Patent Application
20180281011
The present disclosure relates to coating of a substrate, particularly a substrate comprising a plurality of pores or channels therein, with a low viscosity coating solution.
Catalytic converters are well known for the removal and/or conversion of the harmful components of exhaust gases. While catalytic converters have a variety of constructions for this purpose, one form of construction is a catalytically coated rigid skeletal monolithic substrate, or honeycomb-type element which has a multiplicity of longitudinal channels or cells to provide a catalytically coated body having a high surface area. The rigid, monolithic substrate can be fabricated from ceramics and other materials. Such materials and their construction are described, for example, in U.S. Pat. Nos. 3,331,787 and 3,565,830 each of which is incorporated herein by reference.
A monolithic honeycomb substrate will typically have an inlet end and an outlet end, with multiple mutually adjacent cells extending along the length of the substrate body from the inlet end to the outlet end. These honeycomb substrates typically have from about 100 to 600 cells-per-square-inch (cpsi); however, cell density can be in the range of about 10 cpsi to about 1200 cpsi. The cells can have round, square, triangular, or hexagonal cell shapes.
The open frontal area of a monolithic honeycomb substrate may comprise about 50% to about 85% of the surface area, and the cell wall thickness may be about 0.5 mils to about 10 mils, where 1 mil is 0.001 inches. The cells also may be separated from one another by walls with a thickness in the range of about 0.5 mils to about 60 mils (0.012 mm to 1.5 mm). The open frontal area may be as much as 91% for a 600 cpsi substrate with 2 mil cell wall thickness.
The cell walls of the substrate may be porous or non-porous, smooth, or rough. For porous walls, an average wall pore diameter may be from about 0.1 microns to about 100 microns, and wall porosity can be in the range of 10% to about 85%.
Such monolithic catalytic substrates may have one, two, or more catalytic coatings deposited on the cell walls of the substrate. The catalytic material may be carried as a dissolved compound in a solution or as a suspended solid in a slurry. The carrier and coating is introduced into the cells and deposits on the walls in a wet state that may then be dried and calcined. This coating process has involved using a vacuum to suck up the solution or slurry an intended distance into the cells, where an intended amount of catalytic material may then adhere to the walls when the carrier liquid is removed. The coating operation may not deposit the same amount of catalytic material onto the walls of different cells, or may not suck the solution or slurry a uniform distance into each of the cells. Moreover, low viscosity materials can be difficult to evenly distribute through the substrate, and it can be difficult to accurately draw a low viscosity material into a substrate by an applied vacuum (e.g., avoiding overshoot and fouling of equipment). Further, when using known systems for drawing a solution into a substrate, it is common for solutions with a low solids content to drip out of the substrate or otherwise contact equipment and/or personnel in an undesirable manner. It would be desirable to decrease the time required for coating a monolithic catalytic substrates while increasing the homogeneity of the depth and loading of catalytic material to improve manufacturing efficiency. It likewise would be desirable to address the further difficulties noted above.
The present disclosure provides coating systems and methods useful for providing one or more washcoats onto a substrate. In particular, a washcoat including catalytic materials may be applied to channel walls in a substrate to form a catalytic substrate. The coating systems and methods can be utilized as part of a multi-station coating system and method.
In one or more embodiments, the present disclosure thus can provide a coating system comprising:
The receiving chamber can be configured so that the coating solution may pass through the substrate with substantially none of the coating solution passing between the substrate and the wall of the receiving chamber.
The fluid inlet can be positioned above the vessel valve.
The fill sensor can be positioned in the vessel cover.
The coating system further can comprise a tail pipe extending below the vessel valve and having outlet.
The tail pipe can extend into a collection box.
The vacuum pump can be included and can be in fluid connection with a suction port on the collection box. The suction port can be positioned above the outlet of the tail pipe.
The further can comprise a separator between and in fluid communication with the vacuum pump and the suction port.
The separator can comprise a spout in fluid connection with the collection box at a position below the outlet of the tail pipe.
The coating system further can comprise a controller configured to receive a signal from the sensor and send a control signal.
The controller can be configured to control one or both of the supply pump and the vessel valve.
The coating system further can comprise a controller configured to receive a control signal and execute a control command relative to one or more of the return pump, the vacuum pump, and the vessel cover.
The coating system further can comprise a substrate clamp or air bladder configured for moveably engaging the substrate.
In one or more embodiments, the present disclosure can provide a method for coating a substrate with a low viscosity coating solution, the method comprising:
The positioning can comprise moving the substrate from a non-coating position to the receiving chamber with a moveable substrate clamp or air bladder.
The pumping can be carried out such that the low viscosity coating solution passes through the pores or channels of the substrate with substantially none of the low viscosity coating solution passing between the substrate and the wall of the receiving chamber.
The pumping can continue until the low viscosity coating solution reaches a pre-defined height in the receiving chamber. The pre-defined height can substantially correspond to the top of the substrate.
The pumping can continue until a fill level control signal from a sensor is sent to a controller indicating the low viscosity coating solution has sufficiently migrated upward through the pores or channels present in the substrate.
The sensor can be positioned in the vessel cover.
Upon receipt of the fill level control signal, the controller can execute one or both of the following commands—automatically stop a supply pump that is pumping the low viscosity coating solution through the fluid inlet; and automatically open the vessel valve.
The non-coating portion of the low viscosity coating solution draining through the vessel valve can pass through an outlet of a tail pipe and into a collection box.
After opening the vessel valve, the method further can comprise pumping the non-coating portion of the low viscosity coating solution from the collection box and recycling the non-coating portion of the low viscosity coating solution for further coating of a substrate.
A controller can automatically start a return pump for pumping the non-coating portion of the low viscosity coating solution at a defined time relative to the opening of the vessel valve.
After opening the vessel valve, the method further can comprise actively withdrawing the non-coating portion of the low viscosity coating solution from the substrate. Active withdrawing can comprise drawing a vacuum through the collection box with a vacuum pump. A controller can automatically start the vacuum pump at a defined time relative to starting of the return pump.
