BACKGROUND OF INVENTION
Field of the Invention
[0001] Embodiments disclosed herein relate generally to polymeric composite structures.
In some embodiments, the composite structure may include a substrate having a desired
combination of performance properties including high softness and high loft. More
specifically, embodiments disclosed herein relate to polymeric composite structures
that have an open-cell foam layer, a substrate layer, and optionally at least one
cleaning surfactant, active agent, or enhancing filler.
Background
[0002] Dry and wet, or pre-moistened, wipes are well known consumer products available in
many forms. Dry wipes may include a substrate, with or without additives, such as
antibacterial substances or cleansing agents that may be released upon contact with
skin, oil, or water. Wet wipes include a substrate, such as a non-woven web, which
may be pre-moistened with a mild surfactant-based solution, and may include lotions,
cleansing agents, or other additives. Such wet and dry wipes have been used for baby
wipes, hand wipes, household cleaning wipes, industrial wipes, body and facial wipes,
and the like. Typically, wipes are provided as either folded, stacked sheets or as
a perforated roll, where the sheets are meant to be used one at a time.
[0003] Initially, wet wipe products were made of traditional non-woven materials based on
paper making technology (pulp based products). These products were well accepted but
deficient in softness of the fabric material. The introduction of spunlace non-woven
technology offered products that, compared to traditional paper based products, were
superior in terms of softness. This is mainly due to (i) the use of long soft fibers
(most frequently rayon and polyethylene terephthalate/polypropylene or a mixture of
these fibers) in the spunlace process and (ii) the fact that during the spunlace process
no binder is added to the fabric.
[0004] Other conventional wet wipes have included a single layer of a substantially homogeneous
material. For example, conventional wet wipes have included an air laid web of fibers
that are uniformly mixed or distributed throughout the web. The wipes have included
polymeric fibers, such as polyester, polyethylene, and polypropylene, and natural
or synthetic fibers, such as cellulosic fibers. Other conventional wet wipes have
included a co-formed web of polypropylene and cellulosic fibers uniformly mixed throughout
the web.
However, other forms of a wet wipe or wipe-type product include a wipe product having
a non-woven, layered base sheet. The layered base sheet may include at least two layers
positioned in facing relation with each other where one of the layers includes fibers
that are not included in the other layer, such as where one layer includes polyethylene
fibers and one layer includes polypropylene fibers. In alternate forms, the layers
may include similar materials, but in differing amounts. One layer may be configured
to provide different physical properties, such as softness, to the wipe product while
another layer may be configured to provide other properties, such as strength, to
the wipe product.
WO 1998/003713, corresponding to
US Patent No. 6,028,018 discloses one example of a wet wipe having a multilayer base sheet.
WO-A-2007/100312 describes a composition which contains a mixture of a shear thickening fluid and
at least one inert filler and said shear thickening fluid and filler remain in a conformable
form.
WO-A-2006/060520 relates to processes and apparati for selectively electroplating a metal layer or
layers into recessed topographic features on a conductive surface.
WO-A-2004/046214 relates to a polymer comprising one or more C
3 to C
40 olefins, optionally one or more diolefins, and less than 15 mole % of ethylene, where
the polymer has a) a Dot-T-Peel of 1 Newton or more; and b) a branching index (g')
of 0.95 or less measured at the M
z of the polymer; c) an M
w of 100,000 or less.
WO-A-2005/019241 relates to compositions of novel antimicrobial peptides. The peptides exhibit high
antibacterial activity and low hemolytic activity.
WO-A-2004/078900 discloses foamed polyurethane articles comprising one or more quaternary ammonium
compounds having germicidal properties.
A recent innovation to improve loft of wipes includes the controlled formation of
machine direction voids within a spunlaced non-woven. Void formation may be introduced
to a spunlaced non-woven by placing stationary parallel tubes between two continuous
layers of carded fibres. The tubes may extend into a spunlacer, where the top and
bottom fiber layers are spunlaced together around the tubes and the tubes are removed
from the spunlaced non-woven to form the void spaces. The voids may increase the loft
and feel of the non-woven and may be filled with a liquid or powder additive through
the tubes.
[0005] Even with recent innovations, the balance of physical properties, such as softness,
loft, volume, drapability, fuzz resistance, flexibility, strength, integrity, cloth-like
feel, and resiliency, of wet wipes has not been completely optimized. For example,
in facial cleaning wipes it is desirable to have a soft, high loft, flexible, fuzz
resistant product with a more cloth-like feel while retaining cleaning efficacy and
durability. Obtaining the desired balance of properties is especially challenging
as desirable attributes may be opposing, e.g. a stronger product typically reduces
the flexibility of the product. The physical property balance has been particularly
difficult of users desiring improved softness. For example, certain fibers that may
be used for wet wipes are stiffer and can provide strength and resiliency, but are
not as soft or flexible as other fibers. Other fibers that may be used for wet wipes
are softer but may not have sufficient wet strength to withstand the forces exerted
by the user. Moreover, the different types of fibers that may provide the desired
properties, such as fibers for strength and fibers for softness, have been difficult
to combine in a homogenous layer due to incompatibilities with each other.
