METHOD OF TREATING DUST-CONTAINING GAS AND APPARATUS THEREOF

Abstract: A method of treating dust-containing gas comprises feed­ ing a dust-containing gas to one of spaces which are sepa­ rated by a vertically arranged filtration wall made of a solid porous material from the upper side of said one space to collect dust at the lower side of said one space while said dust-containing gas is caused to pass through said filtration wall to the other space to be a clean gas.

Description: The present invention relates to a method of treating a high temperature dust-containing gas with a filtration wall made of a solid porous material and an apparatus for treating such gas. There has so far been known an apparatus for removing dust in a dust-containing gas with use of filtration tubes made of a solid porous material as shown in Figure 1. In Figure 1, a plurality of filtration tubes 1 made of a solid porous material having gas-permeability are vertically arranged in parallel each others, with their lower ends closed and their upper end opened. The filtration tubes 1 whose outer and upper ends are supported by a supporting plate 70 in an gas-tight manner, are received in a middle case 2b which is provided with a dust-containing gas inlet 3 in its side wall. A lower case 2c functions as a hopper for dust separation and is provided at its bottom part with a dust discharging port 5 and a discharging valve 5a through which dust separated is intermittently taken out. A clean gas outlet 4 is formed at the top of an upper case 2a. In the operation of the conventional apparatus, a dust-containing gas fed through the dust-containing gas inlet 3 is introduced into a space outside the filtration tubes and only a clean gas is caused to pass through the tube wall of the filtration tubes 1 from the outside of the tubes to the inside thereof due to pressure difference between the interior and the exterior of the filtration tubes and thereafter, the clean gas is discharged through the clean gas outlet 4 out of the system. On the other hand, dust blocked to pass through the filtration tubes gradually accumulates on the outer wall of the filtration tubes with the lapse of time. The dust having accumulated on the outer walls occasionally falls on the bottom of the lower case 2c to be collected, while the accumulated dust forms a filtration layer which performs a precise filtration for a dust-containing gas. When the thickness of dust layer formed by accumulation of dust increases, pressure difference between the exterior and the interior of the filtration tube becomes large. Accordingly, the dust layer on the filtration tubes should be removed by reverse cleaning at predetermined time intervals to reduce permeation resistance. Such dust removing apparatus is disclosed, for example, in "Wasser Luft und Betrieb" 16 (1972) Nr2 Page 61-62, titled "Verfahren zur Trockenreinigung von heißen Gasen"; "Chemical Engineering" October 1981, Page 34-49, titled "Ceramic filter and application thereof"; Japanese Unexamined Patent Publication No. 3620/1983 and Japanese Unexamined Patent Publication No. 3621/1983. Filtration of a dust-containing gas with use of a gas-permeable porous material is performed by using a surface filtration structure in which a dust layer accumulated on the surface of the porous material is used as a filtration layer. Accordingly, when a porous cylindrical body is used, it is advantageous from the viewpoint of pressure loss to use an outer wall having a large surface area as a filtration surface, but not an inner wall having a small surface area. In this case, even when dust enters into the outer surface of the filtration tube to certain extent to cause abnormally large pressure loss in the filtration tube 1, it is easy to reuse it by scraping the outer wall of the filtration tube by a brush or a whetstone. Similarly, in a case using the outer wall of the filtration tube 1 as a filtration surface, even when dust enters inside the filtration tube to fill pores, the dust can be easily removed by means of reverse cleaning, i.e. reversely flowing of a clean gas from the side of inner wall because distribution of pores is substantially uniform in the radial direction of the filtration tube and a sectional area through which a gas is passed becomes large along the flow of the gas, in other words, the number of branch of open pores communicated from the inner wall side to the outer wall side increases toward the outer surface side of the filtration tube 1. Although the conventional dust removing apparatus has advantage as above-mentioned, it has not been practised of a large size and in an industrial scale. The reason of this is considered as follows. Use of a filtration tube made of a material such as ceramics is desirable under an elevated temperature condition. However, the length of a single filtration tube is limited to at most about 2 meters or so because the ceramic filtration tube before sintering, generally has an extremely small strength and particularly, the filtration tube of a considerable length is apt to be deformed in the course of handling and sintering. There has been proposed a technique to bond with an adhesive filtration tubes in the longitudinal direction. It, however, causes difficulty in its bond strength. Further, there is another system as shown in Figure 2 in which a plurality of