Method and apparatus for liquid coating for honeycomb structure

Abstract: A liquid coating method for coating a liquid to inner cells of a honeycomb structure includes the steps of supplying a liquid to an inside of a honeycomb structure vertically arranged from its lower part to cause the liquid to adhere to the inner cells therein, and supplying pressurized air to an upper part of the honeycomb structure to discharge the liquid within the inner walls. A holding apparatus for holding an article includes an outer cylinder in a form of a pipe having an inner wall with an inner diameter which allows an article to be held to pass therethrough easily and has a suffi­ cient strength, a resilient tube having an inner diameter which prevents the article to be held from passing there­ though under non tension and having ends each sealingly connected to the outer cylinder, thus defining together with the inner wall of the outer cylider sealed space therebetween, means for discharging a fluid from the sealed space; and means for supplying the fluid to the sealed space.

Description: The present invention relates to a liquid coating method and apparatus for coating a liquid in inner cells in a honeycomb structure. More particularly, the present invention relates to a coating method and a coating apparatus for causing a fluid such as slurry to adhere to inner cells of honeycomb structures for use, for example, in treating exhaust gas of cars. For the treatment of exhaust gas from cars and the like, there has been known a method in which catalysts are carried in honeycomb structures made of metal or ceramics. Various types of honeycomb structures have been proposed. For example, one of the known honeycomb structures has a large number of inner cells inside thereof which extend longitudinally along the length of the honeycomb structure and have open ends on the both sides thereof. Another type of the known honeycomb structure has also a large number of longitudinally arranged cells inside thereof which have an open end on one side and a closed end on the other side thereof and are arranged alternately so that every other adjacent cell has an open end (or a closed end) on one side and a closed end (or an open end) on the other side of the honeycomb structure and communicate with each other through holes in the walls of the cells. In order to have catalyst components carried on the walls of the cells of the honeycomb structure of the above-described type in a suitable manner, it is necessary to coat various liquids including among others a slurry which contains catalyst components on the walls of the cells. Examples of the liquids to be applied to the walls of the cells are as follows. (a) Chemicals to be used in pretreatment of post-treatment in the production of catalysts, for example, acids, aqueous alkali solutions, and organic substances. These are aqueous solutions which contain no catalyst component. (b) Aqueous solutions containing catalyst components such as aqueous solutions of palladium compounds, aqueous solutions of platinum compounds, and aqueous solutions of rhodium compounds. (c) Slurries containing catalyst components and mainly composed of catalyst components such as platinum, palladium and rhodium, refractory metal oxides such as aluminum oxide and cerium oxide. The slurries may contain one or more of various metal compounds, acid, organic substances, and the like. Generally, the slurries have a high viscosity (e.g., on the order of from 100 to 500 cps), a specific gravity of from 1.0 to 2.0 g/ml, and a component particle size of no greater than 10 µm. (d) Slurries mainly composed of refractory metal oxides such as aluminum oxide and cerium oxide. The slurries may contain one or more of various metal compounds, acids, organic substances and the like. They contain no catalyst component represented by precious metals. Their physical characteristics are the same as the slurries described in (c) above. As a coating method for applying the above-described various liquids to the walls of numerous cells in the honeycomb structure having the construction described above, a method has been used in which a honeycomb structure in a vertical position is dipped in a desired liquid contained in a storage tank, the honeycomb structure is then taken out from the liquid bath and left to stand as is for a while to extract or separate the liquid from the honeycomb structure by free fall of the liquid, and the liquid still remaining in the cells is removed forcibly by air-knife which blasts high-pressure air. However, the conventional method have the following problems. Firstly, it takes a considerably long time for the liquid to adhere all over the walls of the inner cells in the honeycomb structure, which makes it difficult to carry out the treatment efficiently. The cells have a considerably small sectional area and the pressure posed on the liquid while it rises within the cell is generated by the difference between the level of the liquid surface in the storage tank and that of the liquid surface in the cell. Hence, this pressure is not so high. In addition, usually the liquid to be coated has a high viscosity. Therefore, in the above-described method, the speed at which the liquid rises within the cells is not high enough. Secondly, the amount of the liquid which adheres to the wall of the cells is not equal from cell to cell. Upon the separation of the