The method can comprise disengaging the vessel cover from the coating vessel sufficiently to release the fluid-tight seal. A controller can automatically disengage the vessel cover from the coating vessel at a defined time relative to starting of the vacuum pump.
A separator can be positioned between and in fluid communication with the vacuum pump and the collection box.
The method can comprise emptying a fraction of the non-coating portion of the low viscosity coating solution collected in the separator into the collection box at a position below the outlet of the tail pipe.
The method can comprise stopping of the vacuum pump, and emptying can be carried after the stopping of the vacuum pump.
One or more of the following conditions can be met: a controller can automatically stop the vacuum pump based upon one or both of a sensor output and an algorithm related to flow of the non-coating portion of the low viscosity coating solution; a controller can automatically open a valve for emptying of the separator at a defined time relative to the stopping of the vacuum pump; and a controller can automatically close the vessel valve based upon one or both of a sensor output and an algorithm related to flow of the non-coating portion of the low viscosity coating solution.
The further can comprise at least partially drying the coating portion of the low viscosity coating solution that is in the pores or channels of the substrate by carrying out one or more drying steps.
The further can comprise calcining the substrate with the at least partially dried coating portion of the low viscosity coating solution in the pores or channels thereof.
In one or more embodiments, the disclosure can relate to a multi-station coating system wherein a coater as described herein is combined with one or more of a weighing station, a drying station, and a calcining station. The multi-station coating system can include control elements so that a substrate may be sequentially passed from one station to another to automatically form a catalytic substrate.
The invention includes, without limitation, the following embodiments.
A coating station comprising:
The coating station of any previous or subsequent embodiment, wherein the receiving chamber is configured so that the coating solution may pass through the substrate with substantially none of the coating solution passing between the substrate and the wall of the receiving chamber.
The coating station of any previous or subsequent embodiment, wherein fluid inlet is positioned above the vessel valve.
The coating station of any previous or subsequent embodiment, wherein the fill sensor is positioned in the vessel cover.
The coating station of any previous or subsequent embodiment, further comprising a tail pipe extending below the vessel valve and having outlet.
The coating station of any previous or subsequent embodiment, wherein the tail pipe extends into a collection box.
The coating station of any previous or subsequent embodiment, wherein the vacuum pump is included and is in fluid connection with a suction port on the collection box.
The coating station of any previous or subsequent embodiment, wherein the suction port is positioned above the outlet of the tail pipe.
The coating station of any previous or subsequent embodiment, further comprising a separator between and in fluid communication with the vacuum pump and the suction port.
The coating station of any previous or subsequent embodiment, where the separator comprises a spout in fluid connection with the collection box at a position below the outlet of the tail pipe.
The coating station of any previous or subsequent embodiment, further comprising a controller configured to receive a signal from the sensor and send a control signal.
The coating station of any previous or subsequent embodiment, wherein the controller is configured to control one or both of the supply pump and the vessel valve.
The coating station of any previous or subsequent embodiment, further comprising a controller configured to receive a control signal and execute a control command relative to one or more of the return pump, the vacuum pump, and the vessel cover.
The coating station of any previous embodiment, further comprising a substrate clamp configured for moveably engaging the substrate.
A method for coating a substrate with a low viscosity coating solution, the method comprising:
The method of any previous or subsequent embodiment, wherein said positioning comprises moving the substrate from a non-coating position to the receiving chamber with a moveable substrate clamp.
The method of any previous or subsequent embodiment, wherein said pumping is carried out such that the low viscosity coating solution passes through the pores or channels of the substrate with substantially none of the low viscosity coating solution passing between the substrate and the wall of the receiving chamber.
The method of any previous or subsequent embodiment, wherein said pumping continues until the low viscosity coating solution reaches a pre-defined height in the receiving chamber.
The method of any previous or subsequent embodiment, wherein the pre-defined height substantially corresponds to the top of the substrate.
The method of any previous or subsequent embodiment, wherein said pumping continues until a fill level control signal from a sensor is sent to a controller indicating the low viscosity coating solution has sufficiently migrated upward through the pores or channels present in the substrate.
The method of any previous or subsequent embodiment, wherein the sensor is positioned in the vessel cover.
The method of any previous or subsequent embodiment, wherein, upon receipt of the fill level control signal, the controller executes one or both of the following commands:
The method of any previous or subsequent embodiment, wherein the non-coating portion of the low viscosity coating solution draining through the vessel valve passes through an outlet of a tail pipe and into a collection box.
The method of any previous or subsequent embodiment, wherein after opening the vessel valve, the method further comprises pumping the non-coating portion of the low viscosity coating solution from the collection box and recycling the non-coating portion of the low viscosity coating solution for further coating of a substrate.
The method of any previous or subsequent embodiment, wherein a controller automatically starts a return pump for pumping the non-coating portion of the low viscosity coating solution at a defined time relative to the opening of the vessel valve.
The method of any previous or subsequent embodiment, wherein after opening the vessel valve, the method further comprises actively withdrawing the non-coating portion of the low viscosity coating solution from the substrate.
The method of any previous or subsequent embodiment, wherein said actively withdrawing comprises drawing a vacuum through the collection box with a vacuum pump.
The method of any previous or subsequent embodiment, wherein a controller automatically starts the vacuum pump at a defined time relative to the starting of the return pump.
The method of any previous or subsequent embodiment, wherein the method comprises disengaging the vessel cover from the coating vessel sufficiently to release the fluid-tight seal.
The method of any previous or subsequent embodiment, wherein a controller automatically disengages the vessel cover from the coating vessel at a defined time relative to starting of the vacuum pump.
The method of any previous or subsequent embodiment, wherein a separator is positioned between and in fluid communication with the vacuum pump and the collection box.
The method of any previous or subsequent embodiment, wherein the method comprises emptying a fraction of the non-coating portion of the low viscosity coating solution collected in the separator into the collection box at a position below the outlet of the tail pipe.
The method of any previous or subsequent embodiment, wherein the method comprises stopping of the vacuum pump, and wherein said emptying is carried after the stopping of the vacuum pump.
