Abstract:
The method and apparatus of the present invention prevents the formation of pin-holes during stretching of strip laminates in the cross-machine direction (CD). Pin-holes are prevented by creating slack areas ( 10   a ) along the length of the laminate ( 10 ) where the edges of the non-woven strips ( 14 ) meet with the polymer film ( 12 ), pressing the slack areas ( 10   a ) into the interdigital stretching rollers ( 26 ) without stretching the slack areas ( 10   a ), and stretching the remainder of the laminate ( 10 ) in a typical manner. The slack areas ( 10   a ) are formed prior to interdigitation by, for example, formation of a furrow, a fold or a corrugation.

Description:
This is a divisional of application Ser. No. 09/124,583, filed Jul. 29, 1998, now U.S. Pat. No. 6,265,045. 
    
    
     FIELD OF THE INVENTION 
     The present invention relates to methods and devices for preventing the formation of pinholes in the production of laminates of non-woven webs and polymer film. In particular, these laminates have spaced laminated strips of non-woven webs and film with areas of nonlaminated film therebetween (herein referred to as “zone laminates”). 
     BACKGROUND OF THE INVENTION 
     Methods of making microporous film products have been known for some time. For example, U.S. Pat. No. 3,832,267, to Liu, teaches the melt-embossing of a polyolefin film containing a dispersed amorphous polymer phase prior to stretching or orientation to improve gas and moisture vapor transmission of the film. According to the Liu &#39;267 patent, a film of crystalline polypropylene having a dispersed amorphous polypropylene phase is embossed prior to biaxially drawing (stretching) to produce an oriented imperforate film having greater permeability. The dispersed amorphous phase serves to provide microvoids to enhance the permeability of the otherwise imperforate film to improve moisture vapor transmission (MVT). The embossed film is preferably embossed and drawn sequentially. 
     Many other patents and publications disclose the phenomenon of making microporous thermoplastic film products. For example, European patent 141,592 discloses the use of a polyolefin, particularly ethylene vinyl acetate (EVA) containing a dispersed polystyrene phase which, when stretched, produces a voided film which improves the moisture vapor permeability of the film. The EP &#39;592 patent also discloses the sequential steps of embossing the EVA film with thick and thin areas followed by stretching to first provide a film having voids which, when further stretched, produces a net-like product. U.S. Pat. Nos. 4,596,738 and 4,452,845 also disclose stretched thermoplastic films where the dispersed phase may be a polyethylene filled with calcium carbonate to provide the microvoids upon stretching. Later U.S. Pat. Nos. 4,777,073; 4,921,653; and 4,814,124 disclose the same processes described by the above-mentioned earlier publications involving the steps of first embossing a polyolefin film containing a filler and then stretching that film to provide a microporous product. 
     U.S. Pat. Nos. 4,705,812 and 4,705,813 disclose microporous films having been produced from a blend of linear low density polyethylene (LLDPE) and low density polyethylene (LDPE) with barium sulfate as the inorganic filler having an average particle diameter of 0.1-7 microns. It is also know to modify blends of LLDPE and LDPE with a thermoplastic rubber such as KRATON. Other patents such as U.S. Pat. No. 4,582,871 disclose the use of thermoplastic styrene block tripolymers in the production of microporous films with other incompatible polymers such as styrene. There are other general teachings in the art such as the disclosures in U.S. Pat. Nos. 4,921,652 and 4,472,328. 
     The stretching, as discussed above, results in the appearance of stripes along the length of the web. These stripes are caused by the difference in appearance between the highly stretched areas, occurring between the digits on the interdigital rolls, and the areas at the digits which are not as highly stretched. These methods result in stripes of highly stretched, highly porous areas adjacent moderately stretched, but still substantially porous, areas. 
     Relevant patents regarding extrusion lamination of unstretched non-woven webs include U.S. Pat. Nos. 2,714,571; 3,058,868; 4,522,203; 4,614,679; 4,692,368; 4,753,840 and 5,035,941. The above &#39;863 and &#39;368 patents disclose stretching extruded polymeric films prior to laminating with unstretched non-woven fibrous webs at pressure roller nips. The &#39;203 and &#39;941 patents are directed to co-extruding multiple polymeric films with unstretched non-woven webs at pressure roller nips. The &#39;840 patent discloses preforming non-woven polymeric fiber materials prior to extrusion laminating with films to improve bonding between the non-woven fibers and films. More specifically, the &#39;840 patent discloses conventional embossing techniques to form densified and undensified areas in non-woven base plies prior to extrusion lamination to improve bonding between non-woven fibrous webs and films due to the densified fiber areas. The &#39;941 patent also teaches that unstretched non-woven webs that are extrusion laminated to single-ply polymeric films are susceptible to pinholes caused by fibers extending generally vertically from the plane of the fiber substrate and, accordingly, this patent discloses using multiple co-extruded film plies to prevent pinhole problems. Furthermore, methods for bonding loose non-woven fibers to polymeric film are disclosed in U.S. Pat. Nos. 3,622,422; 4,379,197 and 4,725,473. 