liquid, the liquid is left to fall free followed by the removal of the liquid is carried out by using air-knife. As a result, it is often the case that a large amount of the liquid remains in some cells while only a small amount of the liquid remains in other cells, thus failing to cause the liquid to adhere to the honeycomb structure uniformly. It is desirable and important to uniformly distribute catalyst components and the like on the walls of the inner cells in the honeycomb structure because in the case of the treatment of exhaust gas, for example, the reaction occurs when the exhaust gas contacts the catalyst component on the honeycomb structure. Thirdly, unnecessary liquid adheres to the side surface of the honeycomb structure. The right portion where liquid is to adhere is the walls of the inner cells in the honeycomb structure through which the exhaust gas passes but it is unnecessary to allow the liquid to adhere on the side surface of the honeycomb structure. The liquid adhering on the side surface is of no use. As described hereinbelow, in the liquid coating method and apparatus for the honeycomb structure of the present invention, a honeycomb structure, which is an article to be held, having a shape of a circular column, an elliptic column, a circular cylinder, an elliptic cylinder, or the like, must be held and the outer periphery of the article to be held must be covered partly or entirely. For this purpose, a holder can be used which is composed of two halves having each shape of a longitudinally split circular cylinder provided with a recess or groove that defines an inner cavity having a contour corresponding to that of the article to be held when the halves are put together in close contact with each other. However, if the size and shape of the article to be held, i.e., honeycomb structure, fluctuate, a problem arises that when the article to be held is relatively large, the holder is closed incompletely to fail to establish complete seal and on the other hand, when the article to be held is relatively small, it does not contact the holder closely, resulting in that the force of holding given by the holder is not strong enough. A method and an apparatus might be considered useful in which articles to be held are held by using a rubber tube having an inner diameter sufficiently larger than the outer diameters of the articles to be held and forcibly introducing air into the tube to reduce its inner diameter to hold the articles in close contact therewith. However, in the above-described apparatus, a problem arises that when air is introduced into the rubber tube, wrinkles tend to occur in the rubber from part to part, resulting in that the sealing of those parts with wrinkles is incomplete. For example, when it is contemplated to coat a liquid on an inside surface of an article to be held having a shape of a circular cylinder and provided only inside thereof with one or more tubes extending in an axial direction, as honeycomb structure, the article to be held is held by a holder, a liquid tank is coupled with the lower end of the article, and a liquid is supplied from the liquid tank and forced to rise into the inside of the article to coat the liquid only on the inside thereof. In this case, the use of the conventional holder with a rubber tube results in the occurrence of wrinkles in the rubber as earlier explained, and the liquid forced upward flows upward between the article and the rubber tube via channels formed by the wrinkles and thus the liquid adheres also to the outside of the article, thus failing to achieve the purpose. The conventional technique suffers from a problem that when the size and shape of the article to be held fluctuate more or less, it is difficult to hold the article certainly and in addition seal between the article and the holder is insufficient. In order to solve the above-described problems, the present invention provides a liquid coating method for coating a liquid in inner cells in a honeycomb structure, characterized by comprising the steps of: supplying a liquid to an inside of a honeycomb structure vertically arranged from its lower part to cause the liquid to adhere to the inner cells; and supplying pressurized air onto an upper part of the honeycomb structure to discharge the liquid within the inner cells. According to the method of the present invention, a liquid to be coated is introduced into the inside of a honeycomb structure arranged vertically from its lower part so that the liquid to be coated can adhere to the inner cells of the honeycomb structure. Then, pressurized air is supplied to the upper part of the honeycomb structure to discharge to liquid which remains within the inner cells. Thus, the liquid is introduced forcibly from below and discharged or expelled by pressurized air. This makes it possible to cause the liquid to adhere speedily and uniformly without causing the liquid to adhere to the side surface of the honeycomb structure. According to a preferred embodiment of the present invention, the above-described method comprises the steps of: providing a liquid storage tank for storing a liquid to be coated, the liquid storage tank having an upper opening at its upper part and an air discharge outlet, and an air duct having a lower opening at its lower part; connecting the upper opening of the liquid storage tank to a bottom of the honeycomb structure vertically arranged; further