CA2340972C - Durably wettable, liquid pervious webs - Google Patents

Abstract

Disclosed are durably wettable, liquid pervious webs that are particularly useful as topsheet materials for absorbent articles, such as baby and adult diapers, feminine hygiene products and the like. The durab ly wettable, liquid pervious webs are formed by applying a relatively permanent hydrophilic coating onto at least one surface of a web (a polymeric film or nonwoven) via plasma polymerization. Also disclosed are absorbent articles which include the durably wettable, liquid pervious webs as a topsheet, as well as the plasma polymerization process for making the durably wettable, liquid pervious webs.

Description

DURABLY WETT.~BLE, LIQUID PERVIOUS WEBS
' TECHNICAL FIELD
The present invention relates to a durably wettable, liquid pervious web chat is particularly suitable as a topsheet for absorbent articles. More particularly, the invention relates to a polymeric film or nonwoven to which is applied a thin coating of organic material onto at least one surface of the film or nonwoven. The thin organic coating is applied by a plasma-induced chemical vapor deposition process.
The thin organic coating renders the web more permanently hydrophilic than other methods known in the art. The invention further relates to a process for making the durably wettable, liquid pervious web, and to articles containing the durably wettable, liquid pervious web as a topsheet.
BACKGROUND OF THE INVENTION
Polymeric and nonwoven webs are common components of disposable absorbant articles, dryer sheets and the like. More particularly, macroscopically expanded, three-dimensional, polymeric films have been utilized as topsheet materials for disposable absorbent ~ articles. As used hcrcin, the term "macroscopically expanded", when used to describe three-dimensional webs, refers to webs which have been caused to conform to the surface of a three-dimensional forming structure so that both surfaces thereof exhibit the three-dimensional pattern of the forming structure or webs that have an inherent threc-dimensional pattern arising from their structure. Regardless of whether the three-dimensional pattern is inherent or generated by application of a forming process, the pattern is readily visible to the naked eye when the petpertdicular distance between the viewei s eye and the plane of the web is about 12 inches. By way of contrast, the term "planar", when utilized herein to describe nonwovens and polymeric films, refers to the overall condition of the web when viewed by the naked eye on a macroscopic scale. In this context "planar" webs may include webs having fine-scale surface aberrations on one or both sides, the surface aberrations not being readily visible to the naked eye when the perpendicular distance between the viewer's eye and the plane of the web is about l2 inches or greater.
One macroscopically expanded. three-dimensional aperntred polymeric web which is particularly well suited to transferring liquid deposited on one surface thereof to its opposite surface and thereafter isolating the transferred liquid from a wearer's skin is disclosed in commonly assigned U.S. Patent No.
3.929,135 issued to Thompson on Dec. 30, 1975.

.2.
Thompson describes a macroscopically expanded, three dimensional web (e.g., a topsheet) comprised of liquid impermeable material, but provided with a pattern of tapered capillaries, the capillaries having a base opening in the plane of the topsheet and an apex opening remote from the plane of the topsheet, the apex opening being in intimate contact with the absorbent pad utilized in the disposable absorbent article. The 40 Thompson topsheet allows the free transfer of liquids from the wearer's body into the absorbent element of the device while inhibiting the reverse flow of these liquids. This provides a relatively much drier surface in contact with the user than had previously been obtainable. Another macroscopically expanded three-dimensional apertured plastic web well suited for use as a topsheet on absorbent articles such as sanitary napkins is disclosed in commonly assigned U.S. Patent No. 4,342,314 issued to Radel et al. on Aug. 3, 45 1982. The macroscopically expanded, three-dimensional plastic web disclosed in the Radel patent exhibits a fiber-like appearance and tactile impression which has been favorably received by consumers when used as a wearer contacting surface. According to the teachings of the commonly assigned patents to Thompson and to Radel, et al., plastic webs of the aforementioned type can be made by applying a pressure differential to the web while it is supported on a three-dimensional forming structure until the web is 50 macroscopically expanded to comply with the three-dimensional cross-section of the forming structure on which it is supported. When aperiuring of the macroscopically expanded, three-dimensional web is desired, the pressure (vacuum is described) differential is applied continuously until such time as aperturixig of the web in areas coinciding with the apertures in the forming structure has been completed.
A mufti-phase, liquid-based process such as that described in U.S. Patent No.
4.609,518, issued 55 September 2, 1986 to Curro et al. (hereafter referred to as "'518 patent"), was also developed to provide a film with very small and very large apertures immediately adjacent one another. As the patent discloses, the formation of the very small (inciudine micro-sized) apertures in the direction opposite those formed for large apertures hinders the ability of initially unabsorbed liquid from running off the web's surface. Thus, liquid not immediatciy transported through the large apertures is restrained from running off the web's 60 surface, and is subsequently taken up through the larger apertures and is deposited in the article's core where the web is used as a topsheet material. These outwardly formed small apertures also reduce the level of web/skin contact and reduce the rigidity of the film, and thereby feel more comfortable to the user.
Wearers have reported that such topsheets have a soft silky surface.
Altemativcly, the '518 patent discloses films where the very small apcrtures are formed in the same direction as the macro-apertures.
65 Regardless of the means employed for aperture formation, where a wettable film material is desired, the above refcrences generally obtain such a structure by surface treating the naturally hydrophobic polymeric web with a wetting agent. Surface treatment is generally accomplished by either spraying surfactant onto the web's surface or by dipping the web in a surfactant-containing bath. Regardless of which of these methods is employed, surface treatment suffers from the inahiliry~ to precisely control the 70 location and level of treatmcnt, as well as adversc effecu caused by migration of significant amounts of surfactant into apertures and othcr components (e.g., absorbcnt core) when the apertured film is used as a topsheet in an absorbent article. Surface acatment further suffers from the disadvantage that desirable wetting agents, or surfactants, tend to be washed off upon repeated exposure to such liquids. Thus, when 75 used as a fopsheet in an absorbent article. the treated films lose their ability to transport liquid away from the skin and into the article's core after repeated wettings.
f U.S. Patent No. 4,535,020, issued to Thomas et al._on August 13, 1985, addresses some of the problems associated with surface treating vacuum-formed apertured films by incorporating hydrophilic surfactant in the polymeric resin before . extrusion for film formation (referred to herein as "resin 80 incoiporated surfat:zant", or "RIS"). (Sec also commonly assigned U.S.
Patent No. 5,792,412 to Y. P.
Lee et al., issued August 11, 1998; U.S.. Patent No. 4,923,914 to Nohr et al., issued May 8, ) 990; U.S. Patent No. 5,07,262 to Nohr et al., issued October 15, 1991; U.S. Patent No. 5,120,888 to Nohr et al., issued June 9. .1992.) According to the teachings of Thomas, after extrusion of the resin/surfactant mixture, and subsequent formation of the apertures, the incompatible surfactant eventually 85- blooms to the film's surface to provide a more durably wettable web.
However, as with surface treatment, RIS suffers from some degree of surfactant wash-off during use and/or during manufacture, particularly if liquid pressure differentials are used to form the web's apertures. Also, hydrophilic webs formed using RIS
techniques arc not immediately wettable. and depending on the relationship between the resin and the surfactant and environmental conditions, may not become wettable for finite periods of time. Similarly, 90 when such webs are used in absorbent articles, there will be some time delay before surfactant (that is washed off during wear) is replenished at the we'b's surface.
In spite of the teachings of the prior art, there remains a need for a liquid pervious web or film material that offers improved durable wenabiiiry after the passage of time and/or after exposure to. liquid insults. Such materials have particular suitability for use in disposable absorbent structures. There also 9~ remains the need for a process that provides such a durably wettable, liquid pervious web.
Accordingly, it is an object of an aspect of the present invention to provide a liquid pervious web having improved durable wettability. This durable wettabiiity is attained by applying a plasma-induced hydrophilic coating onto at least one surface of the starting web, to render the resulting web durably hydrophilic.