     U.S. patent application Ser. No. 08/547,059 (herein incorporated by reference in its entirety), now abandoned, discloses a process and apparatus to continuously perform web splitting, separating, guiding and laminating steps in a single unit. A single wide web of a non-woven is slit into a number of narrow webs which are separated by the use of turning bars and steered into a laminator. More specifically, a web is unrolled from a wide roll of non-woven material. The incoming web is slit into narrow webs, the narrow webs move down line to turning bars which are displaced one from the other by a desired web separation distance. The spaced narrow webs are then guided into a nip of rollers for extrusion lamination with a polymer film. A molten polymer is extruded into the nip at a temperature above its softening point to form a polymeric film laminated to the narrow webs. The compressive force between the webs and the extrudate at the nip is controlled to bond one surface of the web to the film to form the laminate. The resulting laminate includes spaced strips of non-woven laminated to the polymer film with areas of nonlaminated film between the strips. 
     U.S. patent application Ser. No. 08/722,286 (herein incorporated by reference in its entirety), a Continuation-in-Part of U.S. patent application Ser. No. 08/547,059, discloses a process and apparatus to continuously perform lamination of a polymer to another material to which it is laminated. The &#39;286 application is directed to a process and apparatus to continuously perform non-woven web splitting, folding, guiding and laminating steps in a single unit. Depending on the spacing between folded webs, each strip of polymer may include a loose flap on either side of the laminate area which may be suitable for forming a barrier cuff in a diaper or other hygiene product. The spacing between folded webs determines the width of the loose polymer flap which is formed. Again, the resulting laminate includes spaced strips of non-woven laminated to the polymer film with areas of nonlaminated film between the strips. These laminates, having spaced laminated strips of non-woven and film with areas of nonlaminated film therebetween, are referred to as zone laminates. The resulting laminate includes spaced strips of non-woven laminated to the polymer film with areas of nonlaminated film between the strips. 
     SUMMARY OF THE INVENTION 
     With the development of the above referenced zone laminates, it has been discovered that pin-holes form at the boundary area between the laminated and non-laminated areas when the zone laminate is made microporous by stretching across the length of the strip. The method and apparatus of the present invention prevents the formation of pin-holes during such stretching of zone laminates. Pinholes are prevented by creating slack areas along the length of the web where the edges of the non-woven strips meet with the polymer film, pressing the slack areas into interdigital stretching rollers without stretching the slack areas, and stretching the remainder of the web by interdigitation. The slack regions are formed prior to interdigitation by, for example, formation of a furrow, a fold or a corrugation. 
     In one embodiment, the present invention includes a first interdigital roller and a second interdigital roller and at least one disc for contacting a slack area in the laminate and pressing the slack area into the first interdigital roller without stretching the slack area. In a preferred form, the device includes at least one disc which interengages with spaced rollers to create a slack area along the length of a laminate, the interengaged disc and rollers being laterally adjustable to create the slack area in a predetermined position on the width of the web. 
     These and other advantages and features, which characterize the invention, are set forth in the claims. For a better understanding of the invention, and of the advantages and objectives attained through its use, reference should be made to the Drawings, and to the accompanying descriptive matter, in which exemplary embodiments of the invention are described. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     FIG. 1 is a schematic perspective view showing an apparatus for pinhole prevention in zone laminates in accordance with one embodiment of the present invention. 
     FIG. 2 is a cross-sectional view showing an apparatus for pinhole prevention suitable for use in accordance with one embodiment of the present invention. 
     FIG. 3 is a cross-sectional view taken along line  3 — 3  of FIG. 2 of spacer discs and a furrow disc suitable for creating a slack area in a laminate in accordance with the present invention. 
     FIG. 3A is an enlarged plan view of the spacer discs and furrow discs shown in FIG.  3 . 
     FIG. 4 is a cross-sectional view taken along line  4 — 4  of FIG. 2 of the presser disc forcing the laminate into the grooves on the first interdigital roller in accordance with one embodiment of the present invention. 
     FIG. 5 is a cross-sectional view taken along line  5 — 5  of FIG. 2 showing the intersection of the first and second interdigital rollers used for stretching the laminate in the cross-machine direction. 
     FIG. 6 is a plan view of a progressive roll former suitable for use in creating a slack area in the laminate in accordance with one embodiment of the present invention. 
     FIG. 7 is a cross-sectional view taken along line  7 — 7  of FIG.  6 . 
     FIG. 8 is a schematic perspective view of a corrugator suitable for creating a slack area in the non-woven laminate suitable for use in the present invention. 
     FIG. 9 is a cross-sectional view taken along line  9 — 9  of FIG.  8 . 
     FIG. 10 is a graph showing the relationship between line speed and screw RPM of an extruder for use with the present invention. 
     FIG. 11 is a graph demonstrating the relationship between moisture vapor transmission properties and incremental stretching. 
     FIG. 12 is a graph showing the relationship between moisture vapor transmission rate and finish roll temperature prior to CD intermeshing. 
     FIG. 13 is an enlarged schematic cross-sectional view of the boundary area of the laminate after interdigital stretching. 
    
