AU679865C - Cross-linked pvoh coatings having enhanced barrier characteristics - Google Patents

Description

CROSS-LINKED PVOH COATINGS HAVING ENHANCED

BARRIER CHARACTERISTICS

The present invention relates to cross-linked PVOH coatings having enhanced barrier characteristics and, more particularly, to PVOH coatings which exhibit improved processing characteristics resulting in cross-linked coatings providing improved oxygen barriers especially at high relative humidities.

Poly (vinyl alcohol) ("PVOH") coatings have been applied to various substrates in the past, and are known to provide a barrier to the transmission of oxygen. PVOH, however, is soluble in water and therefore is susceptible to attack by moisture. Various attempts have been made to decrease the sensitivity of PVOH to moisture.

One known method of decreasing the sensitivity of the PVOH coating to moisture is to cross-link the poly(vinyl alcohol). For example, a cross-linking agent and catalyst may be applied along with the poly(vinyl alcohol) such that the agent interconnects and thereby cross-links the

poly(vinyl alcohol) molecules as such coating is dried. The catalyst is present to facilitate the cross-linking process.

U.S. Patent No. 5,380,586 discloses a polymeric substrate having a cross-linked layer of PVOH adhered thereto. The PVOH layer includes a cross-linking agent such as melamine or urea formaldehyde, which is cross-linked in the presence of a sulfuric acid catalyst. The resultant film exhibits enhanced oxygen barrier characteristics, as compared to barrier films of the prior art.

However, it can be difficult in the prior art films, including the film disclosed in U.S. Patent No. 5,380,586, to ensure that the layer of poly(vinyl alcohol) cross-links fully throughout itself. In this regard, it is believed that the degree of cross-linking is indicative of the oxygen barrier characteristics of the resultant film.

Stated differently, poly(vinyl alcohol) layers that are fully cross-linked tend to exhibit better barrier

characteristics than those layers which are less than fully cross-linked .

The prior art films, in an attempt to achieve maximum cross-linking, are often dried and/or stored for an

extended period of time. For example, it may be necessary to store a film for weeks, or even months, before such film has reached its point of maximum cross-linking. The aforementioned storage period increases the production time and cost for manufacturing polymeric films having cross- linked PVOH coatings thereon.

There is therefore a need in the art for a method of providing a PVOH coating on a substrate, such as a

polymeric film, which upon drying is substantially 100% cross-linked thereby eliminating or, at the minimum, greatly reducing the storage period. The resultant coating should exhibit improved oxygen barrier characteristics and improved rubbing resistance especially at high relative humidities. Moreover, the resultant coating should bond firmly to the underlying substrate.

The present invention, which addresses the needs of the prior art, relates to a method of providing an improved moisture resistant oxygen barrier having a reduced number of imperfections onto the surface of a substrate. The method includes the step of coating the surface of the substrate with a solution of poly(vinyl alcohol), glyoxal and tensoactive agent and thereafter cross-linking the poly(vinyl alcohol) in the absence of a catalyst to provide the moisture resistant oxygen barrier.

In a preferred embodiment, the poly(vinyl alcohol) has a hydrolysis level of above 99%, usually 99.5%. The

poly(vinyl alcohol) is preferably a low viscosity grade PVOH. In particular, the viscosity of the PVOH is preferably from 5 cps to 15 cps (at 4% solution and 20°C). Moreover, the tensoactive agent is preferably a C₄ to C₁₀ alcohol, particularly 1-octanol.

The present invention also provides a polymeric film structure having an improved oxygen barrier firmly bonded to an underlying substrate. The film structure is produced by the process of preparing a solution of poly(vinyl alcohol) and glyoxal. The process includes the further step of adding an effective amount of tensoactive agent to the solution to reduce foaming of the solution during both agitation and application of the solution and to reduce the solution's surface tension whereby improved bonding between the barrier and the substrate is achieved. The process includes the further step of coating the solution on at least one side of the substrate and thereafter cross- linking the poly(vinyl alcohol) in the absence of a

catalyst to provide the oxygen barrier.

