Patent Application
20140047806
This patent application claims the benefit of European Patent Application No. 12 180 896.8, filed Aug. 17, 2013, which is incorporated by reference.
The present invention relates to a filter module, especially for gas filtration purposes, and filter system comprising the inventive filter modules.
For gas filtration, especially hot gas filtration processes filter modules have been suggested in the prior art in various configurations.
The U.S. Pat. No. 5,482,537 A suggests to filter high temperature gases, e.g., from a fluidized bed reactor in an assembly comprising an outer upright vessel and an inner upright vessel, the inner vessel incorporating a gas impervious peripheral wall which divides the gas volume in the outer vessel into clean and raw gas volumes. A number of monolithic ceramic filter modules are mounted in openings disposed in the peripheral walls of the inner vessel and allow clean gas to flow through the filter modules from the dirty gas volume to the clean gas volume. The clean gas is discharged from the clean gas volume via a clean gas outlet. The filter modules are of a honeycomb structure, the filter elements and clean gas ducts of which are oriented in a horizontal direction.
The U.S. Pat. No. 5,593,471 A discloses a dust collecting apparatus comprising a housing having an inlet and an outlet and one or more filter modules accommodated therein. The filter modules are of a honeycomb structure and arranged in vertical or horizontal direction. The clean gas ducts of the filter modules open into a closed chamber within the housing. The closed chamber comprises a clean gas outlet which is in fluid connection with the outlet of the housing. The apparatus further includes backwash device to deliver high pressure gas to the closed chamber in a backwash operation in order to clean the filter elements of the filter modules.
According to another approach filter modules in the form of tubular filter candles are used in hot gas filtration as disclosed for example in WO 00/62902 A1. A filter vessel comprises a tube sheet which divides the interior of the vessel into a raw gas and a clean gas chamber. The tube sheet comprises openings which accommodate the filter candles at one end thereof. The filter candles depend from the tube sheet into the raw gas chamber. The filter vessel further includes a backwash system for detaching the particulate matter accumulated during filtration from the filter candles.
In hot gas filtration large volumes of gases are to be dealt with requiring a substantial amount of filter area.
Typical prior art hot gas filtration systems use filter candles made of ceramic or metal material. Filter areas of these candles are limited so that for higher volume flows thousands or ten thousands of filter candles are necessary to be incorporated in housings.
This requires very big filter vessels or several vessels operated in parallel. For volume flow rates of about 1 million m3 per hour or more, use of ceramic or metallic filter candles of 2 or even 3 m length is no longer adequate.
An object of the present invention is to provide a filter module and a filter system comprising same which has an improved ratio of filter area per volume of the filter system and a high packing density in the filter system.
The present invention solves this object with a filter module having the characteristics of claim 1.
The key element of the present invention resides in the honeycomb structure of filter elements and regularly interposed clean gas ducts provided with a clean gas collecting and discharge arrangement extending across all of the clean gas outlets of the clean gas ducts. At the closed ends of the filter elements, i.e., the discharge side of the filter module, clean gas flow is deflected and directed transverse to the vertical of the discharge side surface of the unit(s). The deflection and direction of the clean gas flow from all the clean gas ducts is substantially uniform. Said clean gas outlets of the clean gas ducts are in fluid communication with the clean gas collecting and discharge arrangement. This allows a very efficient and compact structure of the filter modules.
Preferably, the clean gas opening is provided at a lateral face of the filter module.
The tubular wall parts of the filter elements and optionally the closed ends of the filter elements and/or the clean gas ducts of the inventive filter modules are preferably made of ceramic, metal and/or polymeric material. The porous structure may be created by sintering grains and/or fibers of such material.
The filter module may comprise a multi-block structure of two or more block-shaped units arranged in parallel and connected to one another at their side faces, e.g., by gluing, welding or sintering the individual block-shaped units together or by accommodating the individual block-shaped units in a common frame structure. The block-shaped units within the frame structure are sealed against one another in order to avoid by-passes leading from the feed side of the module to the clean gas collecting and discharge arrangement.
It is especially preferred to use a frame structure to accommodate the individual block-shaped units in a multi-block embodiment in case the block-shaped units are made of ceramic material.
Preferably, the frame structure is made of metal.