The method of any previous or subsequent embodiment, wherein one or more of the following conditions is met:
The method of any previous or subsequent embodiment, further comprising at least partially drying the coating portion of the low viscosity coating solution that is in the pores or channels of the substrate by carrying out one or more drying steps.
The method of any previous embodiment, further comprising calcining the substrate with the at least partially dried coating portion of the low viscosity coating solution in the pores or channels thereof.
A multi-station coating system comprising a coating station according to any previous or subsequent embodiment.
The multi-station coating system according to any previous or subsequent embodiment, further comprising one or more of a weighing station, a drying station, and a calcining station.
These and other features, aspects, and advantages of the disclosure will be apparent from a reading of the following detailed description together with the accompanying drawings, which are briefly described below. The invention includes any combination of two, three, four, or more of the above-noted embodiments as well as combinations of any two, three, four, or more features or elements set forth in this disclosure, regardless of whether such features or elements are expressly combined in a specific embodiment description herein. This disclosure is intended to be read holistically such that any separable features or elements of the disclosed invention, in any of its various aspects and embodiments, should be viewed as intended to be combinable unless the context clearly dictates otherwise.
In order to provide an understanding of embodiments of the invention, reference is made to the appended drawings, which are not necessarily drawn to scale, and in which reference numerals refer to components of exemplary embodiments of the invention. The drawings are exemplary only, and should not be construed as limiting the invention.
Before describing several exemplary embodiments of the invention, it is to be understood that the invention is not limited to the details of construction or process steps set forth in the following description. The invention is capable of other embodiments and of being practiced or being carried out in various ways.
The present disclosure provides systems and methods suitable for coating a solution onto at least a portion of a substrate. In particular, a substrate having a plurality of pores and/or channels formed therein can be provided with a washcoat on the walls defining the pores and/or the channels.
In one or more embodiments, the washcoat, also referred to as a wet coating, may be formed by preparing a slurry containing a specified solids content (e.g., about 5% to about 60% by weight) of a catalyst or another material in a liquid carrier or vehicle, which is then coated onto a substrate and dried to provide a washcoat layer. As used herein, the term “washcoat” has its usual meaning in the art of a thin, adherent coating of a catalytic or other material applied to a substrate material, such as a honeycomb-type carrier member, which is sufficiently porous to permit the passage of a gas stream being treated. A washcoat or wet coating applied according to systems and methods of the present disclosure can comprise a metal catalyst. For example, the metal catalyst can be selected from the group consisting of calcium, barium, strontium, cerium, cesium, copper, iron, nickel, cobalt, manganese, chromium, vanadium, zirconium, and combinations thereof. The metals particularly may be in the form of a compound, such as a metal salt, that is soluble in a liquid carrier, particularly an aqueous carrier (e.g., H2O). In some embodiments, the slurry may comprise alumina, molecular sieves, silica-alumina, zeolites, zirconia, titania, lanthana, and combinations thereof. In some embodiments, the slurry may comprise metal oxides, including but not limited to oxides of calcium, barium, strontium, cerium, cesium, copper, iron, nickel, cobalt, manganese, chromium, vanadium, and combinations thereof. In some embodiments, the slurry may comprise metal compounds that are not oxides but that are adapted to convert to a metal oxide before, during, or after deposition on the substrate. For example, various metal salts may be used. In certain exemplary embodiments, nickel nitrate may be provided in solution to be applied as a washcoat on a substrate, and the nickel nitrate can be reacted so as form nickel oxide on the substrate. Other non-limiting examples of metal salts that can be used include copper nitrate and iron nitrate.
In various embodiments, the concentration of the coating solution for preparing a washcoat may be about 0.5% to about 5% by weight of platinum group metal (PGM), or alternatively, the coating solution may have a concentration of about 1% to about 2% by weight of platinum group metal, or about 1.5% by weight of platinum group metal. In some embodiments, the total concentration of metal species in the coating solution can be about 0.5% to about 20% by weight, about 0.75% to about 15% by weight, or about 1% to about 10% by weight.
The coating solution, in some embodiments, can be a low viscosity coating solution. A low viscosity coating solution can be defined as being a solution with a viscosity of about 50 centipoise (cP) (50 mPa·s) or less, for example, about 1 cP (1 mPa·s) to about 50 cP (50 mPa·s). A low viscosity coating solution can be defined as being a solution with a viscosity of about 45 cP (45 mPa·s) or less, for example, about 2 cP (2 mPa·s) to about 45 cP (45 mPa·s). A low viscosity coating solution can be defined as being a solution with a viscosity of about 40 cP (40 mPa·s) or less, for example, about 3 cP (3 mPa·s) to about 450 cP (40 mPa·s). A low viscosity coating solution can be defined as being a solution with a viscosity of about 35 cP (35 mPa·s) or less, for example, about 4 cP (4 mPa·s) to about 35 cP (35 mPa·s). A low viscosity coating solution can be defined as being a solution with a viscosity of about 30 cP (30 mPa·s) or less, for example, about 5 cP (5 mPa·s) to about 30 cP (1 mPa·s). A low viscosity coating solution can be defined as being a solution with a viscosity of about 25 cP (25 mPa·s) or less, for example, about 5 cP (5 mPa·s) to about 25 cP (25 mPa·s). A low viscosity coating solution can be defined as being a solution with a viscosity of about 20 cP (20 mPa·s) or less, for example, about 5 cP (5 mPa·s) to about 20 cP (20 mPa·s).
A coating solution according to one or more embodiments of the present disclosure can be defined in relation to its total solids concentration, which can directly affect solution viscosity. Solids may comprise a metal species and/or alumina (e.g., zeolite) particles. Preferably, a coating solution according to the present disclosure will have a total solids concentration of about 1% to about 40% by weight, about 2% to about 35% by weight, about 3% to about 30% by weight, about 4% to about 25% by weight, or about 5% to about 20% by weight. In some embodiments, the coating solution can be limited to Newtonian fluids—i.e., fluids wherein flow viscosity and strain rate are linearly related at every point.
