COMBINATION ROLL AND DIE COATING METHOD AND APPARATUS WITH IMPROVED DIE LIP

Abstract: A die coating method and apparatus includes a die (40) having an upstream bar (64) with an upstream lip (60) and a downstream bar (66) with a downstream lip (62). The upstream lip is formed as a land (68) and the downstream lip is formed as a sharp edge (70). Coating fluid exists the die (40) from the slot to form a continuous coating bead between the upstream die lip, the downstream die lip, and the surface being coated. A metering roller (332) removes excess coating fluid from the coated web. The apparatus can include a roller (330) on which the coating fluid is initially coated and which contacts a web. A doctor blade (338) or a metering roller removes excess coating fluid from the roller.

Description: COMBINATION ROLL AND DIE COATING METHOD AND APPARATUS WITH IMPROVED DIE LIP TECHNICAL FIELD The present invention relates to coating methods. More particularly, the present invention relates to coating methods using a die. BACKGROUND OF THE INVENTION U.S. Patent No. 2,681,294 discloses a vacuum method for stabilizing the coating bead for direct extrusion and slide types of metered coating systems. Such stabilization enhances the coating capability of these systems. However, these coating systems lack sufficient overall capability to provide the thin wet layers, even at very low liquid viscosities, required for some coated products. U.S. Patent No. 4,445,458 discloses an extrusion type bead-coating die with a beveled draw¬ down surface to impose a boundary force on the downstream side of the coating bead and to reduce the amount of vacuum necessary to maintain the bead. Reduction of the vacuum minimizes chatter defects and coating streaks. To improve coating quality, the obtuse angle of the beveled surface with respect to the slot axis, and the position along the slot axis of the bevel toward the moving web (overhang) and away from the moving web (underhang) must be optimized. The optimization results in the high quality needed for coating photosensitive emulsions. However, the thin-layer performance capability needed for some coated products is lacking. Figure 1 shows a known coating die 10 with a vacuum chamber 12 as part of a metered coating system. A coating liquid 14 is precisely supplied by a pump 16 to the die 10 for application to a moving web 18, supported by a backup roller 20. Coating liquid is supplied through a channel 22 to a manifold 24 for distribution through a slot 26 in the die and coating onto the moving web 18. As shown in Figure 2, the coating liquid passes through the slot 26 and forms a continuous coating bead 28 between the upstream die lip 30 and the downstream die lip 32, and the web 18. Dimensions f 1 and f , the width of the lips 30, 32 commonly range from 0.25 to 0.76 mm. The vacuum chamber 12 applies a vacuum upstream of the bead to stabilize the bead. While this configuration works adequately in many situations, there is a need for a die coating method which improves the performance of known methods. SUMMARY OF THE INVENTION The present invention is a die coating apparatus for coating fluid coating onto a surface. The apparatus includes a die having an upstream bar with an upstream lip and a downstream bar with a downstream lip. The upstream lip is formed as a land and the downstream lip is formed as a sharp edge. A passageway runs through the die between the upstream and downstream bars. The passageway has a slot defined by the upstream and downstream lips, and coating fluid exits the die from the slot to form a continuous coating bead between the upstream die lip, the downstream die lip, and the surface being coated. A metering roller removes excess coating fluid. The bead does not significantly move into the space between the land and the surface to be coated even as vacuum is increased. Alternatively the apparatus can include a roller on which the coating fluid is initially coated and which contacts the web. An excess coating fluid remover removes excess coating fluid from the roller. A die coats the coating fluid onto the roller. The remover can be a doctor blade or a metering roller and the coating liquid on the roller can be kiss transferred to the web. A method of die coating according to the present invention includes passing coating fluid through a slot; improving coating performance by changing at least one of the relative orientations of the land and the sharp edge; removing excess coating fluid from the surface to be coated using a metering roller; selecting the length of the land, the edge angle of the downstream bar, the die attack angle between the downstream bar surface of the coating slot and a tangent plane through a line on the surface to be coated parallel to, and directly opposite, the sharp edge, and the coating gap distance between the sharp edge and the surface to be coated in combination with each other; and selecting the slot height, the overbite, and the convergence in combination with each other. BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a schematic, cross-sectional view of a known coating die. Figure 2 is an enlarged cross-sectional view of the slot