Process for the manufacture of microporous film

Abstract

A vapor permeable and liquid impermeable microporous film suitable for diaper back sheets and other disposable applications is produced by first abrading a filled, unoriented film by passing it through at least one set of at least two cooperating nip rollers, each having an abrasive grit surface and then subjecting the unoriented abraded film to a corona treatment.

Description

BACKGROUND OF THE INVENTION

Porous plastic films can be grouped into two different types: (1) macroporous films which are both vapor and liquid permeable and (2) microporous films which are vapor permeable but impermeable to liquids.

Various processes have been disclosed for the manufacture of porous films of both types, all of them involving the formation of pores or perforations extending through the film from one film surface to the other.

One group of such processes entail the formation of an unfilled thermoplastic resin film and then perforating or piercing the film during its passage through the nip of two rollers. For instance, in the process of U.S. Pat. No. 3,302,501, the piercing objects are pins or needle-like projections extending from the surface of one or both rollers. Other processes utilize pairs of rollers, one of these having a smooth, often heated surface, and the other having either projections in its surface as in U.S. Pat. No. 3,073,304 or an abrasive surface coating as in U.S. Pat. No. 3,718,059. The latter processes have not been entirely successful because of the manufacturing cost of the rollers having surface projections and also because of operational problems causing undesired large variations in the film pore diameters. In addition, the improvements in the moisture vapor transmission rates have been less than desired using the smooth pressure roller techniques.

A second group of such perforation processes employs differential pressure, e.g., vacuum, between the surfaces of a heated film as the film is passed over a perforated screen, causing the film to be drawn into the openings of the screen and thereby become perforated. Such processes are disclosed in U.S. Pat. Nos. 4,351,784 and 4,456,570. The resulting perforated films are macroporous and are liquid permeable.

A third group of processes accomplish the perforation by first forming a film of an incompatible polymer matrix, either polymer-to-filler as in U.S. Pat. No. 4,472,328 and British Application No. 2,151,538, or incompatible polymer-to-polymer as in Japanese Patent No. 73-28789, and then stretching the film in one or more directions causing the formation of microtears in the film. Generally, the physical properties, especially the strength and the hydrostatic pressure resistance of the films so produced are not as good as would be desired.

There is also a process disclosed in U.S. Pat. No. 4,364,985 for preparing a porous microfilled thermoplastic film, wherein the inorganic filler particles are required to have an effective diameter larger than the thickness of the film. Small spaces are formed around the particles and when the filled film is passed over a set of serially positioned abrading rollers for the purpose of rubbing off the surfaces of the film that overlie the outermost portions of the filler particles, there is formed a multitude of fine pores extending from one film surface to the other. This technology has severe extrusion problems due to particle size requirement and hence weak properties.

U.S. Pat. No. 3,880,966 discloses a process for the manufacture of microporous films which involves the corona treatment of a nonporous, elastic starting film followed by a series of necessary steps comprised of cold stretching, hot stretching and heat setting to render to the corona treated film a microporous structure. The physical properties of these films, especially then the strength and hydrostatic pressure resistance, are not sufficiently high to utilize the films for many applications.

Also, corona treatments have been disclosed as useful in further improving the liquid permeability of macroporous films, such as the vacuum formed perforated films previously mentioned in U.S. Pat. Nos. 4,351,784 and 4,456,570.

It is therefore, an object of the present invention to provide a novel process for the production of a microporous filled film which is moisture permeable and liquid impermeable as measured by moisture vapor transmission rate and hydrostatic pressure resistance.

DESCRIPTION OF THE DRAWING

The FIGURE shows a schematic diagram of an embodiment of the process of the present invention.