    
     DETAILED DESCRIPTION 
     The method and apparatus of the present invention prevent the formation of pin-holes at the boundary area of a zone laminate at the edges of a non-woven strip during interdigital stretching. Pin-holes form at the edge of the non-woven strip because the film and non-woven laminate is substantially stronger than the adjacent unlaminated polymer film; therefore, substantially all of the stretching occurs in the unlaminated film of the boundary area. It has been discovered that this excessive stretching in the boundary areas causes the formation of pin-holes. 
     In order to prevent pin-holing, the present invention provides for the formation of a slack area  10   a  at the boundary areas of the laminate, that is, where the edge of the non-woven strips  14  meet the polymer film  12  in laminate  10 , as shown in FIGS. 1,  3 A and  13 . In order to create these slack areas a number of spacer discs  18  which are slidably mounted on axle  16  are positioned such that the gap between adjacent discs  18  align with the boundary areas. Furrow discs  22  are slidably mounted on axle  20  so that each furrow disc  22  is received in the gap between adjacent spacer discs  18  at the boundary areas. A set of two spacer discs  18  and one furrow disc  22  interengage (as shown in FIGS. 3 and 3 a ) to create a slack area  10   a  along the length of the laminate  10 . The laminate  10 , including slack area  10   a , travels to the first interdigital roller  26  where the slack area is forced into the interdigital grooves  28  on roller  26  by presser disc  32 . Presser disc  32  includes a presser area  34  which conforms to the cross section of grooves  28 . The presser discs  32  force slack area  10   a  into the grooves  28  on the first interdigital roller  26  and form taut  37  areas along the remaining width of laminate  10 . The taut areas  37  pass between first roller  26  and second roller  38  and are stretched by interdigital grooves  28  and  40  to form microporous laminate  50 . 
     The microporous laminate may optionally be stretched along the length of microporous laminate  50  to increase porosity. The lengthwise stretching may be performed by any known method of forming micropores such as interdigital rolling or differential speed stretching of the laminate  10  either before or after stretching in the cross-machine direction. 
     As can be seen in FIG. 2, spacer discs  18  are mounted upon axle  16  by collar  18   a  and set screw  18   b . Furrow discs  22  are mounted upon axle  20  by collar  22   a  and set screw  22   b . Axle  20  is mounted upon a rotatable axle support  20   a  which pivots from a nonengaged position to an engaged position (shown in FIG.  2 ). The capacity to move furrow discs  22  to a nonengaged position allows for simplified threading of laminate  10  between spacer discs  18  and furrow discs  22 . When engaged, a furrow disc  22  is interengaged with a pair of spacer discs  18  to form a furrow which creates slack area  10   a  at the boundary areas of laminate  10 . Interdigital roll  26  is rotatably mounted on axle  24  and presser discs  32  are rotatably mounted on axle  30 . Presser discs  32  are movable along the length of axle  30  by collar  32   a  and set screw  32   b . Presser discs  32  are movable along axle  30  in a method similar to the movement of furrow discs  22  along axle  20  as discussed above. The presser disc  32  includes a presser area  34  around its periphery which is complimentary to the grooves on roll  26 . Presser area  34  presses the slack area  10   a  of laminate  10  into the grooves  28  on roll  26  without stretching of the slack area  10   a . The width of the laminate  10 , other than the slack areas  10   a , are held taut against the grooves of roller  26  so that the taut areas  37  are interdigitally stretched between roller  26  and roller  38 . 
     The intermeshing rollers  26 , 38  are capable of large engagement depths which may stretch the laminate up to about 200% or more of the original width to form the micropores. The equipment incorporates a controller (not shown) for the shafts  24 , 36  of the two intermeshing rollers  26 , 38  to control the degree of intermeshing and hence the amount of stretching imparted to the laminate. The controller also keeps shafts  24 , 36  parallel when the top shaft is raised or lowered to assure that the teeth of one intermeshing roller always fall between the teeth of the other intermeshing roller to avoid potentially damaging physical contact between intermeshing teeth. This parallel motion is assured by a rack and gear arrangement (not shown) wherein a stationary gear rack is attached to each side frame in juxtaposition to vertically slidable members. A shaft traverses side frames and operates a bearing in each of the vertically slidable members. A gear resides on each end of the shaft and operates in engagement with the racks to produce the desired parallel motion. 