and lip of the die of Figure 1. Figure 3 is a cross-sectional view of an extrusion die of the present invention. Figure 4 is an enlarged cross-sectional view of the slot and lip of the die of Figure 4. Figure 5 is a cross-sectional view of the slot and lip similar to that of Figure 4. Figure 6 is a cross-sectional view of an alternative vacuum chamber arrangement. Figure 7 is a cross-sectional view of another alternative vacuum chamber arrangement. Figure 8 is a cross-sectional view of an alternative extrusion die of the present invention. Figures 9a and 9b are enlarged cross- sectional views of the slot, face, and vacuum chamber of the die of Figure 8. Figures 10a and 10b are schematic views of the die of Figure 8. Figure 11 shows coating test results which compare the performance of a known extrusion die and an extrusion die of the present invention for a coating liquid of 1.8 centipoise viscosity. Figure 12 shows comparative test results for a coating liquid of 2.7 centipoise viscosity. Figure 13 is a collection of data from coating tests. Figure 14 is a graph of constant G/Tw lines for an extrusion coating die of the present invention for nine different coating liquids. Figure 15 is a schematic view of a three roll reverse roll coater using the die of the present invention. Figure 16 is schematic view of a two roll reverse roll coater using the die of the present invention. Figure 17 is a schematic view of a gravure coater using the die of the present invention. Figure 18 is a two roll extrusion coater using the die of the present invention. Figures 19a, 19b, and 19c are cross- sectional views of a kiss coater using the die of the present invention. Figures 20a, 20b, and 20c are cross- sectional views of a kiss coater using the die of the present invention. Figure 20d is a cross-sectional view of a kiss coater using the die of Figure 19c. DETAILED DESCRIPTION This invention is a die coating method and apparatus where the die includes a sharp edge and a land which are positioned to improve and optimize performance. The land is configured to match the shape of the surface in the immediate area of coating liquid application. The land can be curved to match a web passing around a backup roller or the land can be flat to match a free span of web between rollers. Figure 3 shows the extrusion die 40 with a vacuum chamber 42 of the present invention. Coating liquid 14 is supplied by a pump 46 to the die 40 for application to a moving web 48, supported by a backup roller 50. Coating liquid is supplied through a channel 52 to a manifold 54 for distribution through a slot 56 and coating onto the moving web 48. As shown in Figure 4, the coating liquid 14 passes through the slot 56 and forms a continuous coating bead 58 among the upstream die lip 60, the downstream die lip 62, and the web 48. The coating liquid can be one of numerous liquids or other fluids. The upstream die lip 60 is part of an upstream bar 64, and the downstream die 62 lip is part of a downstream bar 66. The height of the slot 56 can be controlled by a U- shaped shim which can be made of brass or stainless steel and which can be deckled. The vacuum chamber 42 applies vacuum upstream of the bead to stabilize the coating bead. As shown in Figure 5, the upstream lip 60 is formed as a curved land 68 and the downstream lip 62 is formed as a sharp edge 70. This configuration improves overall performance over that of known die- type coaters. Improved performance means permitting operating at increased web speeds and increased coating gaps, operating with higher coating liquid viscosities, and creating thinner wet coating layer thicknesses. The sharp edge 70 should be clean and free of nicks and burrs, and should be straight within 1 micron in 25 cm of length. The edge radius should be no greater than 10 microns. The radius of the curved land 68 should be equal to the radius of the backup roller 50 plus a minimal, and non-critical, 0.13 mm allowance for coating gap and web thickness. Alternatively, the radius of the curved land 68 can exceed that of the backup roller 50 and shims can be used to orient the land with respect to the web 48. A given convergence C achieved by a land with the same radius as the backup roller can be achieved by a land with a larger radius than the backup roller by manipulating the land with the shims. Figure 5 also shows dimensions of geometric operating parameters for single layer extrusion. The length Li of the curved land 68 on the upstream bar 64 can range from 1.6 mm to 25.4 mm. The preferred length Li is 12.7 mm. The edge angle Ai of the downstream bar 66 can range from 20° to 75°, and is preferably 60°. The edge radius of the sharp edge 70 should be from about 2 microns to about 4 microns and preferably less than 10 microns. The die attack angle A 2 between the downstream bar 66 surface of the coating slot 56 and the tangent plane P through a line on the web 48 surface parallel to, and directly opposite, the sharp edge 70 can range from 60° to 120° and is preferably 90°-95°, such as 93°. The coating gap Gi is the perpendicular distance between the sharp edge 70 and the web 48. (The coating gap Gi is measured at the sharp