SUMMARY OF THE INVENTION
The present invention relates to a durably wettable, liquid pervious web that is particularly useful as a topshect material for absorbent articles. In one respect, the inventions relates to a durably-wettable, liquid pervious web which comprises:
105 (t) a web selected from the group consisting of polymeric fiitns and nonwovens;
(ii) a substantially continous hydrophilic coating, less than about 2.5 microns thick, on at least one surface of the web, wherein said hydrophilic coating is applied to the web by plasma polymerization;
wherein at least one surface of the durably-wettablc, liquid pervious web has a Post Aging contact angle 110 that is not more than about 60 degrees greater than the Pre Aging contact angle.
In a similar aspect respect, at least one surface of the treated web will have a Post Washing contact angle that is not more than about 60 degrees greater than the Pre Washing contact angle. Preferably, both conditions will exist in a single web.
The invention also relates to an absorbent article comprising a durably wettable, 115 liquid pervious topsheet, the topsheet comprising a web and a hydrophilic coating on at least one surface of the web, wherein the hydrophilic coating is applied to the substrate by plasma polymerization.
According to an aspect of the present invention, there is provided a process for making a durably wettable, liquid pervious apertured web for use as a topsheet in an 120, absorbent article, the process comprising the steps of:
a) forming apertures in a web, which is a polymeric film or nonwoven web;
b) direct plasma polymerizing the apertured web of step (a) by:
(i) introducing the web in a plasma reaction zone; and (ii) coating at least one surface of the web with a coating of polymerized 125 monomers, wherein the coating is less than 2.5 microns thick and is derived from a monomer gas stream that provides a hydrophilic coating upon plasma polymerization, whereby the polymerized monomers cause the at least one surface of the web to become durably wettable.
According to an aspect of the present invention, there is provided the use of a web produced by the process described above for use as a topsheet in an absorbent article.
130 Finally, the invention relates to a plasma polymerization process for making the durably wettable, liquid pervious webs described herein.
DETAILED DESCRIPTION OF THE INVENTION
135 I. Durably Wettable, Liquid Pervious Webs As discussed in detail below, the present invention relates to a durably wettable web that is prepared by applying a hydrophilic coating to a starting polymeric film or nonwoven, using a plasma polymerization process.
As used herein, the term "web" refers to the starting substrate (i.e., a polymeric film 140 or nonwoven) to which the hydrophilic coating is applied. In contrast, the terms "durably wettable, liquid pervious web" or "treated web" refer to the final product -the polymer film or nonwoven having the durable hydrophilic coating.
As used herein, the term "liquid pervious" refers to the ability of a web or treated web to transport liquids from one surface of the web or treated web to the opposite surface of the 145 web or treated web in a sufficiently efficient manner so as to allow the treated web to be used 4a as a component of a disposable article. Webs may be inherently liquid pervious or may be made liquid pervious by application of a processing step. such as, aperturing.
As used herein, the term "substantially continuous" means sufficiently continuous to provide the hydrophilic or wettable properties as defined by the stated or claimed contact 150 angle limitations.
As used herein, the terms "hydrophilic" and "wettable" are used interchangeably and refer to surfaces that are wettable by aqueous liquids (e.g., aqueous body liquids) deposited on these surfaces. Hydrophilicity and wettability are typically defined in terms of contact angle and the surface tension of the liquids and solids involved. This is discussed in detail in the 155 American Chemical Society publication entitled Contact Angle, Wettability and Adhesion, edited by Robert F. Gould (Copyright 1964). A web surface is said to be wetted by a liquid (i.e., hydrophilic) when either the contact angle between the liquid and the web surface is less than 900, or when the liquid tends to spread spontaneously across the surface of the web, both conditions normally co-existing. Conversely, a surface is considered to be hydrophobic if the 160 contact angle is greater than 900 and the liquid does not spread spontaneously across the surface of the web. In general, the lower the contact angle between the surface and the liquid, the more hydrophilic the surface.
The durably wettable, liquid pervious webs of the present invention are "durably wettable", insofar as the hydrophilic character engendered to the otherwise more hydrophobic 165 film is maintained over time and after exposure to liquids. As discussed above, prior approaches directed at making hydrophobic films wettable result in initial improvements in wettability, but suffer from the negative attribute that wettability is lost over time and/or exposure to liquids. While not being bound by theory, it is believed that typical 150 hydrophilic polymer and surface-treated polymer systems, such as corona discharge treatments, go through a "hydrophobic recovery" process. During the hydrophobic recovery process, surface wettabiliky tends to decay over time because thermodynamics favors the exposure of lower surface energy molecular chain segments at polymer surface. Upon aging, hydrophilic molecular segments reorient and embed themselves and expose hydrophobic segments at polymer surface. If chemical crosslinking is induced at the polymer 155 surface, the crosslinking tends to limit polymer chain mobility, thus significantly slowing the "hydrophobic recovery" process and therefore preserving polymer surface wettability over time. Since Applicants' invention provides for polymer chemical crosslinking, via a radiation curing process, a durably wettable, liquid pervious web can be produced.
Durable wettability is described herein in terms of the ability of a durably wettable, liquid pervious 160 web (as indicated, also referred to herein as a "treated web", to distinguish from the starting more hydrophobic "web") to retain its wettable character after aging (referred to as "Post Aging") and/or after exposure to liquids (referred to as "Post Washing"). The methods for measuring Post Aging contact angle and Post Washing contact angle are discussed below.
As indicated, the durable wettability of the present durably wettable, liquid pervious webs is 165 attained by use of a plasma process. Plasma is often referred to as the fourth state of matter. When energy is applied to a solid (e.g., a polymeric film or nonwoven), the solid can undergo a transition to the liquid state. If further energy is applied, the liquid becomes a gas. If additional energy of the proper kind is applied, the gas dissociates and becomes plasma. Plasmas exist in a variety of forms. The preferred plasma useful herein is a low pressure or vacuum process, which allows processing of the web at or near ambient 170 temperature, i.e.: about 20°C. This prevents thermal degradation of the web being processed andior thermal distortion of the formed web that is being treated. Within the plasma chamber where the web is to be treated, active species in the form of electrons, free-radicals, ions and energetic neutrals collide with the surface of the web, e.g. polymer, breaking molecular bonds and creating new functional groups on the surface. These active and energetic species also react in the gas phase, resulting in a thin coating being 175 deposited on at least one surface of the web.
Suitable plasma systems for use in the present invention incorporate a parallel plate electrode design where materials to be treated are exposed directly to the primary field of RF energy, but are not part of the circuitry. The subsequent primary plasma is particularly more uniform and more efficient since the part is exposed in al! three dimensions to the glow discharge. With higher pressure processes (but still 180 within the general definition of a cold gas plasma), some form of gas delivery system, designed to create a uniform laminar flow of process gas throughout the entire chamber volume is beneficial. In multiple electrode/shelf designs, it is important that each of the electrodes receive equal amounts of RF energy. In this manner a uniform glow discharge is created between each shelf or in each plasma zone. Solid state components and microprocessor control of the system parameters of process time, flow rate, power level, .6-185 and working pressure, will also ensure process uniformity, efficiency, and repeatability.
Since plasmas are electrically conductive atmosphetta, they carry a charactetutic impedance to the output of the RF generator. Therefore, the preferred plasma process utilizes a matching netwotk to constantly tune the plasma impedance to the output irttpedance of the RF