THE INVENTION

In accordance with the present invention there is provided a process for the production of an unoriented microporous film which is moisture permeable and liquid impermeable which comprises:

(a) providing an unoriented film made from a blend of a high-molecular weight thermoplastic resin and an inorganic particulate filler, said thermoplastic resin being selected from the group consisting of polyethylene, linear low density polyethylene, polypropylene, polybutylene, ethylene-propylene copolymers and mixtures thereof, the effective average particle diameter of the filler being less than the thickness of the film;

(b) passing the film through at least one set of at least two cooperating nip rollers, each nip roller being provided with an abrasive surface,

(c) withdrawing from the last set of nip rollers an unoriented abraded film having an MVTR of at least about 100 gm/m.sup.2 /24 hours;

(d) subjecting the film from step (b) directly to at least one corona discharge treatment, and

(e) recovering an unoriented microporous film having an enhanced MVTR as compared to that of the film of step (c) while retaining other physical properties including hydrostatic pressure resistance at levels substantially unchanged as compared to those of the film of step (c).

For diaper back sheets and other leak-proof clothing and sanitary applications, a particularly suitable resin is one comprised of from about 65 wt % to about 95 wt % of a low density polyethylene having a density in the range from about 0.910 to about 0.935 gms/cc, and at least 5 wt % of a resin component selected from the group consisting of high density polyethylene having a density exceeding about 0.940, a linear low density polyethylene of a density in the range from about 0.915 to about 0.945 gms/cc, high molecular weight polybutylene and mixtures thereof. The linear low density polyethylene is an interpolymer of ethylene and one or more C.sub.4 -C.sub.12 alpha olefins. Especially preferred are the copolymers of ethylene with hexene-1 and/or octene-1. The melt index of the total resin should be between 0.5 and about 10 g/10 min.

The resin composition also contains an inorganic filler, such as calcium carbonate, barium sulfate, mica, titanium dioxide and the like. The concentration of the filler should range between about 5 and about 25 parts by weight per 100 parts by weight of the resin, and the average effective particle size of the filler should be less than the film thickness. Generally, the average particle size is in the range between about 3 and about 30 microns, the thinner the film thickness the smaller the particle size. Preferably, the filler is calcium carbonate.

For appearance, the resin composition usually contains a whitener such as titanium dioxide pigment when titanium dioxide is not the principal filler. The concentration thereof is generally maintained between about 3 and about 16 parts by weight per 100 parts by weight of the resin.

Other additives such as antioxidants, lubricants, stabilizers, etc. may also be added for their known purposes and in conventional quantities.

The film can be produced by any known commercial process, e.g. by casting or blown film techniques. The film thickness should range between about 0.9 mil and about 6 mil. Prior to treatment according to the process of this invention, the film may be subjected to an embossment or other treatment to impart a decorative pattern onto the surface of the film.

The nip rollers each have an abrasive surface which is usually provided in the form of coating with an abrasive material such as sand paper, emery cloth, garnet paper, aluminum oxide, etc. The abrasive typically has a grit size ranging between about 80 and about 250 grain. It is not necessary that the entire surface of each of the rollers be covered with the abrasive. The pressure at the nip of the rollers can vary between 10 psig and about 100 psig. The temperature is maintained at ambient conditions.

It is not necessary that a set of the cooperating nip rollers have equal roller diameters, but one roller can have a larger diameter than the other. It is also possible to have one larger roller in cooperative relationship with more than one other abrasive roller of smaller diameter. For instance, the equivalence of five serially positioned nips can be accomplished by passing the film over an abrasive nip roller partially surrounded by and in cooperative relation with five abrasive nip rollers of smaller diameter.

In passing the filled film through a nip section, the rollers crush particles buried in the body of the film and also extract particles from the film surfaces. In the very small spaces where such particles have been crushed or extracted, the effective mass of the polymer is reduced but not to the extent that any significant perforation of the film occurs. The microporous films produced by the abrasion process step, therefore, exhibit enhanced moisture vapor transmission rates while being impermeable to liquids as measured by the hydrostatic pressure resistance.

The abrasion treatment should be carried to produce a film having a moisture vapor transmission rate of at least 100 gm/m.sup.2 /24 hours and preferable between about 500 to about 150 than 100 MVTR the subsequent corona discharge treatment does not have any significant effect upon enhancing the rate.