Undesirably, low viscosity solutions (i.e., solutions with a low solids content) can present containment difficulties when being applied using known systems and methods. For example, known systems utilize a vacuum to suction a solution into a substrate, and the substrate commonly must be flipped during the process. With low viscosity, low solids content solutions, such flipping can cause the solution to be “slung” from the substrate, fouling equipment and/or contacting personnel. Such conditions can be particularly undesirable when the coating solution includes a content of materials that may be considered undesirable for human contact, such as some metal-containing solutions. The presently disclosed systems and methods can substantially reduce and/or eliminate such problems.
A low viscosity coating solution according to the present disclosure can particularly be useful as a base coat upon which another catalytic material can be coated. Thus, the present disclosure specifically encompasses systems and methods configured for applying multiple washcoats to the same substrate.
A catalytic substrate useful according to various embodiments of the present disclosure can comprise a monolithic ceramic or metal honeycomb structure, and the monolithic substrate can have fine, parallel gas flow passages extending longitudinally such that the passages are open to fluid flow there through. The passages, which are essentially straight paths from their fluid inlet to their fluid outlet, are defined by walls on which the catalytic material is coated as a washcoat so that the gases flowing through the passages contact the catalytic material. The flow passages of the monolithic substrate can be thin-walled channels, which can be of any suitable cross-sectional shape and size such as trapezoidal, rectangular, square, sinusoidal, hexagonal, oval, circular, etc. Such structures may contain from about 60 to about 900 or more gas inlet openings (i.e., cells) per square inch of cross section.
In one or more embodiments, the catalytic substrate may have a circular cross-section, a rectangular cross-section, or a square cross-section, with a width, diagonal distance, or diameter in the range of about 2 inches to about 14 inches, and a length (height) in the range of about 2 inches to about 12 inches. In various embodiments, the catalytic substrate may have a width, diagonal distance, or diameter in the range of about 3 inches to about 7 inches, and a length (height) in the range of about 4 inches to about 8 inches. In certain embodiments, the height and the largest perpendicular dimension (width, length, diameter) does not exceed 7 inches.
In one or more embodiments, the present disclosure relates to a coating system. The system can be configured for applying a coating solution to a substrate, particularly a catalytic substrate, such as a monolithic ceramic or metal honeycomb structure. The coating system is particularly configured for applying a low viscosity coating solution. As noted above, when applying a low viscosity coating solution to a honeycomb substrate or the like, it can be difficult to precisely control the height through the substrate to which the solution is applied, and fouling of the equipment often occurs when the coating solution over-shoots the end of the substrate and is drawn into the vacuum equipment used to draw the solution through the substrate.
A coating system of the present disclosure can be configured to apply a coating solution to a substrate through application of positive pressure. In particular, the coating solution can be pumped from the below the substrate upwardly through the substrate. The coating system can be configured for pumping the coating solution, detecting completion of the coating of the substrate, and recovering excess coating solution from the substrate at least partially through only gravitational force. The functional aspects of the coating system will become more apparent in light of the description of an exemplary coating system as provided below.
Referring to
The substrate 105 can be positioned within the receiving chamber 112 so that a longitudinal axis of the substrate is substantially aligned with a longitudinal axis of the receiving chamber. A pressure sensor 111 (e.g., a transducer) can be positioned on the coating vessel 110 or in the receiving chamber 112 and can be configured for sensing the pressure within the receiving chamber.
The coating vessel 110 further includes a fluid inlet 115 positioned below the receiving chamber 112. The fluid inlet 115 is in fluid connection with a supply pump 120 that is configured to deliver the coating solution to the fluid inlet. An inlet supply valve 122 can be interposed between the supply pump 120 and the fluid inlet 115. The supply pump 120 can be configured to deliver the coating solution from a supply source 101 to the fluid inlet 115 at a variable pressure that can be configured to force the coating solution against gravitational force upward (see arrow 10) into and through the substrate 105 positioned in the receiving chamber 112 of the coating vessel 110. The coating solution may be pumped at a substantially constant pressure, an increasing pressure, or a decreasing pressure. The supply pump 120, for example, can provide the coating solution as a pressure sufficient to at least support a column of fluid equivalent to the weight of the coating solution in the receiving chamber 112. In some embodiments, the system can comprise a supply pump controller 124 operatively associated with the supply pump 120 and configured to adjust the pressure at which the coating solution is delivered to the receiving chamber 112. For example, the supply pump controller 124 can adjust the pressure of the coating solution pumped through the supply pump 120 based upon a pressure reading taken from the pressure sensor 111.
The coating vessel 110 also includes a vessel valve 117 positioned below the receiving chamber 112 and, optionally, positioned below the fluid inlet 115. In some embodiments, the vessel valve 117 can be a separate element from the coating vessel 110 but still be in fluid connection with the receiving chamber 112 of the coating vessel. The vessel valve 117 can specifically be a full port valve—i.e., having a pass-through opening of a size that is substantially identical to the size of the piping on either side of the valve. Preferably, the vessel valve 117 has a pass-through opening that is at least 85%, at least 90%, at least 95%, or at least 98% (such as about 85% to about 110% or about 90% to about 100%) of the size (e.g., diameter) of the piping on either side of the valve. The vessel valve 117 can be controllably opened and closed to allow coating solution to drain out of the receiving chamber 112 (and the substrate 110 present in the receiving chamber). The vessel valve 117 preferably provides a fluid tight seal at all pressures at which the coating solution may be pumped into the coating vessel 110 from the supply pump 120.