connecting the lower opening of the air duct to a top of the honeycomb structure, and supplying the liquid to be coated from the liquid storage tank into the inner cells in the honeycomb structure to cause the liquid to adhere to the inner cells. Further, according to another preferred embodiment of the present invention, the method comprises the steps of supplying pressurized air from the air duct to the upper part of the honeycomb structure and discharging the pressurized air from the air discharge outlet of the liquid storage tank to discharge the liquid in the cell. As described above, according to the preferred embodiments of the present invention, a liquid storage tank having an upper opening and an air discharge outlet, and an air duct having a lower opening are provided. A honeycomb structure vertically arranged is connected at its bottom to the upper opening of the storage tank, and at its top to the lower opening of the air duct. The liquid to be coated is supplied from the liquid storage tank into the inner cells of the honeycomb structure. By doing so, the liquid to be coated is caused to adhere to the inner cells. Then, pressurized air is supplied to the upper part of the honeycomb structure from the air duct and the pressurized air is discharged from the air discharge outlet of the liquid storage tank so that the liquid within the cells can be discharged. As result, the liquid can be caused to adhere to the inner cells speedily and uniformly, thus enabling coating treatment without causing the liquid to adhere to the side surface of the honeycomb structure. Furthermore, in order to solve the above-described problems, the present invention provides a liquid coating apparatus for coating a liquid in inner cells in a honeycomb structure, characterized by comprising: a liquid storage tank for storing a liquid to be coated, the storage tank having an upper opening and an air discharge outlet; an air duct for supplying air stream, the air duct having a lower opening to supply pressurized air onto the upper part of the honeycomb structure and discharge the liquid within the inner cells; a first sealing element for sealingly connecting a bottom of the honeycomb structure to the upper opening of the liquid storage tank; a second sealing element for sealingly connecting a top of the honeycomb structure to the lower opening of the air duct; and an apparatus for raising the liquid within the liquid storage tank through the upper opening and the inner cells in the honeycomb structure. The liquid coating apparatus of the present invention includes a liquid storage tank for storing a liquid to be coated, which has an upper opening at its upper part and an air discharge outlet, and an air duct for supplying air stream, which has a lower opening at its lower part. The bottom of the honeycomb structure is sealingly connected to the upper opening of the liquid storage tank by a first sealing element. On the other hand, the top of the honeycomb structure is sealingly connected to the lower part opening of the air duct by a second sealing element. The liquid in the liquid storage tank is raised by a device for raising the liquid through the upper opening and the inner cells in the honeycomb structure. On the other hand, pressurized air is supplied from the top of the honeycomb structure by the air duct. This construction makes it possible to cause the liquid to be coated to adhere speedily and uniformly to the target and thus carry out the coating treatment without causing the liquid to adhere to the side surface of the honeycomb structure. In addition, in order to solve the above-described problems, the present invention provides a liquid coating apparatus for coating a liquid on walls of inner cells in a honeycomb structure, characterized by comprising: a liquid storage tank having a first tank sealed from outside, and a second tank having an upper opening which is adapted to be communicated to a bottom of a honeycomb structure and a communication opening which communicates to a lower part of the first tank; and an air supplier for supplying pressurized air to an upper part of the first tank. The apparatus according to the above-described embodiment of the present invention includes a liquid storage tank which has a first and second tanks. The first tank is sealed from the outside, and a second tank has an upper opening at its upper part. The air supplier supplies pressurized air to the upper part of the first tank. As a result, the liquid rises in the second tank and in the inside of the honeycomb structure. This construction makes it possible to cause the liquid to adhere speedily and uniformly and thus carry out the liquid coating without causing the liquid to the side surface of the honeycomb structure. Fig. 1 is a schematic diagram of the liquid coating apparatus for the honeycomb structure according to a preferred embodiment of the present invention; Fig. 2 is a schematic diagram of the holding apparatus used in the liquid coating apparatus illustrated in Fig. 1; Fig. 3 to 6 are each a schematic diagram illustrating the operation of the liquid coating apparatus illustrated in Fig. 1; and Fig. 7 is a schematic perspective view of the apparatus for measuring the fluctuation of value B measured in Example 3, showing the position at which value B is measured. Now, referring to the attached drawings, the coating apparatus and method according to