filtration tubes are stacked in the longitudinal direction, a flange 31 is applied at the lowermost end to support a series of the filtration tubes, the flange is suspended with a metallic long bolt 33 which is inserted from the top of the series of filtration tubes to pass through the inside thereof and a spring 32 is provided on the uppermost filtration tube to compensate the thermal expansion of the long bolt 33. The system has, however, many disadvantages that an excessive elongation of the long bolt 33 takes place in the time of passing a high temperature gas; a creep and corrosion may be caused in the long bolt 33; the apparatus is unstable in structure against earthquakes and vibrations, and if an arm (not shown in the drawing) is secured to the middle case 2b to support the flange 31 for a stable structure against the earthquakes and vibrations dust tends to accumulate on such supporting means as the arm and remains on it. These problems has prevented use of a long filtration tube and accordingly, the amount of gas to be treated per unit area for installation is extremely small and the conventional apparatus has not been suitable for industrial use for treatment of a large amount of gas. Further, when a gas having a high dust concentration should be treated, since dust deposits on the outer surface of the filtration tube 1 except for relatively coarse particle dust which freely falls, increase of pressure difference between the inner and outer walls of the filtration tube is so rapid that it is necessary to carry out frequently reverse cleaning to thereby increase the cost of electric power for a blower for reverse cleaning and that an additional gas-treating apparatus should be installed taking into account of reduction in throughput at the time of the reverse cleaning and accordingly, initial investment is large. It is an object of the present invention to provide a method of treating a dust-containing gas with use of a filtration wall made of a gas-permeable solid porous material in which the amount of gas to be treated per unit area for installation can be large and even when a gas having a high dust concentration is treated, the frequency of reverse cleaning can be small or the reverse cleaning can be needless and an apparatus for carrying out such method. This object is achieved by the apparatus of claim 1. A more complete appreciation of the invention and many of the attendant advantages thereof will be readily obtained as the same becomes better understood by reference to the following detailed description when considered in connection with the accompanying drawings, wherein: Figures 1 and 2 are respectively vertical cross-sectional views of conventional dust removing apparatuses; Figures 3 and 4 are respectively a vertical cross-sectional view and a plane view of an embodiment of the gas treating apparatus of the present invention; Figures 5, 6 and 7 are respectively enlarged views of Q part, R part and S part in Figure 3; and Figurs 8 and 9 are respectively vertical views of separate embodiments of the gas treating apparatus of the present invention. In the following, the present invention will be explained in detail. A dust-containing gas used in the present invention refers to a gas containing dust. A clean gas refers to a gas substantially containing no dust. It may, however, contain a slight amount of dust. Namely, the dust-containing gas is a relative concept with respect to the clean gas and a gas having a concentration of dust lower than the dust-containing gas is referred to as a clean gas. Normally, dust means useless material; it is, however, not limited to the definition and it may be useful material. Accordingly, the gas treating method or apparatus of the present invention may be used for various purposes of obtaining a clean gas from a dust-containing gas, of obtaining dust from a dust-containing gas such as, for example, recovery of useful powdery products produced by a gas phase reaction or of obtaining dust and a clean gas together. In the present invention there is prepared a filtration wall made of a gas-permeable solid porous material arranged in the vertical direction, preferably, a filtration tube made of such a solid porous material, particularly a filtration tube formed by connecting a plurality of unit filtration tubes in a coaxial manner. A dust-containing gas is fed from the upper side of one of spaces separated by the filtration wall or from the upper side of the filtration tube at a relatively high velocity to collect coarse particles in the dust by utilizing the inertial movement while the main stream of dust-containing gas is caused to pass through the filtration wall or the filtration tube to obtain a clean gas from the other space; thus, a precise filtration is carried out. The coarse particle dust falling at a high velocity usually scrapes the dust accumulated on the filtration wall whereby it is unnecessary to carry out the reverse cleaning of the filtration wall or the frequency of the reverse cleaning is reduced even though it is necessary, or a portion to be subjected to the reverse cleaning are limited. In this case, the amount of the gas to be treated per unit area for installation increases as the flow rate of the dust-containing gas fed to one of the spaces separated by the filtration wall increases to thereby increase the