The coating system 100 further can comprise a vessel cover 130. While the receiving chamber 112 of the coating vessel 110 is configured for receiving the substrate 105, the receiving chamber can be configured so that substantially all of the substrate is received therein, or the receiving chamber can be configured so that a portion of the substrate extends from the top of the receiving chamber. As such, the vessel cover 130 can be configured to fit over a top portion of the substrate 105, or the vessel cover can be configured to simply mate with the coating vessel 110. For example, the vessel cover 130 can be configured to fit over about 1% to about 50% of the height of the substrate, more particularly about 2% to about 30%, about 3% to about 20, or about 5% to about 15% of the height of the substrate. The vessel cover 130 can be positioned relative to the coating vessel 110 so as to be coaxial therewith and may move longitudinally relative to the coating vessel. The longitudinal motion of the vessel cover 130 can be controlled by an actuator 137, which can include an actuator controller 138, which can cause automatic movement of the vessel cover based upon receipt of an input signal from a computing element. The vessel cover 130 may move linearly between an open position and a closed position (in contact with the coating vessel 110). The actuator 137 may also provide for rotational movement of the vessel cover or another cover (e.g., pressure cap 131) into and out of alignment with the coating vessel 110. The vessel cover 130 can be configured for forming a fluid-tight engagement with the coating vessel 110. For example, one or both of the coating vessel 110 and the vessel cover 130 can include a gasket 139.
In one or more embodiments, a fill sensor 135 can be included with the vessel cover 130 (although such sensor may be included with the coating vessel 110). The fill sensor 135 can be configured to detect a fluid level within the receiving chamber 112 (which can include the overall volume defined by the wall 113 of the receiving chamber and the vessel cover 130. In particular, the fill sensor 135 can be configured to detect when the coating solution has reached a defined height within the receiving chamber 112 and/o when the coating solution has reached the inner surface of the vessel cover 130. The fill sensor 135 can be operatively connected with the supply pump controller 124 such that the supply pump 120 may be shut off when the desired amount of coating solution has been pumped to the receiving chamber 112 so as to sufficiently coat the substrate 105 therein.
Typically, the coating solution pumped into the receiving chamber 112 will substantially fill the empty volume of the channels and/or pores in the substrate. As it is typically desirable, however, to have open channels with only a washcoat of the coating solution on the channel walls, excess coating solution may be removed from the substrate. In the exemplary embodiments illustrated according to
In the illustrated embodiments, the tail pipe 140 can extend into a collection box 150, which can provide several functions. For example, the collection box 150 can provide a vessel generally in which the coating solution can be collected. In some embodiments, though, it can be particularly useful to facilitate active draining of the coating solution from the coating vessel 110 and the substrate 105, and the collection box 150 can provide an intermediate vessel for application of a vacuum to the system. In one or more embodiments, the collection box 150 can include a suction port 154, which can be in fluid communication with a vacuum pump 162. Preferably, the suction port 154 can be positioned above the outlet 141 of the tail pipe 140 such that negative pressure may be applied through the tail pipe without substantial intake of coating solution to the vacuum pump 162 through the suction port. As illustrated, the collection box 150 further can include mist packing 152, which can be positioned between the outlet 142 of the tail pipe 140 and the suction port 154. The mist packing 152 preferably is air permeable but does not substantially reduce the suction pressure applied to the tail pipe 140 from the vacuum pump 162. Mist packing can be formed from any suitable material, such as natural or synthetic fibers, ceramics, and the like.
In some embodiments, a separator 164 can be between and in fluid connection with the vacuum pump 162 and the suction port 154. The separator 164 can be configured such that any coating solution that may pass through the suction port 154 can be collected therein and thus avoid fouling of the vacuum pump 162.
The system further can include a return pump 170 that is configured to receive the coating solution draining from the coating vessel 110 through the vessel valve. The return pump 170 can be in fluid connection with the collection box 150 (although the pump may be directly connected to the tail pipe 141 or the vessel valve 117 (if desired). As illustrated in
Coating solution collected in the separator 164 can be returned or recycled to the supply source (or other container). For example, the separator 164 can include a spout 166 in fluid connection with the collection box 150, more particularly with the transverse section 155 of the collection box, which specifically can be at a position below the outlet 141 of the tail pipe 140. A valve 168 can be positioned in-line between the spout 166 of the separator 164 and the transverse section 155 of the collection box 150.
In use, a substrate 105 is positioned within the receiving chamber 112 of the coating vessel 110 in order to be coated with a coating solution. For example, a substrate clamp 132 can be configured to moveably engage the substrate 105 for placement within the receiving chamber 112 and optionally for movement from the coating system 100 to one or more further systems/modules where further actions can be taken relative to the substrate (e.g., drying, calcining, etc.). The coating is further illustrated in
The vessel cover 130 is engaging the coating vessel 110, and a gasket 139 is utilized to ensure a fluid-tight engagement. The coating solution 102 is pumped through fluid inlet 115 to fill the lower portion of the coating vessel 110 and contact the substrate. Pumping continues until, as seen in
Because the coating solution 102 is pumped upward through the substrate 105 against gravity, passive draining can be used for removal of the excess coating solution from the substrate and the coating vessel 110. If desired, positive pressure (e.g., pumped air or other gas) may be applied against the top surface 105a of the substrate 105 while still in the coating vessel 110 to assist in removal of excess coating solution 102. For example, pulsed air may be pumped through the vessel cover 130. As such, the vessel cover 130 can also function as a pressure cap. Alternatively, the vessel cover 130 may be removed, and a separate pressure cap 131 may engage the coating vessel so that pulsed air can be applied to the substrate 105 through the pressure cap. In one or more embodiments, the vessel cover 130 can be disengaged from the coating vessel, and negative pressure can be applied to the bottom surface 105b of the substrate 105. Returning to
In
In one or more embodiments, the coating system 100 can include one or more controllers and control elements configured for automated functioning of the system. For example, the coating system 100 can include a controller configured to receive a signal from the fill sensor 135 and send a control signal. In some embodiments, vessel valve controller 118 can be configured to receive a control signal related to a signal from the fill sensor 135, and the vessel valve controller can automatically open and/or close the vessel valve 117. In some embodiments, supply pump controller 124 can be configured to receive a control signal related to a signal from the fill sensor 135, and the supply pump controller 124 can automatically start, stop, increase an output pressure and/or decrease an output pressure of the supply pump 120. The supply pump controller 124 may also automatically open and/or close valve 122. Further, supply pump controller 124 can be configured to receive a pressure reading from pressure sensor 111, and the supply pump controller can automatically increase and/or decrease its output pressure based upon the pressure reading. In some embodiments, such as where a known volume of coating solution is to be pumped to the substrate, the supply pump controller 124 can be configured to automatically start and then stop after pumping of the specific volume of coating solution. As