Patent Grant
7279042
This invention relates to devices and methods for coating substrates and for improving the uniformity of non-uniform or defective coatings.
There are many known methods and devices for coating a moving web and other fixed or moving substrates. Several are described in Booth, G. L., “The Coating Machine”, Pulp and Paper Manufacture, Vol. 8, Coating, Converting and Processes, pp 76-87 (Third Edition, 1990). For example, gravure roll coaters (see, e.g. U.S. Pat. No. 5,620,514) can provide relatively thin coatings at relatively high run rates. Attainment of a desired specific average caliper usually requires several trials with gravure rolls of different patterns. Runtime factors such as variations in doctor blade pressure, coating speed, temperature, or liquid viscosity can cause overall coating weight variation and uneven localized caliper in the machine or transverse directions.
Barmarks and chatter marks are bands of light on heavy coating extending across the web. These are regarded as defects, and can be caused by factors such as vibration, flow pulsation, web speed oscillation, gap variation and roll drive oscillation. Chatter marks are commonly periodic, but barmarks can occur as the result of random system upsets. Gutoff and Cohen, Coating and Driving Defects (John Wiley & Sons, New York, 1995) discusses many of the sources of cross web marks and emphasizes their removal by identifying and eliminating the fundamental cause. This approach can require substantial time and effort.
Multiple lane coaters include those shown in U.S. Pat. Nos. 3,920,862; 5,599,602; 5,733,608 and 5,871,585. Gravure coating can also be used to produce down web lanes of a single formulation at a coating station, by using spaced circumferential patterns on the gravure roll or circumferential undercuts on the web back up roll. However, due to intermixing that occurs at the nip, abutting lanes of different formulations can not be applied from the same gravure roll.
Under some gravure roll coating run conditions, a gravure roll pattern appears in the wet coating. Gravure roll marks can be removed with an arcuate flexible smoothing film located down web from the gravure roll (see, e.g., U.S. Pat. No. 5,447,747); with a smoothing roll or rolls bearing against an intermediate coating roll (see, e.g., U.S. Pat. No. 4,378,390) or with a set of smoothing rolls located down web from the gravure roll (see, e.g., U.S. Pat. No. 4,267,215). In Examples 1-7 and 10 of the '215 patent, a continuous coating was applied to a plastic film and subsequently contacted by an undriven corotating stabilizing roll 68 and a set of three equal diameter counter rotating spreading rolls 70. The respective diameters of the stabilizing roll and spreading rolls are not disclosed but appear from the Drawing to stand in a 2:1 ratio. In Example 10 of the '215 patent, the applicator roll speed was increased until the uniformity of the coating applied to the web began to deteriorate (at a peripheral applicator roll speed of 0.51 m/s) and surplus coating liquid began to accumulate on the web surface upstream of the rolls 70 (at a peripheral applicator roll speed of 0.61 m/s). Coatings having thicknesses down to 1.84 micrometers were reported.
Several coaters having brush or roller smoothing devices are also shown in the above-mentioned Booth article.
Very thin coatings (e.g., about 0.1 to about 5 micrometers) can be obtained on gravure roll coaters by diluting the coating formulation with a solvent. Solvents are objectionable for health, safety, environmental and cost reasons.
Multiroll coaters (see, e.g., U.S. Pat. Nos. 2,105,488; 2,105,981; 3,018,757; 4,569,864 and 5,536,314) can also be used to provide thin coatings. Multiroll coaters are shown by Booth and are reviewed in Benjamin, D. F., T. J. Anderson, and L. E. Scriven, “Multiple Roll Systems: Steady-State Operation”, AIChE J., V41, p. 1045 (1995); and Benjamin, D. F., T. J. Anderson, and L. E. Scriven, “Multiple Roll Systems: Residence Times and Dynamic Response”, AIChE J., V41, p. 2198 (1995). Commercially available forward-roll transfer coaters typically use a series of three to seven counter rotating rolls to transfer a coating liquid from a reservoir to a web via the rolls. These coaters can apply silicone release liner coatings at wet coating thickness as thin as about 0.5 to about 2 micrometers. The desired coating caliper and quality are obtained by artfully setting roll gaps, roll speed ratios and nipping pressures.
U.S. Pat. No. 4,569,864 describes a coating device in which a thick, continuous premetered coating is applied by an extrusion nozzle to a first rotating roll and then transferred by one or more additional rolls to a faster moving web. The extrusion nozzle is placed very close to the first roll (e.g., 25 to 50 micrometers) in order to obtain an even and smoothly distributed coating on the first roll.
U.S. Pat. No. 5,460,120 describes a coating device in which a coating is spray-applied to the underside of a moving web immediately upstream from a resilient, compressible, saturable applicator.
Electrostatic spray coating devices (see, e.g., U.S. Pat. Nos. 4,748,043; 4,830,872; 5,326,598; 5,702,527 and 5,954,907) atomize a liquid and deposit the atomized droplets assisted by electrostatic forces. In some applications the desired coating thickness is larger than the droplet diameter and the droplets just land on top of each other and coalesce to form the coating. In other applications the desired coating thickness is smaller than the droplet diameter. For these thin film coatings a solvent can be used, but if a solventless coating is desired, then the drops must land on the web some distance apart from each other in order to satisfy the small volume requirement of the thin film coating. Then the droplets must spread in order to merge into a continuous voidless coating. Spreading takes time and can be a rate-limiting step for these electrostatic spray coating processes. If the surface chemistry is such that the liquid does not sufficiently spread on the substrate in the available time before cure or hardening, then voids will remain in the coating.
The present invention provides, in one aspect, a method for improving the uniformity of a wet coating on a substrate comprising contacting the coating at a first position with wetted surface portions of:
The invention also provides a method for applying a coating to a substrate comprising applying to the substrate an uneven wet coating, contacting the coating at a first position with wetted surface portions of:
In another aspect, the invention provides a method for coating at least one lane comprising at least one coating on a substrate, and for optionally abutting more than one of such lanes without substantial intermixing of the coatings in the lanes.