Accordingly, there exists a need for wet wipes with improved softness and flexibility
while maintaining the strength, integrity, resiliency, fuzz resistance, and other
properties of the wipes.
SUMMARY OF THE INVENTION
[0006] The present invention relates to a composite structure comprising:
at least one substrate layer;
at least one layer comprising an open-cell polyolefin foam having a density in the
range of from 0.03 to 0.07 g/cc disposed on the substrate layer;
wherein the substrate layer comprises a polyurethane or polyolefin non-woven having
a basis weight of 15 to 250 grams per square meter; and
wherein the composite structure has a basis weight of 15 to 500 grams per square meter.
A method of forming a composite structure including at least one substrate layer and
at least one layer comprising an open-cell foam is also described. The method may
include applying a froth to a substrate, wherein the froth comprises water and a thermoplastic
polymer, and removing at least a portion of the water from the froth to form a foam.
Other aspects and advantages of the invention will be apparent from the following
description and the appended claims.
BRIEF DESCRIPTION OF THE DRAWINGS
[0007]
Figure 1 illustrates the formation of foam from froth in accordance with embodiments
disclosed herein.
Figure 2 schematically illustrates an extrusion apparatus that may be used in embodiments
disclosed herein.
Figure 3 is a micrograph of a cross-section of one embodiment of the composite structures
disclosed herein
Figure 4 is a graphical representation of bending rigidity test results for embodiments
of the composite structures disclosed herein as compared to commercially available
comparative samples.
Figure 5 is a graphical representation of the fuzz resistance test results for embodiments
of the composite structures disclosed herein as compared to commercially available
comparative samples.
Figure 6 is a graphical representation of the results for hand measurements normalized
by sample basis weight for embodiments of the composite structures disclosed herein
as compared to commercially available comparative samples
Figure 7 is a graphical representation of the results for hand measurements normalized
by sample volume for embodiments of the composite structures disclosed herein as compared
to commercially available comparative samples
Figure 8 is a graphical representation of the results for Kawabata Evaluation System
measurements for compression resilience for embodiments of the composite structures
disclosed herein as compared to commercially available comparative samples
Figure 9-11 are graphical representations of the PPT tear strength test results for
embodiments of the composite structures disclosed herein as compared to commercially
available comparative samples.
Figure 12 is a graphical representation of the results for Kawabata Evaluation System
measurements for geometric roughness for embodiments of the composite structures disclosed
herein as compared to commercially available comparative samples.
Figure 13 is a graphical representation of the results for Kawabata Evaluation System
measurements for coefficient of friction for embodiments of the composite structures
disclosed herein as compared to commercially available comparative samples.
DETAILED DESCRIPTION
[0008] In one aspect, embodiments disclosed herein relate to composite structures having
a balance of softness, weight, and other properties which may include bending rigidity,
coefficient of friction, fuzz resistance, loft, volume, and others.
[0009] In other aspects, embodiments disclosed herein relate to composite structures having
a balance of properties, wherein the composite structure includes at least one substrate
layer and at least one open-cell foam layer. The substrate may include non-wovens,
fabrics, and the like. Incorporation of open-cell foams with a substrate (e.g., non-wovens,
fabrics, etc.) into wipes or other articles may impart additional softness, loft,
and volume to the article. The additional loft and volume may be achieved while enhancing
and/or maintaining the desired, pre-existing surface feel of the substrate alone.
The incorporation of the open-cell foam may also increase the available void volume
and/or surface area for the inclusion and delivery of active agents when compared
to the fabric or non-woven layer alone.
[0010] In other aspects, embodiments disclosed herein relate to a composite structure including
an open-cell foam layer, a substrate layer, and optionally at least one cleaning surfactant,
active agent, or enhancing filler. Embodiments of the composite structure may exhibit
a desired combination of performance properties, including high softness and high
loft, and/or excellent resistance to surface abrasion. The soft, high loft composite
structure may be useful for disposable and semi-disposable applications related to
personal care, medical, shipping, and household markets. The composite structure may
also be capable of delivering wet active agents or dry active agents requiring wetting
for cleansing, polishing, or medical applications.