The embodiments comprising a frame structure to accommodate a multiplicity of block-shaped units preferably have the clean gas collecting and discharge arrangement provided as a part of the frame structure.
The clean gas collecting and discharge arrangement typically extends substantially across the whole discharge side of the one or more block-shaped units of a filter module. Preferably, the discharge end of the clean gas collecting and discharge arrangement is about flush with a side wall of the filter module.
Furthermore, the block-shaped units may be arranged back to back, i.e., their discharge sides facing each other, and sharing one common clean gas collecting and discharge arrangement.
The transverse direction in which the clean gas collecting and discharge arrangement deflects and directs the clean gas flow preferably may be oriented in an angle to the vertical of the discharge side surface of about 30° or more, more preferably about 60° or more, especially about 90°.
This angle of deflection is defined in a preferred embodiment by the orientation of a wall or walls of the channel(s) of the clean gas collecting and discharge arrangement extending across the discharge side of the block-shaped unit(s) of the filter module.
The preferable axial length of the tubular wall parts of the filter elements ranges from about 10 to about 300 mm, more preferably from about 30 to about 150 mm. The preferable axial length of the tubular wall parts allows an efficient discharge of particulate matter from the filter elements during back-pulsing even when the longitudinal axis of the filter elements is in a horizontal orientation.
Preferably, such wall or walls of the channels of the clean gas collecting and discharge arrangement are arranged at a distance (clearance) to the discharge side surface of the block-shaped units from about 0.1 to about 0.7 times, more preferably from about 0.3 to about 0.5 times the lengths of the tubular wall parts of the filter elements.
In case the discharge side surfaces of the block-shaped units are provided with a safety fuse element the distance (clearance) is determined as from the downstream surface of the safety fuse element instead of the discharge side surface.
In case of a back-to-back arrangement of the multiplicity of block-shaped units the discharge side surfaces of the respective other block-shaped unit(s) form such wall or walls and delimit the clean gas collecting and discharge arrangement in one direction. Typically, the distance (clearance) of the respective discharge side surfaces of two block-shaped units in a back-to-back arrangement is preferably in the range of about 0.2 to about 1.4 times the lengths of the tubular wall parts of the filter elements since the clean gas collecting and discharge arrangement receives larger volumes of clean gas. More preferably the distance (clearance) is in the range of from about 0.6 to about 1 times the length of the tubular wall parts of the filter elements.
Preferably, the block-shaped units in a back-to-back arrangement are provided with their discharge side surfaces in a parallel orientation. The angle of deflection of the clean gas exiting the clean gas ducts is then about 90°.
However, the block-shaped units in a back-to-back arrangement may have their discharge side surfaces arranged diverting from the parallel orientation. However, the deflecting angle for the clean gas exiting the clean gas ducts is preferably about 30° or more, more preferably about 60° or more.
The grain size typically used will have an average size of about 1 to about 450 μm. Fibers used typically have an average diameter of from about 1 to about 400 μm and an average length of from about 1 to about 50 mm.
The number of filter elements per 10 cm2 cross-section of the feed side of a block-shaped unit preferably ranges from about 1 to about 100, more preferably from 2 to about 10. Typically, the same number of clean gas ducts is provided per 10 cm2 cross-sectional area.
Preferably, the clean gas ducts are defined by longitudinal sections of tubular wall parts of three or more of the filter elements, i.e., the wall parts of the filter elements form the walls of the clean gas ducts. No additional structure is necessary to build the clean gas ducts.
More preferably the tubular wall parts of adjacent filter elements are in direct contact with one another delimiting the clean gas ducts between their closed and open ends.
The cross-section of the tubular wall parts of the filter elements may be of polygonal, especially rectangular, more preferably square, circular or oval shape.
The tubular wall parts have cross-sectional areas corresponding to the area of a square with an edge length of about 3 to about 20 mm, preferable of about 5 to about 10 mm. Corresponding cross-sectional areas are also preferable for filter elements designed with another rectangular, oval or circular cross-sections.
The length of the tubular wall parts of the filter elements amount to about 300 mm or less, preferably about 30 to about 200 mm, more preferably about 50 to 150 mm.