preferred embodiments of the present invention will be described in greater detail hereinbelow. While the embodiments described below relate to a coating apparatus and method for coating a slurry containing catalyst components to a honeycomb structure having a shape of a circular cylinder, it will be apparent that various modifications or variations which are obvious to the skilled artisan may be made on the embodiments, if desired, to modify them to a coating apparatus and method for coating various liquids such as those described above to honeycomb structures having various shapes and forms. The coating apparatus for a honeycomb structure illustrated in Fig. 1 includes a liquid storage tank 10, a slurry storage device 12 from which a slurry is supplied to the liquid storage tank 10, an air supply device 14 which supplies pressurized air to the liquid storage tank 10, air duct 16, an air control device 18 which controls the supply of the pressurized air from a pressurized air source A to the air duct 16, a holding device 22 for sealingly supporting a honeycomb structure 20 between the liquid storage tank 10 and the air duct 16, a cyclone device 24, connected to the liquid storage tank 10, and a gravimetric device 25 for measuring the weight of, for example, the liquid storage tank 10 containing slurry therein. The liquid storage tank 10 has a first tank, i.e., an outer tank 26, second tank, i.e., an inner tank 28, and a stirrer 30 for rendering uniform the density of the slurry in the outer tank 26, and retains a predetermined amount of the slurry therein. The outer tank 26 has on its upper part an air supply port 32 which communicates to the air supply device 14. The upper part of the outer tank 26 is sealed from the outside so that air in the upper part of the outer tank 26 will not leak to outside. The outer tank 26 has on its lower part a slurry supply port 34 which communicates to the slurry supply device 12 and a discharge port 36 having a valve which is usually closed. The inner tank 28 has on its upper part a horizontally extending upper wall 38 which defines an upper opening 40, and an air discharge port 42 which communicates to the cyclone device 24, and on its lower part a communication port 44 which communicates to the outer tank 26. Because the liquid storage tank 10 has the above-described construction, the supply of a predetermined amount of pressurized air from the air supply device 14 to the liquid storage tank 10 through the air supply port 32 increases the pressure of the air in the upper part of the outer tank 26, which in turn increases the level of the slurry in the inner tank 28, resulting in that the slurry rises to a predetermined level above the upper end surface of the honeycomb structure 20 as described below. In order to supply a sufficient amount of the slurry from the outer tank 26 to the inner tank 28, the horizontal sectional area of the outer tank 26 is preferably sufficiently larger than the horizontal sectional area of the inner tank 28 and the communication port 44 of the inner tank 28 opens downward. In this embodiment, the height of the slurry which is caused to rise depends on the amount of the slurry in the liquid storage tank 10 and the amount of the pressurized air supplied from the air supply device 14. For example, the level of the liquid surface of the slurry which has risen may be detected by providing a detector in the air duct 16. Alternatively, it is possible to supply a predetermined amount of the slurry, instead of the pressurized air, to the liquid storage tank 10 and determine the level of the liquid surface of the slurry which is caused to rise. The slurry storage device 12 has a slurry tank 46 for storing the slurry, stirrer 47, a pump 48 and a control valve 50, and controls the amount of the slurry supplied from the slurry tank 46 to the liquid storage tank 10 by means of the pump 48 and the control valve 50. The control valve 50 of the slurry supply device 12 and the slurry supply port 34 of the liquid storage tank 10 are connected to each other with a flexible tube 52. It is preferred to construct the apparatus such that the pump 48 and the control valve 50 can be controlled by signals issued from the gravimetric device 25, for example, as described below in order for a given amount of the slurry to be retained before the coating operation starts. The air supply device 14 has an air chamber 54 to which pressurized air is supplied from the pressurized air source A, an air pump 56 connected to the air chamber 54, a control valve 58, and a exhaust valve 59 for discharging the air in the upper part of the outer tank 26. The air pump 56 further pressurizes the pressurized air supplied from the air chamber 54 and supplies it to the control valve 58. The control valve 58 is opened or closed by a control device (not shown) or manually. The control valve 58 and the exhaust valve 59 are connected to the air supply port of the liquid storage tank 10 through a flexible tube 60. When the air pump 56 is actuated to open the control valve 58, the pressurized air is supplied from the control valve 58 to the upper part of the outer tank 26 through the air supply port 32. As a result, the slurry in the inner tank 28 is caused to rise as described above and rise further through the upper opening 40 of the liquid storage tank 10 and the inside of the honeycomb structure 20. As other device for causing the slurry