effect of scraping the dust accumulated on the filtration wall due to the coarse particle dust. However, when the flow rate of the dust-containing gas is excessively high, not only the dust layer accumulated but also the filtration wall itself is scraped depending on a particle size distribution in the dust-containing gas and the amount and the shape of hard particles contained in the dust. It is therefore preferable that the velocity of the gas stream at the upper part of the filtration wall, especially the downward component of the velocity is 100 m/s or less, more preferably 50 m/s or less taking into account of pressure loss. When the downward component of the velocity at the upper part of the filtration wall is about 2 m/s or so, the scraping effect obtained by the coarse particle dust becomes small. Accordingly, the gas velocity is preferably 5 m/s or more. Since the downward component of the velocity of the dust-containing gas in one of the spaces separated by the filtration wall becomes small with the lower part of the filtration wall, the downward velocity of the dust becomes small due to viscosity of the gas. Therefore, while fine particles collide each other to become coarse particles as the dust goes downward in the space, the effect of inertial dust collection decreases and the effect of scraping of the accumulated dust by the coarse particle dust also becomes small due to reduction in the downward velocity of the dust. In an embodiment of the present invention, a part of dust-containing gas is taken out from the lower part of one of the spaces together with the dust so that a relatively large downward movement of the coarse particle dust is obtained even at the lower part of the filtration wall whereby the effect of scraping the accumulated dust is attained in the almost entire region of the filtration wall as well as the inertial dust collection effect. In this case, a technique of delivering for circulation of a part of the dust-containing gas taken out from the lower part of the space to the upper portion of the space is included in a desirable embodiment of the present invention. Thus, it is possible to isolate only a clean gas and dust out of the system from the dust-containing gas fed into the system. A technique of delivering for circulation of a part of the dust-containing gas taken out from the lower part of the space to a dust producing source is also contained in a desirable embodiment of the present invention. As a result, when, for example, a dust-containing gas source is a fluid catalytic cracking apparatus, a gas including cracking catalyst which is a useful and reusable dust can be effectively recovered for its reuse in addition that heat energy contained in the gas can be also effectively utilized. A filtration wall and a filtration tube or a unit filtration tube, which will be described in detail, should have an adequate gas-permeability and a high temperature resistance. Although they can be formed of a sintered body of powder metallurgy consisting of a material such as carbon steel, stainless steel, a sintered body of ceramics is preferably utilized because of its having excellent high temperature resistance and anticorrosion properties. Particularly, it is most preferable to use ceramics such as mullite, cordierite, fused silica, lithium aluminum silicate, aluminum titanate, silicon carbide, silicon nitride, carbon and so forth. Although the average diameter of pores of the solid porous material is suitably selected depending on the average particle diameter and the particle size distribution of the dust in the dust-containing gas and the dust concentration in a clean gas to be obtained, it is preferable that the average diameter of pore of the solid porous material is 0.2-6 times as large as the average particle diameter of the dust, especially 0.5-3 times as large as the average particle diameter to perform high dust collecting efficiency and high gas-treating rate. In the present invention, a plurality of filtration tubes having open upper and lower ends may be arranged in parallel to each other to define a plurality of spaces The inner part of the filtration tubes is used as the space through which the dust-containing gas flows. Thus, with use of the filtration tubes there is obtainable a gas treating apparatus constructed in such a manner that the mechanical strength of the filtration wall is improved and the clean gas and dust are easily separated by feeding the dust-containing gas in the inner part of the filtration tubes. The filtration tubes are preferably of a circular shape in cross section taking account of easiness of manufacture and strength although they may have a square shape in cross section. It may be such that the dust-containing gas is fed in the filtration tubes so as to cause swirling movement in the peripheral direction of the filtration tubes with the consequence that the coarse particle dust in the dust-containing gas is subject to a strong centrifugal force and it descends with swirling movement along the inner wall of the filtration tubes while fine particle dust in the dust-containing gas is subject to a high viscosity and disturbance in the gas stream and it descends with swirling movement along the central portion of the filtration tubes at a high velocity. Thus, coarse particle dust in the dust-containing gas is