Preferably, the tubular wall parts and optionally the closed ends of the filter elements and/or the clean gas ducts have a pore size of about 0.1 to about 150 μm, more preferably of about 1 to about 100 μm, most preferably of about 2 to about 10 μm.
The average porosity of the tubular wall parts and optionally of the closed ends of the filter elements and/or the clean gas ducts is in the range of about 25 to about 90% by volume.
According to another embodiment of the inventive filter modules the tubular wall parts of the filter elements are arranged with respect to the vertical of the feed side surface, preferably at an angle from about 10° to about 60°, more preferably from about 30° to about 60°. During operation of an inventive filter module the feed side surface is typically in a vertical orientation.
The advantage of the inventive filter modules over the prior art resides especially in their ability to provide high surface areas per cubic meter consumed when such filter elements are accommodated in a housing.
Preferred filter modules according to the present invention provide a surface area of about 40 m2 or more per m3 of a housing volume section, preferably about 60 m2 or more per m3. When calculating this ratio, only such volume section of the housing is taken into account which is occupied by the filter modules when arranged fully operative and ready to use within the housing.
The invention further relates to filter systems comprising one or more of the inventive filter modules.
The inventive filter system typically comprises a housing accommodating one or more filter modules and preferably comprises common feed and/or discharge channels for the raw gas and the clean gas, respectively.
Preferably, the clean gas collecting and discharge arrangements of the filter modules directly discharge the clean gas into the common clean gas discharge channel of the system via their discharge ends.
The filter module 10 comprises one block-shaped unit 12 comprising a plurality of filter elements 14 having a longitudinal, porous tubular wall part 16 with an open end 18 and a closed second end 20. The tubular wall parts 16 have a square cross-section and are arranged in a checkerboard pattern together with a plurality of clean gas ducts 22 which are substantially coextensive with, oriented parallel to and regularly interposed between the filter elements 16. The clean gas ducts 22 are open at one end 24 and closed at the other end 26 thereof. The open ends 18 of the filter elements and the closed ends 26 of the clean gas ducts form a first checkerboard pattern on the upstream or feed side surface 28 of the filter module 10. A checkerboard pattern of closed ends 20 of the filter elements 14 and the open ends 24 of the clean gas ducts is provided on the opposite or downstream face 30 of the block-shaped unit 12. This face 30 is the discharge side surface of the block-shaped unit 12. The tubular wall parts 16 of the filter elements 14 are of a porous material, e.g., sintered ceramic material, sintered metallic material or a sintered polymer material with a certain average pore size. The wall parts 16 at the same time delimit the clean gas ducts 22 along their longitudinal direction.
Raw gas entering the feed side 28 of the filter module 10 flows into the open ends of the filter elements 14, penetrates their porous tubular wall parts 16, and clean gas is received in the clean gas ducts 22 from where it is discharged at the discharge side surface 30 of the block-shaped unit 12.
On the discharge side surface of the block-shaped unit 12, a clean gas collecting and discharge arrangement 32 is provided in the form of a channel with a closed back wall and three closed lateral faces. The channel is open at the face 34 shown in the front of
The clean gas received by the channel of the clean gas collecting and discharge arrangement 32 is deflected by about 90° and directed transverse to the vertical of the discharge side of the filter module 10 (in other words, substantially parallel to the discharge side of the filter module 10).
The clean gas exits the filter module 10 through that opening 36. The distance of the closed back wall of the channel 32 to the discharge side surface of the unit 12 (clearance h) preferably amounts to about 0.3 to about 0.5 times the axial length of the tubular wall parts 16 of the filter elements 14.
To facilitate mounting of the filter module 10 in a housing of a filter system, the filter module 10 comprises on its front side face an outwardly projecting flange 38.
According to the present invention, preferably the length of the tubular wall parts of the filter elements 14 is limited to about 300 mm or less, which surprisingly allows very easy cleaning of the filter module and its filter elements from particulate matter collected during filtering operation on the tubular wall parts 16.
The lateral surfaces of the filter module 10 are preferably covered by a metal frame structure 40 which may incorporate the clean gas collecting and discharge arrangement 32. On one of the lateral surfaces (the front surface in
The distance of the closed back wall of the channel 32 to the downstream surface of the safety fuse 44 of the unit 12 (clearance h) preferably amounts to about 0.3 to about 0.5 times the axial length of the tubular wall parts 16 of the filter elements 14.