edge but is shown in some Figures spaced from the sharp edge for drawing clarity. Regardless of the location of G in the drawings - and due to the curvature of the web the gap increases as one moves away from the sharp edge - the gap is measured at the sharp edge.) Slot height H can range from 0.076 mm to 3.175 mm. Overbite 0 is a positioning of the sharp edge 70 of the downstream bar 66, with respect to the downstream edge 72 of the curved land 68 on the upstream bar 64, in a direction toward the web 48. Overbite also can be viewed as a retraction of the downstream edge 72 of the curved land 68 away from the web 48, with respect to the sharp edge 70, for any given coating gap Gj.. Overbite can range from 0 mm to 0.51 mm, and the settings at opposite ends of the die slot should be within 2.5 microns of each other. A precision mounting system for this coating system is required, for example to accomplish precise overbite uniformity. Convergence C is a counterclockwise, as shown in Figure 5, angular positioning of the curved land 68 away from a location parallel to (or concentric with) the web 48, with the downstream edge 72 being the center of rotation. Convergence can range from 0° to 2.29°, and the settings at opposite ends of the die slot should be within 0.023° of each other. The slot height, overbite, and convergence, as well as the fluid properties such as viscosity affect the performance of the die coating apparatus and method. From an overall performance standpoint, for liquids within the viscosity range of 1,000 centipoise and below, it is preferred that the slot height be 0.18 mm, the overbite be 0.076 mm, and the convergence be 0.57°. Performance levels using other slot heights can be nearly the same. Performance advantages can also be found at viscosities above 1,000 centipoise. Holding convergence at 0.57°, some other optimum slot height and overbite combinations are as follows: Slot Height Overbite 0.15 mm 0.071 mm 0.20 mm 0.082 mm 0.31 mm 0.100 mm 0.51 mm 0.130 mm In the liquid viscosity range noted above, and for any given convergence value, the optimum overbite value appears to be directly proportional to the square root of the slot height value. Similarly, for any given slot height value, the optimum overbite value appears to be inversely proportional to the square root of the convergence value. As shown in Figure 6, the vacuum chamber 42 can be an integral part of, or clamped to, the upstream bar 64 to allow precise, repeatable vacuum system gas flow. The vacuum chamber 42 is formed using a vacuum bar 74 and can be connected through an optional vacuum restrictor 76 and a vacuum manifold 78 to a vacuum source channel 80. A curved vacuum land 82 can be an integral part of the upstream bar 64, or can be part of the vacuum bar 74, which is secured to the upstream bar 64. The vacuum land 82 has the same radius of curvature as the curved land 68. The curved land 68 and the vacuum land 82 can be finish-ground together so they are "in line" with each other. The vacuum land 82 and the curved land 68 then have the same convergence C with respect to the web 48. The vacuum land gap G 2 is the distance between the vacuum land 82 and the web 48 at the lower edge of the vacuum land and is the sum total of the coating gap Gi, the overbite 0, and the displacement caused by convergence C of the curved land.68. (Regardless of the location of Gi in the drawings the gap is the perpendicular distance between the lower edge of the vacuum land and the web.) When the vacuum land gap G 2 is large, an excessive inrush of ambient air to the vacuum chamber 42 occurs. Even though the vacuum source may have sufficient capacity to compensate and maintain the specified vacuum pressure level at the vacuum chamber 42, the inrush of air can degrade coating performance. In Figure 7, the vacuum land 82 is part of a vacuum bar 74 which is attached to the upstream bar 64. During fabrication, the curved land 68 is finished with the convergence C "ground in." The vacuum bar 74 is then attached and the vacuum land 82 is finish ground, using a different grind center, such that the vacuum land 82 is parallel to the web 48, and the vacuum land gap G 2 is equal to the coating gap Gi when the desired overbite value is set. The vacuum land length L 2 may range from 6.35 mm to 25.4 mm. The preferred length L 2 is 12.7 mm. This embodiment has greater overall coating performance capability in difficult coating situations than the embodiment of Figure 6, but it is always finish ground for one specific set of operating conditions. So, as coating gap Gi or overbite O are changed vacuum land gap G may move away from its optimum value. In Figures 8 and 9 the upstream bar 64 of the die 40 is mounted on an upstream bar positioner 84, and the vacuum bar 74 is mounted on a vacuum bar positioner 86. The curved land 68 on the upstream bar 64 and the vacuum land 82 on the vacuum bar 74 are not connected directly to each other. The vacuum chamber 42 is connected to its vacuum source through the vacuum bar 74 and the positioner 86. The mounting and positioning for the vacuum bar 74 are separate from those for the upstream bar 64. This improves performance