such, one or more flow sensors can be included with the supply pump 120 and/or with the coating vessel 110 and/or in a line between the supply pump and the coating vessel. Although supply pump controller 124 is illustrated as being in direct contact with the supply pump 120, and the vessel valve controller 118 is illustrated as being in direct contact with the vessel valve 117, it is understood that one or both of the respective controllers may be only in electrical connection with the respective element. As further examples, the coating system 100 can include one or more of an actuator controller 138 that can be configured to automatically direct movement of the actuator 137, a vacuum pump controller 161 that can be configured to automatically start, stop, increase vacuum pressure and/or decrease a vacuum pressure of the vacuum pump 162, and a return pump controller 171 that can be configured to automatically start, stop, increase a pump rate and/or decrease pump rate of the return pump 170. Again, although the three respective controllers are illustrated as being in direct contact with their three respective elements, it is understood that one or all of the respective controllers may be only in electrical connection with their respective elements. Moreover, while illustrated separately, it is understood that any two or more of controllers 118, 124, 138, 161, and 171 can be combined as a single controller that can provide the control functions of the combined controllers. In other words, any two or more of the vessel valve, the supply pump, the actuator 138, the vacuum pump 161, and the return pump 171 can be controlled by the same controller
In one or more embodiments, the present disclosure can provide methods for coating a substrate. In particular, the coating methods can be adapted for coating of a low viscosity coating solution. For example, a method for coating a substrate with a low viscosity coating solution can comprise the following steps: positioning a substrate within a receiving chamber of a coating vessel, the receiving chamber being defined by a wall, and the substrate being positioned so as to define a top and a bottom; engaging a vessel cover with the coating vessel to form a fluid-tight engagement; pumping the low viscosity coating solution through a fluid inlet positioned below the receiving chamber at a pressure sufficient to cause the coating solution to enter the receiving chamber, enter the bottom of the substrate, and migrate upward through pores or channels present in the substrate; and opening a vessel valve positioned below the receiving chamber so as to allow a non-coating portion of the low viscosity coating solution to drain from the substrate through the vessel valve and leave a coating portion of the low viscosity coating solution in the pores or channels of the substrate.
More particularly, in some embodiment, the substrate can be moved from a non-coating position to the receiving chamber, such as with the substrate clamp. The non-coating position can be, for example, a weighing station, a drying station, or a further station of a multi-station system for preparing a catalytic substrate.
During coating of the substrate, the coating solution can be pumped until a one or more conditions are met. In some embodiments, pumping can continue until the low viscosity coating solution reaches a pre-defined height in the receiving chamber. For example, pumping can continue until the coating solution reaches a height that substantially corresponds to the top of the substrate. In one or more embodiments, pumping can continue until a fill level control signal from a sensor is sent to a controller indicating that the low viscosity coating solution has sufficiently migrated upward through the pores or channels present in the substrate. For example, a fill level sensor positioned in the vessel cover can provide the fill signal whereby pumping may cease. Upon receipt of the fill level control signal, the controller can execute one or both of the following commands—automatically stop the supply pump that is pumping the low viscosity coating solution through the fluid inlet; and/or automatically open the vessel valve.
Once the coating solution has substantially filled the substrate, a portion of the coating solution will bond with the substrate so as to form a washcoat thereon, and another portion of the coating solution (i.e., the “non-coating” portion) is allowed to drain out of the substrate. The vessel valve can be opened, and the vessel cover optionally can be released, and the coating solution can drain through the vessel valve and pass through the outlet of a tail pipe and into the collection box. In some embodiments, after opening the vessel valve, the non-coating portion of the coating solution can be pumped from the collection box. The coating solution can be pumped directly back to the solution source or to an intermediate storage location. As such, the method can be characterized as recycling the non-coating portion of the coating solution so it can be used for further coating of a substrate. A controller can automatically start the return pump for pumping the non-coating portion of the coating solution, and such automatic control can be carried out at a defined time relative to the opening of the vessel valve.
The non-coating portion of the coating solution can be passively withdrawn—i.e., by draining by gravitational force; however, active withdrawal can also be carried out. For example, withdrawing can comprise drawing a vacuum through the collection box with the vacuum pump. In some embodiments, the controller can automatically start the vacuum pump at a defined time relative to the starting of the return pump. Disengaging the vessel cover from the coating vessel can be carried out at this point so as to sufficiently release the fluid-tight seal. In some embodiments, the controller can automatically disengage the vessel cover from the coating vessel at a defined time relative to starting of the vacuum pump.
In some embodiments, fractions of the non-coating portion of the coating solution can be captured in the separator that is positioned between and in fluid communication with the vacuum pump and the collection box. As such, the method can include emptying a fraction of the non-coating portion of the coating solution collected in the separator into the collection box at a position below the outlet of the tail pipe, such as the transverse portion. Such emptying can be specifically carried out after stopping of the vacuum pump. In exemplary embodiments, further automatic controls can be utilized. For example, a controller can automatically stop the vacuum pump based upon one or both of a sensor output and an algorithm related to flow of the non-coating portion of the low viscosity coating solution. The sensor output may relate to the flow of coating solution through the tail pipe and/or the drawn pressure through the tail pipe and/or the collection box and/or the separator. The algorithm may relate the calculated time for withdrawal of the non-coating portion of the coating solution based upon the calculated volume of total coating solution and the calculated volume of the non-coating portion of the coating solution. As a further example, a controller can automatically open a valve for emptying of the separator at a defined time relative to the stopping of the vacuum pump. In some embodiments, the controller can be configured to automatically open the valve below the separator substantially immediately upon stopping of the vacuum pump, and the controller can automatically close the valve after a defined time (e.g., a time calculated to be necessary for removal of the volume of coating solution present in the separator) or upon a reading from a flow sensor indicating that no further coating solution is present for withdrawal from the separator. As yet a further example, a controller can automatically close the vessel valve based upon one or both of a sensor output and an algorithm related to flow of the non-coating portion of the low viscosity coating solution. In some embodiments, a sensor can be present to indicate when substantially no further coating solution is draining from the coating vessel and/or a sensor can be present to indicate when substantially no further coating solution is moving through the transverse section of the collecting box. In other embodiments, an algorithm can calculate the volume of the non-coating portion of the coating solution that may be withdrawn from the substrate and the coating vessel based upon the total volume of the coating solution pumped from the solution storage tank.