The clean gas is received by the clean gas collecting and discharge arrangement 32 when it exits the downstream side of the safety fuse 44. The clean gas flow is then deflected by about 90° and directed parallel to the discharge side of the filter module 42.
The filter module 50 comprises one block-shaped unit 52 comprising a plurality of filter elements 54 having a longitudinal, porous tubular wall part 56 with an open end 58 and a closed second end 60. The tubular wall parts 56 have a square cross-section and are arranged in a checkerboard pattern together with a plurality of clean gas ducts 62 which are substantially coextensive with, oriented parallel to and regularly interposed between the filter elements 54. The clean gas ducts 62 are open at one end 64 and closed at the other end 66 thereof. The open ends 58 of the filter elements and the closed ends 66 of the clean gas ducts 62 form a first checkerboard pattern on the upstream or feed side surface 68 of the filter module 50. A checkerboard pattern of closed ends 60 of the filter elements 54 and the open ends 64 of the clean gas ducts 62 is provided on the downstream side or opposite face 70 of the block-shaped unit 52. This face 70 is the discharge side surface of the block-shaped unit 52. The tubular wall parts 56 of the filter elements 54 are of a porous material, e.g., sintered ceramic material, sintered metallic material or a sintered polymer material with a certain average pore size. The wall parts 56 at the same time delimit the clean gas ducts 22 along their longitudinal direction.
Raw gas entering the feed side 68 of the filter module 50 flows into the open ends 58 of the filter elements 54, penetrates their tubular wall parts 56, and clean gas is received in the clean gas ducts 62 from where it is discharged at the discharge side surface 70 of the block-shaped unit 52.
On the discharge side surface 70 of the block-shaped unit 52, a clean gas collecting and discharge arrangement 72 is provided in the form of a single channel which is closed at three lateral faces and open at the front face 74 shown in
The distance of the closed back wall of the channel 72 to the discharge side surface of the unit 52 (clearance h) preferably amounts to about 0.3 to about 0.5 times the axial length of the tubular wall parts 56 of the filter elements 54.
The clean gas exits the filter module 50 through an opening 76 of said front face 74. To facilitate mounting of the filter module 50 in a housing of a filter system (not shown here), the filter module 50 comprises on its front side face 74 an outwardly projecting flange 78.
According to the present invention, preferably the length of the filter elements 14 is limited to about 300 mm or less, which surprisingly allows very easy cleaning of the filter module and its filter elements from particulate matter collected during filtering operation on the tubular wall parts 56.
In contrast to the filter module 10 of
In operation, the interior space of the filter elements 54 may be more easily cleaned from particulate matter which has accumulated during the filtration process because of the slanted configuration of the tubular wall parts 56 of the filter elements 54. The angle of the longitudinal axis of the tubular wall parts to the vertical of the feed surface amounts to about 25°.
Because of the slanted configuration of the filter elements 54 within the block-shaped unit 52, a somewhat lower filtration surface per volume ratio is obtained. This, however, is compensated by the improved regeneration properties of the filter module 50 which in the end allow a longer cycle time of this type of module 50 as compared to the filter module 10.
The block-shaped units 102, 104 both comprise a plurality of filter elements 110, 112 having longitudinal, porous tubular wall parts 114, 116 with open ends 118, 120 and closed second ends 122, 124. The tubular wall parts 114, 116 have a square cross-section and are arranged in a checkerboard pattern together with a plurality of clean gas ducts 126, 128 which are substantially coextensive with, oriented parallel to and regularly interposed between the filter elements 110, 112. The clean gas ducts 126, 128 are open at one end 130, 132 and closed at the other end 134, 136 thereof. The open ends 118, 120 of the filter elements 110, 112 and the closed ends 134, 136 of the clean gas ducts 126, 128 form a first checkerboard pattern on the upstream or feed side surface 140 of the block-shaped units 102, 104. A checkerboard pattern of closed ends 122, 124 of the filter elements 110, 112 and the open ends 130, 132 of the clean gas ducts 126, 128 is provided on the opposite face 142, 144 of the block-shaped units 102, 104. These faces 142, 144 are the discharge side surfaces of the block-shaped units 106, 108. The tubular wall parts 114, 116 of the filter elements 110, 112 are of a porous material, e.g., sintered ceramic material, sintered metallic material or a sintered polymer material with a certain pore size. The wall parts 114, 116 at the same time delimit the clean gas ducts 126, 128 along their longitudinal direction.