[0011] The composite structures disclosed herein may be used for cleaning wipes for skin
contact, and may include wet and/or dry active agents. The composite structures disclosed
herein may also be used for other applications including baby wipes, hand wipes, hard
surface cleaners for home use, and industrial cleaning wipes.
[0012] Enhanced softness or a more cloth-like feel are also desirable for applications beyond
skin cleansing wipes. These applications may include, but are not limited to, applicator
pads, polishing cloths, medical cleansing, shipping/packaging material for sensitive
components, or application pads for topical medicines. Additionally these articles
may be used as a means for the temporary storage of measured amounts liquid materials
[0013] Foams useful in embodiments of the composite structures disclosed herein may be formed
from froths or frothed dispersions. As used herein, the terms "frothing" or "frothed"
refers to a process where substantial volumes of air, or other gas, are incorporated
in a liquid where, in some embodiments, at least 80 volume percent of the resulting
composition (the frothed material) consists of the gaseous component. In other embodiments,
at least 85 volume percent of the frothed material consists of the gaseous component;
and at least 90 volume percent in yet other embodiments. The liquid may be a molecular
solution, a micellar solution, or a dispersion in an aqueous or organic medium. In
general the frothed liquid is created by mechanical methods such as high shear mixing
under atmospheric conditions or optionally injecting gas into the system while mixing.
The term "froth," as used herein, refers to a liquid which has been frothed, as described
above, before drying or removing the liquid medium.
[0014] The term "foam," as used herein, refers to a resilient structure formed by removing
a portion of the liquid medium from a froth, i.e., at least a portion, a substantial
portion, or all of the liquid medium may be removed. As used herein, drying and removing
may be used interchangeably, and may include thermal and/or mechanical removal of
the liquid medium. The formation of a foam from a froth in accordance with embodiments
disclosed herein is illustrated in Figure 1. A froth 5 may include pockets of vapor
7 within dispersion 8, where the dispersion 8 includes polymer particles 10 in a liquid
medium 9. When the liquid medium 9 is removed from the froth 5 during a drying or
removing process 11, the polymer particles 10 coalesce and melt together creating
interconnected film or struts 12 around the entrapped vapor bubbles 13, giving stability
to the resulting structure 14. Film formation may depend upon variables including
the melting point of polymers within the froth, the rate of removal (
i.e., evaporation rate) of the liquid medium, and overall froth composition, among others.
For example, as water is removed from a froth formed from an aqueous dispersion, polymers
contained in the dispersion may coalesce, forming a film, giving structure and resiliency
to the resulting foam. In some embodiments, a foam may be formed where the amount
of residual liquid ranges from 0 to 20 weight percent; 0 to 10 weight percent in other
embodiments; and 0 to 8 percent in yet other embodiments.
[0015] As described above, embodiments of the present disclosure include various substrates,
including non-wovens, fabrics, and foams. Additionally, embodiments disclosed herein
may include various additives, including wet or dry active agents. Each of these components
and methods to form the composite structures disclosed herein are described in more
detail below.
[0016] FOAMS AND FOAM SUBSTRATES
[0017] Foams useful in embodiments include foams formed from polyolefin resins.
[0018] In some embodiments, polyolefin foams may be made from aqueous dispersions. The aqueous
dispersions may be frothed and at least partially dried to result in the desired foams.
Dispersions used in embodiments of the present disclosure may include water, at least
one thermoplastic resin, and a dispersion stabilizing agent. The thermoplastic resin
included in embodiments of the foams of the present disclosure may include a resin
that is not readily dispersible in water by itself. The term "resin," as used herein,
should be construed to include synthetic polymers or chemically modified natural resins.
The thermoplastic resin includes polyolefins. Dispersions may also include various
additives, including frothing surfactants. Each of these is discussed in more detail
below.
[0020] Polyolefin resins used herein may include olefin polymers and elastomers, and blends
of various olefin polymers and/or olefin elastomers. In some embodiments, the olefin
resin is a semicrystalline resin. The term "semi-crystalline" is intended to identify
those resins that possess at least one endotherm when subjected to standard differential
scanning calorimetry (DSC) evaluation. Some semi-crystalline polymers exhibit a DSC
endotherm that exhibits a relatively gentle slope as the scanning temperature is increased
past the final endotherm maximum. This reflects a polymer of broad melting range rather
than a polymer having what is generally considered to be a sharp melting point. Some
polymers useful in the dispersions of the disclosure have a single melting point while
other polymers have more than one melting point.
[0021] In some polymers, one or more of the melting points may be sharp such that all or
a portion of the polymer melts over a fairly narrow temperature range, such as a few
degrees centigrade. In other embodiments, the polymer may exhibit broad melting characteristics
over a range of 20°C. In yet other embodiments, the polymer may exhibit broad melting
characteristics over a range of greater than 50°C.
