    In contrast to this, the present invention has the task of creating a filtering device making possible a reliable cleaning operation without any additional costs arising, but with the longevity of the filtering device being improved in particular also in case of waste gasses containing sulfur and chlorine. 
         [0009]    In accordance with the invention, the flush-gas entrance is supposed to be provided at the same side as the clean-gas exit. The clean gas leaves the filter box at a temperature which is not notably below the entry temperature of the polluted gasses, for instance, thus, at 160° C. This temperature is clearly above the dew point of sulfur, such that a condensation into sulfuric acid is not possible even at what is referred to as “cold spots”. Surprisingly, the flush-gas is heated to such a degree as a result of its being supplied in the “counterflow principle”, that also the flush gas is at a correspondingly elevated temperature. 
         [0010]    In a preferred embodiment, clean gas is used as flush gas, which clean gas is branched off from parallel beds. This clean gas has the desired temperature of about 160° C. in the first place, and it is obvious that also a temperature of for example 130° C. would basically be sufficient. 
         [0011]    Compared with basically known filtering devices which are suitable for multiply polluted gasses and which require temperatures of about 320° to 340° C., this leads therefore to considerable energy savings because the basically known filtering devices require the waste gasses to be re-heated. 
         [0012]    In accordance with the present invention, it is particularly favourable to have, in addition to the flush-gas entrance and the clean-gas exit being provided at the same front side of the bed which is positioned inclined perceived in the cross direction, current-influencing devices provided in the free space beneath the bed. Such current-influencing devices serve to guarantee a secure removal of the compression layer over the entire and considerable length of the bed, so that the compression layer can slide off as a whole and no parts remain in place. 
         [0013]    Although the compression layer has a certain internal cohesion, it tends to be torn into pieces in filtering devices realized so far, surprisingly especially at the front side opposite the flush-gas entrance. In accordance with the present invention, the basically desired flush-gas impulse is actually slowed down now, and as a result the apparently punctually dynamically created lifting impulse is moderated. It is possible that up to now, a standing wave was created due to resonances, whose antinodes led to a partial removal of the compression layer, whereas in accordance with the present invention, the removal impulses are now surprisingly reduced or “feathered” with the help of the flush-current influencing devices. 
         [0014]    Surprisingly, the compression layer is still reliably removed, even though the peaks of the removal impulse are clearly reduced. 
         [0015]    Surprisingly, even a mere division of the flush-gas current into individual currents is suitable to achieve this, for which purpose the current-influencing devices are suited, which are exemplarily provided in the form of baffle plates. The flush-gas current is divided by such baffle plates and is supplied to the bed in individual currents from underneath. The baffle plates are then preferably provided beneath the respective beds, however not diagonally beneath, such that they are not hit either by the compression layer sliding down. 
         [0016]    For further explanations, reference is made to DE 10 2005 022 138 A1. The current-influencing devices prevent current peaks in the current of flush-gas washed through the bed, and it becomes obvious that surprisingly the compression layer is then completely lifted off more easily as a result, basically as a coherent layer, and can therefore slide off. Due to the prevention of peaks, a basically identical pressure is built up beneath the compression layer, which pressure cannot escape either through holes in the compression layer created by current peaks. 
         [0017]    In accordance with the present invention, a more reliable and improved cleaning of the filling is thus surprisingly achieved. 
         [0018]    In a preferred embodiment, it is in addition intended to use and clean the compression layer, which is drained off in a basically known fashion via a conveyor screw, in a partial circulation. For this purpose, this part can for instance be heated to an increased temperature of 300° C.; the dust collected can be blown out or washed out, and the polluted gas created by the further heating can be collected and exerted by means of re-condensation at a cold spot. 
         [0019]    This also permits an at least partial re-use of the granules, with fresh granules being preferably inserted into the circulation. 
         [0020]    In accordance with the present invention, it is particularly preferable that a large number of pollutants can be removed from waste gasses with the help of one compact filter box, for instance dioxins and furans, nitrogen oxides, sulfuric compounds, chloric compounds, and in particular also dust and if necessary even CO. 
         [0021]    In particular, the denox filters known so far did not permit to filter out dust at the same time, such that this means a considerable improvement insofar. In addition, the production costs of the filtering device in accordance with the present invention are reduced by 50% compared with classical denox or desox filtering devices. 
         [0022]    In accordance with the present invention, it is favourable in a preferred embodiment to have the circulating gradient reduced, and also to have multiple small vertical channels provided next to each other in the bed. The vertical longitudinal and cross ribs make it possible to arrange the currents in parallel, even though this is realized over only few centimetres in height. 
