Fibrous Products and Methods of Making and Using Them
This invention relates to the modification of properties of fibrous fabrics and to the resultant fabrics. The invention further relates to making fibrous fabrics having laundry-durable finishes by excitation- induced graft polymerisation of a polymerisable monomer under conditions optimizing the laundry- durability of the finish, other textile properties such as textile handle, drape and breathability, as well as the speed and efficiency of the manufacturing process.
It is well known to apply surface treatments to a fabric (or the yarns or fibres from which it is made) so as to modify the properties of the fabric. These methods all involve the application of a treatment material or finishing agent to the surface of the fabric (or the yarns or fibres from which it is made) under conditions whereby the active material is held to the surface. The treatment material is retained on the fabric chemically and/or physically, depending upon the combination of active chemical, fibre type and method of application.
The most common way of applying treatment material is by applying a solution or emulsion of the chemical by padding, immersion, spraying, printing or other contact technique The solvent is then evaporated to leave the treatment material physically and/or chemically bonded to the fabric. For instance it is conventional to impart water and oil repellence to a fabric by application of an aqueous emulsion of a fluorochemical.
It is also known to treat fabrics by contacting the fabric with the treatment material in vapour form
In order to promote retention of the treatment material on the fabric, it is known to apply it as a polymer and/or in combination with a binder It is also known to apply it in polymerisable form and to polymerise it on the fabric.
As a generality, a problem with fabric treatments is that it is difficult to achieve permanence of the desired effect without sacrificing other desired properties. This is particularly for use of the natural fabrics such as cotton, silk, wool etc. Moreover it is difficult to achieve and maintain a combination of high performance, durability and good textile characteristics under high speed manufacturing conditions.
Accordingly many fabric treatments are insufficiently permanent. This is a particular problem when the fabric is clothing or other domestic textile which is laundered or dry cleaned frequently, since
agitated washing and solvents tend to stπp the deposited treatment material off the fabric and soil deposition can also interfere with performance. For instance known oleophobic treatments normally lose their effectiveness after a few washes or dry cleaning treatments. Moderate permanence on man- made fabrics can sometimes be achieved but only by the use of textile attributes such as a curing system and/or a binder, and this can impair either the softness and or permeability of the fabric.
As an example, it is well known to render a fabric oleophobic by applying an emulsion of perfluoro compound to it. This generates a fabric which is oleophobic and hydrophobic but it has two major disadvantages. One is that the fabric loses permeability and handle. Microscopic examination shows the presence of a large amount of film-forming material bridging between fibres. The other disadvantage is that the treatment is not permanent in that the fabric loses its oleophobic properties relatively quickly upon exposure to normal weather or wear and, in particular, after being subjected to only a few (for instance three or five) normal agitated washes i.e , washes of the normal type to which clothing is subjected in a washing machine. Permanence to dry cleaning, on the other hand, can be even more deficient. Increasing the amount of emulsion above an amount that gives good oleophobicity does not improve permanence, and worsens handle, drape and other textile attributes.
These problems apply in respect of treatments that have been designed specifically for fabrics, but they apply also to treatments which have been developed predominantly for applying active chemicals as films on solid surfaces but which have also been mentioned as capable of being applied to fabrics.
One class of coating treatment involves plasma-enhanced deposition of a treatment material in vapour form onto a substrate. There are various types of plasma-enhanced deposition processes, including deposition at atmospheric pressure or at reduced pressure, deposition by use of a continuous, pulsed or varying flow of active chemical, and deposition using a continuous plasma discharge or a pulsed plasma discharge When a pulsed discharge is used the disclosures show pulses having an "on time" ranging from microseconds (us) up to seconds and an "off time" also ranging from microseconds up to seconds, with the ratio of the on:off times typically ranging from 1:1 to 1 : 10, or sometimes considerably more. The wide range of conditions exists because of the difficulty of selecting conditions which achieve the required amount of activation without causing over-activation or premature activation and consequential unwanted reactions.
There are also disclosures in which a plasma discharge is used to activate the substrate surface before exposing the surface to a treatment material that will react with it (see for example JP 10325078 and US-A-5,328,576). There are also disclosures where a bifunctional reagent is subjected to plasma deposition onto a smooth substrate whereby the bifunctional reagent reacts with one of its functional groups (generally with polymerisation) to the surface of the substrate and its other functional group is subsequently caused to react covalently with a treatment material As a result, the treatment material
is linked to the substrate by the bifunctional reagent that has been deposited by plasma (see for example US-A-5,876,753)
Plasma deposition processes are usually described in the context of providing a continuous film of coating material on a continuous solid substrate However fabrics are included in the list of substrates in a few of the disclosures As an example, in EP-A-0, 896,035 it is described that a transparent film free of pinholes can be obtained on a substrate, and fabrics are included in the list of possible substrates
There have also been a few disclosures of plasma treatments using polymerisable monomers which are specific for fabrics
For example US-A-3,674,667 describes rendering fabπc water repellent by plasma deposition of certain fluorocarbons It warns that if an unsaturated fluorocarbon is used polymerisation will predominate and the treated fabπc will lose its handle and permeability
In US 5,041,304 a fabric is subjected to plasma deposition of a fluorocarbon in an inert gas at atmospheric pressure
In RU-A-1158634, a textile surface is activated by plasma and is then exposed to acrylic monomer vapour