Raw gas entering the feed sides 140 of the filter modules 100 flows into the open ends 118, 120 of the filter elements 110, 112, penetrates their tubular wall parts 114, 116 and clean gas is received in the clean gas ducts 126, 128 from where it is discharged at the discharge side surfaces 142, 144 of the block-shaped units 102, 104.
At the discharge side surfaces 142, 144 of the block-shaped units 102, 104 a common clean gas collecting and discharge arrangement 150 is provided which is delimited by the discharge side surfaces 142, 144 and three closed lateral surfaces. The arrangement 150 is open at the front face 152 shown in
The clean gas received by the clean gas collecting and discharge arrangement 150 is deflected by 90°, directed parallel to the discharge side surfaces of the of units 102, 104 and exits the filter module 100 through an opening 154.
To facilitate mounting of the filter modules 100 in a housing of a filter system, the filter modules 100 comprises on their front faces 156 an outwardly projecting flange 158.
According to the present invention, preferably the length of the tubular wall parts of the filter elements 110, 112 is limited to about 300 mm or less, which surprisingly allows very easy cleaning of the filter module and its filter elements from particulate matter collected during filtering operation on the tubular wall parts 114, 116.
After back-pulsing, the filter modules 100 may be again operated in the filtration mode of a filtering system without having been removed from the filtering system.
However, in contrast to the filter module 10 of
Optionally, the discharge side surfaces of the back-to-back oriented block-shaped units may be provided with a safety fuse element as described in connection with
Therefore, one common clean gas collecting and discharge arrangement 150 is sufficient to collect and discharge the clean gas provided by both block-shaped units 102, 104 in the direction to the front side faces 156 of the filter modules 100 where it exits the opening 152 to be discharged from a filtration system comprising these block-shaped modules 100. The distance between the discharge side surfaces (clearance) is typically lager than the clearance of the clean gas collecting and discharge arrangements described in connection with
As mentioned before, typically, the filter modules of the present invention are used in a multiplicity accommodated in a common housing. This situation is shown schematically in
The filter modules 10 and 50 of
A precautionary measure has to be taken in an arrangement of filter modules 100 as shown in
Upon back-pulsing, in the arrangement of the filter modules 100, a cross-contamination of the two filter modules could occur, and therefore, it is preferable to have a partition plate 160 arranged in between the two feed faces of the filter modules 100.
Within the box-shaped housing 202, two rows of a plurality of filter module stacks 204, 204′, 204″, . . . and 206, 206′, 206″, . . . are arranged with the discharge openings of the filter modules of the two rows facing in opposite directions. Along the longitudinal axis of the box-shaped housing 202 the stacks are arranged in parallel at a certain distance from each other (cf.
Within an individual stack 204, 206 of filter modules 204a, b, c, d and 206a, b, c, d, respectively, the filter modules may be mutually fixed to one another by gluing, welding or sintering them together or by mounting them in a framing.
In an exemplary layout of the filter system 200 the feed side of a filter module 204a, 206a may have length 1500 mm and a height of 1000 mm, the depth of the filter module may be about 200 mm. Such filter module may comprise, for example, 24 block-shaped units the feed side surface of which may have the size of 250 mm×250 mm, the length of the tubular wall parts of the filter elements being about 140 mm. The clearance h of the clean gas collecting and discharge channel would amount to about 60 mm.
The distance between two adjacent stacks 204 and 204′ or 206 and 206′ of filter modules may be set, for example, to about 100 mm.
The housing comprises on its top surface a raw gas supply channel 208 which feeds raw gas into the housing 202 and its stacked filter modules 204, 206. The raw gas supply channel 208 has a decreasing cross-sectional area from the front end shown in front of
On both side faces in longitudinal direction, the housing 202 comprises clean gas discharge channels 210, 212 which open at the rear end 214 of the system 200 where the clean gas may be discharged.