[0022] Examples of the olefin resins that may be used in the present disclosure include
homopolymers and copolymers (including elastomers) of an alpha-olefin such as ethylene,
propylene, 1-butene, 3-methyl-1-butene, 4-methyl-1-pentene, 3-methyl-1- pentene, 1-heptene,
1-hexene, 1-octene, 1-decene, and 1-dodecene, as typically represented by polyethylene,
polypropylene, poly-1-butene, poly-3-methyl-1-butene, poly-3-methyl-1-pentene, poly-4-methyl-1-pentene,
ethylene-propylene copolymer, ethylene-1-butene copolymer, and propylene- 1-butene
copolymer; copolymers (including elastomers) of an alpha-olefin with a conjugated
or non-conjugated diene, as typically represented by ethylene-butadiene copolymer
and ethylene-ethylidene norbornene copolymer; and polyolefins (including elastomers)
such as copolymers of two or more alpha-olefins with a conjugated or non-conjugated
diene, as typically represented by ethylene-propylene-butadiene copolymer, ethylene-propylene-dicyclopentadiene
copolymer, ethylene-propylene-1,5-hexadiene copolymer, and ethyleno-propylene-ethylidene
norbornene copolymer; ethylene vinyl compound copolymers such as ethylene-vinyl acetate
copolymer, ethylene-vinyl alcohol copolymer, ethylene-vinyl chloride copolymer, ethylene
acrylic acid or ethylene-(meth)acrylic acid copolymers, and ethylene-(meth)acrylate
copolymer; styrenic copolymers (including elastomers) such as polystyrene, ABS, acrylonitrile-styrene
copolymer, α-methylstyrene-styrene copolymer, styrene vinyl alcohol, styrene acrylates
such as styrene methylacrylate, styrene butyl acrylate, styrene butyl methacrylate,
and styrene butadienes and crosslinked styrene polymers; and styrene block copolymers
(including elastomers) such as styrene-butadiene copolymer and hydrate thereof, and
styrene-isoprenestyrene tri-block copolymer; polyvinyl compounds such as polyvinyl
chloride, polyvinylidene chloride, vinyl chloride-vinylidene chloride copolynaer,
polymethyl acrylate, and polymethyl methacrylate; polyamides such as nylon 6, nylon
6,6, and nylon 12; thermoplastic polyesters such as polyethylene terephthalate and
polybutylene terephtalate; polycarbonate, polyphenylene oxide, and the like; and glassy
hydrocarbon-based resins, including poly-dicyclopentadiene polymers and related polymers
(copolymers, terpolymers); saturated mono-olefins such as vinyl acetate, vinyl propionate
and vinyl butyrate and the like; vinyl esters such as esters of monocarboxylic acids,
including methyl acrylate, ethyl acrylate, n-butylacrylate, isobutyl acrylate, dodecyl
acrylate, n-octyl acrylate, phenyl acrylate, methyl methacrylate, ethyl methacrylate,
and butyl methacrylate and the like; acrylonitrile, methacrylonitrile, acrylamide,
mixtures thereof; resins produced by ring opening metathesis and cross metathesis
polymerization and the like. These resins may be used either alone or in combinations
of two or more
[0023] In one particular embodiment, the thermoplastic resin may comprise an alpha-olefin
interpolymer of ethylene with a comonomer comprising an alkene, such as 1-octene.
The ethylene and octene copolymer may be present alone or in combination with another
thermoplastic resin, such as ethylene-acrylic acid copolymer. When present together,
the weight ratio between the ethylene and octene copolymer and the ethylene-acrylic
acid copolymer may range from 1:10 to 10:1, such as from 3:2 to 2:3. The polymeric
resin, such as the ethylene-octene copolymer, may have a crystallinity of less than
50%, such as less than 25%. In some embodiments, the crystallinity of the polymer
may range from 5 to 35 percent. In other embodiments, the crystallinity may range
from 7 to 20 percent.