In WO 00/14323 two different processes are described for forming an oleophobic and hydrophobic coating on a textile In one process plasma deposition of a fluorocarbon is utilized, and plasma deposition is defined as providing a partly cross-linked, void-free, continuous coating which is well adherent to the substrate The process conditions involve exposing the substrate to a pulsed plasma with, preferably, an on time of about 10ms and an off time of about 190ms In the other process, the textile is exposed to deposition of a vapour of a perfluoroalkyl acrylate whereby the monomer condenses on the textile surface, and the deposited monomer is then exposed to a source of radiation to cause polymerisation
These processes do not give the optimum combination of oleophobicity, textile handle and permanence
In WO 98/58117 a process is described for coating a surface with a polymer layer by exposure to a plasma containing a monomeπc unsaturated perhalogenated compound whereby the layer renders the surface oil or water repellant In some examples the surface was the surface of a fabric which was exposed to low pressure, pulsed, plasma deposition of a perfluoralkyl acrylate The resultant fabric
was subjected to a single, static, extraction test and was found to retain its hydrophobic and oleophobic properties after this static test This extraction test gives an indication of permanence against a single, static, solvent extraction but gives no indication whatsoever of permanence against the conditions encounted by normal clothing and other normal domestic textiles, especially including repeated agitated wash cycles
There is no indication of the permanence of the coating, and in particular there is no suggestion that the coating might simultaneously give good permanence against agitated washing, while maintaining good permeability and handle In practice fabrics coated according to the conditions disclosed in this patent have been found to display poor durability under typical laundering conditions
An objective of the invention therefore is to provide a finishing process for fabrics intended or suitable for use in typical personal, domestic, institutional and workplace applications which are subject to regular or occasional laundering or cleaning including for example clothing, bedding, curtaining, table linen and related items and apparel and wherein the fabrics are characterized by improved laundry-durability together with other textile properties such as textile handle, drape and breathability Another objective is to provide a process for making oleophobic and hydrophobic sta n- resistant fabrics having improved laundry-durability A further objective is to provide a process for making laundry-durable fabrics based on excitation-mduced graft polymerisation of a polymerisable monomer and which is typified by improved speed and efficiency Yet another objective is to provide a process for making laundry-durable fabrics using polymerisable monomers having improved laundry-durability and stability
Summary of the Invention
According to a first aspect of the invention, there is provided a method for making a fabric having a laundry-durable finish by excitation-induced graft polymerisation of a polymerisable monomer in which the fabric or a region of the fabric (which term includes one or more treatment areas on one or both sides of the fabric) is exposed to atomized condensed polymerisable monomer under conditions of low or zero excitation so as to coat the individual fabric fibres The method also entails exciting the polymerisable monomer in condensed form in a monomer excitation zone before, during or after said exposure step in order to induce graft polymerization of the polymerisable monomer In one process embodiment, the fabnc or a region thereof is exposed to condensed polymerisable monomer prior to or during passage of the fabric through the monomer excitation zone In an alternative process, the polymerisable monomer is excited in the monomer excitation zone in condensed form prior to exposing the fabric or region thereof to the polymerisable monomer for purposes of inducing the graft polymerization process during the subsequent exposure step
The methods of the invention lead to the deposition of an extremely thin but coherent, conformal and durable graft-polymer tsed coating or region at or near the surface of the fibres. In preferred embodiments, the polymer-coated fabric or region thereof has an average fibre-coating thickness of at least about 1 5 nm, preferably at least about 2.5 nm, more preferably at least about 3 nm, and especially at least about 8 nm, the average thickness of the coating ranging up to about 25 nm, preferably about 20 nm and more preferably about 15 nm, such coatings being preferred from the viewpoint of providing optimum durability of the finishing effect during laundering (both wet and dry-cleaning) as well as excellent textile attributes including breathability, drape and handle. In addition, the exposure and excitation conditions are preferably such that the fabric or region thereof has a coating abrasion resistance of at least about 1000, preferably at least about 3000 rubs according to the test protocol described in detail below, the coating abrasion resistance being a measure of the ability of the coated fabric to maintain at least a minimum level of finishing performance (at least 50% of initial) under standard mechanical abrasion conditions (Martindale Abrasion Test, British Standard BS EN ISO 12947-2: 1999, 12kPa load), hi addition it is preferred that the fabric will continue to meet the appropnate minimum industrial standard for the particular fabric finish for at least about 1000, preferably at least about 3000 rubs, for example, in the case of stain resistant finishes, a minimum value of 3 according to the industry standard oil repellency and/or water repellency tests (see below).
The average fibre-coatmg thickness can be determined herein directly (using well-known surface analytical techniques such as sem, fe-sem, aes, cryo-tem, ftir, xps, sims etc) or by estimation from the amount of polymerisable monomer that is deposited and the surface area of the fibres (measured for example by N2-based BET techniques), assuming the polymer and liquid monomer to have the same density (δ). For liquid feed, the average fibre-coating thickness in nm (τ) is defined as τ = fi . ε . 1000 / (aw . af . wb) where fi is the monomer feed rate in ml/min, ε is the empirically-determined deposition efficiency expressed on a fractional basis, aw is the web treatment rate in m2/mιn, af is the surface area of the fibres in m2/g, and wb is the basis weight of the fabric in g/m2, the expression for τ being summed as appropriate where the fabric is subject to multiple passes or repeated treatments. For vapour feed, a similar relationship holds except that the monomer feed rate fv is normally measured in mol/min so that f, = fv . Mw /δ where Mw is the molecular weight of the monomer and δ is the density of the monomer liquid at ambient temperature measured in g/cm3.
For a static process, the web treatment rate is represented by the ratio of the area of the web in m2 and the total reaction time in min (tr).