The corona discharge treatment follows the abrading step directly without any intermediate hot drawing or cold drawing steps. Nor should any of these drawing operations follow the corona discharge treatment. In exposing the film to corona discharge, it is passed between a pair of electrodes, one of which is in the form of a grounded metallic roller or stationary bar and which cooperates with the other electrode connected to a suitable high voltage, high frequency power source. The latter electrode is spaced parallelly from the grounded electrode establishing a uniform air gap between the electrodes. The spacing is usually maintained below about 0.25 inches and preferably between about 0.0005 and about 0.06 inches.

The electrode receiving the high voltage operating potential may consist of a series of metal hinges having finely serrated edges evenly spaced across the width of the electrode. Alternately, the electrode may be in the form of a series of brass brushes. The potential between the electrodes should be maintained between about 3000 and about 50,000 volts and a suitable current is between about 0.35 and about 5 amperes. The treatment is typically carried out at a frequency of from about 50 KHz to about 60 KHz.

In passing the abraded, filled film through the high power corona discharge unit, the discharge takes the path of least resistance. As a result, holes are burned through the film in those locations where the filler particles have been crushed or extracted and the effective mass of the polymer has been decreased.

The films produced by the process of this invention have excellent properties making them especially useful in disposable film applications, such as diaper back sheets, etc. Specifically, the films exhibit excellent moisture vapor transmission rates while having an acceptable hydrostatic pressure resistance. Because no stretching or orientation is required to render the desired porosity, the physical properties are virtually unaffected and remain at desired high levels. Also, the appearance of the film products of the invention as measured by opacity, softness, and gloss is very good.

Reference is now had to the FIGURE which schematically depicts an embodiment of the prodess of the invention.

The plastic film 10, fed from a supply (not shown) and guided by idler rollers 11 and 12, is passed through the nip between abrasive roller 13 and the conductive roller 14, which is grounded (not shown). At 15 there is shown a hinged electrode, which is electrically connected to a suitable high frequency, high voltage power source. The electrode is spaced from the conductive roller and is parallel to the conductive roller axis thereby establishing a uniform air gap between the electrode and the film passing over the roller. The electrostatically treated film having an enhanced microporous structure is guided by roller 16 to wind-up.

For a better understanding of the invention reference is had to the following examples.

EXAMPLES 1-3

A blend was prepared from 75 wt % low density polyethylene (0.918 density, 1.2 MI), 5 wt % high molecular weight polybutylene and 20 wt % calcium carbonate (particle size of 3 microns). A 1.1 mil cast film was produced from this blend and subsequently embossed to produce a patterned film having a thickness of about 2.2 mil. The embossed film was subjected to abrasion without any stretching or orientation in any direction prior to the treatment. The abrasion treatment was carried out by passing the film ten times through the nip of two rollers covered uniformly with 80 grit sand paper at a nip pressure of 40 psi. Each of the rollers had a length of 131/4 inches and a diameter of 4 inches. The speed of each of the rollers was 400 feet per minute and the film passed through the nip at the same rate. The abraded film of Example 1 had an MVTR of about 1250, over a 60 fold increase over that of the embossed film before the abrasion treatment.

In Example 2, the abraded film of Example 1 was subsequently subjected 2 times to a corona discharge treatment by passing the film over a conductive roller at a speed of 400 feet per minute and using a hinged electrode connected to a high voltage power source. The electrode (Model No. 1242) was obtained from Electro Technic Products, Inc., 4644 North Ravenswood Avenue, Chicago, Ill. 60640. The spacing between the electrode and the conductive roller was about 0.002 inches. The voltage used in the treatment was about 40,000 volts, the current about 1-2 amperes and the frequency about 50 KHz.