The invention also provides devices for carrying out such methods. In one aspect, the devices of the invention comprise an improvement station comprising two or more pick-and-place devices that can periodically contact and re-contact a wet coating at different positions on a substrate, wherein the periods of the devices are selected so that the uniformity of the coating is improved. In a preferred embodiment, the improvement station comprises three or more rolls having different rotational periods. In another aspect, the devices comprise a coating apparatus for applying an uneven (and preferably discontinuous) coating to a substrate and an improvement station comprising two or more of the above-mentioned pick-and-place devices for contacting and re-contacting the coating at different positions on the substrate whereby the coating becomes more uniform on the substrate. In yet a further aspect, the invention provides an apparatus comprising a coating station for applying an uneven (and preferably discontinuous) coating to a first substrate, an improvement station comprising two or more of the above-mentioned pick-and-place devices for contacting and re-contacting the coating at different positions on the first substrate whereby the coating becomes more uniform on such first substrate, and a transfer station for transferring the uniform coating from the first substrate to a second substrate. In a further aspect, this latter apparatus comprises a coating station that coats at least one lane on said first substrate and a transfer station that transfers such lane to said second substrate.
The methods and devices of the invention also facilitate much more rapid drying of wet coatings on a substrate. Thus in a further aspect, the methods of the invention further comprise drying the coating, and the devices of the invention include a drying station having a plurality of pick-and-place devices that contact and re-contact a substrate having an uneven wet coating, whereby the pick-and place devices increase the drying rate of the coating.
The methods of the invention can provide extremely uniform coatings and extremely thin coatings, at very high rates of speed. The devices of the invention are simple to construct, set up and operate, and can easily be adjusted to alter the coating thickness.
a is a top view of abutting cross web stripes on a web.
b is a top view of abutting lanes on the web of
a is a top view of separated cross web stripes on a web.
b is a top view of lanes on the web of
Referring to
A type of pick-and-place device 15 that can be used in the present invention to improve a coating on a moving web 10 is shown in
The period of a pick-and-place device can be expressed in terms of the time required for the device to pick up a portion of wet coating from one position along a substrate and then lay it down on another position, or by the distance along the substrate between two consecutive contacts by a surface portion of the device. For example, if the device shown in
Many different mechanisms can produce a periodic contact with the liquid coated substrate, and many different shapes and configurations can be used to form the pick-and-place devices. For example, a reciprocating mechanism (e.g., one that moves up and down) can be used to cause the coating-wetted surfaces of a pick-and-place device to oscillate into and out of contact with the substrate. Preferably the pick-and-place devices rotate, as it is easy to impart a rotational motion to the devices and to support the devices using bearings or other suitable carriers that are relatively resistant to mechanical wear.
Although the pick-and-place device shown in
The invention is especially useful for, but not limited to, coating moving webs. Rotating pick-and-place devices are preferred for such coating applications. The devices can translate (e.g., rotate) at the same peripheral speed as the moving web, or at a lesser or greater speed. If desired, the devices can rotate in a direction opposite to that of the moving web. Preferably, at least two of the rotating pick-and-place devices have the same direction of rotation and are not periodically related. More preferably, for applications involving the improvement of a coating on a web or other substrate having a direction of motion, the direction of rotation of at least two such pick-and-place devices is the same as the direction of substrate motion. Most preferably, such pick-and-place devices rotate in the same direction as and at substantially the same speed as the substrate. This can conveniently be accomplished by using corotating undriven rolls that bear against the substrate and are carried with the substrate in its motion.
When initially contacting the coating with a pick-and-place device like that shown in
There is no guarantee that the liquid split ratio between the web and the surface will remain always at a constant value. Many factors can influence the split ratio, but these factors tend to be unpredictable. If the split ratio changes abruptly, a periodic down web caliper variation will result even if the pick-and-place device has been running for a long time. If foreign material lodges on a transfer surface of the pick-and-place device, the device may create a periodic down web defect at each contact. Thus use of only a single pick-and-place device can potentially create large lengths of scrap material.
The invention employs two or more, preferably three or more, and more preferably five or more or even eight or more pick-and-place devices in order to achieve good coating uniformity. When coating a moving web, these devices can be arranged down web from a coating station in an array that will be referred to as an “improvement station.” After the coating liquid on the pick-and-place transfer surfaces has built to an equilibrium value, a random high or low coating caliper spike may pass through the station. When this happens, and if the defect is contacted, then the periodic contacting of the web by a single pick-and-place device, or by an array of several pick-and-place devices having the same contact period, will repropagate a periodic down web defect in the caliper. Again scrap will be generated and those skilled in coating would avoid such an apparatus. It is much better to have just one defect in a coated web rather than a length of web containing multiple images of the original defect.
We have discovered that more than one pick-and-place device can produce improved coating uniformity instead of extended lengths of defective coating. A single device, or a train of devices having identical or reinforcing periods of contact, can be very detrimental. However, we have found that a random initial defect entering the station or any defect generated by the first contacting can be diminished by using an improvement station comprising more than two pick and place devices whose periods of contact are selected to reduce rather than repropagate the defect. We have found that such an improvement station can diminish input defects to such an extent that the defects are no longer objectionable. By using the methods and devices of the invention, a new down web coating profile can be created at the exit from the improvement station. That is, by using multiple pick-and-place devices we can modify the multiple defect images that are propagated and repropagated by the first device with additional multiple defect images that are propagated and repropagated from the second and any subsequent devices. We can do this in a constructively and destructively additive manner so that the net result is near uniform caliper or a controlled caliper variation. We in effect create multiple waveforms that are added together in a manner so that the constructive and destructive addition of each waveform combines to produce a desired degree of uniformity. Viewed somewhat differently, when a coating upset passes through the improvement station a portion of the coating from the high spots is in effect picked off and placed back down in the low spots.
Mathematical modeling of our new improvement process is helpful in gaining insight and understanding. The modeling is based on fluid dynamics, and provides good agreement to observable results.
Similar coating improvement results are obtained when the random defect is a depression (e.g., an uncoated void) or bar mark rather than a spike.