of the die and allows precise, repeatable vacuum system gas flow. The robust configuration of the vacuum bar system also aids in the improved performance as compared with known systems. Also, this configuration for the vacuum bar 74 could improve performance of other known coaters, such as slot, extrusion, and slide coaters. A flexible vacuum seal strip 88 seals between the upstream bar 64 and the vacuum bar 74. The gap G between the vacuum land 82 and the web 48 is not affected by coating gap Gi, overbite 0, or convergence C changes, and may be held at its optimum value continuously, during coating. The vacuum land gap G 2 may be set within the range from 0.076 mm to 0.508 mm. The preferred value for the gap G 2 is 0.15 mm. The preferred angular position for the vacuum land 82 is parallel to the web 48. During coating, the vacuum level is adjusted to produce the best quality coated layer. A typical vacuum level, when coating a 2 centipoise coating liquid at 6 microns wet layer thickness and 30.5 m/min web speed, is 51 mm H 2 0. Decreasing wet layer thickness, increasing viscosity, or increasing web speed could require higher vacuum levels exceeding 150 mm H 2 0. Dies of this invention exhibit lower satisfactory minimum vacuum levels and higher satisfactory maximum vacuum levels than known systems, and in some situations can operate with zero vacuum where known systems cannot. Figures 10a and 10b show some positioning adjustments and the vacuum chamber closure. Overbite adjustment translates the downstream bar 66 with respect to the upstream bar 64 such that the sharp edge 70 moves toward or away from the web 48 with respect to the downstream edge 72 of the curved land 68. Adjusting convergence rotates the upstream bar 64 and the downstream bar 66 together around an axis running through the downstream edge 72, such that the curved land 68 moves from the position shown in Figure 10, away from parallel to the web 48, or back toward parallel. Coating gap adjustment translates the upstream bar 64 and the downstream bar 66 together to change the distance between the sharp edge 70 and the web 48, while the vacuum bar remains stationary on its mount 86, and the vacuum seal strip 88 flexes to prevent air leakage during adjustments. Air leakage at the ends of the die into the vacuum chamber 42 is minimized by end plates 90 attached to the ends of the vacuum bar 74 which overlap the ends of the upstream bar 64. The vacuum bar 74 is 0.10 mm to 0.15 mm longer than the upstream bar 64, so, in a centered condition, the clearance between each end plate 90 and the upstream bar 64 will range from 0.050 mm to 0.075 mm. One unexpected operating characteristic has been observed during coating. The bead does not move significantly into the space between the curved land 68 and the moving web 48, even as vacuum is increased. This allows using higher vacuum levels than is possible with known extrusion coaters, and provides a correspondingly higher performance level. Even where little or no vacuum is required, the invention exhibits improved performance over known systems. That the bead does not move significantly into the space between the curved land 68 and the web 48 also means that the effect of "runout" in the backup roller 50 on downstream coating weight does not differ from that for known extrusion coaters. Figure 11 graphs results of coating tests which compare the performance of a known extrusion die with an extrusion die of this invention. In the tests, the 1.8 centipoise coating liquid containing an organic solvent was applied to a plain polyester film web. The performance criterion was minimum wet layer thickness at four different coating gap levels for each of the two coating systems, over the speed range of 15 to 60 m/min. Curves A, B, C, and D use the known, prior art die and were performed with coating gaps of 0.254 mm, 0.203 mm, 0.152 mm, and 0.127 mm, respectively. Curves E, F, G, and H use a die according to this invention at the same respective coating gaps. The lower wet thickness levels for this invention, compared to the prior art die, are easily visible. Figure 12 shows comparative test results for a similar coating liquid of 2.7 centipoise viscosity, at the same coating gaps. Once again, the performance advantage for this invention is clearly visible. Figure 13 is a collection of data from coating tests where liquids at seven different viscosities, and containing different organic solvents, were applied to plain polyester film webs. The results compare performance of the prior art extrusion coater (PRIOR) and this invention (NEW) . The performance criteria are mixed. Performance advantages for this invention can be found in web speed (Vw) , wet layer thickness (Tw) , coating gap, vacuum level, or a combination of these. One measure of coater performance is the ratio of coating gap to wet layer thickness (G/Tw) , for a particular coating liquid and web speed. Figure 14 shows a series of constant G/Tw lines and viscosity values of an extrusion die of this invention, for nine different coating liquids. The liquids were coated on plain polyester film base at a web speed of 30.5 m/min. A few viscosity values