     As shown in FIG. 3, the force of furrow discs  22  between spacer discs  18  causes the formation of a furrow to form slack area  10   a  between spacer discs  18 . As shown in detail in FIG. 3A the slack area  10   a  is preferably formed at the boundary areas of the zone laminate where the edges of the non-woven  14  meet polymer film  12 . The laminate  10 , including slack areas  10   a , travels from spacer discs  18  and furrow discs  22  to the first interdigitating roller  26 . As the first interdigitating roller  26  rotates about axle  24 , slack area  10   a  is pressed into the grooves  28  of the first interdigitating roller  26  by the complimentary structure  34  of presser rollers  32 , as shown in FIG.  4 . Due to the creation of the slack area  10   a , the laminate  10  is pressed into grooves  28  to form taut areas  37  but without stretching the web. The web then rotates about first interdigitating roller  26  to meet second interdigitating roller  38 . Interdigitating roller  38  rotates about axle  36  and grooves  40  intermesh with grooves  28  to stretch the taut areas  37  of laminate  10  in the cross-machine direction, that is, substantially no stretching occurs where the slack areas  10   a  have been pressed into the grooves  28  on the first roller  26 . 
     As can be seen in FIG. 3 the spacer discs  18  may be variously positioned along axle  16  by use of clamping collars  18   a  and clamping screws  18   b . Each furrow disc  22  includes a clamping collar  22   a  with a set screw  22   b  to allow the furrow disc to be variably positioned along axle  20 . Similarly, presser discs  32  include clamping collar  32   a  and set screw  32   b  to allow the presser discs  32  to be variably positioned along axle  30 . This adjustability allows for the processing of various widths of laminate without the need for substantial time spent setting up the machinery. 
     As seen in FIGS. 4 and 5, presser disc  32  interengages with grooves  28  on interdigital roll  26  by complimentary presser area  34  such as circumferential grooves to interact with a cross directional interdigital stretcher, a helical gear to interengage with a diagonal intermeshing stretcher, or a deformable member which conforms to the surface of roll  26 . Presser roller  32  forces the slack area  10   a  of laminate  10  into the grooves of roller  26  so that the taut areas  37  of laminate  10  are formed on either side of the presser roller  32 . These taut areas  37  are subsequently stretched between interdigital rollers  26 , 38  to form the microporous zone laminated sheet  50  having substantially unstretched portions along the length thereof. FIG. 13 shows the stretched laminate  50  including micropores  12   a  in the taut areas  37  of the polymer film  12  and the lack of micropores in the boundary area. 
     Other methods of forming a slack area  10   a  are shown in FIGS. 6-9. As shown in FIGS. 6 and 7 a progressive roll former  100  which includes a series of increasingly overlapped rollers may be used to create slack area  10   a . The first set of rollers  102   a ,  104   a ,  106   a  deform the laminate  10  to form a small slack area. The second set of rollers  102   b ,  104   b ,  106   b  have a larger overlap and thus form a larger slack area. The third set of rollers  102   c ,  104   c ,  106   c  are overlapped to form a slack area  10   a  of the desired shape. 
     A corrugator  120 , as seen in FIGS. 8 and 9 includes a first support plate  122  having a female corrugator  124  and a second support plate  126  which includes male corrugator section  128 . The male  128  and female  124  corrugator sections have an increasing cross-sectional area along the length of the web and are nested to cause the laminate  10  to deform and thus create slack area  10   a.    
     The laminate of the present invention may be achieved with the use of a wide variety of polymer films; however, in a preferred form the film is manufactured by first melt blending a composition of: 
     (a) about 35% to about 45% by weight of a linear low density polyethylene, 
     (b) about 3% to about 10% by weight of a low density polyethylene, 
     (c) about 40% to about 50% by weight calcium carbonate filler particles, and 
     (d) about 2% to about 6% by weight of a triblock copolymer of styrene selected from the group consisting of styrene-butadiene-styrene, styrene-isoprene-styrene, and styrene-ethylene-butylene-styrene, and blends thereof, 
     extruding the melt blended composition into a nip of rollers with an air knife to form a film at a speed on the order of at least about 550 fpm to about 1200 fpm without draw resonance, and 
     applying an incremental stretching force to the film along lines substantially uniformly across the taut areas of the laminate and throughout its depth to provide a microporous film. 
     More particularly, in a preferred form, the melt-blended composition consists essentially of about 42% by weight LLDPE, about 4% by weight LDPE, about 44% by weight calcium carbonate filler particles having an average particle size of about 1 micron, and about 3% by weight triblock polymer, especially styrene-butadiene-styrene. If desired, the stiffness properties of the microporous film products may be controlled by including high density polyethylene on the order of about 0-5% by weight and including 0-4% by weight titanium dioxide. Typically, a processing aid such as a fluorocarbon polymer in an amount of about 0.1% to about 0.2% by weight is added, as exemplified by 1-propene,1,1,2,3,3,3-hexafluoro copolymer with 1,1-difluoroethylene is included in the melt. The triblock polymer may also be blended with oil, hydrocarbon, antioxidant and stabilizer. 