[0024] Embodiments disclosed herein may also include a polymeric component that may include
at least one multi-block olefin interpolymer. Suitable multi-block olefin interpolymers
may include those described in, for example,
U.S. Provisional Patent Application No. 60/818,911. The term "multi-block copolymer" or "multi-block interpolymers" refers to a polymer
comprising two or more chemically distinct regions or segments (referred to as "blocks")
preferably joined in a linear manner, that is, a polymer comprising chemically differentiated
units which are joined end-to-end with respect to polymerized ethylenic functionality,
rather than in pendent or grafted fashion. In certain embodiments, the blocks differ
in the amount or type of comonomer incorporated therein, the density, the amount of
crystallinity, the crystallize size attributable to a polymer of such composition,
the type or degree of tacticity (isotactic or syndiotactic), regio-regularity or regio-irregularity,
the amount of branching, including long chain branching or hyper-branching, the homogeneity,
or any other chemical or physical property. The multi-block copolymers are characterized
by unique distributions of polydispersity index (PDI or M
w/M
n), block length distribution, and/or block number distribution due to the unique process
making of the copolymers. More specifically, when produced in a continuous process,
embodiments of the polymers may possess a PDI ranging from 1.7 to 8; from 1.7 to 3.5
in other embodiments; from 1.7 to 2.5 in other embodiments; and from 1.8 to 2.5 or
from 1.8 to 2.1 in yet other embodiments. When produced in a batch or semi-batch process,
embodiments of the polymers may possess a PDI ranging from 1.0 to 2.9; from 1.3 to
2.5 in other embodiments; from 1.4 to 2.0 in other embodiments; and from 1.4 to 1.8
in yet other embodiments.
[0025] One example of the multi-block olefin interpolymer is an ethylene/α-olefin block
interpolymer. Another example of the multi-block olefin interpolymer is a propylene/α
olefin interpolymer. The following description focuses on the interpolymer as having
ethylene as the majority monomer, but applies in a similar fashion to propylene-based
multi-block interpolymers with regard to general polymer characteristics.
[0026] The ethylene/α-olefin multi-block copolymers may comprise ethylene and one or more
co-polymerizable α-olefin comonomers in polymerized form, characterized by multiple
(i.e., two or more) blocks or segments of two or more polymerized monomer units differing
in chemical or physical properties (block interpolymer). In some embodiments, the
copolymer is a multi-block interpolymer. In some embodiments, the multi-block interpolymer
may be represented by the following formula:

where n is at least 1, and in various embodiments n is an integer greater than 1,
such as 2, 3, 4, 5, 10, 15, 20, 30, 40, 50, 60, 70, 80, 90, 100, or higher; "A" represents
a hard block or segment; and "B" represents a soft block or segment. Preferably, A's
and B's are linked in a linear fashion, not in a branched or a star fashion. "Hard"
segments refer to blocks of polymerized units in which ethylene is present in an amount
greater than 95 weight percent in some embodiments, and in other embodiments greater
than 98 weight percent. In other words, the comonomer content in the hard segments
is less than 5 weight percent in some embodiments, and in other embodiments, less
than 2 weight percent of the total weight of the hard segments. In some embodiments,
the hard segments comprise all or substantially all ethylene. "Soft" segments, on
the other hand, refer to blocks of polymerized units in which the comonomer content
is greater than 5 weight percent of the total weight of the soft segments in some
embodiments, greater than 8 weight percent, greater than 10 weight percent, or greater
than 15 weight percent in various other embodiments. In some embodiments, the comonomers
content in the soft segments may be greater than 20 weight percent, greater than 25
eight percent, greater than 30 weight percent, greater than 35 weight percent, greater
than 40 weight percent, greater than 45 weight percent, greater than 50 weight percent,
or greater than 60 weight percent in various other embodiments.
[0027] In some embodiments, A blocks and B blocks are randomly distributed along the polymer
chain. In other words, the block copolymers do not have a structure like:

[0028] In other embodiments, the block copolymers do not have a third block. In still other
embodiments, neither block A nor block B comprises two or more segments (or sub-blocks),
such as a tip segnent.
[0029] The multi-block interpolymers may be characterized by an average block index, ABI,
ranging from greater than zero to 1.0 and a molecular weight distribution, M
w/M
n, greater than 1.3. The average block index, ABI, is the weight average of the block
index ("BI") for each of the polymer fractions obtained in preparative TREF from 20°C
and 110°C, with an increment of 5°C:

where BI
i is the block index for the i
th fraction of the multi-block interpolymer obtained in preparative TREF, and w
i is the weight percentage of the i
th fraction.
[0030] Similarly, the square root of the second moment about the mean, hereinafter referred
to as the second moment weight average block index, may be defined as follows:

[0031] For each polymer fraction, BI is defined by one of the two following equations (both
of which give the same BI value):

where T
x is the analytical temperature rising elution fractionation (ATREF) elution temperature
for the i
th fraction (preferably expressed in Kelvin), P
x is the ethylene mole fraction for the i
th fraction, which may be measured by NMR or IR as described below. P
AB is the ethylene mole fraction of the whole ethylene/α-olefin interpolymer (before
fractionation), which also may be measured by NMR or IR. T
A and P
A are the ATREF elution temperature and the ethylene mole fraction for pure "hard segments"
(which refer to the crystalline segments of the interpolymer). As an approximation
or for polymers where the "hard segment" composition is unknown, the T
A and P
A values are set to those for high density polyethylene homopolymer.