In order to accommodate the increasing amount of clean gas received from the multiple filter module stacks 204, 206 along the longitudinal axis of the housing 202, the cross-section of the clean gas discharge channels 210, 212 increases gradually in the direction of the rear end 214 of the system 200.
The clean gas discharge channels 210, 212 can in accordance with one variant be removable as a whole when the filter module stacks 204, 206 have to be exchanged. Alternatively, as shown in
The system 200 incorporates a back-pulsing facility receiving back-pulsing gas by a pipe 260 which is shown schematically only.
Extending from the back-pulsing gas pipe 260 a plurality of back pulse supply tubes 264 direct the blow-back gas to the various filter module stacks 204, 204′, 204″, . . . .
The back-pulsing pressure supplied via the clean gas openings into the stacked individual filter modules 204a, 204b, 204c, 204d and 206a, 206b, 206c, 206d detaches particulate matter which has been collected during the filtration operation from the filter elements of these filter modules.
The particulate matter discharged during back-pulsing is collected in conically shaped dust collectors 262 arranged at the bottom of housing 202.
In
The housing 302 is divided into a raw gas chamber 310 and a clean gas chamber 312 by a tube sheet 314 which spans across the whole cross-section of the cylindrical wall portion 304 at its upper end.
The raw gas chamber 310 is accessible via a feed gas inlet 316 through which raw gas can be introduced into the raw gas chamber 310.
The dome-shaped portion 306 of the housing 302 comprises a clean gas outlet 318 through which clean gas may be discharged.
The tube sheet 314 comprises a plurality of rectangular openings 320 which accommodate a plurality of candle-shaped filter modules 330 according to the present invention.
The candle-shaped filter modules 330 are shown in more detail in
The individual filter modules 330 comprise five block-shaped units 334, 335, 336, 337 and 338 stacked on top of one another, all facing with their feed side to the left as shown in
On the discharge side surface opposite to the feed side surface, the block-shaped units 334 to 338 are covered by a common clean gas collecting and discharge arrangement which essentially consists of one clean gas channel 340 which is open at its upper end 342 in order to discharge the clean gas into the clean gas chamber 312 of housing 302. Similar to what has been shown in
The candle-type filter modules 330 are arranged in the tube sheet 314 in a parallel, staggered arrangement where the feed sides of the individual filter modules face the clean gas channels of neighboring filter modules 330.
Therefore, upon back-pulsing, when particulate matter is detached from the filter elements of the block-shaped units of the filter modules, no cross-contamination between neighboring filter modules 330 can occur.
For regenerating the individual filter modules 330, the filter system 300 includes a back-pulsing system 350 comprising a pressure source 352 as well as a plurality of supply lines 354 which end within the dome-shaped cover 306 above the individual filter modules 330.
The particulate matter which is detached from the filter elements of the filter modules 330 is collected by gravity within the dust collecting cone-shaped housing portion 308.
A similar inventive system of a third embodiment is shown in
In
The housing 402 is divided into a raw gas chamber 410 and a clean gas chamber 412 by a tube sheet 414 which spans across the whole cross-section of the cylindrical wall portion 404 at its upper end.
The raw gas chamber 410 is accessible via a feed gas inlet 416 through which raw gas can be introduced into the raw gas chamber 410.
The dome-shaped portion 406 of the housing 402 comprises a clean gas outlet 418 through which clean gas may be discharged.
The tube sheet 414 comprises a plurality of rectangular openings 420 which accommodate a plurality of candle-shaped filter modules 430 according to the present invention.
The candle-type filter modules 430 are shown in more detail in
The individual filter modules 430 comprise five pairs of back-to-back positioned block-shaped units 434, 435, 436, 437 and 438 stacked on top of one another. The paired units 434 to 438 have about the same configuration as shown in
A clean gas collecting and discharge arrangement 440 substantially consisting of one clean gas channel 442 common for all paired block-shaped units 434 to 438 is positioned in between the back-to-back positioned units with an opening 444 at the upper end of the module 430 for discharge of the clean gas into the clean gas chamber 412 of the housing 402.