     Both embossed and flat films may be produced according to the principles of this invention. In the case of an embossed film, the nip of rollers comprises a metal embossing roller and a rubber roller. The compressive force between the rollers forms an embossed film of desired thickness on the order of about 0.5 to about 10 mils. It has also been found that rollers which provide a polished chrome surface form a flat film. Whether the film is an embossed film or a flat film, upon incremental stretching at high speeds, microporous film products are produced having high moisture vapor transmission rate (MVTR) within the acceptable range of about 1000 to 4000 gms/m 2 /day. It has been found that flat film can be incrementally stretched more uniformly than embossed film. The process may be conducted at ambient or room temperature or at elevated temperatures. As described above, laminates of the microporous film may be obtained with non-woven fibrous webs. 
     The non-woven fibrous web may comprise fibers of polyethylene, polypropylene, polyesters, rayon, cellulose, nylon, and blends of such fibers. A number of definitions have been proposed for non-woven fibrous webs. The fibers are usually staple fibers or continuous filaments. The non-wovens are usually referred to as spunbond, carded, meltblown and the like. The fibers or filaments may be bicomponent to facilitate bonding. For example, a fiber having a sheath and core of different polymers such as polyethylene (PE) and polypropylene (PP) may be used or mixtures of PE and PP fibers may be used. As used herein “non-woven fibrous web” is used in its generic sense to define a generally planar structure that is relatively flat, flexible and porous, and is composed of staple fibers or continuous filaments. For a detailed description of non-wovens, see “Nonwoven Fabric Primer and Reference Sampler” by E. A. Vaughn, Association of the Non-woven Fabrics Industry, 3d Edition (1992). 
     In a preferred form, the microporous laminate employs a film having a gauge or a thickness between about 0.25 and 10 mils and, depending upon use, the film thickness will vary and, most preferably, in disposable applications, is on the order of about 0.25 to 2 mils in thickness. The non-woven fibrous webs of the laminated sheet normally have a weight of about 5 gms/yd 2  to 75 gms/yd 2 , preferably about 20 to about 40 gms/yd 2 . The composite or laminate can be incrementally stretched in the cross-machine direction (CD) to form a CD stretched composite. Furthermore, CD stretching may be followed by stretching in the machine direction (MD) to form a composite which is stretched in both CD and MD directions. As indicated above, the microporous film or laminate may be used in many different applications such as baby diapers, baby training pants, catamenial pads and garments, and the like where moisture vapor and air transmission properties, as well as fluid barrier properties, are needed. 
     The laminate is then incrementally stretched in the cross-machine direction (CD) or diagonally using the apparatus of the present invention to form a stretched laminate having unstretched regions along the length of the laminate. Furthermore, stretching according to the present invention may be followed by stretching in the machine direction (MD). 
     A number of different stretchers and techniques may be employed to stretch the film or laminate of a non-woven fibrous web and microporous-formable film. These laminates of non-woven carded fibrous webs of staple fibers or non-woven spun-bonded fibrous webs may be stretched with the stretchers and techniques described as follows: 
     The diagonal intermeshing stretcher consists of a pair of left hand and right hand helical gear-like elements on parallel shafts. The shafts are disposed between two machine side plates, the lower shaft being located in fixed bearings and the upper shaft being located in bearings in vertically slidable members. The slidable members are adjustable in the vertical direction by wedge shaped elements operable by adjusting screws. Screwing the wedges out or in will move the vertically slidable member respectively down or up to further engage or disengage the gear-like teeth of the upper intermeshing roll with the lower intermeshing roll. Micrometers mounted to the side frames are operable to indicate the depth of engagement of the teeth of the intermeshing roll. 
     Air cylinders are employed to hold the slidable members in their lower engaged position firmly against the adjusting wedges to oppose the upward force exerted by the material being stretched. These cylinders may also be retracted to disengage the upper and lower intermeshing rolls from each other for purposes of threading material through the intermeshing equipment or in conjunction with a safety circuit which would open all the machine nip points when activated. 