In a preferred embodiment, the coated substrate is dried at a temperature of from 80ºC to 150ºC for period of from 4 seconds to 8 seconds. The coating is substantially 100% cross-linked upon completion of the drying period.

As a result, the present invention provides an improved PVOH coating for application on a substrate which is 100% cross-linked upon drying of the applied coating. The cross-linking time is therefore reduced from a matter of weeks, or even months, to a matter of seconds.

Moreover, the resultant cross-linked coating exhibits improved oxygen barrier characteristics and improved rubbing resistance. The bonding between the barrier and the substrate is also enhanced. Finally, the manufacturing process is facilitated in that the present coating exhibits a reduced tendency to foam during both agitation and application of the solution and also exhibits an enhanced ability to "wet-out" when applied to the substrate thereby providing a film having an improved lay-flat quality. The films of the present invention are produced by coating at least one side of a substrate with a solution of poly(vinyl alcohol), glyoxal and tensoactive agent. The poly(vinyl alcohol) is thereafter cross-linked to provide an oxygen barrier, i.e., a polymeric layer which resists the transmission of oxygen therethrough.

The improved oxygen barrier layer of the present

invention may be adhered to any number of substrates, including polymeric films, boxboards, metallic films and paper. The oxygen barrier layer is preferably adhered to a polymeric film such as a polyolefin. One particularly preferred polyolefin is polypropylene.

To ensure that the oxygen barrier layer of the present invention properly adheres to the substrate, the substrate preferably includes at least one side that is adapted for receipt of the layer. Particularly, the side of the substrate to be coated should have surface properties which facilitate the securing of a poly(vinyl alcohol) layer thereto. For example, the side to be coated may be treated with a primer such as poly(ethyleneimine). Of course, other suitable primers may also be utilized. The side to be coated may also be adapted for subsequent receipt of a poly(vinyl alcohol) layer during formation of the substrate itself. For example, a polymeric substrate, e.g.,

polypropylene, may include a material such as maleic acid which improves the ability of poly(vinyl alcohol) to bond thereto. Finally, the substrate may include a side which is naturally adapted for receipt of a poly(vinyl alcohol) layer, i.e., the side to be coated requires no treatment.

As known to those skilled in the art, poly(vinyl alcohol) is typically produced by hydrolyzing poly(vinyl acetate). Specifically, the hydrolysis reaction replaces the acetate groups with alcohol groups. The more acetate groups that are replaced, the greater the hydrolysis of the PVOH. It is believed that the presence of more alcohol groups (i.e., greater hydrolysis) provides better barrier properties.

However, even after hydrolysis of the PVOH, a certain number of acetate groups remain attached to the PVOH molecule. For example, in a 95% hydrolyzed PVOH, 5% of the originally-present acetate groups remain attached to the molecule; whereas in a 99% hydrolyzed PVOH, 1% of the originally-present acetate groups remain attached to the molecule.

Poly(vinyl alcohol) may be produced with various

viscosities and various degrees of hydrolysis. Viscosity is typically a function of the molecular weight of the PVOH molecule. Specifically, a solution of PVOH in which the individual molecules are relatively large (i.e., a high molecular weight PVOH) tends to have a higher viscosity than a solution of PVOH in which the individual molecules are relatively small (i.e., a low molecular weight PVOH). It is believed that Van der Waals forces develop between the larger-sized molecules because such molecules tend to align themselves with one another, thus increasing the viscosity of the PVOH.

A poly(vinyl alcohol) such as Elvanol 71-30 (produced by Du Pont) is typically referred to as a medium viscosity, fully hydrolyzed PVOH. Specifically, the degree of

hydrolysis of a fully hydrolyzed PVOH is 98%. Further, the viscosity of a medium viscosity grade PVOH such as Elvanol 71-30 is 30 cps at 4% solution and 20ºC.

Another commercially available PVOH is Elvanol 75-15 (also produced by Du Pont), which is a low viscosity, fully hydrolyzed PVOH. Specifically, the degree of hydrolysis is 98% and the viscosity is 13 cps at 4% solution and 20ºC.