[0032] T
AB is the ATREF elution temperature for a random copolymer of the same composition (having
an ethylene mole fraction of P
AB) and molecular weight as the multi-block interpolymer. T
AB may be calculated from the mole fraction of ethylene (measured by NMR) using the
following equation:

where α and β are two constants which may be determined by a calibration using a number
of well characterized preparative TREF fractions of a broad composition random copolymer
and/or well characterized random ethylene copolymers with narrow composition. It should
be noted that α and β may vary from instrument to instrument. Moreover, one would
need to create an appropriate calibration curve with the polymer composition of interest,
using appropriate molecular weight ranges and comonomer type for the preparative TREF
fractions and/or random copolymers used to create the calibration. There is a slight
molecular weight effect. If the calibration curve is obtained from similar molecular
weight ranges, such effect would be essentially negligible. In some embodiments, random
ethylene copolymers and/or preparative TREF fractions of random copolymers satisfy
the following relationship:

[0033] The above calibration equation relates the mole fraction of ethylene, P, to the analytical
TREF elution temperature, T
ATREF, for narrow composition random copolymers and/or preparative TREF fractions of broad
composition random copolymers. T
XO is the ATREF temperature for a random copolymer of the same composition and having
an ethylene mole traction of P
X. T
XO may be calculated from LnP
X = α/T
XO + β. Conversely, P
XO is the ethylene mole fraction for a random copolymer of the same composition and
having an TREF temperature of T
X, which may be calculated from Ln Pxo = α/T
X + β.
[0034] Once the block index (BI) for each preparative TREF fraction is obtained, the weight
average block index, ABI, for the whole polymer may be calculated. In some embodiments,
ABI is greater than zero but less than 0.4 or from 0.1 to 0.3. In other embodiments,
ABI is greater than 0.4 and up to 1.0. In yet other embodiments, ABI should be in
the range of from 0.4 to 0.7, from 0.5 to 0.7, or from 0.6 to 0.9. In some embodiments,
ABI is in the range of from 0.3 to 0.9, from 0.3 to 0.8, or from 0.3 to 0.7, from
0.3 to 0.6, from 0.3 to 0.5, or from 0.3 to 0.4. In other embodiments, ABI is in the
range of from 0.4 to 1.0, from 0.5 to 1.0, or from 0.6 to 1.0, from 0.7 to 1.0, from
0.8 to 1.0, or from 0.9 to 1.0,
[0035] Another characteristic of the multi-block interpolymer is that the interpolymer may
comprise at least one polymer fraction which may be obtained by preparative TREF,
wherein the fraction has a block index greater than 0.1 and up to 1.0 and the polymer
having a molecular weight distribution, M
w/M
n, greater than 1.3. In some embodiments, the polymer fraction has a block index greater
than 0.6 and up to 1.0, greater than 0.7 and up to 1.0, greater than 0.8 and up to
1.0, or greater than 0.9 and up to 1.0. In other embodiments, the polymer fraction
has a block index greater than 0.1 and up to 1.0, greater than 0.2 and up to 1.0,
greater than 0.3 and up to 1.0, greater than 0.4 and up to 1.0, or greater than 0.4
and up to 1.0. In still other embodiments, the polymer fraction has a block index
greater than 0.1 and up to 0.5, greater than 0.2 and up to 0.5, greater than 0.3 and
up to 0.5, or greater than 0.4 and up to 0.5. In yet other embodiments, the polymer
fraction has a block index greater than 0.2 and up to 0.9, greater than 0.3 and up
to 0.8, greater than 0.4 and up to 0.7, or greater than 0.5 and up to 0.6.
[0036] Ethylene / α-olefin multi-block interpolymers used in embodiments disclosed herein
may be interpolymers of ethylene with at least one C
3-C
20 α-olefin. The interpolymers may further comprise C
4-C
18 diolefin and/or alkenylbenzene. Suitable unsaturated comonomers useful for polymerising
with ethylene include, for example, ethylenically unsaturated monomers, conjugated
or non-conjugated dienes, polyenes, alkenylbenzenes, etc. Examples of such comonomers
include C
3-C
20 α-olefins such as propylene, isobutylene, 1-butene, 1-hexene, 1-pentene, 4-methyl-1-pentene,
1-heptene, 1-octene, 1-nonene, 1-decene, and the like. In certain embodiments, the
α-olefins may be 1-butene or 1-octene. Other suitable monomers include styrene, halo-
or alkyl-substituted styrenes, vinylbenzocyclobutane, 1,4-hexadiene, 1,7-octadiene,
and naphthenics (such as cyclopentene, cyclohexene, and cyclooctene, for example).