to rise, there can be used, for example, a pump for injecting the slurry to the liquid storage tank 10, or a device which includes a part of the outer wall of the liquid storage tank which is constructed by a flexible material capable of being deformed so as to reduce the inside volume of the liquid storage tank. The air duct 16 is arranged above the liquid storage tank 10 and has an air inlet port 61 and a lower opening 62 arranged as opposing the upper opening 40 of the liquid storage tank 10. The air duct 16 has inner space of a considerably large volume so that the air stream can be discharged from the lower opening 62 at a constant pressure. The air duct 16 has also a horizontally extending flange-shaped lower wall 64 on the lower part thereof, which can move slightly up and down so that the holding device 22 can be arranged sealingly between the liquid storage tank 10 and the air duct 16. The air control device 18 has a control valve 65 and an exhaust valve 66, and supplies pressurized air at a predetermined pressure at a predetermined timing to the air duct 16 by means of a control device (not shown) or manually, and discharges the pressurized gas in the air duct 16. The air control device 18 may have a pressure control device (not shown) and an additional passage or channel (not shown) to the air duct 16, if desired, in order to supply a desired pressurized air to the air duct 16. The exhaust valve 66 of the air control device 18 and the air inlet port 61 of the air duct 16 are connected to each other with a flexible tube 67. The holding device 22 has a shape of a circular cylinder having a inner hole of a circular column in shape. The holder device is composed of two splittable parts, or halves, as shown in Fig. 2. The two halves may be connected to each other with a connecting device (not shown) and arranged so that the inner side surface of the holding device 22 can closely contact the side surface of the honeycomb structure 20. Of course, the holding device 22 may be divided into three, four or more parts instead of two parts. It is preferred that the holding device 22 be made of a material which is hard to deform and has resistance to chemicals, such as MC nylon. Further, the holding device 22 may be provided with a sheet of solid or porous, i.e., spongy rubber having a thickness on the order of from 1 to 5 mm on its upper surface, lower surface and inner side surface in order to increase its sealing ability. The diameter of the inner hole of the holding device 22, i.e., the outer diameter of the honeycomb structure 20, is smaller than the diameter of the upper opening 40 of the liquid storage tank 10 and that of the lower opening 62 of the air duct 16. On the other hand, the outer diameter of the holding device 22, i.e., the diameter of the outer side wall, is larger than the diameter of the upper opening 40 of the liquid storage tank 10 and that of the lower opening 62 of the air duct 16. Because of this construction, when the slurry is urged upward to above the liquid storage tank 10, the slurry comes to rise through all the cells in the honeycomb structure 20. Alternatively, the slurry can be caused to rise through all the cells in the honeycomb structure 20 even when the outer diameter of the honeycomb structure 20 is larger than the diameter of the upper opening 40 of the liquid storage tank 10 and that of the lower opening 62 of the air duct 16, if the honeycomb structure 20 is supported in a mid position of the holding device 22, for example, using the holding device 22 of a large height instead of using the above-described construction. The holding device 22 is arranged so that its inner side surface can closely contact the side surface of the honeycomb structure 20, and the holding device 22 thus arranged is positioned between the liquid storage tank 10 and the air duct 16 after raising the air duct 16 to some extent. Then, by lowering the air duct 16, the honeycomb structure 20 is set to the position as illustrated in Fig. 1. In this position, the lower surface of the holding device 22 sealingly contacts the upper wall 38 of the liquid storage tank 10, and the upper surface of the holding device 22 sealingly contacts the lower wall 64 of the air duct 16. The inner side surface of the holding device 22 sealingly contacts the side surface of the honeycomb structure 20. With this construction, when the slurry is pushed up to above the liquid storage tank 10, the slurry rises through the inner cells of the honeycomb structure 20 without causing the leakage of the slurry to the outside through between the lower surface of the holding device 22 and the upper wall 38 of the liquid storage tank 10 as well as through between the upper surface of the holding device 22 and the lower wall 64 of the air duct 16, and without rising through between the inner side surface of the holding device 22 and the side surface of the honeycomb structure 20. As described above the holding device 22 includes the first sealing element for sealingly connecting the liquid storage tank 10 to the honeycomb structure 20, and the second sealing element for sealingly connecting the air duct 16 to the honeycomb structure 20, integrally assembled with each other. These sealing elements may be of any type so far as they have the above-described function but are limited in no way to those illustrated in the attached drawings. For example, it may be constructed