Still another commonly available PVOH is Elvanol 90-50 (also produced by Du Pont), which is a low viscosity, super hydrolyzed PVOH. The degree of hydrolysis in a super hydrolyzed PVOH is 99.5%. The viscosity of a low viscosity grade PVOH such as Elvanol 90-50 is 13 cps at 4% solution and 20ºC.

Although poly(vinyl alcohol) provides a barrier to the transmission of oxygen, it is soluble in water and

therefore susceptible to attack by moisture. As a result, poly(vinyl alcohol) layers which will be exposed to

moisture are typically cross-linked. The cross-linking of the layer substantially reduces its susceptibility to attack by moisture.

However, it is often difficult to readily and

consistently produce a poly(vinyl alcohol) layer which, when dried, becomes fully cross-linked. The current procedure for producing oxygen barriers of poly(vinyl alcohol) often requires the film to be stored for a period of weeks, or even months, following manufacture of the film to allow the poly(vinyl alcohol) layer to fully cross-link. This storage requirement increases both the production cost and production time. It also results in the film being exposed to moisture prior to becoming fully cross-linked, which may negatively affect the final properties of the film.

It has been discovered that a formulation of poly(vinyl alcohol), glyoxal and a tensoactive agent will cross-link upon drying of the applied coating, thereby eliminating the need to store the film. This cross-linking occurs in the absence of an acid catalyst and results in an improved oxygen barrier, as compared to other cross-linked PVOH coatings.

The poly(vinyl alcohol) is preferably a low viscosity grade PVOH having a viscosity of from 5 cps to 15 cps (at 4% solution and 20ºC). As mentioned above, a low molecular weight PVOH includes relatively small PVOH molecules, thereby providing a PVOH formulation having a lower

viscosity. It is believed that the smaller PVOH molecules, together with the relatively small glyoxal cross-linking molecules, allow a "tightly packed" matrix to be formed. As a result, the formed matrix is resistant to the

penetration of oxygen therethrough.

Glyoxal, also known as ethanedial or oxalaldehyde, is a two carbon dialdehyde having an empirical formula C₂H₂O₂. In solution, glyoxal exists as a mixture of hydrates, dimers and oligomers. The glyoxal utilized in the present invention is preferably an aqueous 40% by weight solution and is present in the resultant cross-linked coating in an amount of from 5% to 30% by weight and, preferably, from 15% to 25% by weight.

Glyoxal is a relatively small molecule, as compared to the PVOH and as compared to other various known cross- linkers. As a result, it is believed the glyoxal molecules tend to readily "fit" between adjacent PVOH molecules such that the cross-linked layer has a minimum of void space. It is further believed that the reduced void space enhances the oxygen barrier characteristics of the resultant film.

As mentioned above, it has been discovered herein that the cross-linking process between the PVOH and the glyoxal does not require a catalyst. This lack of need may result from the functionally active condition of the glyoxal, and is significant in that the typically employed catalysts (e.g., acid catalysts) often prove difficult to utilize in a commercial setting. Particularly, such catalysts are extremely corrosive and potentially damaging to the coating machinery. Moreover, the use of a catalyst significantly reduces the pot life of the coating solution.

In a preferred embodiment, the tensoactive agent is added to the solution to reduce foaming during both agitation of the solution and application of the solution to the

substrate. The addition of the agent to the solution also reduces the surface tension of the solution, thereby providing better wetout of the poly(vinyl alcohol) on the substrate which in turn results in a barrier layer having an improved lay-flat quality. This reduced surface tension also provides an enhanced bond between the cross- linked coating and the substrate.

It has been discovered that the addition of tensoactive agent, particularly 1-octanol, to a super hydrolyzed low viscosity PVOH such as Elvanol 90-50 provides a coating solution having an unexpectedly low level of surface energy. The reduced surface energy improves the processing characteristics of the solution, particularly the ability of the solution to "wet-out" when applied to the substrate without formation of voids or imperfections, thereby resulting in a coating having enhanced oxygen barrier characteristics.

In a preferred embodiment of the present invention, the tensoactive agent is a C₄ to C₁₀ alcohol such as octanol, particularly 1-octanol. The octanol is present in the solution in a concentration of from 5 ppm to 0.5% by weight. The octanol is dispersed throughout the solution and, at the concentrations employed in the present

formulation, remains dispersed in the solution. Of course, other suitable tensoactive agents are also contemplated.