generator. Advanced plasma systems suitable Yor use in the present invention art: available from HIMONT
Plasma Science; Foster City, 190 CaliC. (a btuinas unit of HIMONT U.SA., lac.), and incorporate an automatic matching type of network and provisions for crro~r checking during the process. . . .
'the low temperature plasma is generated in a gaseous atmosphere at reduced pressure of from about 0.001 to about 10 Torn, preferably from about 0.01 to about 5 'Corn, more preferably from about 0.05 to about 1 Totr, and most preferably from about 0.05 to about 0.4 Totz. The electric power can be suppliod 195 to the equipment at a high radio frequency, from about 40 Kliz to about 3 GHz, preferably from about 13 to about 27 MHz, and most conveniently at about 14 MHz. To achieve the desired plasma condition in the gaseous atmosphere, the electric power delivered to the apparatus can vary over a range of from about 10 to about IO,fi00 watts; preferably from about 50 to.about 5,000 watts, more preferably from about 250 to about 3000 watts, most preferably from about 500 to about 2500 watts. The power used is somewhat 200 dependent on the chamber's working volume. The mo *prefeaed range of about 500 to about 2500 watts is appropriate for HIMONT Plasma 'Science PSOSOOD gas plasma apparatus with a working vohvae of about 5.0 cubic feet. The plasma acatment time varies from a few seconds to several minutes, preferably from about 20 seconds to about 30 minutes, most preferably from about 60 seconds to about 20 asiautes.
h should be appreciated that treatment presstue, time and power are intemlated, rather than 205 independent, variables. The effect of the level selected for each of these variables will determine the extent of web surface modification and/or coating thickness; also related are the chamber vohtme and geometry as well as the sample size and surface geometry. 'The selection of the level for these variables is well within the ordinary skill of practitioners in the art to which this invention pertains.
The hydrophilic coating layer is deposited onto the surface of a suitable web (either previously 210 apertured or unapertured) by low temperature plastna~induced vapor deposition (i.e., polymtrization) of a monomer or a combination of monomers, such that a hydrophilic coating will be applied to the web. In a prefetsed embodiment, the monomers will be silicon-containing compounds having one to three silicon atoms. which compounds are selected from the group consisting of (i) silanes of the formuL SiR, where each R is the same or different and is selected from H; a C,~C, linear or branched alkyl or alkoxy; a C6-C,°
215 aryl, unsubstituted or substituted with C,-C, linear or branched alkyl; a vinyl radical, i.e. --CH~CH=; or a C~~C~ allyl radical; provided that when R is H only one or two Rs are H; (ii) organosilicones based on a structure consisting of alternate silicon and oxygen atoms with various organic radicals attached to the silicon having the formula R'R"R'"Si-[-O-Si(R')(R")-]~ R'", where R', R" and R'" can be the same or different and are C,~C, linear or branched alkyl or alkoxy, R' and R" can also be hydrogen provided that no 220 more than 50% of the R' and R" groups are hydrogen, and n is 1, 2 or 3;
and (iii) mixtures thereof.
Representative silicon compounds include, but are not limited to, hcxamethyldisiloxane (HMDSO), methyltrimethoxy silanc (MTMS), vinyltrimethoxy silane (VTMS), vinyltriethoxy silane . , * = Trade-mark .7.
(VTES), cthylmcthoxy silane (EMS), ethyltrimeehoxy silane (ETMS), tetraethoxy silane (TES), cyclohexylmcthyl-dimethoxy silane (CMDMS), diryclopenryl-dimethoxy siltae (DCDMS), 225 phenyltriethoxy silane (PES), diphenyldimethoxy silaate (DPDMS),.tetramethyldisiloxane (TMDSO);~and hexamethyltrisiloxane (HMTSO), The silicon corrrpounds employed are introduced into thr plasma deposition chamber in the gaseous state. Prior to being introduced into the chariiber, the silicon compound is heated to a tempennue of from about 40° to about 100°C, generally from about 40° to about 60°C, to vaporize the compound and create sufficient vapor pressure such that the coating is deposited at a . 230 reasonable speed. Oxygen in gaseous form and argon are fed into the deposition chartibtr simultaneously with, but etit:h with a separatt iceding means end ttaass flow controller, the gaseous silicon compound.
Dtpeading upon the application, the O, flow rate ranges from about 25 standard cubic ceatimeter/minute ("seem") to about 1200 seem, the gaseous silicon compound flow is from about 10 seem to about 25Q .
seem, and Ar flow is from about 1 scan to about 150 acccrs.. Argon is used to enhance the rate of deposition 235 of the gaseous materials being employed sad, therefore, it is. pKferable to use Argon iin the process. With respect to the flow rates for argon and oxygen versus the monomer (e.g HMDSO) flow rate, the following are preferred: assuming that the mass flow Q1 represents 3% argon and 97. %
oxygen and vapor mass flow Q2 represents the mass flow for the monomer, the prefered ratio of Qi:Q2 is from about 10:1 to about 1:2, more prefered is from about 5:1 to about 1: J, and most preferred is about 3:2.
240 Oxygen is essential to the plasma deposition process with the silicon compounds according to this invention. Without oxygen, it is not possible to obtain a plasr»a~induccd hydrophilic'coating using the aforementioned silicon compounds. Whatever oxidizing effect it bas, it'sppears to be necessary to utilize oxygen it one is to obtain the hydrophilic coatings of this invention.
The total vapor pressure of the gaseous materials introduced into the plasma deposition chamber 245 for the deposition of the hydrophilic coating layer is about 0.04 to about 0:5 Torr, preferably about 0.35 to about 0.45 Torn, most preferably about 0.4 Torn. The process pressure must be such that a low bias potential on the RF-driven electrode is achieved. The total vapor pressure for the hydrophilic coating Layer is from about 0.04 to about 0.4 Totr, preferably from about 0.06 to aboutØ13 Torn, depending on the process used and the substrate being treated.
250 Alternatively, monomer deposition may be achieved via the flash vapori2ation technique that is described in U.S, Patent No. 4,842,893.issued to Yializia on Apr. 29, 1988.
" The web to be subjected to plasma polymerization may be flat (two dimensional) or complex (three dimensional, including previously apertured films and nonwovens). That is, plasma treatment may be conducted either before or after fottnacion of the apertures of the web. In a preferred embodiment, 255 plasma treatment will be conducted after aperture formation, so as to better preserve a uniform hydrophilic coating on the web's surface.
Tht* forementioned advanced plasma systems available from HIMONT Plasma Science, such as the' PSOSOOD rtactor are equipped with a throttle valve, thereby making it possible to achieve a range of process pressures with the same gas flow rate.
* = Trade-mark _$_ The plasma treatment time for obtaining the desired hydrophilic coatings is from typically about 1 minute to about 10 minutes, preferably about 1.5 to about 4 minutes, most preferably about t.5 to about 2.5 minutes; and the RF power used to cause reaction of the vapor is typically from about 200 to about 1500 watts, preferably about 1000 to about 1400 watts, most preferably about 1100 to about 1300 watts. The RF
265 power typically employs ranges from about 1200 to about 2500 watts and depends on the substrate being treated and the throughput requirements. The resulting hydrophilic coatings can be produced in different thicknesses, but are typically from about 0.1 to about 2.S micmns; preferably about 1 to about 2 microns.
As indicated, the plasma induced hydrophilic coating exhibits a contact angle for water of less than about 90 degree, such that any water placed on the treated web will tend to spread spontaneously over 270 the treated web's coated surface. In a preferred embodiment, the treated web may be further treated by exposure to a low temperature plasma gas composition (also referred to herein as a "surface modifying gas saearri') or an energy source (also referred herein as "radiation curing") such as an apparatus that emits, including but not limited to, infra red, election beam, thermionic or ultra violet radiation. Apparatuses that are suitable as energy sources in the present invention are disclosed in U.S.
Patent No. 4,842,893 issued to 275 Yializis on Apr. 29, 1988.
In the surface modifying gas stream embodiment the gas stream preferably comprises N:O and CO=, to enhance the durability of the hydrophilic coating. In one such preferred embodiment, the plasma gas composition will comprise from about 80 to about 40 mol % N:O and from about 20 to about 60 mol CO:, preferably from about 70 to about 4S mol % N:O and from about 30 to about 55 mol % CO=, most 280 preferably from about 60 to about 45 mol % N,O and from about 40 to about SS mol % CO,, where the amount of 1;:0 and CO= in the mixture equals 100 to 10 mol %, for a time sufficient to modify the surface of the hydrophilic coating to enhance its durability.