The random spike and depression defects discussed above are one general class of defect that may be presented to the improvement station. The second important class of defect is a periodically repeating defect. Of course, in manufacturing coating facilities it is common to have both classes occurring simultaneously. If a periodic train of high or low coating spikes or depressions is present on a continuously running web, the coating equipment operators usually seek the cause of the defect and try to eliminate it. A single periodic pick-and-place device as illustrated in
Referring for the moment to pick-and place roll 112, the liquid coating splits at lift off point 119. A portion of the coating travels onward with the web and the remainder travels with roll 112 as it rotates away from lift off point 119. Variations in coating caliper just prior to lift off point 119 are mirrored in both the liquid caliper on web 111 and the liquid caliper on the surface of roll 112 as web 111 and roll 112 leave lift off point 119. After the coating on web 111 first contacts roll 112 and roll 112 has made one revolution, the liquid on roll 112 and incoming liquid on web 111 meet at the initial contact point 118, thereby forming a liquid filled nip region 126 between points 118 and 119. Region 126 is without air entrainment. To a fixed observer, the flow rate of the liquid entering this nip contact region 126 is the sum of the liquid entering on the web 111 and the liquid entering on the roll 112. The net action of roll 112 is to pick material from web 111 at one position and place a portion of the material down again at another position.
In a similar fashion, the liquid coating splits at lift off points 121, 123 and 125, and a portion of the coating re-contacts web 111 at contact points 120, 122 and 124 and is reapplied thereto.
As with the trains of intermittent pick-and-place contacting devices discussed above, random or periodic variations in the liquid coating caliper on the incoming web will be reduced in severity and desirably the variations will be substantially eliminated by the pick-and-place action of the periodic contacting rolls. Also, as with the devices discussed above, a single roll running in contact with the liquid coating on the web, or a train of periodically related rolls, will generally tend to propagate defects and produce large amounts of costly scrap.
By using multiple devices and properly selecting their periods of contact, we can substantially improve the quality of even a grossly non-uniform input coating.
Factors such as drying, curing, gellation, crystallization or a phase change occurring with the passage of time can impose limitations on the number of rolls employed. If the coating liquid contains a volatile component, the time necessary to translate through many rolls may allow drying to proceed to the extent that the liquid may solidify. Drying is actually accelerated by our invention, providing certain advantages discussed in more detail below. In any event, if a coating phase change occurs on the rolls for any reason during operation of the improvement station, this will usually lead to disruptions and patterns in the coating on the web. Therefore, in general we prefer to produce the desired degree of coating uniformity using as few rolls as possible.
By using multiple pick-and-place rolls we can simultaneously reduce the amplitude of and merge successive spikes or depressions together to form a continuously slightly varying but spike- and depression-free coating of good uniformity. As shown in
A recommended procedure for determining a set of pick-and-place roll diameters and therefore their periods is as follows. First, measure the down web coating weight continuously and determine the period, P, of the input of an undesired periodic defect to the improvement station. Then select a series of pick-and-place roll diameters with periods ranging from less than to larger than the input period avoiding integer multiples or divisors of that period. From this group, determine which roll gives the best improvement in uniformity by itself alone. From the remaining group, select a second roll that gives the best improvement in uniformity when used with the first selected roll. After the first two rolls are determined, continue adding additional pick-and-place rolls one by one on the basis of which of those available gives the best improvement. The best set of rolls is dependent upon the uniformity criterion used and the initial unimproved down web variation present. Our preferred starting set of rolls include those with periods, Q, ranging from Q=0.26 to 1.97 times the period of the input defect, in increments of 0.03. Exceptions are Q=0.5, 0.8, 1.1, 1.25, 1.4, and 1.7. Periods of (Q+nP) and (Q+kP) where n is an integer and k=1/n are also suggested.
Belt 170 circulates past undriven corotating pick-and-place rolls 174, 176 and 178 having respective relative diameters of, for example, 1.36, 1.26 and 1, thereby bringing the lengthwise variable coating into contact with the surfaces of pick-and-place rolls 174, 176 and 178 at the liquid-filled nip regions 183, 184 and 185. Following startup of the equipment and a few rotations of belt 170, the coating liquid wets the surfaces of the pick-and-place rolls 174, 176 and 178. As with the device shown in
The embodiment of
As with direct web coating, when the amount of liquid necessary for the desired average coating caliper is applied intermittently to wet belt 170, the period and number of pick-and-place rolls preferably is chosen to accommodate the largest spacing between any two adjacent, down web deposits of coating. As with direct web coating, a significant advantage of our method is that it is often easy to produce heavy cross web stripes or zones of coating on a belt but difficult to produce thin, uniform and continuous coatings. Another important attribute of our method is that it has pre-metering characteristics, in that coating caliper can be controlled by adjusting the amount of liquid applied to the belt.
Although a speed differential can be employed between belt 170 and any of the other rolls shown in
As mentioned in connection with
Most known coating methods can be operated in non-preferred operating modes to apply uneven down web coatings. For example, a gravure coater can be operated so that it deliberately produces a coating with gravure marks, bar marks, or chatter. All such methods for producing an uneven coating fall within the scope of this invention. In a particularly preferred embodiment, we apply a discontinuous set of cross web coating stripes to a web. The cross web coating stripes need not be perpendicular to the web edge. The stripes can be diagonal across the web. Periodic initial placement of liquid onto the web is preferred, but it is not necessary. The stripes are easily applied. For example, a simple hose or number of hoses periodically swept back and forth across the web width can be used to apply a metered amount of coating discontinuously. This represents a very low cost and easily constructed coating device. It has a premetering capability, in that the overall final coating caliper can be calculated in advance and varied as needed by metering the stripe period or stripe width or the instantaneous flow rate to the stripe applicator.