Commercially suitable coating processes include a reverse direct gravure process and a smooth rod process. As is known to those skilled in the art, the gravure process typically produces a higher level of foam than the smooth rod process. The tensoactive agent reduces the degree of foaming, while simultaneously lowering the surface energy of the coating solution. The combination of reduced foaming and lower surface energy provides improved

processing characteristics which result in a barrier exhibiting reduced transmission of oxygen, particularly at high relative humidities.

With respect to the gravure process, the coating solution of the present invention preferably includes 200 to 500 ppm of 1-octanol and, more preferably, 250 ppm of 1-octanol. With respect to the smooth rod process, it has been discovered herein that the coating solution preferably includes from 5 ppm to 50 ppm of 1-octanol. This lower level of tensoactive agent provides the above-mentioned improved processing characteristics. In addition, it is believed that this lower level of tensoactive agent reduces the likelihood that the subsequently-formed oxygen barrier will suffer any negative impacts from the inclusion of such agent in the solution.

The solution, which is preferably aqueous, is prepared by adding the poly(vinyl alcohol) to cold water, which is thereafter heated to a temperature sufficient to dissolve the PVOH. The water and dissolved PVOH are then cooled. The cross-linking agent (i.e., the glyoxal) is then added to the cooled PVOH and water. Thereafter, an effective amount of the tensoactive agent is added to the solution. It is this resultant solution that is then coated on the polymeric substrate.

In a preferred embodiment, the aqueous solution includes from 4% to 14% by weight of solids and, preferably, from 5% to 10% by weight of solids. The solids content is made up from 70% to 95% by weight of poly(vinyl alcohol), from 5% to 30% by weight of cross-linking agent and from 5 ppm to 0.5% by weight of octanol.

It has been discovered that the aqueous solution of the present invention is stable in comparison to prior art formulations. This stability, together with the use of the low viscosity PVOH, allows the solids content of the solution to be increased. By increasing the solids content of the solution, the percentage of water in the solution is reduced. Accordingly, the applied coating is more readily dried. This reduced drying time results in an energy savings and/or a speed increase from the coating machinery. It is also believed to facilitate the cross-linking

process. Finally, this stability results in a longer pot life for the solution. Particularly, once the coating is applied to the

substrate, the film is rolled through a drying oven. A typical drying oven is 60 feet long and adapted to heat the film to 130ºC. The film is rolled through the oven at speeds of about 305 m/minute (1000 ft/minute). As the film rolls through the oven, the water in the applied coating is driven off which, in turn, increases the concentration of the solids content. At some point (i.e., at a particular concentration and temperature), the cross-linking process is initiated. This cross-linking process occurs rapidly and completely throughout the PVOH layer such that the film is 100% cross-linked by the time such film leaves the drying oven.

The following examples illustrate the enhanced barrier characteristics of films produced in accordance with the present invention.

EXAMPLE 1

Sample 1 was produced. A solution of Elvanol 71-30, Parez 613 (a methylated melamine formaldehyde) and ammonium chloride was coated onto a polymeric substrate of

polypropylene .75 mil thick. The solution contained 6% by weight of solids. In turn, the solids contained 83% by weight of PVOH, 15% by weight of methylated melamine formaldehyde and 2% by weight of ammonium chloride.

The substrate was treated with a poly (ethyleneimine) primer prior to application of the coating. The coating was applied to the polypropylene substrate using a reverse direct gravure coating process. Specifically, the coating was applied with a 92Q gravure roll. The control sample was then dried and stored until the layer was fully cross- linked, a process requiring about 3 weeks. The film was then measured for oxygen transmission at 0% relative humidity and 75% relative humidity.

Sample 1 exhibited an oxygen transmission rate of 0.95 x 10^-4 cc/cm²/24 hr (0.061 cc/100 in²/24 hr) at 0% relative humidity and 15. 004 x 10^-4 cc/cm²/24 hr ( 0 . 968 cc/100 in²/24 hr) at 75% relative humidity.