In the radiation curing embodiment, the radiation source is preferably a gas discharge electron beam gun. The gun directs a flow of electrons through a emitter window onto the monomer, thereby 28S further curing the monomer, which enhances the durability of the hydrophilic coating. Curing is controlled by matching the electron beam voltage to the dielectric thickness of the monomer coating. For example, a Kv electron voltage will penetrate about 1 micron of deposited monomer.
The plasma process is generally practiced as follows. The starting web to be treated is placed into a vacuum chamber and the chamber pressure is reduced, typically to about 0.005 Totr. The process gas or 290 gas mixture employed is introduced to the chamber and the chamber pressure is stabilized at a pressure of 0.04-0.4 Torn. The interior dimension of the work area is approximately 1.73.X
0.7G~.X 1.02 meters (width x height x depth) Cor a total working volume of 1.34 cubic meters. A suitable high frequency form of energy, typically 13.56 MHz radio frequency energy, is used to create the plasma: in the system described, this is achieved with a total power input capacity of up to 2500 watts. The RF
energy dissociates the gas, 295 creating a plasma characterized by a distinctive glow. Since the process is conducted at reduced pressures, the bulk temperature of the gas is near ambient temperature, thus the reference to a cold gas plasma, a glow discharge, or a cold gas glow discharge. Because the web being subjected to the plasma conditions is located within the electric fie'id. the process is referred to as direct plasma polymerization. In contrast, see _g.
The electrons or ions created in the plasma bombard the web's surface, abstracting atoms or breaking 300 bonds, creating free radicals. These free radicals are unstable and seek to satisfy a more stable state by reacting with free radicals or groups within the plasma gas, also establishing new moieties on the surface of the web. In addition, the energetic electrons in the glow discharge fragment the molecules in the gas phase, leading to complex chemical reactions that result in a thin hydrophilic coating being deposited on at least one surface of the web.
30S Typically, and preferably, before plasma deposition of the hydrophilic coating onto the web, an initial step is performed. The purpose of this step is to clean the web's surface to promote adhesion of the subsequently deposited thin hydrophilic coating. Cleaning may be accomplished by subjecting the web's i surface to radiation (herein referred to as radiation cleaning) from an energy source including but not limited to, infra red, electron beam, thermionic or ultra violet radiation or by plasma cleaning. Apparatuses 310 that are suitable' as energy sources in the prcscnt invention are disclosed in U.S. Patent No. 4,842,893 issued to Yializis on Apr. 29, 1988. In the radiation cleaning embodiment, the radiation source is preferably a gas discharge electron beam gun. The gun directs a flow of electrons through a emitter window onto the web's surface, thereby abstracting atoms or breaking bonds, thus creating free radicals.
These free radicals are unstable and seek to satisfy a more stable state thus they serve as bonding sites for 31 S the monomers that are used to produce the web's hydrophilic coating.
Cleaning is controlled by matching the electron beam voltage to the dielectric thickness or depth of cleaning that is desired. For example, a 10 Kv electron voltage will penetrate to a web depth of about 1 micron.
In the plasma cleaning embodiment, the gases are usually either Ar alone, O, alone, or mixtures (e.g.. l:1 ratio) of Ar and O,. Gas flow rates are typically in the range of about 20 to about 100 seem 320 (standard cc/min), preferably about 40 to about 80 seem, and most preferably about 50 to about 60 seem.
RF power is approximately 1100 watts, and process pressure is about 0.040 Torn.
After the optional initial step, the next step is the plasma deposition of the hydrophilic coating, as described above and in more detail in the examples below. Often, but not always, a step subsequent to the CO. and N:O surface treating step is used to enhance the durability or uniformity of the plasma coating.
325 Useful process gases are Ar andlor O=. Process times are usually about 1 to about 3 minutes, with about 2 minutes typically being optimum. Gas flows range from about 40 to about 250 seem, with process pressures from about 0.200 to about 0.400 Torn, and RF input power from about 150 to about 1500 watts.
The materials useful as polymeric films to be plasma treated to provide a hydrophilic coating will be derived from thermoplastic polymers. In general, the term "thermoplastic polymei' is used herein to 330 mean any thcrtnoplastic polymer which can be used for the preparation of films. Examples of thermoplastic polymers include, by way of illustration only, end-capped polyacetals, such as poly(oxymethylene) or ', polyfottnaldehyde, poly(trichloroacetaldehyde), poly(n-valeraldehyde), poly(acetaldehyde), poly(propionaldehyde), and the like: acrylic polymers, such as polyacrylamide, poly(acrylic acid), poly(methacrylic acid), poly(ethyl acrylate), poly(methyl methacrylate), and the like;
fluorocarbon polymers, such as poly(tetrafluoroethylene), perfluorinated ethylene-propylene copolymers, ethylene-tetrafluoroethylene copolymers, poly(chlorotrifluoroethylene), ethylene-chlorotrifluoroethylene 340 copolymers, poly(vinylidene fluoride), polyvinyl fluoride), and the like;
polyamides, such as poly(6-aminocaproic acid) or poly(s-caprolactam), poly(hexamethylene adipamide), poly(hexamethylene sebacamide), poly(11-aminoundecanoic acid), and the like; polyaramides, such as poly(imino-I,3-phenyleneiminoisophthaloyl) or poly(m-phenylene isophthalamide), and the like;
polyarylenes, such as poly-p-xylylene, poly(chloro-p-xylylene), and the like; polyaryl ethers, such as poly(oxy-2,6-dimethyl-1,4-345 phenylene) or polyp-phenylene oxide), and the like; polyaryl sulfones, such as poly(oxy-1,4-phenylenesulfonyl-I,4-phenyleneoxy-1,4-phenyIene-isopropylidene-1,4-phenylene), poly(sulfonyl-1,4-phenyleneoxy-1,4-phenylene-sulfonyl-4,4'-biphenylene), and the like;
polycarbonates, such as poly(bisphenol A) or poly(carbonyldioxy-1,4-phenylene-isopropylidene-1,4-phenylene), and the like;
polyesters, such as polyethylene terephthalate), poly(tetramethylene terephthalate), poly(cyclohexyiene-350 1,4-dimethylene terephthalate) or poly(oxymethylene-1,4-cyclohexyl-enemethyleneoxyterephthaloyl), and the like; polyaryl sulfides, such as polyp-phenylene sulfide) or poly(thio-1,4-phenylene), and the Like;
polyimides, such as poly(pyromellitimido-1,4-phenylene), and the like;
polyolefins, such as polyethylene, polypropylene, poly(1-butene), poiy(2-butene), poly(1-pentene), poly(2-pentene), poly(3-methyl-1-pentene), poiy(4-methyl-1-pentene), 1,2-poly-1,3-butadiene, 1,4-poly-1,3-butadiene, poiyisoprene, 355 polychloroprene, polyacrylonitrile, polyvinyl acetate), poly(vinylidene chloride), polystyrene, and the like;
copolymers of the foregoing, such as acrylonitrile-butadiene-styrene (ABS) copolymers, and the like.
Preferred polymers are polyolefins and polyesters, with polyolefins being more preferred. Even more preferred are those polyolefins which contain only hydrogen and carbon atoms and which are prepared by the addition polymerization of one or more unsaturated monomers.
Examples of such 360 polyolefins include, among others, polyethylene, polypropylene, poly( 1-butene), poly(2-butene), poly( 1 pentene), poly(2-pentene), poly(3-methyl-1-pentene), poly{4-methyl-1-pentene), 1,2-poly-1,3-butadiene, 1,4-poly-1,3-butadiene, polyisoprene, and the like. In addition, such term is meant to include blends of two or more polyolefins and random and block copolymers prepared from two or more different unsaturated monomers. Because of their commercial importance, the most preferred polyolefins are polyethylene and 365 polypropylene.
In addition to polymeric films, webs that can be used to produce the durably wettable, liquid pervious webs of the present invention include but are not limited to spun bonded, hydroentangled, needled and polymericly bound nonwovens. Suitable nonwoven webs are typically formed from organic textile fibers including but not limited to cotton, wool, wood, jute, viscous rayon, nylon, polyester, polyolefins, 370 carbon, or mixtures thereof. Inorganic fibers such as glass and metal can be used alone or in combination or further combined with organic fibers . In the case of staple fibers, fiber length varies from about 1/4 inch to about 2 or more inches. In the case of spun bonded webs, the fiber lengths are indefinite. The staple fibers used in hydroentangled, needled and polymericly bound nonwovens are processed through conventional textile machinery.