Although the average fibre-coating thickness is extremely small, preferably the coating has an average thickness greater than the xps inelastic mean free path parameter (λ) across the range of electron energies typically encountered in the xps of organic materials (200-800eV) whereby there is essentially no contribution to the xps spectrum from atoms of the underlying bulk fibre material (such as C, N and O) Moreover, the fibre coating preferably meets this thickness cπteπon across at least about 50%, more preferably at least about 75%, and especially at least about 95% of the fabπc or treated region thereof
It is also preferred that the polymer be graft-polymerised substantially wholly on or in the individual fabπc fibres with substantially no coalescence of fibre bundles whereby there are substantially no films of treatment material interconnecting adjacent, substantially parallel fibres of the fibre bundles, this being important again for maintaining excellent textile handle, drape and breathability characteristics Coalescence or partial coalescence of fibre bundles can be observed directly in 500X photomicrographs of the fabric, but coalescence can in turn lead to yam shrinkage and this manifests itself in terms of increased inter-yam pore size and air permeability Preferably therefore the air permeability (measured for example using a Textest FX3300 Air Permeability Tester III at a pressure gradient of 125Pa according to ASTM D737-96) of the fabric or region thereof after treatment and prior to laundering should be withm about ±20%, more preferably about ±15%, and especially about ±10% of that of the untreated fabric By controlling the average fibre-coatmg thickness, the polymerisable monomer type, monomer adjuncts and the exposure and excitation conditions to control abrasion resistance, it becomes possible to deliver at one and the same time excellent finish performance characteristics such as oleophobic and hydrophobic stain repellence as well as improved durability and permanence of the finishing effect during wet and dry laundering without adversely impacting on other textile attributes such as drape, breathability and handle.
Thus in preferred process aspects, the polymerisable polymer and exposure conditions are such that the resulting polymer-coated fabric or region thereof has an average fibre-coating thickness of from about 1.5 to about 25 nm, preferably from about 3 to about 20 nm, and more preferably from about 8 to about 15 nm, and wherein the polymer is graft-polymeπsed substantially wholly on or in the individual fabric fibres with substantially no coalescence of fibre bundles Preferably the coating abrasion resistance of the fabric or region thereof is at least about 1000, more preferably at least about 3000 rubs (Martindale Abrasion Test, ISO 12947-2, 12kPa load, 50% minimum finishing performance), while the air permeability of the fabπc or region thereof after treatment is preferably within about ±20%, more preferably about ±15%, and especially about ±10% of that of the untreated fabric
As a result of fibre bridging by films of treatment material or of uneven surface treatment, conventional coating processes can also lead to an increase in the surface area of the fibre bundles,
which can be measured for example by BET analysis (for example using a Micromeritics Gemini with N2 as the operating gas). Accordingly it is preferred that the BET surface area of the fabric or region thereof after treatment (sometimes referred to herein as the fibre surface area) is preferably withm about ±20%o, more preferably about ±15%, and especially about ±10% of that of the untreated fabπc.
A wide range of polymeπsable monomers as well as finishing materials and compositions incorporating polymerisable monomers are suitable for application to fabrics herein, the monomer being selected on the basis of the desired fabric finish and on the ability of the monomer to impart the required finish by polymerisation or graft polymerisation Preferably however, the polymerisable monomer is selected to impart one or more laundry-durable finishes selected from oleophobicity, hydrophobicity, stain repellency stam release, soil-resistance, soil release, malodor resistance, malodor release, crease resistance, softness, flame retardancy, color-bleeding resistance, dye-transfer inhibition, and odor receptivity
Of the above, highly preferred are monomers designed to impart laundry-durable stain repellency, and especially laundry-durable oleophobic stain repellency, particularly under medium to heavy soil load conditions and on natural and semi-natural fabrics, two areas in which the prior art has proved notably deficient m delivering effective laundry-durable performance. Thus in highly preferred embodiments herein, the fabric is a natural or semi-natural, preferably multifilament yam-based woven fabric made, for example, of cotton, silk, wool, linen, rayon or of mixtures thereof, or a blend of natural fibres with one or more synthetic polymers in fibre form
The stain repellency of the treated fabrics for oil- and water-based stains can be measured in a number ways including use of the industrial standards AATCC 118-1997 (technically equivalent to ISO 14419) for oil (or oleophobic) stain repellency and 3M's Water Repellency Test for water-based (hydrophobic) stam repellency, the protocols for which are set out below Using the industry standard tests, the fabπc of the invention, or at least the treated region thereof, preferably has a stam repellency value (at least one and preferably both of oleophobic and hydrophobic stain repellency) prior to first laundering of at least 5, more preferably at least 6, and most preferably at least 7. Moreover, the fabπc will preferably maintain a stain repellency value of at least 3 for 10 or more laundry treatments (wet or dry), and preferably for at least 15 or 20 laundry treatments under medium soil load conditions (see typical multi-cycle wash conditions set out below) Ideally, the fabπc will have a grade of 3 or higher for as much as 30 or 40 laundry treatments or more. Although the stam-repellent effect can be partially restored and the durability of stam repellency prolonged by hot ironing the fabπc after laundering, it is a feature of the invention that hot ironing is not required to achieve excellent durability By contrast the known commercial treatments of fabrics based on emulsion polymerisation chemistry achieve only poor durability, even after 'prolongation' by hot ironing.