EXAMPLE 2

Sample 2 was produced. A solution of Elvanol 75-15 and Sunrez 740 (a cyclic amide-aldehyde copolymer) was coated onto a polypropylene substrate prepared in accordance with Example 1 by a reverse direct gravure process. The

solution contained 8% by weight of solids. In turn, the solids contained 75% by weight of PVOH and 25% by weight of cross-linking agent. The oxygen transmission

characteristics of the film were thereafter measured.

Sample 2 exhibited an oxygen transmissive rate of 1.24 x 10^-4 cc/cm²/24 hr (0.08 cc/100 in²/24 hr) at 0% relative humidity and 12.555 x 10^-4 cc/cm²/24 hr (0.81 cc/100 in²/24 hr) at 75% relative humidity.

EXAMPLE 3

Sample 3 was produced. A solution of Elvanol 90-50 and Sunrez 740 was coated onto the polypropylene substrate described in Example 1 by a reverse direct gravure process. The solution contained 8% by weight of solids. In turn, the solids contained 85% by weight of PVOH and

approximately 15% by weight of cross-linking agent. The oxygen transmission characteristics of the film were thereafter measured.

Sample 3 exhibited an oxygen transmissive rate of 0.465 x 10^-4 cc/cm²/24 hr (0.03 cc/100 in²/24 hr) at 0% relative humidity and 4.03 x 10^-4 cc/cm²/24 hr (0.26 cc/100 in²/24 hr) at 75% relative humidity.

EXAMPLE 4

Sample 4 was produced. A solution of Elvanol 75-15 and Glyoxal 40 was coated onto the polypropylene substrate described in Example 1 by a reverse direct gravure process. The solution contained 8% by weight of solids. In turn, the solids contained 85% by weight of PVOH and 15% by weight of cross-linking agent. The oxygen transmission characteristics of the film were thereafter measured.

Sample 4 exhibited an oxygen transmissive rate of 0.62 x 10^-4 cc/cm²/24 hr (0.04 cc/100 in²/24 hr) at 0% relative humidity and 3.565 x 10^-4 cc/cm²/24 hr (0.23 cc/100 in²/24 hr) at 75% relative humidity.

EXAMPLE 5

Sample 5 was produced. A solution of Elvanol 90-50 and Glyoxal 40 was coated onto the polypropylene substrate described in Example 1 by a reverse direct gravure process. The solution contained 8% by weight of solids. In turn, the solids contained 75% by weight of PVOH and 25% by weight of cross-linking agent. The oxygen transmission characteristics of the film were thereafter measured.

Sample 5 exhibited an oxygen transmissive rate of 0.93 x 10^-4 cc/cm²/24 hr (0.06 cc/100 in²/24 hr) at 0% relative humidity and 2.015 x 10^-4 cc/cm²/24 hr (0.13 cc/100 in²/24 hr) at 75% relative humidity.

EXAMPLE 6

Sample 6 was produced. A solution of Elvanol 75-15, Glyoxal 40 and 1-octanol was coated onto the polypropylene substrate described in Example 1 by a reverse direct gravure process. The solution contained 8% by weight of solids. In turn, the solids contained 75% by weight of PVOH 25% by weight of cross-linking agent and 250 ppm of 1- octanol. The oxygen transmission characteristics of the film were thereafter measured.

Sample 6 exhibited an oxygen transmissive rate of 0.775 x 10^-4 cc/cm²/24 hr (0.05 cc/100 in²/24 hr) at 0% relative humidity and 4.495 x 10^-4 cc/cm²/24 hr (0.29 cc/100 in²/24 hr) at 75% relative humidity. EXAMPLE 7

Sample 7 was produced. A solution of Elvanol 90-50, Glyoxal 40 and 1-octanol was coated onto the polypropylene substrate described in Example 1 by a reverse direct gravure process. The solution contained 8% by weight of solids. In turn, the solids contained 85% by weight of PVOH, 15% by weight of cross-linking agent and 250 ppm of 1-octanol. The oxygen transmission characteristics of the film were thereafter measured.