such that the upper and lower sealing elements are connected to each other with a connection rod, with the upper sealing element sealingly contacting the lower wall 64 of the air duct 16 and the side surface of the honeycomb structure 20, and on the other hand, the lower sealing element sealingly contacting the upper wall 38 of the liquid storage tank 10 and the side surface of the honeycomb structure 20. Alternatively, the upper and lower sealing elements may be supported by the lower wall 64 of the air duct 16 and the upper wall 38 of the liquid storage tank 10, respectively, without using the connection rod. The cyclone device 24 has an air inlet port 68 connected to the air discharge port 42 of the liquid storage tank 10, a gas component discharge port 70 provided with a control valve 69, and a liquid component discharge port 72 provided with a control valve 71. The cyclone device 24 separates the pressurized air containing a liquid component such as slurry supplied from the air discharge port 42 of the liquid storage tank 10 into gas components and liquid components, and discharges them through the gas component discharge port 70 and the liquid component discharge port 72, respectively. The air inlet port 68 of the cyclone device 24 and the air discharge port 42 of the liquid storage tank 10 are connected to each other with a flexible tube 74. The gravimetric device 25 is provided under the liquid storage tank 10, and measures the total weight of the liquid storage tank 10 itself and of the slurry contained therein. From this, the amount of the liquid storage tank 10 can be known. That is, as described earlier, the control valve 50 of the slurry storage device 12 and the slurry supply port 34 of the liquid storage tank 10 are connected to each other with the flexible tube 52; the control valve 58 and the exhaust valve 59 of the air supply device 14 are connected to the air supply port 32 of the liquid storage tank 10 with the flexible tube 60; and further, the air inlet port 68 of the cyclone device 24 is connected to the air discharge port 42 of the liquid storage tank 10 with the flexible tube 74; hence the weight of the liquid storage tank 10 itself and the weight of the slurry in the tank 10 are posed on the gravimetric device 25. Before starting the coating operation, the amount of the slurry in the liquid storage tank 10 is measured using the gravimetric device 25, and the pump 48 and the control valve 50 of the slurry storage device 12 are actuated in accordance with the measured amount to supply a predetermined amount of the slurry to the liquid storage tank 10 so that always a constant amount of the slurry can be retained in the liquid storage tank 10 before the coating operation starts. Now, referring to Figs. 3 to 6, the operation of the liquid coating apparatus illustrated in Fig. 1 is explained. At first, the honeycomb structure 20 and the holding device 22 are sealingly arranged between the liquid storage tank 10 and the air duct 16 as illustrated in Fig. 3, and the amount of the slurry is measured by means of the gravimetric device 25, with replenishing the slurry from the slurry storage device 12 so that a predetermined amount of the slurry can be retained in the liquid storage tank 10, and then the control valve 50 of the slurry storage device 12 is closed (cf. Fig. 1). Next, as illustrated in Fig. 4, a predetermined amount of pressurized air is supplied from the air supply device 14 to the upper part of the outer tank 26 through the air supply port 32 to lower the level of the liquid surface in the outer tank 26, to elevate the level of the liquid surface in the inner tank 28, and then the level of the slurry to a position above the upper end surface of the honeycomb structure 20. The pressure in the air duct 16 is retained substantially at atmospheric pressure by means of the exhaust valve 66 of the air control device 18, which causes the slurry to rise through the inner cells in the honeycomb structure 20 so that the level of the liquid surface can reach a position higher than the upper end surface of the honeycomb structure 20 when the pressurized air supplied as described above. After completion of the supply of the pressurized air from the air supply device 14 to the upper part of the outer tank 26, it is preferred to retain that state for a while, for example, for from 1 to 10 seconds. This is sometimes necessary, for example, in the case where the slurry has a high viscosity, the speed of slurry rising in the honeycomb structure 20 is low and thus it is necessary to await until the liquid surface reaches a position higher than the upper end surface of the honeycomb structure 20 completely. The speed at which the slurry rises in the honeycomb structure 20 is preferably from 5 to 20 cm/sec. If this speed is too high, speeds at which the slurry in a great number of cells in the honeycomb structure differ from cell to cell, and therefore, there is a possibility that in some cells the coating treatment is performed in a state in which the slurry rises insufficiently. On the other hand, if the speed is too low, the efficiency of the coating operation is aggravated. In order for the slurry to adhere to all of the plurality of cells in the honeycomb structure 20 all over the entire lengths of the respective cells, it is preferred to cause to rise the slurry so that the level of the liquid surface of the slurry can reach to a