     A drive is typically utilized to drive the stationery intermeshing roller. If the upper intermeshing roller is to be disengagable for purposes of machine threading or safety, it is preferable to use an antibacklash gearing arrangement between the upper and lower intermeshing rollers to assure that upon reengagement the teeth of one intermeshing roller always falls between the teeth of the other intermeshing roller and potentially damaging physical contact between addenda of intermeshing teeth is avoided. If the intermeshing rollers are to remain in constant engagement, the upper intermeshing roll typically need not be driven. Drive may be accomplished by the driven intermeshing roller through the material being stretched. 
     The intermeshing rollers closely resemble fine pitch helical gears. In the preferred embodiment, the rollers have 5.935″ diameter, 45° helix angle, a 0.100″ normal pitch, 30 diametral pitch, 14½ pressure angle, and are basically a long addendum topped gear. This produces a narrow, deep tooth profile which allows up to about 0.090″ of intermeshing engagement and about 0.005″ clearance on the sides of the tooth for material thickness. The teeth are not designed to transmit rotational torque and do not contact metal-to-metal in normal intermeshing stretching operation. With such a diagonal intermeshing stretcher, a presser disc  32  having the configuration of a helical gear would be used. The use of a diagonal intermeshing stretcher provides for a stretching force having force components in both the cross-machine direction and the machine direction of the laminate. 
     The drive for the CD intermeshing stretcher typically operates both upper and lower intermeshing rollers except in the case of intermeshing stretching of materials with a relatively high coefficient of friction. The drive need not be antibacklash, however, because a small amount of machine direction misalignment or drive slippage will cause no problem. 
     The CD intermeshing elements are machined from solid material but can best be described as an alternating stack of two different diameter disks. In the preferred embodiment, the intermeshing disks would be 6″ in diameter, 0.031″ thick, and have a full radius on their edge. The spacer disks separating the intermeshing disks would be 5½″ in diameter and 0.069″ in thickness. Two rolls of this configuration would be able to be intermeshed up to 0.231″ leaving 0.019″ clearance for material on all sides. As with the diagonal intermeshing stretcher, this CD intermeshing element configuration would have a 0.100″ pitch. 
     The MD intermeshing stretching equipment is identical to the diagonal intermeshing stretch except for the design of the intermeshing rollers. The MD intermeshing rolls closely resemble fine pitch spur gears. In the preferred embodiment, the rolls have a 5.933″ diameter, 0.100″ pitch, 30 Diametral pitch, 14½° pressure angle, and are basically a long addendum, topped gear. A second pass was taken on these rolls with the gear hob offset 0.010″ to provide a narrowed tooth with more clearance. With about 0.090″ of engagement, this configuration will have about 0.010″ clearance on the sides for material thickness. 
     The above described diagonal or CD intermeshing stretchers may be employed with the pin-hole prevention apparatus of the present invention to produce the incrementally stretched film or laminate of non-woven fibrous web and microporous-formable film to form the microporous film products of this invention. For example, the stretching operation may be employed on an extrusion laminate of a non-woven fibrous web of staple fibers or spun-bonded filaments and microporous-formable thermoplastic film. In one of the unique aspects of this invention, a laminate of a non-woven fibrous web of spun-bonded filaments may be incrementally stretched to provide a very soft fibrous finish to the laminate that looks like cloth. The laminate of non-woven fibrous web and microporous-formable film is incrementally stretched using, for instance, the CD and/or MD intermeshing stretcher with one pass through the stretcher with a depth of roller engagement at about 0.060 inch to 0.120 inch at speeds from about 550 fpm to 1200 fpm or faster. The results of such incremental or intermesh stretching produces laminates that have excellent breatheability and liquid-barrier properties, yet provide superior bond strengths and soft cloth-like textures. 
     The microporous laminate typically employs a film having a gauge or a thickness between about 0.25 and 10 mils and, depending upon use, the film thickness will vary and, most preferably, in disposable applications is the order of about 0.25 to 2 mils in thickness. The non-woven fibrous webs of the laminated sheet normally have a weight of about 5 grams per square yard to 75 grams per square yard preferably about 20 to about 40 grams per square yard. 
     The following examples illustrate the method of making microporous film and laminates of this invention. In light of these examples and this further detailed description, it is apparent to a person of ordinary skill in the art that variations thereof may be made without departing from the scope of this invention. 
     EXAMPLES 1-5 
     Blends of LLDPE and LDPE having the compositions reported in the following TABLE 1 were extruded to form films and the films were then incrementally stretched to provide microporous films. 
     