Polymerisable monomers suitable for use herein for providing stam repellency can also be selected on the basts of contact angle hysteresis factors, this being a measure of the relattve difference of advancing and receding contact angles for various liquids on the surface of the polymer-coated fabπd. Thus in preferred embodiments, the polymer-coated fabric or region thereof has an average wetting hysteresis factor for n-hexadecane of less than about ±30%, preferably less than about ±20% and more preferably less than about ±10%, wherein the n-hexadecane wetting hysteresis factor is defined as (θa hex - θr hex)/ θa ,1cx, and θa hex, θr 1,ex are respectively the advancing and receding contact angles for n- hexadecane on the polymer coated fabric or region thereof at 20°C. Moreover, the fabric or region thereof preferably also has an average wetting hysteresis factor for water of less than about ±30%, preferably less than about ±20% and more preferably less than about ±10%, wherein the water wetting hysteresis factor is defined as (θa wat - θr wat)/ θa Wdt, and θa wat, θr wdl are respectively the advancing and receding contact angles for deionised water on the polymer coated fabric or region thereof at 20°C.
In the methods of the invention, the fabric or a region thereof is directly exposed to polymerisable monomer in atomized condensed form. By 'exposure to condensed polymerisable monomer' is meant that the monomer is at least partly in a condensed state of matter (liquid, semi-liquid, solid or mixtures thereof) immediately prior to and during deposition of the monomer on or into the fabric fibres. Furthermore, in order to minimize fragmentation of the polymer during excitation-induced polymerization and in order to achieve a uniform distribution of polymer over the fibre surfaces with minimum filling of the inter-fibre and intra-yarn pores and coalescence of fibre bundles, it is also preferred to expose the fabric to monomer under low or zero excitation conditions, i.e. conditions normally promoting excitation-induced polymerization of the monomer. The excitation conditions during exposure can be expressed in terms of average excitation power density, this being the average power per unit area of the treated fabric or region. Preferably, the fabric or fabric region thereof is exposed to polymerisable monomer at an average excitation power density of less than about 10"2 Watts/cm2, more preferably less than about 10"3 Watts/cm2, and especially less than about 10"4 Watts/cm2.
In preferred embodiments, the polymerisable monomer is deposited on the fabric fibres in atomised form using for example one or more piezoelectric, ultrasonic, electrostatic or acoustic atomisers or a combination thereof. The median size of the atomized droplets is preferably from about lμm to about lOOμm, more preferably from about 15μm to about 70μm. Suitable ultrasonic atomizers for use herein include those supplied by Sono-Tek Corporation, Milton, New York, USA. The monomer will generally be fed to the atomizer in liquid or hquefiable form using gravity feed or preferably a positive displacement or other suitable metering pump designed to provide a feed rate generally m the range from about 0.05ml/mιn to about lOOOml/min, preferably from about lml/mm to about 200ml/mιn, more preferably from about 5 to about lOOml/mm.
Graft-polymerisation of the polymer to the fabric fibres is undertaken using excitation-mduced polymerization within an excitation zone. Suitable excitation processes include radiative processes using for example UV and electron beam excitation, but highly preferred herein from the viewpoint of providing optimum finishing performance and laundry durability are plasma-based excitation processes. Accordingly, the excitation zone herein is preferably selected from radiofrequency- and microwave-generated plasma zones as discussed in more detail below.
In a preferred aspect of the invention, the fabπc is exposed to the polymerisable monomer in atomized condensed form prior to or during passage of the fabric through the monomer excitation zone (a so- called 'pre-exposure' process). In such a process, the excitation zone preferably takes the form of a pulsed plasma and especially a sub-atmospheric vacuum pulsed plasma, wherein the duty cycle, excitation power and other plasma conditions are adjusted so as to maximize graft polymerization and minimize both polymer fragmentation and inter-fibre or intra-yarn film formation whilst maintaining high throughput rates via atomization of the monomer.
Although a broad range of excitation conditions and duty cycles are suitable herein depending, among other things, on monomer type, reactivity and state of matter at the point of excitation, pulsed plasmas for the atomized monomers herein typically have a pulse on-time (toπ) in the range from about 40μs to about 2ms, preferably from about lOOμs to about 1ms. The pulse off-time (toff) on the other hand is generally at least 1ms and preferably is in the range from about 2ms to about 50ms, and more preferably from about 5ms to about 30ms. Meanwhile the duty cycle (ton/(ton+ toff)) for the atomized monomers herein preferably lies in the range from about 1/4 to about 1/300, more preferably from about 1/5 to about 1/40. In the case of atomized monomers, however, it will be understood that continuous rather than pulsed plasma operating conditions may be suitable in many instances.
In addition, the pulsed plasma or other excitation zone for the atomized monomers herein preferably has an average excitation power density (average power applied per unit area of fabric) in the range from about 10"7 to about 10"', preferably about 10"6 to about 10"2 Watts/cm2, with from about 10"4 to about 10"2 Watts/cm2 being preferred, the pulsed plasma power being defined as usual as (ton/(ton+ toff))'W0„ where Won is the power applied during the pulse on-time.
Thus, in a preferred process embodiment of the 'pre-exposure' type, there is provided a method of making a fabπc having a laundry-durable finish by excitation-induced graft-polymerisation of a polymerisable monomer, the method comprising a) exposing the fabric or a region thereof to atomized condensed polymerisable monomer under conditions of low or zero excitation so as to coat the individual fabric fibres, and b) simultaneously or thereafter passing the fabric or region thereof through a monomer excitation zone at an average power density in the range from about 10"7to about 10'1, preferably from about
104 to about 10"2 Watts/cm2 so as to graft polymerize the polymerisable monomer to the fabπc fibres
In an alternative process embodiment using condensed monomers, the polymerisable monomer is excited within the monomer excitation zone in atomized form prior to exposing the fabπc to the polymerisable monomer (so-called 'pre-excitation' process). In pre-excitation processes using atomized condensed monomers, a wider range of excitation power densities and plasma types is possible and preferably the average excitation power density is in the range from about 10'7 to about 1 Watts/cm2 The excitation zone, on the other hand, can be an atmospheric or sub-atmospheric pulsed or continuous plasma.