position higher, for example, by from 0.5 to 10 cm than the upper end surface of the honeycomb structure 20. This preferred height varies depending on the density, length, shape and the like factors of the cells and generally higher density of the cells gives higher level of the liquid surface. Particularly preferred height is, for example, from 0.5 to 1 cm at a cell density of below 62 cell/cm² (400 cell/inch²), and from 1 to 3 cm at a cell density of 62 cell/cm² (400 cell/inch²). Because all the valves of the cyclone device 24 (cf. Fig. 1) are closed, the level of the liquid surface at the air discharge port 42 does not rise so high. Next, the exhaust valve 59 of the air supply device 14 is opened, and then the control valve 69 of the cyclone device 24 (cf. Fig. 1), followed by supplying a small amount of pressurized air from the air control device 18 (cf. Fig. 1) to the air duct 16 as illustrated in Fig. 5 to discharge most part of the slurry in the cells of the honeycomb structure 20. Then, as illustrated in Fig. 6, pressurized air is supplied from the air control device 18 (cf. Fig. 1) to the air duct 16 at an air flow of from 20 to 40 m³/minute and at a pressure of from 0.1962 to 0.981 bar (0.2 to 1.0 kg/cm²) to remove excessive slurry which adhered to the cells in the honeycomb structure 20 so that the clogging can be prevented which would otherwise occur at the lower part of the honeycomb structure 20. Particularly preferred pressure of pressurized air in the blowing step is from 0.2943 to 0.5886 bar (0.3 to 0.6 kg/cm²). The time of single blowing operation is preferably from 0.3 to 1.0 second. The blowing is carried out preferably from 1 to 3 times. The liquid coating method and apparatus for the honeycomb structure according to the present invention makes it possible to coating the inner cells in the honeycomb structure speedily and uniformly. The liquid coating method and apparatus for honeycomb structure according to the present invention enables the coating of the inner cells in the honeycomb structure without causing the liquid to adhere to the side surface of the honeycomb structure. Example 1 A honeycomb structure was used which was made of a ceramics having a shape of a circular cylinder of a diameter of 93 mm and a height of 75 mm, having a cell density of 46.5 cell/cm² (300 cells/inch²). As the liquid for coating, slurry was used which is composed mainly of platinum, aluminum oxide, cerium oxide, acetic acid, a defoaming agent and water. The specific gravity of the slurry was 1.55 g/ml. The solid content was 46.08 %. Using the apparatus exactly as illustrated in Fig. 1, the above-described honeycomb structure as described above was set between the liquid storage tank and the air duct using the holding device. The amount of the slurry retained in the liquid storage tank and the amount of pressurized air to be supplied by the air supply device are adjusted so that the slurry was able to be pushed upward to a level of about 2 cm above the upper end surface of the honeycomb structure, and after retaining the system under these conditions for one second after completion of the supply of the pressurized air from the air supply device, pressurized air at a pressure of 3.6297 bar (3.7 kg/cm²) was supplied into the air duct for 2 seconds to completely expel the slurry which remained in the cells. Thereafter, pressurized air at 0.36297 bar (0.37 kg/cm²) was supplied into the air duct for 0.5 second, with interruption for 1 second, and again pressurized air at 0.36297 bar (0.37 kg/cm²) was supplied into the air duct for 0.5 second. Twenty honeycomb structures thus teated were measured for recording the amount of the slurry which adhered to the honeycomb structure and the time required for the coating. The weight of the slurry which adhered to the honeycomb structure was on average 116.2 g, and as indicated in Table 1, fluctuation A of the amount of the slurry which adhered was 5.00 %as 30 %. The time T required for the operation was 25 seconds/number of article. Comparative Example 1 The same honeycomb structure and slurry as used in Example 1 were used. The honeycomb structure was completely dipped in the slurry charged in the storage tank, taken out from the slurry, and passed below air-knife jetting high-pressure air to blast off the slurry remaining in the cells. Twenty honeycomb structures thus obtained were measured for recording the fluctuation A in the amount of the slurry which adhered to the honeycomb structure and the time T required for the coating. Table 1 shows the results. Example 2 A honeycomb structure was used which was made of a ceramics having a shape of an ellipse in cross section of a major axis of 14.6812 cm (5.78 inch) and a minor axis of 7.6962 cm (3.03 inch), a height of 5.715 cm (2.25 inch), having a cell density of 62 cells/cm² (400 cells/inch²). The coating was carried out with other conditions being the same as those in Example 1. Twenty honeycomb structures thus obtained were measured for recording the fluctuation A in the amount of the slurry which adhered to the honeycomb structure and the time T required for the coating. Table 1 shows the results. Comparative Example 2 The same honeycomb structure as used in Example 2 was coated in the same manner as in Comparative Example 1. Twenty honeycomb structures thus obtained were measured for recording the fluctuation A in the amount of the slurry which adhered to