Coating liquids can be applied in a variety of uneven patterns other than stripes, and by using methods that involve or do not involve contact between the applicator and the surface to which the coating is applied. For example, the above-described needle applicator can contact or not contact the surface to which the coating is applied. Also, a pattern of droplets can be sprayed onto the substrate using a suitable non-contacting spray head or other drop-producing device. If a fixed flow rate to a drop-producing device is maintained, the substrate translational speed is constant, and most of the drops deposit upon the substrate, then the average deposition of liquid will be nearly uniform. However since the liquid usually deposits itself in imperfectly spaced drops, there will be local variations in the coating caliper. If the drop deposition frequency is low or the drop size is low, the drops may not touch, thus leaving uncoated areas in between. Sometimes these sparsely placed drops will spontaneously spread and merge into a continuous coating, but this may take a long time or occur in a manner that produces a non-uniform coating. In any event we prefer to employ an improvement station of our invention (e.g., a set of multiple contacting rolls having selected periods) in order to improve the uniformity of the applied drops or other uneven coating. The improvement station can convert the drops to a continuous coating, or improve the uniformity of the coating, or shorten the time and machine length needed to accomplish drop spreading. The act of contacting the initial drops with rolls or other selected periodic pick-and-place devices, removing a portion of the drop liquid, then placing that removed portion back on the substrate in some other position increases the surface coverage on the substrate, reduces the distance between coated spots and increases the drop population density. The contacting action also creates pressure forces on the drop and substrate, thereby accelerating the rate of drop spreading. Contact in the area around and at a drop may produce a high liquid interface curvature at or near the spreading line and thereby enhance the rate of drop spreading. Thus the use of selected periodic pick-and-place devices makes possible rapid spreading of drops applied to a substrate and improves the uniformity of the final coatings.
If the spraying deposition rate is large enough to produce a continuous coating, the statistical nature of spraying will produce non-uniformities in the coaling caliper. Here too, the use of rolls or other selected periodic pick-and-place devices can improve coating uniformity.
Spraying can be accomplished using many different types of devices. Examples include point source nozzles such as airless, electrostatic, spinning disk and pneumatic spray nozzles. Line source atomization devices are also known and useful. The droplet size may range from very large (e.g., greater than 1 millimeter) to very small. The nozzle or nozzles can be oscillated back and forth across the substrate, e.g, in a manner similar to the above-described needle applicator.
This beneficial application of the periodic pick-and-place devices of our invention can be tested experimentally or simulated for each particular application. Many criteria can be applied to measure coating uniformity improvement. Examples include caliper standard deviation, ratio of minimum (or maximum) caliper divided by average caliper, range (which we define as the maximum caliper minus the minimum caliper over time at a fixed observation point), and reduction in void area. For example, through the use of our invention, range reductions of greater than 75% or even greater than 90% can be obtained. For discontinuous coatings (or in other words, coatings that initially have voids), our invention enables reductions in the total void area of greater than 50%, greater than 75%, greater than 90% or even greater than 99%. Those skilled in the art will recognize that the desired degree of coating uniformity improvement will depend on many factors including the type of coating, coating equipment and coating conditions, and the intended use for the coated substrate.
Through the use of our invention, 100% solids coating compositions can be converted to void-free or substantially void-free cured coatings with very low average calipers. For example, coatings having thicknesses less than 5 micrometers, less than 1 micrometer, less than 0.5 micrometer or less than 0.1 micrometer can readily be obtained. Coatings having thicknesses greater than 5 micrometers can also be obtained. In such cases it may be useful to groove, knurl, etch or otherwise texture the surfaces of one or more (or even all) of the pick-and-place devices so that they can accommodate the increased wet coating thickness.
Further understanding of our invention can be obtained by reviewing
Every point on the improvement diagrams represents the dimensionless minimum caliper obtained for a coating station/improvement station combination made according to certain fixed parameters discussed below and certain variables indicated on the abscissa and ordinate of each diagram. These variables include dimensionless roll sizes and dimensionless stripe widths. The dimensionless roll size is the time period of the roll rotation divided by the period of the input non-uniformity. If the roll size does not vary, and its surface speed equals the web speed, the dimensionless roll size is equivalent to the roll circumference divided by the non-uniformity wavelength where the wavelength is the length between successive coating stripes. In the improvement diagrams, the wavelength was assumed to be constant. The dimensionless stripe width is the stripe machine direction width divided by the wavelength, or the time for the stripe to pass an observer divided by the non-uniformity period. It is possible to apply very thick caliper stripes of coating. These will often spread into wider stripes after the first passage through a nip. The stripe width for this discussion is defined as the width immediately after the first passage through a nip.
The required dimensionless minimum caliper will depend on the particular application. For example, the requirements for coated abrasives, tape and optical films will all differ from one another. The requirements will also differ within a class of products. For example, coarse abrasives used for woodworking have a less stringent caliper uniformity requirement than microabrasives used for polishing disk drive parts. In general, the thinner the average caliper, the more stringent the uniformity requirement. As a broad generality, superior uniformity means that the minimum coating caliper (the minimum of the coating distribution) will be 90 to 100 percent of the average caliper, equivalent to a dimensionless minimum caliper of 0.9 to 1.0. The legends accompanying the improvement diagrams identify a range of dimensionless minimum caliper values assigned to each of several grey scale values. White areas on the improvement diagrams represent areas of higher dimensionless minimum caliper and darker areas represent areas of lower dimensionless minimum caliper, but the associated ranges are not the same on each improvement diagram.
The improvement diagrams in
The improvement diagrams in
We have found that for typical industrial coating materials, easily obtainable dimensionless stripe widths generally are in the range of about 0.05 to about 0.15. For such materials and dimensionless stripe widths we prefer to use at least three rolls all of different sizes, and more preferably four or more rolls all of different sizes.
We have also found by performing numerous mathematical simulations of our method that there are preferred choices of dimensionless roll sizes and dimensionless stripe widths when multiple rolls are used to spread a pattern of periodic stripes into a continuous coat. These sizes are related to the width of the stripes. If the dimensionless stripe width is represented by the symbol Y and the dimensionless roll size is represented by the symbol X, then combinations of choices of these variables can be represented by points on the rectangular plane formed on an X-Y plot between lines Y=0, Y=1, X=0, and X=1. We have found that preferred combinations are points lying in the regions between the numerous pairs of lines A and A′ where A is a line described by the formula X=m Y+b and A′ is a line described by the formula X=m′Y+b′. The values of the parameters m, m′, b and b′ are described in more detail below. Thus expressed as a fourth rule of thumb, we prefer to use roll size and stripe width combinations that lie between the lines X=m Y+b and X=m′Y+b′.