Thus, in a preferred process embodiment of the 'pre-excitation' type, there is provided a method for making a fabric having a laundry-durable finish by excitation-mduced graft-polymerisation of a polymerisable monomer, the method comprising a) exciting the polymerisable monomer in atomized condensed form withm a monomer excitation zone, and b) thereafter exposing the fabric or a region thereof to the atomized condensed polymerisable monomer under conditions of low or zero excitation so as to coat and graft-polymerise the polymerisable monomer to the individual fabric fibres
Sub-atmospheπc vacuum pulsed plasmas herein preferably operate at a pressure (measured downstream of the vacuum chamber housing - see Fig. 1) in the range from about 7 5 to about 7500mTorr (0 01 to lOmbar; 1 to lOOOPa), more preferably from about 50 to about 2000mTorr (0.067 to about 2.67mbar, 6 7 to 266.6Pa), especially from about 75 to about 400mTorr (0.1 to about 0.533mbar, 10 to 53 3Pa) and at an electrode temperature in the range from about 0°C to about 100°C, preferably from about 20°C to about 80°C, more preferably from about 30°C to about 70°C, an elevated electrode temperature being valuable herein in the case of polymerisable monomers of intermediate or low volatility for controlling polymerization rate and other process variables.
The polymerisable monomer preferred for use herein for purposes of providing optimum oleophobic and hydrophobic stain resistance is a saturated or unsaturated long-cham fluoro-substituted monomer containing an uninterrupted fluoroalkyl group of formula CnX2n+i wherein each X is independently selected from halogen and H and wherein the fluoroalkyl group contains at least n, preferably at least 2n-3 and more preferably 2n+l fluoro substituents, wherein n is in the range from about 4 to about 20, preferably from about 5 to about 15, more preferably from about 5 to about 12, and especially from about 6 to about 10 The fluoroalkyl group can be linear or branched but preferably it contains a linear fluorocarbon segment of at least about 4, more preferably at least about 5 carbon atoms in length. By 'uninterrupted' is meant that the fluoroalkyl group contains no chain-interrupting CH2 groups The term ' linear segment' on the other hand refers to a segment of the fluoroalkyl group
having linearly-connected carbon atoms, albeit possibly with one or more side-chains branched therefrom, which side-chains do not count towards the total number of carbon atoms in the segment. Preferably the fluoroalkyl group has the general formula C„F2n+i Such monomers are especially effective for stain resistance and durability in the preferred plasma-induced polymerization processes of the invention
More specifically, suitable polymerisable monomers for purposes of stam resistance preferably have the general formula [C„X2n+ιYTQ]mR, wherein R is selected from optionally halo-substituted C,-C8- alkyl or alkylene, C3-C3-cycloalkyl or cycloalkylene, C2-C8-heterocycloalkyl or heterocycloalkylene, C2-C3-alkenyl or alkenylene, C2-C8-alkynyl or alkynylene, and C4-C8-alkadιenyl or alkadienylene, m is from 1 to 3, preferably 1, T represents (C(R')2)P wherein each R' independently represents H, halogen, hydroxy, an optionally hydroxy- or halo-substituted C C4 alkyl group, or a mono- or poly- Cι-C4-alkylene oxide moiety and p is from 0 to 10, preferably from 0 to 5, more preferably from 0 to 2, each Q independently represents a direct bond or a linking moiety selected from O, (C=0), 0(C=0), (C=0)0, NR2, NR2(C=0), (C=0)NR2, 0(C=0)NR2 and (R2)2Sι, wherein, each R2 independently represents an optionally halo-substituted Cι-C4 group, and Y is a direct bond or a sulphonamide group, for example of formula S02N(R3) wherein R3 is hydrogen or an optionally halo- substituted C,-C4 group, preferably methyl or ethyl, provided that when Y is a sulphonamide group, the corresponding T moiety has a p value of at least 1. Where Y represents a direct bond and p is greater than 0, carbon atoms are assigned between the fluoroalkyl group and T following the rule that the fluoroalkyl group contains no chain-interrupting CH2 groups.
Preferred polymerisable monomers herein are unsaturated or cyclic (the unsaturated monomers being preferred) and include a) substituted alkene compounds of formula CnX2n+jR, wherein R is selected from optionally halo- substituted alkenyl groups having from 2 to 8, preferably from 2 to 4, and more preferably 2 carbon atoms, b) substituted alkyne compounds of formula C„X2n+|R, wherein R is selected from optionally halo- substituted alkynyl groups having from 2 to 8, preferably from 2 to 4, and more preferably 2 carbon atoms, c) substituted alkadienyl compounds of formula C„X2n+ιR, wherein R is selected from optionally halo-substituted alkadienyl groups having from 4 to 8, preferably from 4 to 6, and more preferably 4 carbon atoms, d) substituted heterocycloalkyl compounds of formula C„X n+ιR, wherein R is selected from optionally halo-substituted heterocycloalkyl groups having from 2 to 8, preferably from 2 to 5, more preferably 2 to 3 cyclic carbon atoms and one or more heteroatoms, preferably O,
e) alkenoic acid esters of formula CnX2n+ι02CR wherein R is selected from optionally halo- substituted alkenyl groups having from 2 to 8, preferably from 2 to 4, and more preferably 2 carbon atoms, and f) sulphonamide-substituted alkenoic acid esters of formula C„X2H+ιS02N(R3)(C(R1)2)p02CR wherein R is selected from optionally halo-substituted alkenyl groups having from 2 to 8, preferably from 2 to 4, and more preferably 2 carbon atoms, each R' independently represents H, halogen, or an optionally halo-substituted C C4 alkyl group, p is from 1 to 10, preferably from 1 to 5, more preferably 2, and R3 is hydrogen or an optionally halo-substituted Cι-C4 group, preferably methyl or ethyl,
The processes of the invention are capable of providing stain repellent fabrics having a high fluorine surface density to provide excellent repellency performance that is maintained for 10 or more laundry treatments (wet or dry), and preferably for at least 15 or 20 laundry treatments. Preferably the fabrics when made have an F:C ratio as determined by XPS of at least about 1.10, preferably at least about 1.15, more preferably at least about 1.20, and especially at least about 1.25. The surface fluorine atomic concentration, on other hand, is preferably at least about 48%, more preferably at least about 50% and especially at least about 52%. The CF2:CχHv ratio determined from XPS C(ls) spectra is preferably at least about 1.0, more preferably at least about 2.0, even more preferably at least about 2.5 and especially at least about 3.0, wherein CχHy is the reference offset at 285eV and the CF2 peaks generally he between about 5.5 and 7.5eV above reference.