         [0023]    In a modified embodiment, it is intended to realize as the current-influencing device a nozzle slide driving in a longitudinal direction along beneath the bed. It is provided with a slot nozzle of the same width as the bed, i.e. 1 m for instance, which is penetrated by a rather strong flow. In this case, it is acceptable, in contrast to the present invention, that the compression layer gets torn. The current created is so strong, however, that no parts of the compression layer will remain in place despite this, and also in this case clean gas from parallel beds can be used as the flush gas. 
         [0024]    Further advantages, details and features of the present invention will become clearer from the following detailed description of several embodiments of the present invention in connection with the attached drawings, which show: 
     
    
     
       BRIEF DESCRIPTION OF THE FIGURES 
         [0025]      FIG. 1  a section through a first embodiment of a filtering device in accordance with the present invention; 
           [0026]      FIG. 2  a longitudinal section through the embodiment of  FIG. 1 ; 
           [0027]      FIG. 3  a schematic view of another embodiment of a filtering device in accordance with the present invention; 
           [0028]      FIG. 4  a section through the embodiment of  FIG. 3  from the viewpoint of arrow B in  FIG. 3 ; 
           [0029]      FIG. 5  the side view of an embodiment of the filtering device in accordance with the present invention, integrated in a container; 
           [0030]      FIG. 6  a view from the left to the embodiment of  FIG. 5 , with an indicated interior structure of the filtering device in accordance with the present invention; 
           [0031]      FIG. 7  a section through the embodiment of  FIG. 5  along the cutting line A-A of  FIG. 6 ; 
           [0032]      FIG. 8  a section through the embodiment of  FIG. 5  along the cutting line C-C of  FIG. 6 ; 
           [0033]      FIG. 9  a view from the right to the embodiment of  FIG. 5 ; 
           [0034]      FIG. 10  a top view of the embodiment of  FIG. 5 ; 
           [0035]      FIG. 11  a section through the embodiment of  FIG. 5  along the cutting line B-B of  FIG. 10 ; 
           [0036]      FIG. 12  the bottom view of the embodiment of  FIG. 5 ; 
           [0037]      FIG. 13  a perspective section through the embodiment of  FIG. 5  along the cutting line D-D of  FIG. 6 ; and 
           [0038]      FIG. 14  a perspective view of the container of  FIG. 5 . 
       
    
    
     DETAILED DESCRIPTION 
       [0039]    The embodiment of a filtering device  10  in accordance with the present invention depicted in  FIG. 1  has several inclined beds  12 ,  14 ,  16  and  18  which extend in a firtree-like fashion in the exemplary embodiment shown. A filling  20  made up of catalytic material is provided which is supplied in a uniform fashion in an insertion hopper  22  along the length of filter box  24 . For this purpose, the individual hopper  22  is provided with a dosing screw  26  extending in the longitudinal direction of filter box  24  and serving for the uniform supply of filling  20 . 
         [0040]    The catalytic material of filling  20  slides onto beds  12  and  18  in a basically known fashion, with the inclination of the beds corresponding to the filling angle of the catalytic material. At the lower longitudinal side  30  of each bed, a retaining wall  32  is provided, which needs not be formed in a vertical position, but which may for instance also extend horizontally, as can be taken from the above-mentioned disclosure to which reference is made. 
         [0041]    Beneath each bed, a free space is provided, such as for example free space  34  beneath bed  12 , which is in each case closed gas-tight at its bottom side as well as on all front sides. Free space  34  has a parallelepiped-shaped cross section and a width of about 1 m—corresponding to the width of the bed. Bed  12  has a grate made up of a grid, with the longitudinal and cross ribs having a height of about 3 cm each. This grate is covered by a large-surface sieve holding the filling. 
         [0042]    In normal operation, bed  12  is penetrated by gas diagonally from top to bottom, i.e. from above bed  12  into free space  34 . In this fashion, a clean gas is created which is output through clean-gas exit  36 . In the normal operation or filtering operation, the incoming dust will be collected on the upper surface of the filling in bed  12 , in such a fashion that a compression layer will form there. 
         [0043]    In the cleaning operation, the direction of the current through bed  12  is inversed, and flush gas enters free space  34  and will flow through bed  12  from bottom to top. 
         [0044]    From  FIG. 2 , the arrangement in accordance with the present invention becomes clear in detail. The clean gas flows out from free space  34  through clean-gas exit  36 . In the area of the same front side  38  of bed  12 , a flush-gas entrance  40  is provided, with a switching between flush gas and clean gas made possible with the help of a combined switching damper  42 . The current of flush gas is depicted in broken lines, whereas the current of clean gas is depicted by a black arrow. 