The parameter m′ preferably equals 0.85 times m, and the parameter b′ preferably equals b. We prefer that m and b have values that are related to certain preferred fractions. The preferred fractions are given by n/d where n and d are integers and d is less than 41 and not zero. The term n may be any integer larger than zero. The term m may have any of the values given by the relationships m=k/(d) and m=−k/(d), where k is an integer and can take on all values between 1 and 5. The term b is given by b=n/d. We also prefer that the dimensionless stripe width is greater than 0.05. Thus expressed as a fifth rule of thumb, when there is variation in the stripe period or dimensionless stripe width we prefer to use dimensionless roll size and dimensionless stripe width combinations that lie between the lines X=0.85 m Y+b and X=m′Y+b′.
When roll sizes are chosen, our studies have found that fractional roll sizes preferably are avoided. We have also found other combinations of sizes that preferably are avoided. These lie in regions related to the fractional roll sizes between the curves S and the lines Y=0 on an X-Y plot, where the S curves are described by the formula:
S=hC(4000{abs(X−n/d)}Q+1/d+2(X−n/d)sign(n/d−X))
where:
C is equal to 1 (or 0.85 when there are random variations in the period or the width of the stripe).
Thus expressed as a sixth rule of thumb, we prefer to use roll size and stripe width combinations that lie in the regions between the curves S and the line Y=0.
As noted above, the method of the invention can employ driven pick-and-place rolls whose rotational speed is selected or varied before or during operation of the improvement station. The period of a pick-and-place roll can be varied in other ways as well. For example, the roll diameter can be changed (e.g., by inflating or deflating or otherwise expanding or shrinking the roll) while maintaining the roll's surface speed. The rolls do not have to have constant diameters; if desired they can have crowned, dished, conical or other sectional shapes. These other shapes can help vary the periods of a set of rolls. Also, the position of the rolls or the substrate path length between rolls can be varied during operation. One or more of the rolls can be positioned so that its axis of rotation is not perpendicular (or is not always perpendicular) to the substrate path. Such positioning can improve performance, because such a roll will tend to pick up coating and reapply it at a laterally displaced position on the substrate. In addition, as noted above a periodically applied coating can be fed to the improvement station and that period can be varied. All such variations are a useful substitute for or an addition to the roll sizing rules of thumb discussed above. All can be used to affect the performance of the improvement station and the uniformity of the caliper of the finished coating. For example, we have found that small variations in the relative speeds or periodicity of the devices, or between one or more of the devices and the substrate, are useful for enhancing performance. Random or controlled variations can be employed. The variation preferably is accomplished by independently driving the rolls using separate motors and varying the motor speeds. Those skilled in the art will appreciate that the speeds of rotation can also be varied in other ways, e.g., by using variable speed transmissions, belt and pulley or gear chain and sprocket systems where a pulley or sprocket diameter is changed, limited slip clutches, brakes, or rolls that are not directly driven but are instead frictionally driven by contact with another roll. Periodic and non-periodic variations can be employed. Non-periodic variations can include intermittent variations and variations based on linear ramp functions in time, random walks and other non-periodic functions. All such variations appear to be capable of improving the performance of an improvement station containing a fixed number of rolls. Improved results are obtained with speed variations having amplitudes as low as 0.5 percent of the average.
Constant speed differentials are also useful. This allows one to choose periods of rotation that avoid poor performance regions. At fixed rotational speeds these regions are preferably avoided by selecting the roll sizes.
Another aspect of our invention is that it increases the rate of drying volatile liquids on a substrate. Drying is often carried out after a substrate has been treated by washing or by passage through a treating liquid. Here the main process objective is not to apply a liquid coating, but instead to remove liquid. For example, droplets, patches or films of liquid are commonly encountered in web processing operations such as plating, coating, etching, chemical treatment, printing and slitting, as well as in the washing and cleaning of webs for use in the electronics industry.
When a liquid is placed on or is present on a substrate in the form of droplets, patches, or coatings of varying uniformity and if a dry substrate is desired, than the liquid must be removed. This removal can take place, for example, by evaporation or by converting the liquid into a solid residue or film. In industrial settings drying usually is accomplished using an oven. The time required to produce a dry web is constrained by the time required to dry the thickest caliper present. Conventional forced air ovens produce uniform heat transfer and do not provide a higher drying rate at locations of thicker caliper. Accordingly, the oven design and size must account for the highest anticipated drying load.
In typical manufacturing operations, drying can be made more difficult due to unintended but commonly occurring coating process factors such as operator mistakes, system control failures or machinery failures. These factors can cause large increases in coating caliper (e.g., by a factor of 10 or more). One typical example is a momentary loss of the hydraulic pressure that holds closed the metering gap of a reverse roll coater. Unless the drying section of a coating process line is designed with significant overcapacity, the occurrence of such a surge can cause wet web to be wound up at the end of the process line. This can make the entire wound roll unusable. In addition, if the coating liquid contains a flammable solvent, then flammable concentrations of solvent paper can arise at the winder. Since the roll winding station often causes substantial static electrical discharges, fires or explosions can occur.
The improvement stations of our invention substantially reduce the time required to produce a dry substrate, and substantially ameliorate the effect of coating caliper surges. The improvement station diminishes coating caliper surges for the reasons already explained above. Even if the coating entering the improvement station is already uniform, the improvement station greatly increases the rate of drying. Without intending to be bound by theory, we believe that the repeated contact of the wet coating with the pick-and-place devices increases the exposed liquid surface area, thereby increasing the rate of heat and mass transfer. The repeated splitting, removal and re-deposition of liquid on the substrate may also enhance the rate of drying, by increasing temperature and concentration gradients and the heat and mass transfer rate. In addition, the proximity and motion of the pick-and-place device to the wet substrate may help break up rate limiting boundary layers near the liquid surface of the wet. All of these factors appear to aid in drying. In processes involving a moving web, this enables use of smaller or shorter drying stations (e.g., drying ovens or blowers) down web from the coating station. If desired, the improvement station can extend into the drying station.