appear to be out of order, due to the effect of other coatability factors. Four additional performance lines have been added after calculating the G/Tw values for 30.5 m/min web speed from Figures 11 and 12. From top to bottom, the solid performance lines are the G/Tw for liquids of 2.7 centipoise and 1.8 centipoise coated by a known extrusion die and the G/Tw for liquids of 2.7 centipoise and 1.8 centipoise coated by an extrusion die of this invention. The lines for of this invention represent greater G/Tw values than the lines for of the prior art coating die. In addition, the lines for this invention are close to being lines of constant G/Tw, averaging 18.8 and 16.8, respectively. The lines of the known coater show considerably more G/Tw variation over their length. This invention has a much improved operating characteristic for maintaining a coating bead at low wet thickness values, over known systems. Coating dies of this invention can be used as high performance liquid feed devices for roll and kiss coaters. Figure 15 shows a three roll reverse roll coater using an extrusion die 40 to feed coating liquid 14 to a casting roller 330. Because the surface of the casting roller 330 passes the die 40 in a downward direction, the die 40 is inverted and the vacuum chamber 42 is above the slot and the coating bead. This does not affect coating performance. A metering roller 332 removes excess coating liquid, leaving a precise layer on the casting roller 330. A doctor blade 334 removes the excess coating liquid from the metering roller 332 and drops it into a liquid return pan 336 for recirculation. Meanwhile, a bead-splitting action transfers part of the coating liquid from the casting roller 330 to the web 48 moving around the backup roller 50. After the bead splits, a second doctor blade 338 cleans the remaining coating liquid from the casting roller 330 and runs it into the recirculation pan 336. Alternatively, the backup roller 50 can be rubber covered so the casting roller 330 can contact the web and transfer all of the coating liquid in this area to the web. The second doctor blade 338 would then clean any liquid from the casting roller 330 which is outside of the web width. Figure 16 shows a two roll reverse roll coater using an extrusion die 40 to feed coating liquid to the surface of the web 48 moving around the backup roller 14, which is a wrapped casting roller. The metering roller 332 removes excess coating liquid from the surface of the web 48, leaving the desired, precise wet coated layer. The doctor blade 334 cleans the excess coating liquid from the metering roller 332 and runs it into the recirculation pan 336. Use of this system in one example increased the vacuum window from 5.08 mm to over 254 mm H 0, and increased the liquid feed coating gap from 0.10 mm to 0.36 mm, thereby improving stability and practically eliminating streaking. Figure 17 shows a gravure coater using an extrusion die 40 to feed coating liquid to the surface of a knurled roller 340. The die 40 has its vacuum chamber 42 above its coating slot. A doctor blade 342 removes excess coating liquid from the knurl pattern so that the desired amount transfers to the web 48 moving around the rubber-covered backup roller 314. The excess coating liquid recirculates through the pan 336. This method of feeding coating liquid to the surface of a knurled roller can also be used for other forms of gravure coating such as reverse, offset, and differential. Figure 18 shows a two roll extrusion coater using an extrusion die 40 to feed coating liquid to the surface of the casting roller 330, with stability from the vacuum chamber 42. The layer of coating liquid is thin and precise so that a metering roll is not required. The bead split takes place directly to the web 48 moving around the backup roller 314. A doctor blade 338 removes the coating excess liquid from the casting roller 330 and recirculates it through the pan 336. Alternatively, the backup roller 50 can be rubber covered so the casting roller 330 can contact the web and transfer all of the coating liquid in this area to the web. The second doctor blade 338 would then clean any liquid from the casting roller 330 which is outside of the web width. Figure 19a shows a kiss coater where an extrusion die 40 feeds coating liquid through a manifold 54 and a slot 56 to a transfer roller 344 such as a spindle having a diameter ranging from 25.4 mm to 50.8 mm. The coating bead is stabilized by the vacuum chamber 42. The coating liquid on the transfer roller 344 is kiss transferred to form the coated layer on the web 48. The small diameter transfer roller 344 has a small kiss transfer area, and improves web stability over that with a larger transfer roller by reducing web flutter and cross tension marks. The surface of the transfer roller 344 can be, for example, smooth, polished, medium grind, grit blasted, or knurled. Figure 19b shows a kiss coater where the extrusion die 40 with a vacuum chamber 42 feeds coating liquid to the surface of a kiss transfer roller 344. The roller 344 has a larger diameter than the spindle of Figure 19a. The coating liquid is kiss transferred to form the coated