Optionally the block-shaped units of the filter module 430 may be provided with safety fuses on the discharge side surfaces (nor shown) as has been explained in connection with
The candle-type filter modules 430 are arranged in the tube sheet 414 in a parallel, staggered arrangement as is apparent from
The block-shaped units 434 to 438 are assembled in a common frame structure 448 holding the units sealingly together and providing a common clean gas channel 440. The top surface of the frame structure 448 may integrally incorporate the flange 432 and provide the opening 444.
For back-pulsing the individual filter modules 430, the filter system 400 includes a back-pulsing system 450 comprising a pressure source 452 as well as a plurality of supply lines 454 which end within the dome-shaped cover 406 above the individual filter modules 430.
The particulate matter which is detached from the filter elements of the filter modules 430 is collected by gravity within the dust collecting cone-shaped housing portion 408.
Upon back-pulsing, when particulate matter is detached from the filter elements 430, no cross-contamination between neighboring filter modules 430 can occur since their feed faces are shielded by the partition plates 446.
The advantages of the present invention shall be explained in some more detail by way of exemplary designs which are compared with prior art systems comprising tubular candle filter modules.
In a first prior art system a filter surface area of 3325 m2 is provided by 7200 filter candles of a standard geometry of an outer diameter of 60 mm and a length of 2500 mm. In order to accommodate this large number of tubular filter candles a filter vessel with a foot print of 63.7 m2 (corresponding to, e.g., a rectangular area of 3.5 m×18.2 m) is needed. The filtration surface area to foot print ratio calculates as 52.
An inventive system of the type of
The filter module stacks have a height of 4000 mm comprising 4 filter modules as described in connection with
The number of modules needed to provide the filter surface area of at least about 3325 m2 is 128 which requires a foot print for such a system of 17.5 m2 (corresponding to, e.g., 3.5 m×5 m). The ratio of filtration surface area to foot print corresponds to 190.
In a further example of a prior art system using 51 tubular candle type filter modules of a standard geometry of an outer diameter of 60 mm and a length of 2500 mm a filter surface area of 23.5 m2 is provided. A housing accommodating these 51 tubular candle type filter modules with an operatively needed distance in between adjacent filter modules of 30 mm a volume of 0.9 m3 is needed (the calculation does not take into account the volume occupied by the dust collector). This corresponds to a ratio of filter surface area to volume of about 26.
In case the volume of a housing of 0.9 m3 operatively accommodates filter modules as shown in
All references, including publications, patent applications, and patents, cited herein are hereby incorporated by reference to the same extent as if each reference were individually and specifically indicated to be incorporated by reference and were set forth in its entirety herein.
The use of the terms “a” and “an” and “the” and “at least one” and similar referents in the context of describing the invention (especially in the context of the following claims) are to be construed to cover both the singular and the plural, unless otherwise indicated herein or clearly contradicted by context. The use of the term “at least one” followed by a list of one or more items (for example, “at least one of A and B”) is to be construed to mean one item selected from the listed items (A or B) or any combination of two or more of the listed items (A and B), unless otherwise indicated herein or clearly contradicted by context. The terms “comprising,” “having,” “including,” and “containing” are to be construed as open-ended terms (i.e., meaning “including, but not limited to,”) unless otherwise noted. Recitation of ranges of values herein are merely intended to serve as a shorthand method of referring individually to each separate value falling within the range, unless otherwise indicated herein, and each separate value is incorporated into the specification as if it were individually recited herein. All methods described herein can be performed in any suitable order unless otherwise indicated herein or otherwise clearly contradicted by context. The use of any and all examples, or exemplary language (e.g., “such as”) provided herein, is intended merely to better illuminate the invention and does not pose a limitation on the scope of the invention unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the invention.
Preferred embodiments of this invention are described herein, including the best mode known to the inventors for carrying out the invention. Variations of those preferred embodiments may become apparent to those of ordinary skill in the art upon reading the foregoing description. The inventors expect skilled artisans to employ such variations as appropriate, and the inventors intend for the invention to be practiced otherwise than as specifically described herein. Accordingly, this invention includes all modifications and equivalents of the subject matter recited in the claims appended hereto as permitted by applicable law. Moreover, any combination of the above-described elements in all possible variations thereof is encompassed by the invention unless otherwise indicated herein or otherwise clearly contradicted by context.
| Number | Date | Country | Kind |
|---|---|---|---|
| 12 180 896.8 | Aug 2012 | EP | regional |