separated by centrifugal force and is caused forcibly to swirl in the vicinity of the inner wall of the filtration tubes at a high velocity along with the swirling movement of the gas whereby the dust accumulated on the inner wall of the filtration tubes is forcibly scraped by the coarse particle dust. The filtration tubes are connected in the longitudinal direction and the connecting part between the adjacent unit tubes is supported by a third filtration tube supporter which is held by the middle case. Further, between the third filtration tube supporter and a connecting part of the unit filtration tubes, is provided a sealing means for dust. The construction as above-mentioned allows a gas treating apparatus provided with a long filtration tube formed of a plurality of the unit filtration tubes instead of a single integral long filtration tube which is difficult to manufacture and it makes unnecessary to bond with an adhesive the joining parts of the unit filtration tubes. At least one among the first, the second and the third filtration tube supporters may have at its inside a coolant passage. The filtration tube supporters used for the treating apparatus of the present invention are normally made of metal which has been considered to be inadequate from the viewpoint of a high temperature resistance when they are used to treat a high temperature dust-containing gas. It is, however, possible to maintain the filtration tube supporters at a predetermined temperature or below and to improve durability of the sealing means for dust by passing a coolant in the coolant passage. The coolant passage is preferably formed in all the first and the second and the third filtration tube supporters, however, the coolant passage may be formed in any one of the supporters. Further, when a plurality of third filtration tube supporters are used, the coolant passage may be formed in a part of the filtration tube supporters. A preferred embodiment will be described with reference to drawing. In Figure 3, there are provided a plurality of filtration tubes 1 made of a solid porous material with the upper and lower open ends (the thickness of the filtration tube is omitted in the drawing). Each of the filtration tubes is formed of a plurality of unit filtration tubes 1a (five unit filtration tubes are used in the embodiment) made of a solid porous material which is coaxially connected in the vertical direction. A generally tower-shaped container 2 is constituted by an upper case 2a, a middle case 2b and a lower case 2c each being made of steel plate and having an inner lining of a heat insulation material. The upper case 2a is provided with at its top end a dust-containing gas inlet 3, the middle case 2b has a clean gas outlet 4 in its side wall and the lower case 2c, which functions as a dust hopper, is provided with at its bottom part a dust discharging valve 5a and a dust discharging port 5. Each of an upper tube sheet 7a as a first filtration tube supporter, a middle tube sheet 7b as a third filtration tube supporter and a lower tube sheet 7c as a second filtration tube supporter is provided with a plurality of through holes for putting therein a plurality of the filtration tubes 1 respectively and these sheets are supported by the middle case 2b in an gas-tight manner. The upper tube sheet 7a is located at the outside and upper part of the filtration tube 1; the lower tube sheet 7c is located at the outside and lower part of the filtration tube 1 and the middle tube sheet 7b is located at the outside of the connecting part of the unit filtration tubes 1a, these tube sheets 7a, 7b, 7c supporting the filtration tube 1 and the unit filtration tubes 1a as parts of the tube through sealing means for dust, respectively. Each of the tube sheets 7a, 7b, 7c is made of steel plate and has its upper and lower surfaces with an outer lining of a heat insulation material 6a. A coolant passage 8 is formed in each of the tube sheets 7a, 7b, 7c. Thus, a clean gas room 10 is formed by the tube sheets and the middle case 2b. As clearly shown in Figure 4, each of the tube sheets 7a, 7b, 7c is provided with a coolant inlet 8a at an outer peripheral surface of the middle case 2b and a coolant outlet 8b at a position diametrically opposing to the inlet 8a. Figure 5 shows the upper portion of the filtration tube 1 supported by the upper tube sheet 7a through packing members 9 as a sealing means for dust. Figure 6 shows that the middle tube sheet 7b supports the connecting part of the adjacent unit filtration tubes 1a, 1a through packing members 9a and Figure 7 shows the lower end of the filtration tube 1 supported by the lower tube sheet 7c through a socket 7f with its bottom opened, packing members 9 filling a space formed between the outer surface of the filtration tube and the inner surface of the socket 7f. The packing member 9 can be ceramic fiber rope, asbestos rope, carbon fiber rope, metal fiber rope made of a material such as stainless steel, a composite of these materials or a molded product thereof which should have flexibility at a high temperature and prevent the dust in the dust-containing gas from passing through. It is also effective to use combination of ceramic powder and any of these ropes for the purpose of sealing of the dust. The packing member 9a which supports elastically the connecting part of the