The present methods further can include at least partially drying the coating portion of the low viscosity coating solution that is in the pores or channels of the substrate by carrying out one or more drying steps. Drying may be carried out in the coating vessel. Alternatively or additionally, drying may be carried out in a separate drying vessel. Still further, the present methods can include calcining the substrate with the at least partially dried coating portion of the low viscosity coating solution in the pores or channels thereof. Calcining can be carried out in a further module of a multi-station device, or at least partially dried substrates can be transferred to a separate calcining device.
To further exemplify the present invention, methods of coating a substrate can be carried out according to the flow chart shown in
At 305, the substrate can be positioned within the receiving chamber of the coating vessel. Placement can be carried out with a moveable substrate clamp configured to grasp the substrate, align the substrate with the coating vessel, and lower the substrate into the receiving chamber of the coating vessel.
At 310, the vessel cover is engaged with the coating vessel so as to enclose the substrate within the receiving chamber. In the closed configuration, an interior surface of the vessel cover can define a top wall of the receiving chamber. A side wall and a bottom wall of the coating vessel may define the side wall and bottom wall of the receiving chamber. The bottom wall may have an opening therethrough for in-flow and/or out-flow of coating solution.
At 315, the coating solution can be pumped into the receiving chamber through an inlet that is positioned below the substrate. In this manner, the coating solution flows upward (i.e., against gravity) into the receiving chamber and through the substrate. The pumping pressure of the coating solution can be constant, can be variable, can be ramped up, and/or can be ramped down during the coating step.
At 320, pumping of the coating solution can be discontinued. Discontinuance can be based upon a defined filling amount of the coating solution having been pumped into the receiving chamber and/or into the substrate. In some embodiments, pumping can be discontinued when a fill level sensor indicates that a pre-determined fill level has been achieved. In certain embodiments, pumping can be discontinued when a certain volume of coating solution has been pumped. For example, the solution volume can be calculated based upon the total volume of the receiving chamber and the total open space volume (e.g., channel volume) within the substrate.
At 325, the vessel valve below the receiving chamber can be opened so as to allow for draining of the non-coating portion of the coating solution. More particularly, a coating portion of the coating solution will remain in contact with the surfaces of the walls forming the channels in the substrate, and a non-coating portion of the coating solution will be the portion that further filled the channels but did not adhere to or otherwise bond with the channel wall surfaces. The non-coating portion of the coating solution can be collected in a collecting box. The collecting box can be positioned below the coating vessel, and a tail pipe can extend from the vessel valve into the collecting box.
At 330, the return pump can be engaged to transfer collected coating solution from the collecting box to be recycled. The recycled coating solution can be transferred directly to the main storage unit for the coating solution or may be transferred to an intermediate unit.
At 335, the vacuum pump can be engaged to place a negative pressure on the substrate. The vacuum pump can be in fluid connection with the collecting box so that a negative pressure is formed in the collecting box and thus provide suction pressure at the bottom surface of the substrate (i.e., up through the tail pipe and the vessel valve) so as actively drain the non-coating portion of the coating solution from the substrate.
At 340, the vessel cover can be disengaged from the coating vessel. This can facilitate active withdrawal of the non-coating portion of the coating solution from the substrate.
At 345, the vacuum pump can be disengaged. At this point, there can be substantially no draining of coating solution from the substrate.
At 350, the vessel valve can be closed. No further amount of the coating solution may thus be withdrawn from the receiving chamber.
At 355, the valve below the separator is opened so that any coating solution collected in the separator that is in-line between the vacuum pump and the collecting box may be drained into the collecting box (e.g., the transverse section of the collecting box). Such amount of coating solution is pumped out of the collecting box by the return pump.
At 360, the return pump can be stopped. Any remaining open valves can be closed.
In one or more embodiments, the order of one or more of the above-noted steps may be varied. Moreover, one or more of the steps may be carried out substantially simultaneously. For example, steps 320 and 325 can be performed substantially simultaneously. Likewise, steps 335 and 340 can be performed substantially simultaneously. Further, steps 345 and 350 can be performed substantially simultaneously.
As discussed above, the coating system described herein can be included in a multi-station system for forming a catalyst element. In one or more embodiments, the present disclosure further can provide a modular, multi-station coater system for preparing a catalytic substrate.
As illustrated in
In various embodiments, a substrate may initially be weighed on the raw weight station 410 before any other processing steps to determine a baseline dry weight of the unprocessed substrate for comparison with substrate weights after the deposition of one or more catalytic coatings. The changes in weight may be used to calculate the amount of catalytic material(s) deposited on the walls of the substrate cells, and to determine if the substrate is within specification, while it is a work in progress, rather than a final product that may be out of specification. In various embodiments, the raw weight station 410 and the dry weight station 450 (and any further weight stations that may be utilized) may be a digital scale that may be connected to and in electrical communication with a controller 499 over a communication path 498. The controller 499 may be a computer configured to receive electric signals and/or information, store such received information, perform calculations on received, stored and/or programmed information, and send signals to other components connected to and in electrical communication with a controller over a communication path 498.
In some embodiments, a scale may be operatively associated with the drying station 430 and/or the calcining station 440 to determine the wet weight of a catalytic substrate after the application of the coating liquid to the catalytic substrate. A measure of the additional weight of the catalytic substrate after application of the washcoat may be calculated by the difference between the initial raw weight of the substrate and the wet weight measured by respective scales, to determine whether a correct amount of coating liquid was applied.