       
         
               
               
               
               
               
               
             
               
               
               
               
               
               
               
             
               
               
               
               
               
               
             
               
               
               
             
           
               
                 TABLE 1 
               
               
                   
               
               
                 Formulation (by wt.) 
                 1 
                 2 
                 3 
                 4 
                 5 
               
               
                   
               
             
             
               
                 CaCO 3   
                 44.2 
                 44.2 
                 44.2 
                 44.2 
                 44.2 
               
               
                 LLDPE 
                 44.1 
                 44.9 
                 41.9 
                 41.9 
                 41.9 
               
               
                 LDPE 
                 1.5 
                 3.7 
                 3.7 
                 3.7 
                 3.7 
               
               
                 Others* 
                 10.2 
                 10.2 
                 10.2 
                 10.2 
                 10.2 
               
             
          
           
               
                 Screw 
                 A 
                 33 
                 45 
                 57 
                 64 
                 75 
               
               
                 RPM 
                 B 
                 33 
                 45 
                 57 
                 64 
                 75 
               
             
          
           
               
                 Basis wt. (gms/m 2 ) 
                 45 
                 45 
                 45 
                 45 
                 45 
               
               
                 Gauge (mils) 
                 2 
                 2 
                 2 
                 2 
                 2 
               
               
                 Line Speed (fpm) 
                 550 
                 700 
                 900 
                 1000 
                 1200 
               
               
                 Air Knife (cfm/inch) 
                 5-25 
                 5-25 
                 5-25 
                 5-25 
                 5-25 
               