adjacent unit filtration tubes 1a, 1a should have flexibility at a high temperature, but may not have sealing property to prevent the dust from passing if the connecting part of the unit filtration tubes 1a, 1a is closely in contact without any gap. However, from the industrial viewpoint, packing member 9a is preferably the same material as that of the packing member 9 being a sealing means for dust because there is a small gap and one-side contact in the connecting part. The size of the unit filtration tube 1a constituting the filtration tube 1 is determined taking account of its strength, relationship between the natural frequency and an exciting frequency caused by an acoustic resonance, earthquakes and so on, the magnitude of an exciting force, easiness in handling at the time of assembling or repairing of the filtration tube and cost for the tube sheets 7a, 7b, 7c although the unit filtration tube having a smaller length can be used. For example, when ß-cordierite type ceramics excellent in heat shock resistance is used for the unit filtration tube, the length of the tube is preferably in a range from 0.8 to 2 m. The operation of the apparatus according to the present invention will be described. In Figure 3, the dust-containing gas G introduced into the upper case 2a from the dust-containing gas inlet 3 and scattered by the upper tube sheet 7a is fed into each of the filtration tubes 1 downwardly at the velocity of 5-50 m/s at the upper part of the filtration tubes 1. Since the filtration tube 1 of the present invention is made of ceramics having high hardness, being chemically stable and excellent in high temperature resistance unlike a bag filter in which a filter bag is made of woven cloth or felt, there is no risk of causing erosion even though the dust-containing gas is introduced in the filtration tube 1 at such a high velocity. On the other hand, in the bag filter, the velocity of the dust-containing gas introduced into the filter bag is generally limited to 2 m/s or less from the viewpoint of prevention of the filter bag from breaking due to erosion. While the dust-containing gas is caused to fall in the filtration tubes 1, the clean gas G' passes through the wall of the filtation tubes 1 to be discharged from the clean an gas outlet 4. The velocity of the dust-containing gas in the downward direction decreases in a nearly linear manner as the gas goes from the upper part to the lower part of the filtration tubes 1 and becomes almost zero at the lower end of the filtration tubes 1. Since the dust-containing gas is introduced in the filtration tubes 1 at a high velocity, the coarse particle dust containing in the dust-containing gas has a large momentum and it continues to move downwardly even though the velocity of the gas in the downward direction decreases. During downward movement of the gas, coarse particles gradually coagulate due to mutual collision together with deposition of fine particles and the coagulated particles fall in the bottom of the lower case 2c to be discharged. On the other hand, fine particle dust is carried by a gas stream due to viscosity of the gas flowing in the radial direction and fills the pores in the inner wall of the filtation tubes 1 to form a bridge of the fine particles. The dust-containing gas is precisely filtered by the bridge of the dust. Due to scraping effect caused by collision of the coarse particle dust falling at a high velocity, formation of the fine particle dust layer projecting from the inner wall surface of the filtration tubes 1 is prevented. Thus, it is unnecessary to carry out reverse cleaning with use of the clean gas under a certain condition. The frequency of reverse cleaning can be reduced even if it is necessary and sometimes it is sufficient to carry out the reverse cleaning with the lower part of the filtration chamber 10. When the dust-containing gas having a high concentration of dust, momentum of the dust at the inlet of the filtration tubes 1 is large to increase the provability of coagulation caused by mutual collision of the fine particles to thereby render the fine particles to be coarse with the consequence of being useful in inertial dust collection and the scraping effect of the accumulated dust by the coarse particle dust. Thus, use of a plurality of the elongated filtration tubes 1 and introduction of the dust-containing gas into the filtration tubes at a high velocity realize a continuous treatment of the dust-containing gas in an industrial scale. Further, the structure of the filtration tubes 1 are highly reliable. Vibrations in the filtration tubes 1 are damped because the upper and lower ends of the filtration tubes 1 and the connecting parts of the unit filtration tubes 1a, 1a are respectively elastically supported through the packing members 9, 9a. In a case of treating dust-containing gas of a high temperature such as 1000°C, cooling water is passed from the coolant inlet 8a through the coolant passage 8 to the coolant outlet 8b to prevent damage of the tube sheets 7a, 7b, 7c. The heat insulation materials 6, 6a provided on the tube sheets 7a, 7b, 7c and the cases 2a, 2b, 2c allows emission of the clean gas from the filtration chamber 10 through the filtration tubes 1 without heat loss whereby heat energy can be effectively recovered from the clean gas. In the embodiment, water is used as a