375 For example, in producing a polymericly bound, nonwoven web, a carding machine may be used to form a continuous length of rather two-dimensional loosely associated fibers known as a carded web.
These webs may be assembled to form a multiple layer or three-dimensional fibrous web of significant weight, e.g., from about several grams to thousands of grams per yard. In continuous nonwoven fibrous webs, the textile fibers are arrayed at various angles to the lengthwise axis of the web. When a web is 380 fomled by the action of a carding machine, the fibers are usually predominantly oriented in the machine direction and. on the other hand, isotropic webs may be formed such as by air-laying. The fibrous webs described above are typically impregnated with a polymeric binding agent (polymericly bound). In a preferred form, the polymeric binders are applied as emulsions of acrylic, polyvinylacetate, or similar polymeric nature, and mixtures thereof. Preferably, the fibers are unwoven and substantially haphazardly 385 oriented and adhesively bonded together with polymeric binder.
Hydroentangled and needled webs are distinct from polyrnericly bound webs as they rely principally on the physical entanglement of their fibers to provide web integrity. In contrast to polymericly bound and physically entangled webs, spun bond webs typically are composed of fibers of infinite length that are bound together through solvent or melt processes.
390 As indicated, the webs may be in the form of a flat film or may be a previously apertured three dimensional film. The coatings are durable and increase the surface energy of the web to render the treated web more wettable. The coating is durable, in that it is maintained ov er time, even after exposure to water or other aqueous liquids. In this regard, the webs of the present invention are described in one respect in terms of their ability to remain wettable over time and/or after exposure to liquids. The ability to remain 395 wenable over time is assessed by measuring the web's Post Aging contact angle. This measurement involves storing the treated web at 60° C for 16 hours, to artificially age the treated web, before measuring contact angle. The ability to remain wettable after exposure to liquids is assessed by measuring the web's Post Washing contact angle. This measurement involves placing a 2 in. x 2 in.
sample of treated web in a 250 ml water bath at 65°C for 90 sec. with vigorous agitation prior to measuring contact angle. Procedures 400 and devices for measuring contact angle between a liquid and a web surface are well known in the art:
However, water contact angle, measured with a goniometer (Model # 100-00, Rame-Hart, Inc., Mountain Lakes, NJ), is used to assess the web wettability of the present invention.
All contact ankle measurements are rcponcd as the average measurements on 3 samples.
In one aspect, the treated web of the present invention will have a Post Aging contact angle that is 405 not more than about 60 degrees greater than the treated web's Pre Aging contact angle (i.e., the contact angle as measured before storage at 60°C for 16 hours). Preferably, the treated web will have a Post Aging contact angle that is not more than about 40 degrees, more preferably not more than about 20 degrees, still more preferably not mare than about 10 degrees, greater than the Pre Aging contact angle. In another respect, the treated web of the present invention will have a Post Washing contact angle that is not more 410 than about 60 degrees greater than the treated web's Pre Washing contact angle (i.e., the contact angle as measured before the treated web is placed in a 250 ml water bath at 65°
C for 90 sec with vigorous agitation). In this regard, the treated web will preferably have a Post Washing contact angle that is not more than about 40 degrees, more preferably not more than about 20 degrees, still more preferably not more than about 10 degrees, greater than the Pre Washing contact angle. In a prefeaed aspect, the treated 415 web of the present invention will exhibit both the Post Aging and Post Washing requirements discussed above.
The treated webs of the present invention will exhibit either (preferably both) a Post Aging or a Post Washing contact angle of less than about 90 degrees, preferably not more than about 70 degrees, more preferably not more than about 50 degrees. still more preferably not more than about 30 degrees, and most 420 preferably not more than about 20 degrees.
II Absorbent Articles As used herein, the term "absorbent article" refers generally to devices used to absorb and contain 425 body exudates, and more specifically refers to devices which are placed against or in proximity to the body of the wearer to absorb and contain the various exudates discharged from the body. The term "absorbent article" is intended to include diapers, catamenial pads, tampons, sanitary napkins, incontinent pads, training pants and the like, as well as wipes, bandages and wound dressings.
The term "disposable" is used herein to describe absorbent articles which are not intended to be laundered or otherwise restored or reused 430 as an absorbent article (i.e., they are intended to be discarded after limited use, and, preferably, to be recycled, composted or otherwise disposed of in an environmentally compatible manner). A "unitary"
absorbent article refers to absorbent articles which are formed as a single structure or as separate parts united together to form a coordinated entity so that they do not require separate manipulative parts such as a separate holder and pad.
435 It is to be understood that the overall size, shape, and/or configuration of the absorbent article, if any, into which the treated webs according to the present invention are incorporated, or utilized in conjunction with, have no criticality or functional relationship to the principles of the present invention.
Such parameters, however, must be considered along with the intended liquid and intended functionality when determining appropriate web configurations.
440 In addition to the treated webs of the present invention, absorbent articles will also comprise an absorbent core for retention of any absorbed body liquids. Exemplary absorbent structures for use as the absorbent core in the present invention are described in U.S. Patent No.
4,950,264 issued to Osborn on August 21, 1990; U.S. Patent No. 4,610,678 issued to Weisman et al. on September 9, 1986; U.S. Patent No. 4,834,735 issued to Alemany et al. on May 30, 1989; European Patent Application No. 0 198 683, the 445 Procter & Gamble Company, published October 22, 1986 in the name of Duenk et al.; U.S. Patent No.
4,673,402 issued to Weisman et al, on June 16, 1987; and U.S. Patent No.
4,888,231 issued to Angstadt on December 19, 1989. The absorbent core may further comprise the dual core system containing an acquisition/distribution core of chemically stiffened fibers positioned over an absorbent storage core as detailed in U.S. Patent No. 5,234,423, entitled "Absorbent Article With Elastic Waist Feature and Enhanced 450 Absorbency" issued to Aiemany et al., on August 10, 1993; and in U.S.
Patent No. 5,147,345, entitled _13_ "High Efficiency Absorbent Anicles For Incontinence Management" issued to Young, LaVon and Taylor on September 15, 1992.
A preferred embodiment of a unitary disposable absorbent article made in accordance herewith a a catamenial pad, or sanitary napkin, As used herein, the term "sanitary napkin" refers to an absorbent 455 article which is worn by females adjacent to the pudendal region, generally external to the urogenital region, and which is intended to absorb and contain menstrual liquids and other vaginal discharges from the wearer's body (e.g., blood, menses, and urine). Interlabial devices which reside partially within and partially external to the wearer's vestibule are also within the scope of this invention. Suitable feminine hygiene articles are disclosed in U.S. Patent No. 4,556,146, issued to Swanson et al. on Dec. 3, 1985. U.S.