the honeycomb structure and the time T required for the coating. Table 1 shows the results. Fluctuation A Time T Adherence to Side Wall Example 1 5.0 % 25 sec/n No Comparative Example 7.3 % 100 sec/n Yes Example 2 3.3 % 25 sec/n No Comparative Example 8.9 % 100 sec/n Yes Example 3 A honeycomb structure was used which was made of a ceramics having a shape of an ellipse in cross section of a major axis of 7.6962 cm (3.03 inch) and a minor axis of 5.715 cm (2.25 inch), a height of 5.715 cm (2.25 inch), having a cell density of 62 cells/cm² (400 cells/inch²). The coating was carried out under the same conditions as in Example 1, and then calcined in an electric oven at 400°C for 1 hour. Then, Fluctuation B in the amount of the catalyst components carried on each part of the honeycomb structure was measured as follows. An upper 1/3 part of the honeycomb structure was divided into three parts so that a diameter is divided into three equal parts as illustrated in Fig. 7. The maximum value of the contents of catalyst component (% by weight) among the three parts was defined as C MAX , the minimum as C MIN , and an average of the whole values as C AVE , then, the fluctuation B (%) of the amount of the catalyst component carried being represented by the following formula: B = 100 X (C MAX - C MIN )/C AVE The fluctuation B measured as described is shown in Table 2. Comparative Example 3 The same honeycomb structure as that in Example 3 was coated and calcined under the same conditions as in Comparative Example 2; and then fluctuation B was measured as described above. The fluctuation B measured as described above is shown in Table 2. Fluctuation B Example 3 1.8 % Comparative Example 3 14.0 %

Claims: A liquid coating method for coating a liquid in inner cells in a honeycomb structure (20), characterized by comprising the steps of: supplying a liquid to an inside of a honeycomb structure (20) vertically arranged from its lower part to cause the liquid to adhere to the inner cells; and supplying pressurized air onto an upper part of the honeycomb structure (20) to discharge the liquid within the inner cells. A liquid coating method according to claim 1, characterized by further comprising the steps of: providing a liquid storage tank (10) for storing a liquid to be coated, the liquid storage tank (10) having an upper opening (40) at its upper part and an air discharge outlet (42), and an air duct (16) having a lower opening (62) at its lower part; connecting the upper opening (40) of the liquid storage tank (10) to a bottom of the honeycomb structure (20) vertically arranged; further connecting the lower opening (62) of the air duct (16) to a top of the honeycomb structure (20), and supplying the liquid to be coated from the liquid storage tank (10) into the inner cells in the honeycomb structure (20) to cause the liquid to adhere to the inner cells. A method according to claim 1 or 2, characterized by further comprising the steps of: supplying pressurized air from the air duct (16) to the upper part of the honeycomb structure (20); and discharging the pressurized air from the air discharge outlet (42) of the liquid storage tank (10) to discharge the liquid in the cells. A liquid coating apparatus for coating a liquid in inner cells in a honeycomb structure (20), characterized by comprising: a liquid storage tank (10) for storing a liquid to be coated, the storage tank (10) having an upper opening (40) and an air discharge outlet (42); an air duct (16) for supplying air stream, the air duct (16) having a lower opening (62) to supply pressurized air onto the upper part of the honeycomb structure (20) and discharge the liquid within the inner cells; a first sealing element for sealingly connecting a bottom of the honeycomb structure (20) to the upper opening (40) of the liquid storage tank (10); a second sealing element for sealingly connecting a top of the honeycomb structure (20) to the lower opening (62) of the air duct (16); and an apparatus for raising the liquid within the liquid storage tank (10) through the upper opening (40) and the inner cells in the honeycomb structure (20). The liquid coating apparatus according to claim 4, characterized in that said first sealing element and said second sealing element are formed by a holder (22) for holding said honeycomb structure (20). The liquid coating apparatus according to claim 5, characterized in that said holder (22) has a shape of a circular cylinder provided with a cylindrical inner hole, said holder (22) being separable into two halves. A liquid coating apparatus for coating a liquid on walls of inner cells in a honeycomb structure (20), characterized by comprising: a liquid storage tank (10) having a first tank (26) sealed from outside, and a second tank (28) having an upper opening (40) which is adapted to be communicated to a bottom of a honeycomb structure (20) and a communication opening (44) which communicates to a lower part of the first tank (26); and an air supplier (14) for supplying pressurized air to an upper part of the first tank (26).

Inventors: MATSUGU HIDETOMO, WATANABE TADASHI, WATANABE TATESHI, WATANABE TSUNAO, YAMANOUCHI YASUHIRO, MATSUGU, HIDETOMO, WATANABE, TADASHI, WATANABE, TATESHI, WATANABE, TSUNAO, YAMANOUCHI, YASUHIRO
Applicants: N E CHEMCAT CORP, N.E. CHEMCAT CORPORATION
Application year: 1990
Main classification: B01J37
IPC codes: B28B11, B01J37, B01J35, C04B41, C23C4, C23C2