coolant; however, it is possible to use another liquid or gas such as air or fluorinated hydrocarbon. When a dust-containing gas having a relatively low temperature such as, for example, 600°C or less, it may be treated without cooling. When it is unnecessary to cool the tube sheets 7a, 7b, 7c, the coolant passage 8 and the heat insulation material 6a can be omitted and the container 2 should have an outer lining of the heat insulation material 6 instead of an inner lining. In this case, the material for the tube sheets 7a, 7b, 7c and the container 2 may be stainless steel, low alloy steel, mild steel and so on depending on the temperature and the nature of the dust-containing gas. Further, the clean gas inlet for reverse cleaning may be provided in each of the filtration chamber 10. The dust-containing gas may be caused to flow in any direction in the filtration tube 1 as far as the gas flows downwardly in this embodiment. In the next place, the present invention will be described with reference to Figures 8 and 9 in which the same reference numerals as in Figure 3 designate the same part and the description of these parts is omitted. An embodiment shown in Figure 8 is contrived so as to continuously scrape dust accumulated on the inner wall of the filtration tubes 1, namely the dust-containing gas is imparted a certain velocity in the downward direction even at the lower part of the filtration tubes to keep the momentum of the coarse particle dust which falls whereby effect of scraping the accumulated dust by the coarse particle dust is obtained at the lower part of the filtration tubes 1. Namely, a suction tube 11 is placed in the lower case 2c to take out a part of the dust-containing gas from the lower part of the filtration tubes 1 and preferably the opening of the suction tube 11 is directed downwardly at the near center inside the lower case 2c. The suction pipe 11 is connected to a blower 12 (An ejector or an injector may be used.) and further, is connected to the dust-containing gas inlet 3 through a piping 13. With the provision of the suction pipe 11, the dust accumulated on the bottom of the lower case 2c is taken out from the dust discharging port 5 by intermittently opening the dust discharging valve 5a to the outside of the system and a part of the dust-containing gas is taken out continuously from the suction pipe 11 to be delivered for circulation to the upper case 2a through the blower 12. Another embodiment shown in a simplified manner in Figure 9 is constructed in such a manner that a part of the dust-containing gas is continuously sucked through the dust discharging port 5 together with the dust falling on the bottom of the lower case 2c from the lower part of the filtration tubes 1 and these are delivered for circulation to a dust producing source 14 through the blower 12 which may be replaced by an ejector or an injector. The dust producing source 14 is placed at the upstream of the gas treating apparatus connected through a piping so that the dust delivered from the lower case does not directly affect the concentration of dust in the dust-containing gas introduced into the dust-containing inlet 3, the dust producing source being a regenerator or a reactor in the fluid catalytic cracking apparatus, a fluidized calcinator, a fluidized bed boiler, a converter, a blast furnace and so on. In the embodiments shown in Figures 8 and 9, it is unnecessary to carry out the reverse cleaning depending on the flow rate of gas sucked from the lower case 2c, the kind of dust and particle diameter distribution. It is desirable that the flow rate of the gas sucked from the lower case 2c is 5-25% of the flow rate of the dust-containing gas fed into the dust-containing gas treating apparatus (the flow rate of the dust containing gas is the same as that of the clean gas produced) in view of saving power and dust collecting efficiency. The velocity of the gas stream in the downward direction at the lower part of the filtration tubes 1 is preferably in the range from 0.3 to 4 m/s. With increase of the velocity from 0.3 m/s, there also increases falling of the amount of the dust accumulated. When the velocity is about 4 m/s, the gas treating apparatus can be safely and continuously operated without reverse cleaning with a constant pressure difference between the interior and exterior of the filtration tubes 1, the pressure difference being such as 1500 mmAq or so although the operating condition is determined by presence of coarse particles in the dust, the hardness of the particles, the shape of the particles and other conditions. In accordance with the present invention, the following advantages can be provided: the amount of gas to be treated for unit area for installation is remarkably large; a high temperature dust-containing gas having a high dust concentration can be precisely filtered; reverse cleaning is not required as many times as required in the conventional apparatus or is required only in a limited part. Further, the reverse cleaning may not be required at all depending on the kind of dust, particle size distribution and so on. The present invention is applicable to the treatment of a high temperature dust-containing gas to obtain a high temperature clean gas without a substantial amount of heat loss and therefore heat energy can be recovered in the subsequent step.