460 Patent No. 4,589,876, issued to Van Tilberg on April 27, 1993, U.S. Patent No. 4,687,478, issued to Van Tilburg on Aug. 18, 1987, U.S. Patent No. 4,950,264, issued to Osborn, III on Aug. 21, 1990, U.S. Patent No. 5,009,653, issued to Osborn, III on April 23, 1991, U.S. Patent 5,267,992, issued to Van Tilburg on Dec. 7, 1993, U.S. Patent No. 5,389,094, issued to Lavash et al. on Feb. 14, 1995, U.S. Patent No.
5,413,568, issued to Roach et al. on May 9, 1995, U.S. Patent No. 5,460,623, issued to Emenaker et al. on 465 Oct. 24, 1995, U.S. Patent No. 5.489,283, issued Van Tilburg on Feb. 6, 1996, U.S. Patent No. 5,569.231, issued to Emenaker et al. on Oct. 29, 1996, and U.S. Patent No. 5,620,430, issued to Bamber on April 15, 1997.
In a preferred embodiment of the present invention, the sanitary napkin has two flaps each of which arc adjacent to and extend laterally from the side edge of the absorbent core. The flaps are .t70 configured to drape over the edges of the wearer's panties in the crotch region so that the flaps are disposed between the edges of the wearer's panties and the thighs. The flaps serve at least two purposes. First, the flaps help serve to prevent soiling of the wearer's body and panties by menstrual liquid, preferably by forming a double wall barrier alone the edges of the panty. Second, the flaps are preferably provided with attachment means on their garment surface so that the flaps can be folded back under the panty and attached 475 to the garment facing side of the panty. In this way, the flaps serve to keep the sanitary napkin properly positioned in the panty. The flaps can be constructed of various materials including materials similar to the topshect, backsheet, tissue, or combination of these materials. Further, the flaps may be a separate element attached to the main body of the napkin or can comprise extensions of the topsheet and backsheet (i.e., unitary). A number of sanitary napkins having flaps suitable or adaptable for use with the sanitary napkins 480 of the present invention are disclosed in U.S. Patent No. 4,687,478 entitled "Shaped Sanitary Napkin With Flaps", which issued to Van Tilburg on August 18, 1987; and U.S. Patent No.
4,589,876 entitled "Sanitary Napkin", which issued to Van Tilburg on May 20, 1986.
In a preferred embodiment of the present invention, an acquisition layers) may be positioned between the topsheet and the absorbent core. The acquisition layer may serve several functions including 485 improving wicking of exudates over and into the absorbent core. There are several reasons why the improved wicking of exudates is important, including providing a more even distribution of the exudates throughout the absorbent core. and allowing the sanitary napkin to be made relatively thin. The wicking referred to herein may encompass the transportation of liquids in one, two or all directions (i.e., in the x-y 490 plane and/or in the z-direction). The acquisition layer may be comprised of several different materials including nonwoven or woven webs of synthetic fibers including polyester, polypropylene; or polyethylene. natural fibers including cotton or cellulose; blends of such fibers; or any equivalent materials or combinations of materials. An example of a sanitary napkin having an acquisition layer and a topsheet is more fully described in U.S. Patent No. 4,950,264 issued to Osborn. In a preferred embodiment. the 495 acquisition layer may be joined with the topsheet by any of the conventional means for joining webs together, most preferably by fusion bonds as is more fully described in the referenced Cree application.
Catamenial pads may be constructed as follows. Onto silicone-coated release paper a spiral pattern of Ii2031 Findlay hot melt adhesive is applied at 0.04 glint. This adhesive layer is transferred onto the top (wearer-facing) side of a secondary topsheet by rolling the secondary topsheet and coated release paper 500 together with a hand roller. The secondary topsheet is fortrred of a nonwoven material known as Fort James Airlaid Tissue, Grade 817, commercially available from the Fort James Corp. of Green Bay, Wisconsin. A
topsheet of the present invention is applied to the adhesive side of the secondary topsheet and the two are bonded by gently pressing them together with a hand roller. Two strips of one-quarter-inch double-sided tape are applied along both long edges of a polyethylene backsheet. The absorbent core is added to 505 construct the complete absorbent structure.
As used herein, the term "diaper" refers to a garment generally worn by infants and incontinent persons that is worn about the cower torso of the wearer. It should be understood. however, that the present . invention is also applicable to other absorbent arricies such as incontinent briefs, incontinent pads. training pants, diaper inserts, facial tissues, paper towels, and the like. In general, a diaper of the presem invention 510 ~ will comprise a liquid pervious topsheet of the present invention; a liquid impervious backsheet joined with the topsheet; and an absorbent core positioned between the topsheet and the backsheet. Additional structural features such as elastic members and fastening means for securing the diaper in place upon a wearer (such as tape tab fasteners) may also be included.
While the topsheet, the backsheet, and the absorbent core can be assembled in a variety of well 515 known configurations, a preferred diaper configuration is described generally in U.S. Patent No. 3,860,003 (Buell), issued January 14, 1975. Alternatively, preferred configurations for disposable diapers herein are also disclosed in U.S. Patent No. 4,808,178 (Aziz et al.), issued February 28, 1989; U.S. Patent No.
4,695,278 (Lawson), issued September 22, 1987; and U.S. Patent No. 4,816,025 (Foreman), issued March 28, 1989. Suitable incontinence articles for adult wearers are disclosed in U.S. Patent No. 4,253,461 issued 520 to Strickland, et al. on March 3, 1981; U.S. Patent Nos. 4,597,760 and 4,597,761 issued to Buell; U.S.
Patent No. 4,704,115; U.S. Patent No. 4,909,802 issued to Ahr, et al.: U.S.
Patent No. 4,964,860 issued to Gipson, et al, on October 23, 1990; and in PCT Publication No. WO 92/11830 published on July 23, 1992.
The absorbent core of the diaper is positioned between the topsheet and the backsheet. The absorbent core can be manufactured in a wide variety of sizes and shapes (e.g., rectangular, hourglass, 530 asymmetrical, etc.). The total absorbent capacity of the absorbent core should, however, be compatible with the design liquid loading for the intended use of the absorbent article or diaper. Further, the size and absorbent capacity of the absorbent core can vary to accommodate wearers ranging from infants through adults.
As indicated, the absorbent core may include a liquid distribution member. In a preferred 535 configuration, the absorbent core preferably further includes an acquisition layer or member in liquid communication with the liquid distribution member and located between the liquid distribution member and the topsheet. The acquisition layer or member may be comprised of several different materials including nonwoven or woven webs of synthetic fibers including polyester, polypropylene, or polyethylene, natural fibers including conon or cellulose, blends of such fibers, or any equivalent materials or combinations of 540 materials.
In a preferred embodiment. the diaper will comprise elasticized Icg cuffs. The elasticized leg cuffs can be constructed in a number of different configurations, including those described in U.S. Patent No.
3,860.003; U.S. Patent No. 4,909,803, issued to Aziz et al. on Mar: 20, 1990;
U.S. Patent No. 4,695,278, issued to Lawson on Sep. 22, 1987; and U.S. Patent No. 4,795,454, issued to Dragoo on Jan. 3, 1989.
545 In use, the diaper is applied to a wearer by positioning the back waistband region under the wearer's back, and drawing the reminder of the diaper between the wearer's legs so that the front waistband region is positioned across the front of the wearer. The tape-tab or other fasteners are then secured preferably to outwardly facing areas of the diaper.