[0037] The multi-block interpolymers disclosed herein may be differentiated from conventional,
random copolymers, physical blends of polymers, and block copolymers prepared via
sequential monomer addition, fluxional catalysts, and anionic or cationic living polymerization
techniques. In particular, compared to a random copolymer of the same monomers and
monomer content at equivalent crystallinity or modulus, the interpolymers have better
(higher) heat resistance as measured by melting point, higher TMA penetration temperature,
higher high-temperature tensile strength, and/or higher high-temperature torsion storage
modulus as determined by dynamic mechanical analysis. Properties of infill may benefit
from the use of embodiments of the multi-block interpolymers, as compared to a random
copolymer containing the same monomers and monomer content, the multi-block interpolymers
have lower compression set, particularly at elevated temperatures, lower stress relaxation,
higher creep resistance, higher tear strength, higher blocking resistance, faster
setup due to higher crystallization (solidification) temperature, higher recovery
(particularly at elevated temperatures), better abrasion resistance, higher retractive
force, and better oil and filler acceptance.
[0038] Other olefin interpolymers include polymers comprising monovinylidene aromatic monomers
including styrene, o-methyl styrene, p-methyl styrene, t-butylstyrene, and the like.
In particular, interpolymers comprising ethylene and styrene may be used. In other
embodiments, copolymers comprising ethylene, styrene and a C
3-C
20 α-olefin, optionally comprising a C
4-C
20 diene, may be used.
[0039] Suitable non-conjugated diene monomers may include straight chain, branched chain
or cyclic hydrocarbon diene having from 6 to 15 carbon atoms. Examples of suitable
non-conjugated dienes include, but are not limited to, straight chain acyclic dienes,
such as 1,4-hexadiene, 1,6-octadiene, 1,7-octadiene, 1,9-decadiene, branched chain
acyclic dienes, such as 5-methyl-1,4-hexadiene; 3,7-dimethyl-1,6-octadiene; 3,7-dimethyl-1,7-octadiene
and mixed isomers of dihydromyricene and dihydroocinene, single ring alicyclic dienes,
such as 1,3-cyclopentadiene; 1,4-cyclohexadiene; 1,5-cyclooctadiene and 1,5-cyclododecadiene,
and multi-ring alicyclic fused and bridged ring dienes, such as tetrahydroindene,
methyl tetrahydroindene, dicyclopentadiene, bicyclo-(2,2,1)-hepta-2,5-diene; alkenyl,
alkylidene, cycloalkenyl and cycloalkylidene norbornenes, such as 5-methylene-2-norbornene
(MNB); 5-propenyl-2-norbornene, 5-isopropylidene-2-norbornene, 5-(4-cyclopentenyl)-2-norbornene,
5-cyclohexylidene-2-norbornene, 5-vinyl-2-norbornene, and norbornadiene. Of the dienes
typically used to prepare EPDMs, the particularly preferred dienes are 1,4-hexadiene
(HD), 5-ethylidene-2-norbornene (ENB), 5-vinylidene-2-norbornene (VNB), 5-methylene-2-norbornene
(MNB), and dicyclopentadiene (DCPD).
[0040] One class of desirable polymers that may be used in accordance with embodiments disclosed
herein includes elastomeric interpolymers of ethylene, a C
3-C
20 α-olefin, especially propylene, and optionally one or more diene monomers. Preferred
α-olefins for use in this embodiment are designated by the formula CH
2=CHR*, where R* is a linear or branched alkyl group of from 1 to 12 carbon atoms.
Examples of suitable α-olefins include, but are not limited to, propylene, isobutylene,
1-butene, 1-pentene, 1-hexene, 4-methyl-l-pentene, and 1-octene. A particularly preferred
α-olefin is propylene. The propylene based polymers are generally referred to in the
art as EP or EPDM polymers. Suitable dienes for use in preparing such polymers, especially
multi-block EPDM type polymers include conjugated or non-conjugated, straight or branched
chain-, cyclic- or polycyclicdienes comprising from 4 to 20 carbons. Preferred dienes
include 1,4-pentadiene, 1,4-hexadiene, 5-ethylidene-2-norbornene, dicyclopentadiene,
cyclohexadiene, and 5-butylidene-2-norbornene. A particularly preferred diene is 5-ethylidene-2-norbornene.