As shown in Table 1, which lists the pertinent physical properties of the treated films of Examples 1 and 2, the moisture vapor transmission rate was considerably increased by the corona discharge treatment, i.e., from 1250 to over 2000 without any significant alteration in the other physical properties.

However, without the prior abrasion treatment as in Example 3, no significant improvement in the moisture vapor transmission rate was obtained, the unabraded film having an MVTR of 20 before the corona discharge treatment and an MVTR of only 60 after such treatment.

TABLE 1______________________________________Example No. 1 2______________________________________Film Thickness:Initial, mil 1.1 --Embossed, mil 2.2 2.6MI, gms/10 min -- --Opacity, ASTM D-1003 88 88Gloss, ASTM D-245 4.0 4.0ElongationM.D., % 50 50T.D., % 45 45Tensile StrengthM.D., psi 1520 1550T.D., psi 1220 12401% Secant ModulusM.D., psi 7630 7560T.D., psi 9575 9350Tear StrengthM.D., psi 18 18T.D., psi 110 110Coefficient of Friction 0.36 0.36Spencer Impact, gms/mil 45 --MVTR, gm/m.sup.2 /24 hours 1250 2011Hydrostatic Resistance 30 30______________________________________

It is to be understood that many alterations and modifications can be made to the process of this invention. All such departures are considered within the scope of this invention as defined by the specifications and appended claims.

Claims

1. A process for the production of an unoriented microporous film which is moisture permeable and liquid impermeable, which process comprises:

(a) providing an unoriented film made from a blend of a high molecular weight thermoplastic resin and an inorganic particulate filler, said thermoplastic resin being selected from the group consisting of polyethylene, linear low density polyethylene, polypropylene, polybutylene, ethylene-propylene copolymers and mixtures thereof, the effective average particle diameter of the filler being less than the thickness of the film;

(b) without perforation of the film or causing formation of straight through pores in the film passing the film through at least one set of at least two cooperating nip rollers, each nip roller being provided with an abrasive surface,

(c) withdrawing from the last set of nip rollers an unoriented abraded film having an MVTR of at least about 100 gm/m.sup.2 /24 hours;

(d) subjecting the film from step (b) directly to at least one corona discharge treatment, and

(e) recovering an unoriented microporous film having an enhanced MVTR as compared to that of the film of step (c) while retaining other physical properties including hydrostatic pressure resistance at levels substantially unchanged as compared to those of the film of step (c).

2. The process of claim 1 wherein the abraded film prior to corona discharge treatment had an MVTR between about 500 and about 1500 gm/m.sup.2 /24 hours.

3. The process of claim 1 wherein the pressure at the nip of the rollers is between about 10 and about 100 psig.

4. The process of claim 1 wherein the abrasive has a grit size between about 80 and about 250 grain.

5. The process of claim 1 wherein the potential between the electrodes is maintained between about 3000 and about 5000 volts.

6. The process of claim 1 wherein the corona discharge treatment is carried out using a current between about 0.35 and about 5 amperes.

7. The process of claim 1 wherein the corona discharge treatment is carried out at a frequency between about 50 and about 60 KHz.

8. The process of claim 1, wherein the thermoplastic resin contains a filler selected from calcium carbonate, barium sulfate, mica, titanium dioxide and mixtures thereof in a concentration ranging between about 5 and about 25 parts by weight per 100 parts by weight of the resin.

9. The process of claim 8 wherein the average particle size of the filler is ranging from about 3 to about 30 microns.

10. The process of claim 1 wherein the resin composition contains a whitener pigment in an amount ranging from about 3 to about 16 parts by weight per 100 parts by weight of resin.

11. The process of claim 1 wherein the resin is comprised of from about 65 to about 95 wt % of a low density polyethylene having a density in the range from about 0.910 to about 0.935 gm/cc and at least 5 wt % of a resin component selected from the group consisting of high density polyethylene having a density exceeding about 0.940, a linear low density polyethylene having a density in the range from about 0.915 and about 0.945, a high molecular weight polybutylene and mixtures thereof.