In one or more embodiments, a scale may be operatively associated with the calcining station to determine the weight of a catalytic substrate prior to the calcining of the washcoat to the face of the substrate cell walls. Likewise, a scale may be operatively associated with the calcining station to determine if the post-calcining weight falls within intended limits. If it is determined that a catalytic substrate has a weight after calcining that is outside intended limits, the catalytic substrate processing may be interrupted to allow adjustments, calibrations, and/or maintenance before additional substrates that may be out of specification are produced.
In various embodiments, a substrate may be weighed after each processing stage to provide statistical process control and/or process feedback to adjust the various processing parameters (e.g., wet coating viscosity, PGM concentration, ratio of slurry to carrier, drying time, calcining temperature, etc.) at each respective process station. Variations in the process(es) may thereby be followed as multiple substrates are processed by the system, and adjustments made to each of the inline stations and/or out-of-specification substrates removed from the processing sequence before additional time, energy, and expensive materials may be wasted on a defective or otherwise unusable substrate. By correcting deviations in the processing parameters and specifications in real time before a coating or substrate is out-of-specification, scrap may be reduced and the total throughput of the multi-station coater system increased, so at least 25%, 50% or even 100% more finished in-specification catalytic substrates are produced per unit time period (e.g., units per hour) than a coating system that operates in a batch-wise manner (i.e., a block of substrates are completed before testing and/or changes are made to the system).
In one or more embodiments, the substrate may be first weight to establish the raw weight of the substrate for comparison to the substrate weight at further phases of the coating process. The substrate may have a first wet coating introduced into the cells of the substrate by a first coating station 420 to deposit a first catalytic coating (e.g., PGM with or without a support material) over at least a portion of the walls of the cells. In various embodiments, the first coating station 420 may be a coating system as described herein, where the coating solution is pumped into the cells from below the substrate against gravity. The substrate may be dried at first drying station 430 to a desired level of dryness. The wet coating may be dried to remove at least a portion of the carrier fluid prior to being calcined. Removal of a sufficient amount of the carrier fluid allows the catalytic coating portion (i.e., slurry solids) to be retained on the surface(s) of the cells without dripping or running Multiple drying stations may be used. The substrate may be calcined in the first calcining station 440 after the wet coating has been introduced into the substrate and at least partially dried. The catalytic coating may be calcined onto the surface(s) of the cells to provide a substrate with at least a portion of a bottom coat. In various embodiments, calcining of a catalytic coating may drive off remaining carrier fluid, thermally affix the catalytic coating on the cell walls, and/or convert the chemical structure (e.g., phase transition) and/or formula (e.g., chemical decomposition) of at least some of the catalytic coating. The calcined substrate may be weighed on the dry weight station 450 after the catalytic coating has been calcined on the substrate. The actual amount of catalytic coating deposited onto the walls of the cells may be calculated by comparing the initial raw weight of the substrate to the calcined weight of the substrate. The changes in weight may be used to calculate the amount of calcined catalytic material(s) (e.g., PGM and support, metal and molecular sieve, etc.) deposited on the walls of the substrate cells, and to determine if the weight of the calcined substrate is within specification before additional wet coatings are introduced into the substrate (if desired). If the actual amount of catalytic coating is greater or less than the intended amount, an operator may be alerted to the out-of-specification character of the substrate by an alarm, or the substrate may be discharged from the coater system. In various embodiments, an audible and/or visual signal may alert an operator that a substrate is out-of-specification, and/or the substrate may be physically ejected by the transfer mechanism or an ejection mechanism incorporated into or operatively associated with a weight station, where for example the transfer mechanism may open to allow the substrate to fall into a bin or the ejection mechanism is a push bar or air jet that forces a substrate off the scale into a bin.
In one or more embodiments, the present disclosure also can relate to a multi-station system for preparing a catalytic substrate. The system can comprise: at least one catalytic substrate coating station that applies at least one washcoat, also referred to as a wet coating or coating solution, comprising a catalytic slurry and a liquid carrier to at least a portion of the catalytic substrate: at least one drying station that removes at least a portion of the liquid carrier from the at least a portion of the catalytic substrate; at least one calcining station to calcine the catalytic slurry of the washcoat to the cell walls of the catalytic substrate; and a substrate gripper that holds the catalytic substrate and transfers the catalytic substrate between the at least on catalytic substrate coating station, the at least one drying station, and the at least one calcining station.
Further embodiments of a multi-station coater system 500 according to the present embodiment are provided in relation to
A multi-station coating system according to the present disclosure can include any combination of the stations described herein. Further, a multi-station coating system can include further elements, such as those described in U.S. Provisional Patent Application No. 62/140,103, filed Mar. 30, 2015, which is incorporated herein by reference.
The use of the terms “a” and “an” and “the” and similar referents in the context of describing the materials and methods discussed herein (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. 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 materials and methods and does not pose a limitation on the scope unless otherwise claimed. No language in the specification should be construed as indicating any non-claimed element as essential to the practice of the disclosed materials and methods.
Reference throughout this specification to “one embodiment,” “certain embodiments,” “one or more embodiments” or “an embodiment” means that a particular feature, structure, material, or characteristic described in connection with the embodiment is included in at least one embodiment of the invention. Thus, the appearances of the phrases such as “in one or more embodiments,” “in certain embodiments,” “in one embodiment” or “in an embodiment” in various places throughout this specification are not necessarily referring to the same embodiment of the invention. Furthermore, the particular features, structures, materials, or characteristics may be combined in any suitable manner in one or more embodiments.
Although the invention herein has been described with reference to particular embodiments, it is to be understood that these embodiments are merely illustrative of the principles and applications of the present invention. It will be apparent to those skilled in the art that various modifications and variations can be made to the method and apparatus of the present invention without departing from the spirit and scope of the invention. Thus, it is intended that the present invention include modifications and variations that are within the scope of the appended claims and their equivalents.
| Number | Date | Country | |
|---|---|---|---|
| 62264978 | Dec 2015 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | PCT/IB2016/056848 | Nov 2016 | US |
| Child | 16002533 | US |