Moreover, although successive laundry treatments lead eventually to an increase in surface O concentration, at least in part because of soil deposition, stain repellency is surprisingly maintained in the presence of significant surface O. For example, the cotton fabrics of the invention display excellent soil repellency performance at levels of surface O concentration as high as 25% whereas conventionally treated cotton fabrics lose their performance at much lower levels in the region of 10- 18% This reflects the fact that conventionally treated cotton fabrics are particularly prone to loss of soil repellency after washing in medium to high soil loads.
It is also preferred herein that the polymerisable monomer be of low or intermediate volatility with a boiling point in the range from about -50°C to about 150°C, preferably from about -20°C to about 100°C at 8000mTorr (10.7mbar) although mixtures of polymerisable monomers of differing volatility or of volatile or non-volatile polymerisable monomers with polymerisable or non-polymeπsable reactive gases are also suitable for use herein for purposes of optimising e.g. stain resistance and manufacturing rate Thus in a preferred embodiment, the monomer exciting step comprises exciting the polymerisable monomer in atomized condensed form in the presence of a reactive gas, preferably a reactive polymerisable monomer gas.
Thus according to another aspect of the invention, there is provided a method for making a fabric having a laundry-durable finish by excitation-induced graft-polymerisation of a polymerisable monomer, the method comprising a) exposing the fabric or a region thereof to atomized condensed polymerisable monomer under conditions of low or zero excitation so as to coat the individual fabπc fibres, and b) exciting the polymerisable monomer m condensed form and in the presence of a reactive and preferably polymerisable monomer gas within a monomer excitation zone.
In a preferred process the polymerisable monomer is atomised onto the surface of the fabric using one or more piezoelectric, ultrasonic, electrostatic or acoustic atomisers or a combination thereof. In addition the one or more atomisers and fabric are arranged to move continuously or batchwise relative to one another so that the polymerisable monomer is distributed in atomised form over the exposed surface of the fabric or region thereof, this being valuable for providing an even distribution of the monomer on the fabric surface. To this end, the atomisers can take the form of an array arranged generally transverse to the direction of movement, the size and number of atomisers in the array being such as to essentially span the fabric in the transverse direction. Suitable atomizer arrays include those well known from the ink-jet printer industry.
Thus in another aspect on the invention, there is provided a method for making a fabric having a laundry-durable finish by excitation-induced graft polymerisation of a polymerisable monomer, the method comprising a) exposing the fabric or a region thereof to atomized polymerisable monomer, and b) exciting the atomized polymerisable monomer withm a monomer excitation zone, and wherein the polymerisable monomer is atomised using an array of atomizers, the atomizer array and fabπc being arranged to move continuously or batchwise relative to one another so as to distribute the polymerisable monomer in atomised form over the exposed surface of the fabric or region thereof, the atomizer array being arranged generally transverse to the direction of movement, the size and number of atomisers in the array being such as to essentially span the fabric in the transverse direction.
In preferred embodiments herein, the fabric is a natural or semi-natural yam-based woven fabric, especially silk, and the method includes the step of drying the substrate to a moisture regain (at 21°C, 65% RH) of at least about 5%, preferably at least about 6% and more preferably at least about 8% prior to exposing the fabric to the polymerisable monomer, this being valuable herein for achieving fabrics with optimum stam resistance and durability.
The protocol for the oil repellency test (AATCC 118-1997) is as follows. Drops of hydrocarbon liquids of various surface tensions are placed on the fabric's surface and the extent of wetting determined visually. The standard liquids and corresponding surface tensions in dyn cm (rnNm"')at 25°C for each rating are:
1 - refined mineral oil (31.0)
2 - 65/35 vol % (21°C) mix of refined mineral oil and n-hexadecane (29 2) 3 - n-hexadecane (27.3)
4 - n-tetradecane (26.2) 5 - n-dodecane (24.6)
6 - n-decane (23.6) 7 - n-octane (21.3) 8 - n-heptane (19.6)
The test fabric is placed face up on white blotting paper on a flat horizontal surface. Beginning with liquid No. 1, carefully place drops approximately 5mm in diameter or 0.05ml in volume on the fabric or region thereof in five locations. Observe the drops for 30 sec from an approximately 45° angle. Wetting of the fabric is normally shown as darkening at the liquid/fabric interface. On black or dark fabrics, wetting can be detected by a loss of 'sparkle' with the drop. If at least three of the five drops do not penetrate or wet the fabric and do not show wickmg around the drops, place drops of test liquid No. 2 on an adjacent site and repeat. Continue with progressively lower surface tension liquids until at least three of the five drops wet or show wicking into the fabric withm 30 seconds. The liquid's AATCC oil repellency rating is the highest numbered liquid for which at least three of the five drops do not wet or wick into the fabric. An intermediate number may be given for a borderline pass. An example is where three of more of the five drops are rounded, however, there is partial darkening of the specimen around the edge of the drop.
