Post-treatment of non-woven webs

Claim 2

A process of electrostatically charging and improving the filtration performance of a nonwoven web which is consolidated and elastic in the cross-direction, which consolidated web is made from a precursor nonwoven web of non-elastomeric, thermoplastic fibers which process comprises conveying the heated consolidated web in a direction of draw, and subjecting the heated web to an electrostatic charge, whereby the consolidated web is heat-set, has a reduced average pore size not accompanied by significant average fiber diameter reduction in the direction of the draw, has a reduced pore size distribution with respect to the precursor web, and includes a planar layer of randomly organized nonelastomeric thermoplastic fibers bonded to each other, a majority of the fibers being aligned generally in the direction of the draw, and a minority of fibers being aligned generally in the direction of the draw, and a minority of fibers being organized in a cross-direction transverse to the direction of the draw, and further whereby the consolidated web has a maximum pore size of less than 80% of that of the precursor web and a room temperature elongation (strain) at break between 2 to 40%, based on test method ASTM D 1117-717, and cooling the web or permitting the web to cool.

Claim 3

The process of claim 1 wherein the web is heated to a temperature between the softening point and the melting point of the polymer in the web.

Claim 4

The process of claim 1 wherein the web is at a temperature between about 90° C. to about 130° C. while being subjected to the electrostatic charge.

Claim 5

The process of claim 1 wherein the web is cooled or allowed to cool after having been subjected to the electrostatic charge.

Claim 6

The process of claim 1 wherein the charged web is cooled to a temperature below about 90° C. after having been subjected to the electrostatic charge.

Claim 7

The process of claim 1 wherein the electrostatic charge is produced by an electric field ranging from about 1 kVDC/cm to about 10 kVDC/cm.

Claim 8

The process of claim 1 wherein the electric field ranges from about 1 kVDC/cm to about 4 kVDC/cm.

Claim 9

The process of claim 1 wherein the electric field ranges from about 3 kVDC/cm to about 8 kVDC/cm.

Claim 10

The process of claim 1 wherein the electric field is about 6 kVDC/cm.

Claim 11

The process of claim 1 wherein electrodes generate an electric field and the electrodes are maintained at a voltage difference which ranges from about 5 kV to about 20 kV.

Claim 12

The process of claim 10 wherein the voltage difference ranges between about 7.5 kV and about 12.5 kV.

Claim 13

The process of claim 11 wherein the voltage is about 10 kV.

Claim 14

The process of claim 10 wherein the web is generally aligned equidistant from the electrodes.

Claim 15

The process of claim 10 wherein the electrostatic charge is produce by an electric field ranging from about 1 kVDC/cm to about 10 kVDC/cm.

Claim 16

The process of claim 10 wherein one electrode is charged to a positive and the other electrode to a negative voltage.

Claim 17

The process of claim 1 wherein the web is a composite or a laminate.

Claim 18

The process of claim 16 wherein the web is a composite which comprises at least two layers.

Claim 19

The process of claim 16 wherein the web is a composite which comprises more than two layers.

Claim 20

The process of claim 18 wherein the web composite comprises a meltblown web, a different meltblown and a meltblown web.

Claim 21

The process of claim 17 wherein the web comprises a non-thermoplastic web.

Claim 22

The process of claim 16 wherein the laminate comprises at least two nonwoven webs.

Claim 23

The process of claim 1 wherein a pair of rollers convey the web in the direction of draw, and wherein the web is subjected to the electrostatic charge after passing through the rollers.

Claim 24

The process of claim 1 wherein a pair of rollers convey the web in the direction of draw, and wherein the web is subjected to the electrostatic charge before passing through the rollers.

Claim 25

The process of claim 1 wherein the thermoplastic is a polyolefin selected from the group consisting of polypropylene, polyethylene, and copolymers thereof, and the heating step is carried out at a temperature of between 190 to 350 degrees Fahrenheit.

Claim 26

The process of claim 1 wherein the heated web is subjected to the electrostatic charge prior to cooling below about 90° C.

Claim 27

The process of claim 1 wherein the maximum pore size of the consolidated web is reduced by at least 20% and the pore size distribution by at least 20% with respect to the precursor web.

Claim 28

The process of claim 1 wherein the elongation of the web at break is between 5 to 20%.

Claim 29

The process of claim 2 wherein the web is heated to within 15° F. of the melting point of the polymer in the web.

Claim 30

The process of claim 1 wherein the non-elastomeric breaking draw ratio of the web during hot processing is less than 4.0 and greater than about 1.4 while hot drawing at a strain rate grater than 2500% min, and a temperature greater than the softening point but at least 10° F. less than the melting temperature of the polymer.

Claim 31

The process of claim 26 wherein the non-elastomeric fibers of the precursor do not have the ability to stretch at least twice their original length and retract at room temperature.

Claim 32

The process of claim 26 wherein the thermoplastic fibers of the precursor web have a crystallinity of at least 30%.

Claim 33

The process of claim 26 wherein the crystallinity is in the range of 30 to 70%.

Claim 34

The process of claim 1 wherein the consolidated web has an elasticity in the cross-direction of at least 70% recovery from a 50% elongation in the cross-direction.

Claim 35

A process of electrostatically charging and improving the filtration performance of a nonwoven web which is consolidated and elastic in the cross-direction, which consolidated web is made from a precursor nonwoven web of non-elastomeric, thermoplastic polyolefin fibers having a crystallinity of at least 30%, which process comprises conveying the heated consolidated web in a direction of draw, and subjecting the heated consolidated web in a direction of drawn, and subjecting the heated web to an electrostatic charge, whereby the consolidated web is heat-set has a reduced average pore size not accompanied by significant average fiber diameter reduction in the direction of the draw, has a reduced pore size distribution with respect to the precursor web, and includes a planar layer of randomly organized nonelastomeric thermoplastic fibers bonded to each other, a majority of the fibers being aligned generally in the direction of the draw, and a minority of fibers being organized in a cross-direction transverse to the direction of the draw, and further whereby the consolidated web has a maximum pore size of less than 80% of that of the precursor web and has an elasticity in the cross-direction of at least 70% recovery from a 50% elongation in the cross-direction, cooling the web or permitting the web to cool.

Claim 36

A process of electrostatically charging and improving the filtration performance of a nonwoven web which is consolidated and elastic in the cross-direction, which consolidated web is made from a precursor nonwoven web of non-elastomeric, thermoplastic polyolefin fibers having a crystallinity of at least 30%, which process comprises conveying the heated consolidated web in a direction of draw, and subjecting the heated consolidated web in a direction of drawn, and subjecting the heated web to an electrostatic charge, whereby the consolidated web is heat-set has a reduced average pore size not accompanied by significant average fiber diameter reduction in the direction of the draw, has a reduced pore size distribution with respect to the precursor web, and includes a planar layer of randomly organized nonelastomeric thermoplastic fibers bonded to each other, a majority of the fibers being aligned generally in the direction of the draw, and a minority of fibers being organized in a cross-direction transverse to the direction of the draw, and further whereby the consolidated web has a maximum pore size of less than 80% of that of the precursor web and has an elasticity in the cross-direction of at least 70% recovery from a 50% elongation in the cross-direction, cooling the web or permitting the web to cool.

Claim 37

The process of claim 34 wherein the polyolefins fibers are selected from the group of polypropylene and polyethylene.

Claim 38

The process of claim 34 wherein the web are meltblown or spunbond.