The methods and devices of the invention can be used to apply, make more uniform or dry coatings on a variety of flexible or rigid substrates, including paper, plastics, glass, metals and composite materials. The substrates can be substantially continuous (e.g., webs) or of finite length (e.g., sheets). The substrates can have a variety of surface topographies including smooth, textured, patterned, microstructured and porous surfaces (e.g., smooth films, corrugated films, prismatic optical films, electronic circuits and nonwoven webs). The substrates can have a variety of uses, including tapes, membranes (e.g., fuel cell membranes), insulation, optical films or components, electronic films, components or precursors thereof, and the like. The substrates can have one layer or many layers under the coating layer.
The invention is further illustrated in the following examples, in which all parts and percentages are by weight unless otherwise indicated.
Using a modified coating and curing machine, a roll of cast polypropylene film was coated with an ultraviolet (UV) polymerizable epoxy silicone release coating formulation having an epoxy equivalent weight of 530 prepared like the release coating of Example 3 of U.S. Pat. No. 5,332,797. The reactive mixture contained 97 parts epoxy silicone, 2 parts bis(dodecylphenyl)iodonium hexafluoroantimonate, 3 parts ALFOL™ 1012 HA and 0.2 parts 2-isopropylthioxanthone. The polypropylene film was 50 micrometers in caliper and 152 mm wide with a matte surface finish. The coating was not applied directly to the web; instead, it was applied to an endless transfer belt as a periodic pattern of stripes. The coating on the transfer belt was made uniform by passing it through an improvement station. The thus-improved smooth, thin coating was applied to the web via a nip roll assembly. The coating was cured on the web using UV energy.
The web path ran from the unwind roll of a HIRANO MULTI COATER™ Model M-200 coating machine (Hirano Tecseed Company, Ltd.) through the nip of two driven rolls on the coating machine, through a Model 1250 UV curing station (Fusion UV Systems, Inc.) attached to the coating machine, and a web wind-up. The nip had a steel top roll and a rubber bottom roll. The UV curing station was operated at its low power setting.
The improvement station had a train of twelve undriven pick-and-place contacting rolls with diameters of 54.86, 72.85, 69.52, 62.64, 56.90, 52.53, 66.04, 39.65, 41.66, 69.09, 53.92 and 49.33 mm ±0.025 millimeters. The rolls were obtained from Webex Inc. as dynamically balanced steel live shaft rolls with chrome plated roll faces finished to 16 Ra. A silicone-rubber-covered fabric belt 152 millimeters wide and 3.05 meters long was threaded through this improvement station, around the bottom roll of the nip on the coating machine and then past a cross belt stripe application position where the release coating formulation could be applied to the belt. The belt was next threaded around a first set of five pick-and-place contacting rolls with the web path configured so as to achieve at least 45 degrees of wrap around each roll. The belt was then threaded around a MDG SERIES DISPLACEMENT GUIDE belt steering unit (Coast Controls Corp.), used to maintain precise tracking through the improvement station. From the steering unit the belt was threaded past a second set of seven pick-and-place contacting rolls using at least a 45 degree wrap around each roll, into the nip of the coating station and then back to the improvement station. The belt ends were spliced together to form an endless loop. The nip rolls were counter-rotated as a pair with surface speeds matched in the nipping region. The belt was driven by its traction with the rubber roll, and the web was driven by its traction with the steel roll.
The coating station employed an air driven cross belt oscillating mechanism that stroked a catheter needle back and forth across the belt at a rate of 48 cycles per minute. The oscillating mechanism was a Model BC406SK13.00 TOLOMATIC™ Band Cylinder (Tol-O-Matic, Inc.). The catheter needle was a 20 gauge, 32 mm long square tip needle made by Abbott Ireland. The mechanism was adjusted so that the needle tip contacted the belt as it was cycled across the belt. Two parallel interceptor plates were placed 138 mm apart above the belt and intercepting the track of the needle, in order to prevent deposition of the coating liquid along 7 mm wide lanes extending inward from each edge of the belt. A metered flow of the coating liquid was pumped to the needle so as to produce a diagonal stripe across the belt when both the needle and belt were moving. The metering pump was a gear pump with a capacity of 0.292 cubic centimeter per revolution, driven by a type QM digital metering system (both obtained from Parker Hanniford Corp.).
Using this apparatus and a web speed of 3 meters per minute, three different coating liquid flow rates were used to produce coating calipers of 0.2, 0.4 and 0.6 micrometers. The release properties of the coated samples were found to average 398, 458, and 501 grams per 2.54 centimeters of width, respectively. The standard deviations of the release properties were 19, 28, and 24 grams per 2.54 centimeters of width, respectively. This indicates that substantially void-free coatings having very good coating caliper uniformity were obtained.
By further modifying the coating and curing machine of Example 1, a roll of cast polyester film was coated with two silicone release materials in side-by-side abutting stripes. The coating fluid consisted of a two UV polymerizable silicone release coating compositions having different release characteristics. The first composition, a so-called “premium release” formulation, contained 55 parts by weight of RC711™ silicone and 45 parts by weight of RC726™ silicone, both sold by Goldschmidt Chemical Corp. The second composition, a so-called “medium release” formulation, contained 100 parts by weight of RC711 silicone. To each of these compositions 3 parts by weight of DANOCUR™ 1173 curative (Ciba-Geigy Corp.) was added.
The target web was SCOTCHPAR™ polyester film (3M) having a caliper of 35.6 micrometers and a width of 152 mm. A web speed of 16.1 meters per min was used for all samples. A Model 1223 UV curing station (Fusion UV Systems, Inc.) was attached to the coating machine in place of the model 1250 station used in Example 1. The curing station was operated at its low power setting, while maintaining a nitrogen inert atmosphere with an oxygen content of less than 50 parts per million within the curing chamber.