Sample 7 exhibited an oxygen transmission rate of 0.31 x 10^-4 cc/cm²/24 hr (0.02 cc/100 in²/24 hours) at 0% relative humidity and 1.085 x 10^-4 cc/cm²/24 hr (0.07 cc/100 in²/24 hours) at 75% relative humidity.

The results from Examples 1-7 are summarized in Table I.

It is apparent from the data set forth in Table I that the oxygen barrier characteristics of the films produced in accordance with the present invention are vastly superior to those of the prior art. Particularly, at high relative humidity (e.g., 75%) the oxygen

transmission rate (TO₂ in cc x 10^-4/cm²/24 hr) decreased from highs of 15.004 (Sample 1) and 12.555 (Sample 2) to a low of 1.085 (Sample 7). Moreover, the films produced in accordance with the present invention exhibit improved rubbing resistance upon drying as compared to those films produced employing various prior art formulations.

Claims (15)

CLAIMS :

1. A method for providing an improved moisture- resistant oxygen barrier onto a surface of a substrate comprising:

coating said surface of said substrate with a solution of poly(vinyl alcohol), glyoxal and tensoactive agent; and

cross-linking said poly(vinyl alcohol) in the absence of a catalyst to provide said moisture-resistant oxygen barrier.

2. The method according to Claim 1, wherein said poly(vinyl alcohol) has a viscosity of from 5 cps to 15 cps at 4% solution and 20ºC.

3. The method according to Claim 1, wherein said poly(vinyl alcohol) has a hydrolysis level above 99%.

4. The method according to any one of Claims 1 to 3, wherein said tensoactive agent is a C₄ to C₁₀ alcohol.

5. The method according to Claim 4, wherein said alcohol is octanol.

6. The method according to Claim 5, wherein said octanol is 1-octanol.

7. The method according to Claim 1, wherein said solution is prepared by the steps of:

dissolving said poly(vinyl alcohol) in water and thereafter adding said glyoxal; and

adding an effective amount of said tensoactive agent to said solution to reduce the surface tension of said solution whereby improved bonding between said barrier and said substrate is achieved.

8. The method according to any one of Claims 1 to 7, wherein said cross-linking step includes the further step of drying said coated substrate at a temperature of from about 80° C to about 150ºC.

9. The method according to Claim 1, wherein said solution includes from 5% to 10% by weight of solids, said solids comprising from 70% to 95% by weight of poly (vinyl alcohol) having a viscosity of from 5 cps to 15 cps at 4% solution and 20ºC and which is hydrolyzed to a level above 99%, from 5% to 30% by weight of glyoxal and from 5 ppm to 0.5% by weight of 1-octanol.

10. The method according to any one of Claims 1 to 9, wherein said coating step is accomplished through a smooth rod process, and wherein said solution includes from 5 ppm to 50 ppm of tensoactive agent.

11. The method according to any one of Claims 1 to 9, wherein said coating step is accomplished through a reverse direct gravure process, and wherein said solution includes from 200 ppm to 500 ppm of tensoactive agent.

12. A polymeric film structure, comprising:

an improved oxygen barrier firmly bonded to an underlying substrate produced by the process of preparing a solution of poly(vinyl alcohol) and glyoxal;

adding an effective amount of a tensoactive agent to said solution to reduce the surface tension of said solution whereby improved bonding between said barrier and said substrate is achieved; and

coating said solution on at least one side of said substrate and thereafter cross-linking said poly(vinyl alcohol) in the absence of a catalyst to provide an effective oxygen barrier thereon.

13. The structure according to Claim 12, wherein said poly(vinyl alcohol) has a viscosity of from 5 cps to 15 cps at 4% solution and 20ºC and a hydrolysis level above 99%.

14. The structure according to any one of Claims 12 or

13, wherein said tensoactive agent is 1-octanol.

15. The structure according to any one of Claims 12 to

14, wherein said solution includes from 5% to 10% by weight of solids, said solids comprising from 70% to 95% by weight of poly(vinyl alcohol) having a viscosity of from 5 cps to 15 cps at 4% solution and 20ºC and which is hydrolyzed to a level above 99%, from 5% to 30% by weight of glyoxal and from 5 ppm to 0.5% of 1-octanol.