         [0045]    Adjacent to the flush-gas entrances and clean-gas exits, a collection and switching box  44  is provided. With the help of collection and switching box  44 , it is possible to selectively switch one of the beds into cleaning operation. For this purpose, the clean gas is collected from three beds and a portion of the clean gas is supplied to bed  12  as flush gas, with combined switching damper  42  being brought into the position depicted in broken lines, and the flush gas being supplied to free space  34  via flush-gas entrance  40 . 
         [0046]    Each free space has current-influencing devices  50  depicted for free space  46  by way of example. In the embodiment shown, air baffle plates  52  are provided over the length of bed  14 , i.e. spread over about 6 m, which plates divide the entering flush-gas current into individual currents and supply them to bed  14  angularly from underneath. This surprisingly results in the compression layer positioned on bed  14  being uniformly lifted and thus sliding off better. 
         [0047]    Obviously, any other current-influencing devices can be provided instead. For instance, a current resistance can be provided by means of ribs, orifices or the like, or a diversion of air may be realized. 
         [0048]    From  FIG. 3  it can be taken that a partial circulation can be formed for the granules as well as a partial circulation for the clean gas. Same numbers in the figure indicate here, as well as in other figures, same components. Instead of combined switching damper  42 , one switching damper  54  for clean gas and one switching damper  56  for flush gas are provided in this embodiment. Clean-gas exit  36  and flush-gas entrance  40  are combined as fare as their connection is concerned, and the branching is realized few centimetres behind the connection at front side  38  of filter box  58 . As can be seen, filtering device  10  in accordance with the present invention can basically be placed in a rectangular filter box  58  which may have, for example, a width of some more than 2 m, a height of 3 m and a length of 6 m in order to operate a rather small waste-incinerating plant, i.e. it can be placed in an otherwise common standard container. 
         [0049]    The separation of combined switching damper  42  into individual switching dampers  54  and  56  makes it possible as well to specifically switch on the cleaning operation of one of the beds. In the filtering operation, all four switching dampers  56  are closed, and all four switching dampers  54  are open. In the cleaning operation, the switching damper  56  of one bed is open, and correspondingly the switching damper  54  of this bed is closed. Via a compressor  60 , the pressure of clean gas  62  is increased, and on the exit side of the compressor, two pipes  64  and  66  branch off which are connected with flush-gas entrances  40  each. When switching damper  56  is open, the compressed clean gas will therefore flow through the respective flush-gas entrance  40  into free space  34  as flush gas. There it arrives at current-influencing devices  50  which in the exemplary embodiment shown are realized by means of current resistances  68 ,  70 ,  72  positioned in a spread arrangement. The rib-shaped current resistances  68  to  72  break the flush-gas impulse, such that no current peak will penetrate the bed. 
         [0050]    Furthermore, it becomes clear from  FIG. 3  that the compressed granules sliding off over retaining wall  32  are transported away via a conveyor screw  74 . They are collected in the area of front side  76  of filter box  58  and leave filter box  58  when a revolving valve  78  is opened. In a recovery or purification box  80 , the compressed granules are recovered or purified in a suitable fashion, for instance by means of washing, sieving and/or heating. The suitable portions of granules leave recovery or purification box  80  via a return pipe  82 . Fresh granules or catalytic material are/is supplied via a feed pipe  84  and are/is supplied to insertion hopper  22  the circulation together with the returned granules. 
         [0051]    Moreover, in recovery or purification box  80 , the worn-out granules are separated and are output via a pipe  86 . By means of vaporization of the respective salts, dust and gas containing sulfur, chlorine and/or fluorine are created and separated and are condensed separately, if necessary. 
         [0052]    From  FIG. 4  it becomes clear that both the conveyor screws  84  and the revolving valves  78  are provided on both sides of filter box  58 ; it also becomes clear that the filtering device  10  in accordance with the present invention can be put up in a compact fashion with the help of supports  90  and  92 . 
         [0053]      FIG. 5  shows a side view of a standard container  100 , which takes the function of filter box  24  of  FIG. 1  here, with opened doors  102  at its front side. At the opposite front side of container  100 , the drive motor  104  of dosing screw  26 , one of the two drive motors  106  of conveyor screw  74  as well as one of the two raw-gas entrances  108  and clean-gas exits  110  as well as flush-gas entrances  112  are visible. 
         [0054]    In  FIG. 6 , beds  12 ,  14 ,  16 ,  18  as well as insertion hopper  22  and conveyor screws  74  are indicated besides the two raw-gas entrances  108 . 
         [0055]    From  FIG. 7  it can clearly be taken how dosing screw  26  extends over the entire length of the beds of which beds  12  and  14  are perceivable. Dosing screw  26  is driven with the help of motor  104  which is positioned outside container  100 , in order to uniformly supply the catalyst poured into insertion hopper  22 , whose one wall is depicted behind dosing screw  26 , over the entire length of the beds. At the same front side of container  100 , moreover, beneath dosing-screw motor  104 , clean-gas exits  100  are perceivable which lead into common collection and switching box  44  at which the cleaned gas of all four filter beds can be led out collectively. 