The protocol for the water repellency test is as follows. A series of standard test solutions made of isopropyl alcohol and distilled water in various proportions and surface tensions are applied dropwise to fabric's surface and the extent of wetting determined visually. The standard liquids and corresponding surface tensions in dyn cm at 25°C for each rating are:
0 - 100% water (-) 1 - 10% alcohol + 90% water (42)
2 - 20% alcohol + 80% water (33)
3 - 30% alcohol + 70% water (27.5)
4 - 40% alcohol + 60% water (25.4) 5 - 50% alcohol + 50% water (-)
6 - 60% alcohol + 40% water (-)
7 - 70% alcohol + 30% water (-)
8 - 80% alcohol + 20% water (-)
9 - 90% alcohol + 10% water (-) 10 - 100% alcohol (-)
The test fabric is placed face up on white blotting paper on a flat horizontal surface. Beginning with liquid No. 0, carefully place drops approximately 5mm in diameter or 0.05ml in volume on the fabπc or region thereof in three locations at least 2m (5.1cm) apart. Observe the drops for 10 sec from an approximately 45° angle. If at least two of the three drops do not penetrate or wet the fabric and do not show wickmg around the drops, place drops of test liquid No. 1 on an adjacent site and repeat. Continue with progressively lower surface tension liquids until at least two of the three drops wet or show wicktng into the fabric within 10 seconds. The liquid's water repellency rating is the highest numbered liquid for which at least two of the three drops do not wet or wick into the fabric as evidenced by the drops remaining spherical or hemispherical in shape.
Typical laundry wash conditions for the multicycle wash tests performed herein uses test samples of size 20 x 20cm, a 40°C short wash (25 min wash, 75 mm total wash cycle time) performed in a Miele 698 with 1 lOg of a regular European automatic wash powder under medium hardness (10 US gpg) and soil conditions - about 1.8kg of soiled household articles including bedding, towels and tea- towels - followed by tumble drying at 55°C for 45 min. The wash powder is a spray-dried detergent containing approximately (by weight of finished product) 8% anionic surfactant (LAS - linear alkyl benzene sulfonate), 17% aluminosihcate builder, 23% sodium sulfate and 7% sodium carbonate, with various dry admixes including 3% nomonic surfactant (Dobanol 45-E7), 13% percarbonate bleach, 4% tetraacetylethylenediamine bleach activator, 7% sodium carbonate, 4% silicate, 3% citric acid, the remainder enzymes, perfumes, minors and moisture. These testing conditions are sometimes referred to herein as 'cotton cycle' conditions. Testing is also performed herein in the Miele under so-called 'gentle wash' conditions, typified by a smaller number (approximately half) of the mam wash and total wash revolutions of cotton cycle conditions.
The invention will now be described by way of example with reference to the accompanying drawing in which FIG. 1 is a schematic representation of a fabric finishing unit suitable for use in plasma- mduced graft polymerization process embodiments of the invention.
Referring to FIG 1, the fabric finishing unit generally comprises vacuum chamber housing 1 equipped with plasma-generating means 2, fabric-supply and transport mechanism 3, liquid feed system 4, gas feed 5, and vacuum system 6. Plasma generating means 2 generally comprises internal powered electrode 7, internal earthed electrode 8, temperature-regulating means 9, Rf generator 10
including a power supply and meter (not shown), pulse generator 11 and pulse monitoring means 12. Temperature-regulating means 9 is used to heat or cool one of the electrodes, preferably the powered electrode 7, to the required operating temperature. Fabric-supply and transport mechanism 3 comprises feed roll 13 and take-up roll 14, the fabric to be treated passing between electrodes 7 and 8 at a predetermined web speed and in contact with the temperature-regulated electrode. Liquid feed system 4 comprises one or more ultrasonic nozzles 15 with corresponding metering pumps 16 and valves 17, nozzles 15 being arranged within housing 1 over and in close proximity to the fabric upstream of the electrodes whereby the monomer is delivered into housing 1 and deposited on to the fabric in condensed atomized form. In each instance, the electrode operating temperature and system operating pressure are adjusted according to the required monomer delivery and deposition mechanism Gas feed 5 comprises mass flow controller 19 for controlling gas flow rate, gas feed being optionally used in combination with liquid feed as described hereinabove Vacuum system 6 comprises flow control valve 20 and absolute pressure gauge 21 communicating by way of liquid nitrogen cold trap 22 (base pressure of 3mTorr) to vacuum pump means 23 (two stage rotary pump).
Example 1
The fabric finishing unit of FIG. 1 is used for used for graft polymerizing 1H,1H,2H,2H- perfluorooctyl acrylate (Mwt 418, density 1.554 c/cm3) to woven silk fabπc having a basis weight of 82g/m2, an air permeability (Textest FX3300,125Pa) of 72 ml cm"2 s*1, and a fibre surface area (N2- based BET) of 0.45m2/g and which has been preconditioned by drying to a moisture regain (at 21 °C, 65% RH) of 6%). The conditions employed are as follows' 13 56 MHz Rf generator, electrode dimensions 35cm x 40cm, gas feed 5 closed, electrode temperature 35°C, operating pressure lOOmTorr, peak power 40W, plasma on-time 800μs, plasma off-time 10,000μs, average excitation power density 2 12 x 10"3 W/cm2, web speed 0.5 m/min, web width 35cm, two ultrasonic atomizer nozzles, total monomer flow rate O.lml/min, deposition efficiency 51%, average fibre-coating thickness (estimated) 7 9 nm. The treated fabrics demonstrate excellent oil- and water- stam repellency as made and after multi-cycle laundry cleaning under medium soil conditions and multicycle dry cleaning. The air permeability, fibre surface area, handle and drape remain essentially unaffected by the plasma treatment. The treated fabrics also demonstrate improved drying characteristics, reduced dye pick-up and improved whiteness/colour fidelity and malodor resistance When the treatment is repeated twice under identical conditions (estimated fibre-coatmg thickness of 15.8nm), the durability of stain repellency is further enhanced under both gentle and cotton multicycle conditions without negatively impacting textile attributes.