The improvement station and transfer belt were as in Example 1. The nip was configured with a steel roll on the top and a rubber roll on bottom with no undercuts, to give 152 millimeters of nipped contact. The web was wrapped around the top steel roll of the nip, and the belt was wrapped around the bottom rubber roll. The nip rolls were counter-rotated as a pair with surface speeds matched in the nipping region. The belt was driven by its traction with the rubber roll, and the web was driven by its traction with the steel roll.
The coating station employed a side-by-side dual slot applicator die 270 like that shown in
As shown in
We found it both useful and unexpected to be able to apply lanes with controllable caliper and good edge definition, and to be able to apply abutting lanes of different formulations without intermixing between the lanes. Without intending to be bound by theory, we believe this was made possible because we were able to apply metered amounts of the liquids without any excess. This enabled us to avoid the creation of rolling banks of excess liquid. The elimination of these rolling banks may have prevented intermingling. This lack of intermixing is a significant advantage, and difficult to obtain using conventional coating devices. We believe that we obtain this unexpected result because the forces that dominate the flow of liquid are aligned with the belt length direction, and minimal or no cross belt forces appear to be generated.
The coating apparatus of Example 1 was modified by removing the belt and threading the web so that the web directly contacted a train of 13 improvement rolls. The pick-and-place rolls had respective diameters of 5.245, 5.321, 5.398, 5.474, 5.550, 5.626, 5.702, 5.779, 5.855, 5.931, 6.007, 6.083 and 6.160 mm. The apparatus was used to apply a UV curable primer to a 30.5 mm wide, 50 micrometer caliper polyimide film (commercially available from E. I. duPont de Nemours and Co.) traveling at 3 meters per minute. The coating station employed an oscillating needle applicator having a 0.094 mm inside diameter, for application of the primer liquid directly onto the moving polyimide web. The needle oscillated across the web at a rate of one cycle per 2 seconds. The needle could also be used to apply the primer liquid to an intermediate co-rotating transfer roll having a 76 mm diameter. The transfer roll helped to avoid coating beyond the edge of the web, and lessened the chance of the primer liquid going onto the backside of the web. Using either application technique, stripe patterns were initially deposited on the web. The primer liquid was pumped to the applicator at a mass flow rate sufficient to achieve a final uniform wet caliper of 1 micrometer on the web. The resulting coating formed a continuous primer layer on the substrate.
A coating apparatus including an 8 roll improvement station was constructed to apply a UV curable release coating to a 30.5 cm wide, 23.4 micrometer caliper polyester (PET) tape backing. The coating apparatus employed an electrospray coating head as described in U.S. Pat. No. 5,326,598 and a restricted flow die as described in U.S. Pat. No. 5,702,527, mounted above a large, free-rotating grounded metal drum. The drum diameter was 50.8 cm and its width was 61 cm. The die wire was held at a fixed distance of 10.8 cm from the surface of the drum, and at an electrical potential of minus 40,000 volts with respect to ground. The die was 33 cm wide. Due to charge repulsion of the drops within the liquid mist generated by the die, the die was capable of spraying a 38-cm wide mist across the drum.
The moving PET web was brought from an unwind roll and wrapped over the grounded metal drum. The web was pre-charged on the drum just prior to the electrospray coating die using a series of 3 corotron corona chargers to provide a positive potential of at least 1000 volts as measured by an electrostatic voltmeter positioned 1 cm above the web and grounded drum. The web then passed under the electrospray coating die where negatively charged droplets generated at the die were electrostatically attracted to the web. The droplets landed on the web apart from each other and then started to spread in order eventually to form a continuous coating. During this drop spreading time a spot on the web was being moved from the grounded drum a distance of 1.45 m into a UV curing station where the liquid coating was cured to form a solid coating. If the web travels too quickly from the coating station to the cure station then complete drop spreading will not occur and the cured web coating will be in the form of discrete spots or a discontinuous film with many voids, rather than a continuous film. The uncoated areas present a bare substrate surface that will not have good adhesive release properties.
Between the coating and the curing stations at a path length 0.86 m from the application of the spray mist to the web was placed an improvement station containing 8 pick-and-place rolls arranged in a compact tortuous path having a length of 1.14 m. The rolls had respective diameters of 54.86, 69.52, 39.65, 56.90, 41.66, 72.85, 66.04, and 52.53 mm, all with a tolerance of plus or minus 0.025 mm.
The PET web was run through the coating apparatus at line speeds of 15.24, 30.48, 60.96 and 121.92 m/min, each speed being double the previous speed. A solventless silicone acrylate UV curable release formulation as described in Example 10 of U.S. Pat. No. 5,858,545 was prepared and pumped into the die. The flow rate to the die was held fixed at 5.81 cc/min to produce various decreasing coating heights as the web speed increased. Since the flow rate was held constant, this meant that the drops would have to spread farther as the coating became thinner. In a first set of runs, the PET web was coated beneath the die and then fed directly into the UV curing station without passing through the improvement station. In a second set of runs, the PET web was coated beneath the die, fed through the 8 roll improvement station and then fed into the UV curing station. In both sets of runs the web was wound up on a take-up roll after passing through the UV curing station. The power to the UV curing station was held constant for all runs. The UV-C (250-260 nm) energy density or dose was measured using an EIT UVIMAP Model No. UM254L-S UV dosimeter (Electronic Instrumentation and Technology, Inc.). At a web speed of 15.24 m/min, the dose was 32 mJ/cm2. Each time the web speed was doubled, the UV-C dose was effectively halved, so that at a web speed of 121.92 m/min, the UV-C dose was 4 mJ/cm2. The UV dose was sufficient to cure the coating for all runs.
The coated and cured web was unwound and samples removed for an adhesive peel test, in order to evaluate the release properties of the cured coating produced in each run. A standard 180° peel test was performed at a peel rate of 0.23 m/min using SCOTCH™ 845 acrylic book tape and an IMASS™ Model 3M90 slip/peel tester (Imass, Inc.). A 2.04 kg weight was rolled twice back and forth over the tape, followed by 3 days aging at room temperature prior to tape removal. When the pieces of peel test tape used for the 180° peel test were re-applied to a clean glass substrate and then removed, no drop in the re-adhesion values was observed for any of the pieces of peel test tape, indicating that all samples had been completely cured. Set out below in Table I are the run number, web speed, the calculated cured coating thickness, the number of improvement rollers, and the measured initial release force obtained using the 180° peel test.