III. x I s -The following examples are illustrative and are not meant as a limitation of the invention disclosed and-claimed herein. With respect to Example 2, the mass flow controller used to deliver the silicon-eontaining monomer compound for the deposition processes was calibrated for the flow rate of HMDSO.
~ The flow rates of other gases were calculated based on the specific heats of the respective eases. The accuracy of the mass flow controllers in these cases is ~ 5% or better.
xa le This example illustrates the plasma treatment process and benefit of this invention in applying a permanent hydrophilic coating to a flat polyethylene film. Flat polyethylene (PE) film having a 1 mil 560 average thickness is obtained from T*cdegar Film Products, Inc. (Terrc Haute, IN) with material composition designation code X-8318-I. Three-sup plasma treatments are conducted in a plasma reactor (Advanced Plasma System, Model D, radio frequency (RF) : 40 KHz), with the gas input and process conditions indicated in Table 1.
Ta 1 Step t~ Gas Input Flow Rate RF Power Treatmem Time lsccml" (Watt) (min) 1 Ar/O. 1173 500 Z

? Ar/O,/HMDSO 2/73150 S00 10 3 Ar/O. 2173 _ 1 _ ~ 500 s6~ ': Ar: Argon; 0,: oxygen; HMDSO: hexamcthyl disiloxane ": seem: standard cm'/minute The rcsuhing plasma treated web samples are then tested for surface wetiability both before and after rapid aeine_ conditions. Rapid acing condition refers to conditioning the web sample at 60° C for 16 Hours prior to wenabiliry measurement. Water contact angle, measured with a goniometer (Model # 100-570 00, Rame-Hart, Inc., Mountain Lakes, Nl), is used to assess web wettability. Strong wetting durability of EiMDSO-derived plasma coating is established, as demonstrated by comparable contact angles seen between pre-aged and post-aged samples (see Table 2). .
Ta 1 Sample Water Contact Anele'ldeereesl Pre-Aeed Post-Aeed Untreated PE film 96 (3 96 (31 HMDSO- lasma treated 26 ( 1 ) 26 (31 PE web ': Contact angle measured 3 times on the same treated web is averaged and standard deviation is reported 575 in parenthesis.
a a This example illustrates the alternate plasma treatment process and benefit of this invention in applying a permanent hydrophilic coating to a slat PE film. Flat PE film having a 1 mil average thickness is obtained from Trcdegar Film Products, Inc. (Tcrte Haute, IN) with material composition designation * = Trade-mark 580 code X-8318-1. Three-step plasma trcatmenu are conducted in a plasma reactor. (Plasma Science PSOSOOD), with gas input and process conditions indicated in Table 3.
Table 3 ' Ste # Gas Input Flow Rate RF Power Treatment " Time Isccm)' (Watt) Iminl 1 Ar 58 1080 1 2 ArlO-/I-IMDSO43/1560152 1200 2 3 N.O/CO- 200/207 1325 ' seem : standard cm'/minuu " Ar: Argon; O;: oxygen; HMDSO: hexamethyl disiloxane; N:O: nitrous oxide;
585 CO,: carbon dioxide The resuhing plasma treated web samples are then evaluated for surface wettabiliry before and after the water wash test. Water wash test refers to immersing a 2 in. x 2 in, web sample in a 250 ml water bath at 65° C for 90 sec with vigorous agitation (with a Teflon coated stir bar). Water contact angle, measured with a goniomcter (model # 100-00, Rame-Hart, lnc., Mountain Lakes, N.J.), is used to assess the 590 webs' wct:abiliry. Strong wetting durability of HMDSO-derived plasrna coating is established, as is demonstrated by comparing contact angle between pre-washed and post-washed samples (see Table 4).
Ta 4 Sample W atcr Contact Ane )e ' (decrccs Pre-washed Post-washed _ 96 t31 96 (3) Untreated PE Film HMDSO- lasma treated 7 ( 11 14 ( 11 PE web ': contact angle measured 3 times on the same filmiweb is averaged and standard deviation is reported in parenthesis.
595 While specific embodiments of the invention have been described in considerable detail, variations and modifications of these embodiments can be effected without departing from the spirit and scope of the invention as described and claimed.
* = Trade-mark