Example 2
The fabric finishing unit of FIG. 1 is used for used for graft polymerizing 1H,1H,2H,2H- perfluorooctyl acrylate (Mwt 418, density 1 554 c/cra3) to knitted cotton fabπc having a basis weight of 147g/m2, an air permeability (Textest FX3300;125Pa) of 82 ml cm 2 s"', and a fibre surface area (N2-based BET) of 0.5m2/g and which has been preconditioned by drying to a moisture regain (at 21 °C, 65% RH) of 7%. The conditions employed are as follows: 13.56 MHz Rf generator, electrode dimensions 35cm x 40cm, gas feed 5 closed, electrode temperature 35°C, operating pressure lOOmTorr, peak power 40W, plasma on-time 800μs, plasma off-time 10,000μs, average excitation power density 2 12 x 10"3 W/cm2, web speed 0.5 m/min, web width 35cm, two ultrasonic atomizer nozzles, total monomer flow rate 0.11 ml/min, deposition efficiency 55%, and average fibre-coatmg thickness (estimated) 4.7nm. The treated fabrics demonstrate excellent oil- and water- stain repellency as made and after multi-cycle laundry cleaning under medium soil conditions and multicycle dry cleaning. The air permeability, fibre surface area, handle and drape remain essentially unaffected by the plasma treatment. The treated fabrics also demonstrate improved drying characteristics, reduced dye pick-up and improved whiteness/colour fidelity and malodor resistance. When the treatment is repeated twice under identical conditions (estimated fibre-coatmg thickness of 9.4nm), the durability of stam repellency is further enhanced under both gentle and cotton multi-cycle conditions without negatively impacting textile attributes.
Example 3
The fabric finishing unit of FIG. 1 is used for used for graft polymerizing lH,lH,2H-perfluoro- dodecene (Mwt 546, density 1.711 g/cm3) to woven silk fabric having a basis weight of 82g/m2, an air permeability (Textest FX3300;125Pa) of 72 ml cm"2 s"', and a fibre surface area (N2-based BET) of 0.45m2/g and which has been preconditioned by drying to a moisture regain (at 21°C, 65% RH) of 6%. The conditions employed are as follows: 13.56 MHz Rf generator, electrode dimensions 35cm x 40cm, gas feed 5 closed, electrode temperature 35°C, operating pressure lOOmTorr, peak power 40W, plasma on-time 800μs, plasma off-time 10,000μs, average excitation power density 2.12 x 10"3 W/cm2, web speed 0 5 m/min, web width 35cm, two ultrasonic atomizer nozzles, total monomer flow rate 0.06ml/mιn, deposition efficiency 42%, average fibre-coatmg thickness (estimated) 3.9 nm. The treated fabrics demonstrate excellent oil- and water- stam repellency as made and after multi-cycle laundry cleaning under medium soil conditions and multi-cycle dry cleaning. The air permeability, fibre surface area, handle and drape remain essentially unaffected by the plasma treatment. The treated fabrics also demonstrate improved drying characteristics, reduced dye pick-up and improved whiteness/colour fidelity and malodor resistance. When the treatment is repeated twice under identical conditions (estimated fibre-coatmg thickness of 7.8nm), the durability of stam repellency is further enhanced under both gentle and cotton multi-cycle conditions without negatively impacting textile attributes.
Example 4
The fabric finishing unit of FIG. 1 is used for used for graft polymerizing lH,lH,2H-perfluoro- dodecene (Mwt 546, density 1.711 g/cm3) to knitted cotton fabric having a basis weight of 147g/m2, an air permeability (Textest FX3300;125Pa) of 82 ml cm"2 s"1, and a fibre surface area (N2-based BET) of 0.5m2/g and which has been preconditioned by drying to a moisture regain (at 21°C, 65% RH) of 7%. The conditions employed are as follows: 13.56 MHz Rf generator, electrode dimensions 35cm x 40cm, gas feed 5 closed, electrode temperature 35°C, operating pressure lOOmTorr, peak power 40W, plasma on-time 800μs, plasma off-time 10,000μs, average excitation power density 2.12 x 10"3 W/cm2, web speed 0.5 m/min, web width 35cm, two ultrasonic atomizer nozzles, total monomer flow rate 0.09 ml/mm, deposition efficiency 45%, and average fibre-coating thickness (estimated) 3 lnm. The treated fabrics demonstrate excellent oil- and water- stain repellency as made and after multi-cycle laundry cleaning under medium soil conditions and multi-cycle dry cleaning. The air permeability, fibre surface area, handle and drape remain essentially unaffected by the plasma treatment The treated fabrics also demonstrate improved drying characteristics, reduced dye pick-up and improved whiteness/colour fidelity and malodor resistance. When the treatment is repeated twice under identical conditions (estimated fibre-coating thickness of 6.2nm), the durability of stam repellency is further enhanced under both gentle and cotton multi-cycle conditions without negatively impacting textile attributes.