As shown in Table I, when no pick-and-place rollers were used, the release force values increased with increasing web speed. More than an order of magnitude increase was observed, with the rate of increase being especially noticeable at web speeds above 30 m/min. This indicates that the drops had not fully spread at these higher web speeds and that the cured coating contained significant void areas. When the improvement station and its train of 8 pick-and-place rolls was employed between the coating die and the UV curing station, then the release force values did not significantly increase as the web speed increased. Solventless thin-film coatings with calipers below I micrometer are very difficult to achieve. The results shown above demonstrate that substantial improvements in the coating uniformity of these very thin coatings can be achieved using the present invention.
A coating and drying apparatus was constructed to coat and dry a web of 37.5 micrometer caliper film. The apparatus had a 4 roll improvement station with undriven steel pick-and-place rolls having respective diameters of 48.48, 39.91, 52.12 and 55.12 mm. The drying station had four HEPA air filtration units mounted 152 mm above the web, and providing air at 22° C. and 8.5% RH. The coating station was a small hypodermic needle attached to a HARVARD™ syringe pump (commercially available from Harvard Instruments, Inc.), set to deliver 0.01 ml of distilled water per minute to the web in drops having a volume of 0.0009 ml.
The contact angle of the water on the pick-and-place rolls was less than 45°. By wrapping the rolls with a pressure-sensitive tape having a low adhesion backsize coating, the contact angle of water on the rolls could be increased to over 90°.
In a control run, the improvement station was removed, and water was deposited on the moving web using the syringe and followed until it reached the middle of the drying station. The web was stopped and the time required to complete drying was noted by visual examination. The drying time was 45 minutes.
In a series of runs, the web was operated at various line speeds while using the improvement station, and with and without wrapping the pick-and-place rolls with tape. The drying time was noted, and the ratio of drying times with and without the improvement station was recorded. Set out below in Table II are the run number, web speed, whether or not the rolls were wrapped with tape, and the ratio of the control drying time to the drying time using the improvement station.
As shown in Table II, use of the improvement station provided a dramatic increase in drying rate. When the rolls were not wrapped with tape, patches of the liquid were observed on the wet the rolls, and an over 70-fold improvement in drying rate was observed.
Various modifications and alterations of this invention will be apparent to those skilled in the art without departing from the scope and spirit of this invention. This invention should not be restricted to that which has been set forth herein only for illustrative purposes.
This application is a divisional of U.S. Ser. No. 09/757,955, filed Jan. 10, 2001, now U.S. Pat. No. 6,737,113B2, the disclosure of which is herein incorporated by reference.
| Number | Name | Date | Kind |
|---|---|---|---|
| 1043021 | Mayer | Oct 1912 | A |
| 1583788 | Gilman | May 1926 | A |
| 1821209 | Darrah | Sep 1931 | A |
| 2053601 | Cheatham | Sep 1936 | A |
| 2105488 | Massey et al. | Jan 1938 | A |
| 2105981 | Massey et al. | Jan 1938 | A |
| 2229620 | Bradner | Jan 1941 | A |
| 2229621 | Bradner | Jan 1941 | A |
| 2237068 | Bradner | Apr 1941 | A |
| 2245045 | Montgomery et al. | Jun 1941 | A |
| 3018757 | Loppnow | Jan 1962 | A |
| 3169081 | Nelson et al. | Feb 1965 | A |
| 3718117 | Lewicki, Jr. | Feb 1973 | A |
| 3920862 | Damschroder et al. | Nov 1975 | A |
| 4020194 | McIntyre et al. | Apr 1977 | A |
| 4102301 | Reade et al. | Jul 1978 | A |
| 4267215 | Riggs | May 1981 | A |
| 4354449 | Zink | Oct 1982 | A |
| 4378390 | Yoshida et al. | Mar 1983 | A |
| 4569864 | McIntyre | Feb 1986 | A |
| 4748043 | Seaver et al. | May 1988 | A |
| 4830872 | Grenfell | May 1989 | A |
| 4924772 | Schlunke et al. | May 1990 | A |
| 5326598 | Seaver et al. | Jul 1994 | A |
| 5332797 | Kessel et al. | Jul 1994 | A |
| 5409732 | Leonard et al. | Apr 1995 | A |
| 5447747 | Munter et al. | Sep 1995 | A |
| 5460120 | Paul et al. | Oct 1995 | A |
| 5501734 | Oliphant | Mar 1996 | A |
| 5536314 | Rannestad | Jul 1996 | A |
| 5599602 | Leonard et al. | Feb 1997 | A |
| 5620514 | Munter et al. | Apr 1997 | A |
| 5702527 | Seaver et al. | Dec 1997 | A |
| 5733608 | Kessel et al. | Mar 1998 | A |
| 5858545 | Everaerts et al. | Jan 1999 | A |
| 5871585 | Most et al. | Feb 1999 | A |
| 5954907 | LaRose et al. | Sep 1999 | A |
| 5997645 | Grimmel et al. | Dec 1999 | A |
| 6117237 | Yapel et al. | Sep 2000 | A |
| 6206069 | Saukkonen | Mar 2001 | B1 |
| 6471776 | Krossa et al. | Oct 2002 | B1 |
| 6589594 | Hembree | Jul 2003 | B1 |
| Number | Date | Country |
|---|---|---|
| 2 304 987 | Aug 1974 | DE |
| 199 46 325 | Apr 2001 | DE |
| 0 047 887 | Mar 1982 | EP |
| 1 278 099 | Jun 1972 | GB |
| WO 0196661 | Dec 2001 | WO |
| Number | Date | Country | |
|---|---|---|---|
| 20040187773 A1 | Sep 2004 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 09757955 | Jan 2001 | US |
| Child | 10821588 | US |