Claims (15)

THE EMBODIMENTS OF THE INVENTION IN WHICH AN
EXCLUSIVE PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS
FOLLOWS:

1. A process for making a durably wettable, liquid pervious apertured web for use as a topsheet in an absorbent article, the process comprising the steps of a) forming apertures in a web, which is a polymeric film or nonwoven web;
b) direct plasma polymerizing the apertured web of step (a) by:
(i) introducing the web in a plasma reaction zone; and (ii) coating at least one surface of the web with a coating of polymerized monomers, wherein the coating is less than 2.5 microns thick and is derived from a monomer gas stream that provides a hydrophilic coating upon plasma polymerization, whereby the polymerized monomers cause the at least one surface of the web to become durably wettable.

2. The process of Claim 1 wherein the at least one surface of the durably wettable, liquid pervious apertured web has a Post Aging contact angle that is not more than 60 degrees greater than the Pre Aging contact angle.

3. The process of Claim 2 wherein the Post Aging contact angle is not more than 40 degrees greater than the Pre Aging contact angle.

4. The process of Claim 2 wherein the Post Aging contact angle is not more than 20 degrees greater than the Pre Aging contact angle.

5. The process of any one of Claims 1 to 4 wherein the at least one surface of the durably wettable, liquid pervious apertured web has a Post Washing contact angle that is not more than 60 degrees greater than the Pre Washing contact angle.

6. The process of Claim 5 wherein the Post Washing contact angle is not more than 40 degrees greater than the Pre Washing contact angle.

7. The process of Claim 5 wherein the Post Washing contact angle is not more than 20 degrees greater than the Pre Washing contact angle.

8. The process of any one of Claims 1 to 7 wherein the process further comprises the step of cleaning the at least one surface of the web by exposing the at least one surface to plasma conditions or radiation from an energy source selected from the group consisting of infra red radiation, electron beam radiation, thermionic radiation, ultra violet radiation and a mixture thereof, prior to introduction of the monomer gas stream of step (b) (ii).

9. The process of Claim 8 wherein the step of cleaning the at least one surface of the web by exposing the web to plasma conditions comprises introduction of a gas stream comprising a gas selected from the group consisting of Ar, O2, and a mixture thereof.

10. The process of any one of Claims 1 to 9 wherein the process further comprises the step of further modifying the hydrophilic coating by introducing the web formed in step (b) (ii) to a surface modifying gas stream comprising N2O and CO2 or radiation from an energy source selected from the group consisting of infra red radiation, electron beam radiation, thermionic radiation, ultra violet radiation and a mixture thereof.

11. The process of any one of Claims 1 to 10 wherein the apertured web is an apertured polymeric film and is derived from a material selected from the group consisting of polyolefins, polyesters, and a mixture thereof.

12. The process of Claim 11 wherein the polymeric film is derived from a material selected from the group consisting of polyethylene, polypropylene, poly(1-butene), poly(2-butene), poly(1-pentene), poly(2-pentene), poly(3-methyl-1-pentene), poly(4-methyl-1-pentene), 1,2-poly-1,3-butadiene, 1,4-poly-1,3-butadiene, polyisoprene, a blend thereof, a random copolymer thereof, and a block copolymer thereof.

13. The process of any one of Claims 1 to 12 wherein the monomer gas stream comprises a monomer selected from the group consisting of (i) silanes of the formula Si(R)4 where each R is the same or different and is selected from H; a C1-C8 linear or branched alkyl or alkoxy; a C6-C10 aryl, unsubstituted or substituted with C1-C4 linear or branched alkyl; a vinyl radical; or a C3-C5 allyl radical; provided not more than two R
groups are H; (ii) organosilicones of the formula R'R"R"'Si-[-O-Si(R')(R")-]n R"', where R', R" and R"' can be the same or different, and R"' is C1-C8 linear or branched alkyl or alkoxy, and R' and R" are C1-C8 linear or branched alkyl or alkoxy or hydrogen, provided that no more than 50% of the R' and R" groups are hydrogen, and n is 1, 2 or 3;
and (iii) a mixture thereof; and wherein said monomer gas stream further comprises oxygen when said monomer of said gas stream consists only of said silanes.

14. The process of Claim 13 wherein the monomer gas stream comprises a monomer selected from the group consisting of hexamethyldisiloxane, methyltrimethoxy silane, vinyltrimethoxy silane, vinyltriethoxy silane and oxygen, ethylmethoxy silane, ethyltrimethoxy silane, tetraethoxy silane, cyclohexylmethyl-dimethoxy silane, dicyclopentyldimethoxy silane, phenyltriethoxy silane, diphenyldimethoxy silane, tetramethyldisiloxane, hexamethyltrisiloxane, and a mixture thereof; and wherein said monomer gas stream further comprises oxygen when said monomer of said gas stream consists only of said silanes.

15. The process of any one of Claims 1 to 14 wherein the gas of the monomer gas stream is ionized via pulsation of high frequency microwaves or radiowaves.