         [0056]    In  FIG. 8 , beneath the container ceiling, current-influencing devices  114  serving to even out the current of raw gas supplied can be seen. Also well visible in  FIG. 8  is one of the two conveyor screws  74  (shown cut-through here) which also extend over the entire length of beds  12 ,  14 ,  16 ,  18 . With the help of conveyor screws  74  and their drive motors  106 , the worn-out catalytic material is transported away and is supplied to a possible recovery or purification. Through apertures  116  in the bottom surface of the container, the worn-out catalytic material is transported out of the inside of the container. 
         [0057]    From  FIG. 9 , collection box  44  is clearly visible. A pipe for further transport of the clean gas can for example be flange-connected to circular aperture  118 . In circular aperture  118 , two of the total of four clean-gas exits  110  are perceivable which expand to the width of the free spaces  34  positioned beneath the filter beds. The inclined pipes  112  which are positioned above the individual clean-gas exits, respectively, serve the purpose of supplying the flush gas to the individual filter beds. At the two lower corners of the container, the drive motors  106  of conveyor screws  74  are well visible. In the top centre portion, the drive motor  104  of dosing screw  26  is furthermore clearly perceivable. 
         [0058]      FIG. 10  shows a top view onto container  100  on the top surface of which the two raw-gas entrances  108  as well as two flange openings  120  (closed with plates here) for filling in the catalyst are perceivable. On the right side, clean-gas exits  110  whose diameters are reduced towards common switching and collection box  44  as well as the four flush-gas entrances  112  can be perceived clearly. 
         [0059]      FIG. 11  shows container  100 , cut through along line B-B in  FIG. 10 . The two conveyor screws  74  on the left and right sides at the bottom of container  100  as well as dosing screw  26  in the centre of insertion hopper  22  can be perceived clearly. By means of to-and-fro movements of dosing screw  26 , the catalytic material can be moved to both the front and back ends of insertion hopper  22  in a preferred embodiment of the present invention, in order to guarantee a good and equal spreading of the amount of catalytic material over the entire length of insertion hopper  22 . Immediately beneath the container ceiling, at the right and left sides next to the insertion hopper, the thin blades of current-influencing devices  114  for evening out the raw-gas supply current are furthermore visible. 
         [0060]    From  FIG. 12 , exit apertures  116  for the worn-out catalytic material in the bottom surface of container  100  can be seen well once more. Here, in another preferred embodiment of the present invention, devices for recovery or purification of the catalytic material may be connected in order to re-supply this to the filter in accordance with the present invention for further use. 
         [0061]    From  FIG. 13 , besides dosing screw  26  positioned inside insertion hopper  22 , the current-influencing devices  50  arranged beneath the grates of filter beds  12 ,  14  (depicted here), which devices are shaped as thin blades in the embodiment depicted and which are numbered only for bed  14  for reasons of clarity, can be perceived. Through these current-influencing devices  50 , on the one hand, the flush-gas impulse is evened out over the entire length of the filter beds, and on the other hand, the slope of the flow of flush gas arising is “flattened”, which in accordance with the present invention surprisingly leads to a large area of the compression layer of the catalytic material on the filter beds to be cleaned being lifted off. 
         [0062]    In another modified embodiment (not depicted), the raw gas entering the container from the top can first penetrate the upper filter bed, then, instead of immediately being lead out of the inside of the container via the clean-gas exit, be supplied to the lower filter bed for further cleaning of the now already pre-cleaned gas, and in this fashion two filter beds can be cascaded and the cleaning effect can be increased significantly. Obviously, for this purpose one side wall of the otherwise gas-tight free space beneath the upper filter bed must have apertures through which the pre-cleaned gas can flow to the second filter bed via the separation devices mentioned. 
         [0063]      FIG. 14  shows once more a perspective view of the embodiment of the filter in accordance with the present invention in standard container  100 . Back conveyor screw  74 , which transports to the outside worn-out catalytic material taken off filter beds  16  and  18  via exit aperture  116  in the bottom of the container, is clearly visible. 
         [0064]    While a preferred form of this invention has been described above and shown in the accompanying drawings, it should be understood that applicant does not intend to be limited to the particular details described above and illustrated in the accompanying drawings, but intends to be limited only to the scope of the invention as defined by the following claims. In this regard, the terms as used in the claims are intended to include not only the designs illustrated in the drawings of this application and the equivalent designs discussed in the text, but are also intended to cover other equivalents now known to those skilled in the art, or those equivalents which may become known to those skilled in the art in the future.