layer on the web 48. Figure 19c shows a kiss coater where a slide coating die 310 feeds coating liquid to the surface of a kiss transfer roller 344. The coating liquid is kiss transferred to form the coated layer on the web 48. Figure 20a shows a kiss coater where a dual- layer extrusion die 100 feeds two coating liquids 116, 124 through channels 118, 126 to the surface of a spindle, such as a transfer roller 344 having a diameter ranging from 25.4 mm to 50.8 mm. The two coating liquids on the transfer roller 344 are transferred to form two coated layers on the web 48. Figure 20b shows a kiss coater where a dual- layer extrusion die 100 feeds coating liquid to a kiss transfer roller. The roller 344 has a larger diameter than the roller of Figure 20a. Two coating liquids 116, 124 are fed through two separate manifolds and two separate slots to meet at the coating bead. The two coating liquids are transferred to the web forming wet coated layers. Figure 20c shows a kiss coater where a dual- layer extrusion die 100 feeds coating liquid to a kiss transfer roller 344. The two coating liquids 116, 124 are fed through two manifolds, but only one slot, meeting inside the die. The two coating liquids on the surface of the transfer roller 344 are transferred to form the two coated layers on the web 48. Figure 20d shows a kiss coater where a multiple layer coating version of the die 220 of Figure 19c feeds four coating liquids onto the surface of the transfer roller 344. Four liquids 116, 124, 346, 348 are fed through the die 100, down slide surfaces 236 to form four layers on the surface of the transfer roller 344. These layers are transferred to form four coated layers on the web 48.

Claims: CLAIMS 1. A die coating apparatus for coating fluid coating onto a web moving around a backup roller comprising: a die 40 having an upstream bar 64 with an upstream lip 60 and a downstream bar 66 with a downstream lip 62, wherein the upstream lip is formed as a land 68 and the downstream lip is formed as a sharp edge 70; a passageway 52 running through the die between the upstream and downstream bars 64, 66, wherein the passageway comprises a slot 56 defined by the upstream and downstream lips 60, 62, wherein coating fluid exits the die from the slot to form a continuous coating bead between the upstream die lip, the downstream die lip, and a surface being coated; and a metering roller 332 which removes excess coating fluid from the surface being coated. 2. A die coating apparatus for coating fluid coating onto a web comprising: a roller 330 on which the coating fluid is initially coated and which subsequently transfers the coating fluid to the web; means 338 for removing excess coating fluid from the roller wherein the removing means contacts the roller 330 to remove excess coating fluid; a die 40 for coating the coating fluid onto the roller 330 and having an upstream bar 64 with an upstream lip 60 and a downstream bar 66 with a downstream lip 62, wherein the upstream lip is formed as a land 68 and the downstream lip is formed as a sharp edge 70; and a passageway 52 running through the die between the upstream and downstream bars 64, 66, wherein the passageway comprises a slot 56 defined by the upstream and downstream lips 60, 62, wherein coating fluid exits the die from the slot to form a continuous coating bead between the upstream die lip, the downstream die lip, and the surface being coated. 3. The apparatus of claim 2 wherein the removing means 338 comprises a doctor blade. 4. The apparatus of claim 2 wherein the removing means comprises a metering roller 332. 5. The apparatus of claim 3 wherein the coating liquid on the roller is kiss transferred to the web 48. 6. A method of die coating comprising: passing coating fluid through a slot 56 defined by an upstream bar 64 with an upstream lip 60 and a downstream bar 66 with a downstream lip 62, wherein the upstream lip is formed as a land 68 and the downstream lip is formed as a sharp edge 70; improving coating performance by changing the orientation of one of the land 68 and the sharp edge 70; removing excess coating fluid from the surface to be coated using a metering roller 332 which contacts the surface to be coated; selecting a length L of the land, an edge angle Ai of the downstream bar, a die attack angle A 2 between the downstream bar surface of the coating slot and a tangent plane through a line on the surface to be coated parallel to and directly opposite the sharp edge, and a coating gap distance G between the sharp edge and the surface to be coated in combination with each other; and selecting a slot height H, an overbite 0, and a convergence C in combination with each other. 7. The method of claim 6 further comprising the step of applying a vacuum upstream of a formed coating bead to stabilize the bead, wherein the bead does not significantly move into the space between the land and the surface to be coated even as vacuum is increased.

Inventors: BROWN OMAR D, MAIER GARY W, BROWN, OMAR, D., MAIER, GARY, W.
Applicants: MINNESOTA MINING & MFG, MINNESOTA MINING AND MANUFACTURING COMPANY
Application year: 1995
Main classification: B05C5
IPC codes: B05C1, B05C5, B05C9