Claims: An apparatus for treating dust-containing high-temperature gas to separate the dust from the gas, said apparatus comprising: (a) a generally tower-shaped, vertically oriented container (2) comprising an upper case (2a), a middle case (2b), and a lower case (2c) which functions as a dust hopper; (b) an inlet (3) for dust-containing gas connected to said upper case (2a); (c) a discharging port (5) for dust located at the bottom of said lower case (2c); (d) a generally horizontal upper tube supporter (7a) disposed in said container (2) in a gas tight manner between said upper case (2a) and said middle case (2b); (e) a generally horizontal lower tube supporter (7c) disposed in said container (2) in a gas tight manner between said middle case (2b) and said lower case (2c); (f) at least one generally horizontal middle tube supporter (7b) disposed in said middle case (2b) in a gas tight manner between said upper and lower tube supporter (7a,7c); (g) a plurality of vertically disposed, horizontally spaced filtration tubes (1) made of a solid porous material disposed in said middle case (2b) and extending from said upper tube supporter (7a) to said lower tube supporter (7c) through said at least one generally horizontal middle tube supporter (7b), each of said plurality of filtration tubes (1) having an open upper end received in a gas tight manner in said upper tube supporter (7a) and an open lower end received in a gas tight manner in said lower tube supporter (7c), each of said plurality of filtration tubes (1) being formed of a plurality of unit filtration tubes (1a) which are coaxially connected at said middle tube supporter (7b); and (h) at least one clean gas outlet (4) in the side wall of said middle case (2b). An apparatus as recited in claim 1, wherein said container (2) and said tube supporters (7a,7b,7c) are made of steel, and further comprising a passage for coolant (8) disposed at least in one of said tube supporters (7a,7b,7c) with an inlet (8a) and an outlet (8b) for the coolant. An apparatus as recited in claim 2, wherein said container (2) has an inner lining of heat insulation material (6) and the upper and lower surfaces of said tube supporters (7a,7b, 7c) have linings of heat insulation material (6a). An apparatus as recited in any one of claims 1 to 3, wherein the connecting parts between adjacent unit filtrations tubes (1a) are supported by said middle tube supporter (7b) through packing members (9a). An apparatus as recited in any one of claims 1 to 4, wherein between said filtration tubes (1) and said upper and lower tube supporters (7a,7c) are provided packing members (9) made of a material which is flexible at high temperatures, as a sealing means for dust. An apparatus as recited in any one of claims 1 to 5, wherein said filtration tubes (1) are made of ceramics. An apparatus as recited in any one of claims 1 to 6, further comprising means for creating a lower pressure in said lower case (2c) than in said upper case (2a), said means for creating a lower pressure comprising a passage way (13) through which dust containing gas is taken out from said lower case (2c) and fed to the upstream of said upper case (2a). An apparatus as recited in claim 7, wherein said dust containing gas in said lower case (2c) is taken out and fed to a dust producing source (14) in the upstream of said upper case (2a). An apparatus as recited in any one of claims 1 to 8, wherein said at least one middle tube supporter (7b) comprises a plurality of generally horizontal middle tube supporters (7b) disposed in said middle case (2b) between said upper and lower tube supporters (7a,7c) and said middle case (2b) has a plurality of clean gas outlets (4) in its side wall (2b).

Inventors: MORISHITA, TOMOHIRO, NORIYUKI, ODA, WATANABE, HARUO
Applicants: ASAHI GLASS COMPANY LTD.
Application year: 1984
Main classification: B01D46
IPC codes: B01D46