             
          
           
               
                 Wet Stability 
                 Poor 
                 Good web stability without draw 
               
               
                   
                 gauge 
                 resonance 
               
               
                   
                 control 
               
               
                   
                 with draw 
               
               
                   
                 resonance 
               
               
                   
               
               
                 *Other components include 2.5% by weight of a styrene-butadiene-styrene (SBS) triblock polymer,  
               
               
                 # Shell Kraton 2122X, which is an SBS &lt;50% by wt. + mineral oil &lt;30% by wt., EVA copolymer  
               
               
                 # &lt;15% by wt., polystyrene &lt;10% by wt., hydrocarbon resin &lt;10% by wt., antioxidant/stabilizer  
               
               
                 # &lt;1% by wt., and hydrated amorphous silica &lt;1% by wt.  
               
             
          
         
       
     
     Each of the formulations of 1-5 were extruded into films employing an extrusion apparatus. The formulations of Examples 1-5 were fed from an extruder through a slot die to form the extrudate into the nip of a rubber roll and a metal roll. The incoming webs of non-woven material were also introduced into the nip of the rolls. In Examples 1-5, the thermoplastic film was produced for subsequent incremental stretching to form the microporous film. As shown in TABLE 1, over speeds of about 550 fpm to 1200 fpm, a polyethylene film on the order of about 2 mils in thickness was made which is taken off the roller. The compressive force at the nip is controlled such that the film is made without pin-holing and without draw resonance in the case of Examples 2-5. The melt temperatures from the feed zone to the screw tip of extruders were maintained at about 400-430° F. with die temperatures of approximately 450° F. to extrude the precursor film around 2 mils (45 g/m 2 ). 
     As shown in TABLE 1, over speeds of about 550 fpm to 1200 fpm, a polyethylene film on the order of about 2 mils in thickness was made which is taken off the roller. The air knife has a length of about 120″ and an opening of about 0.035″-0.060″ and air is blown through the opening and against the extrudate at about 5 cfm/inch to 25 cfm/inch. The compressive force at the nip and the air knife are controlled such that the film is made without pin-holing and without draw resonance in the case of Examples 2-5. Where the LDPE was included in the composition at a level of 1.5% by weight, draw resonance was encountered at a line speed of 550 fpm. However, when the LDPE was included in the formulation at a level of 3.7% by weight with the LLDPE at a level of 44.1-44.9% by weight, film production was able to be achieved at high speeds greater than 550 fpm up to 1200 fpm without draw resonance. The melt temperatures from the feed zone to the screw tip of the extruders were maintained at about 400-430° F. with die temperatures of approximately 450° F. to extrude the precursor film around 2 mils (45 gms/m 2 ). 
     FIG. 10 is a graph demonstrating the line speeds for Examples 1-5 and the necessary screw speed. Example 1, which contained only 1.5% by weight of LDPE, resulted in a poor film gauge control with draw resonance even with the air knife. However, when the LDPE was increased to about 3.7% by weight, excellent web stability was achieved without draw resonance even when line speeds were increased to about 1200 fpm. 
     FIG. 11 is a graph demonstrating the moisture vapor transmission properties (MVTR) of both embossed and flat films resulting from incrementally stretching the precursor films of Examples 2-5 under different temperatures and stretch roller engagement conditions. The MVTRs for the embossed film on the order of about 1200-2400 gms/m 2 /day were achieved, whereas MVTRs for the flat film on the order of about 1900-3200 gms/m 2 /day were achieved. FIG. 12 shows the impact of the temperature of the CD preheat roller upon MVTR. The MVTR for the film varied between about 2000-2900 gms/m 2 /day with the roller preheat temperature between about 75-220 F. The embossed film was made with a metal embossing roller having a rectangular engraving of CD and MD lines with about 165-300 lines per inch. This pattern is disclosed, for example, in U.S. Pat. No. 4,376,147 which is incorporated herein by reference. This micro pattern provides a matte finish to the film but is undetectable to the naked eye. 
     Those skilled in the art will recognize that the exemplary embodiment illustrated in the drawings is not intended to limit the invention. Indeed, those skilled in the art will recognize that other alternative embodiments may be used without departing from the scope of the invention.