[0041] As one suitable type of resin, the esterification products of a di- or polycarboxylic
acid and a diol comprising a diphenol may be used. These resins are illustrated in
U.S. Patent No. 3,590,000. Other specific examples of resins include styrene/methacrylate copolymers, and styrene/butadiene
copolymers; suspension polymerized styrene butadienes; polyester resins obtained from
the reaction of bisphenol A and propylene oxide followed by the reaction of the resulting
product with fumaric acid; and branched polyester resins resulting from the reaction
of dimethylterephthalate, 1,3-butanediol, 1,2-propanediol, and pentaerythritol, styrene
acrylates, and mixtures thereof.
[0042] Further, specific embodiments of the present disclosure may employ ethylene-based
polymers, propylene-based polymers, propylene-ethylene copolymers, and styrenic copolymers
as one component of a composition. Other embodiments of the present disclosure may
use polyester resins, including those containing aliphatic diols such as UNOXOL 3,4
diol, available from The Dow Chemical Company (Midland, MI).
[0043] In select embodiments, the thermoplastic resin is formed from ethylene-alpha olefin
copolymers or propylene-alpha olefin copolymer. In particular, in select embodiments,
the thermoplastic resin includes one or more non-polar polyolefins.
[0044] In specific embodiments, polyolefin such as polypropylene, polyethylene, copolymers
thereof, and blends thereof, as well as ethylene-propylene-diene terpolymers, may
be used. In some embodiments, preferred olefinic polymers include homogeneous polymers,
as described in
U.S. Patent No. 3,645,992 issued to Elston; high density polyethylene (HDPE), as described in
U.S. Patent No. 4,076,698 issued to Anderson; heterogeneously branched linear low density polyethylene (LLDPE); heterogeneously
branched ultra low linear density polyethylene (ULDFE); homogeneously branched, linear
ethylene/alpha-olefin copolymers; homogeneously branched, substantially linear ethylene/alpha-olefin
polymers, which can be prepared, for example, by processes disclosed in
U.S.Patent Nos. 5,272,236 and
5,278,272 ; and high pressure, free radical polymerized ethylene polymers and copolymers such
as low density polyethylene (LDPE) or ethylene vinyl acetate polymers (EVA).
[0045] Polymer compositions, and blends thereof, described in
U.S. Patent Nos. 6,566,446,
6,538,070,
6,448,341,
6,316,549,
6,111,023,
5,869,575,
5,844,045, or
5,677,383, may also be suitable in some embodiments. In some embodiments, the blends may include
two different Ziegler-Natta polymers. In other embodiments, the blends may include
blends of a Ziegler-Natta polymer and a metallocene polymer. In still other embodiments,
the polymer used herein may be a blend of two different metallocene polymers. In other
embodiments, single site catalyst polymers may be used.
[0046] In some embodiments, the polymer is a propylene-based copolymer or interpolymer.
In some particular embodiments, the propylene/ethylene copolymer or interpolymer is
characterized as having substantially isotactic propylene sequences. The term "substantially
isotactic propylene sequences" and similar terms mean that the sequences have an isotactic
triad (mm) measured by
13C NMR of greater than 0.85 in one embodiment; greater than 0.90 in another embodiment;
greater than 0.92 in another embodiment; and greater than 0.93 in yet another embodiment.
Isotactic triads are well-known in the art and are described in, for example,
U.S. Patent No. 5,504,172 and
WO 00/01745, which refer to the isotactic sequence in terms of a triad unit in the copolymer
molecular chain determined by
13C NMR spectra.
[0047] The olefin polymers, copolymers, interpolymers, and multi-block interpolymers may
be functionalized by incorporating at least one functional group in its polymer structure.
Exemplary functional groups may include, for example, ethylenically unsaturated mono-
and di-functional carboxylic acids, ethylenically unsaturated mono- and di-functional
carboxylic acid anhydrides, salts thereof and esters thereof. Such functional groups
may be grafted to an olefin polymer, or it may be copolymerized with ethylene and
an optional additional comonomer to form an interpolymer of ethylene, the functional
comonomer and optionally other comonomer(s). Means for grafting functional groups
onto polyethylene are described for example in
U.S. Patents Nos. 4,762,890,
4,927,888, and
4,950,541. One particularly useful functional group is maleic anhydride.
[0048] The amount of the functional group present in the functional polymer may vary. The
functional group may be present in an amount of at least 1.0 weight percent in some
embodiments; at least 5 weight percent in other embodiments; and at least 7 weight
percent in yet other embodiments. The functional group may be present in an amount
less than 40 weight percent in some embodiments; less than 30 weight percent in other
embodiments; and less than 25 weight percent in yet other embodiments.
[0049] In other particular embodiments, the thermoplastic resin may be ethylene vinyl acetate
(EVA) based polymers. In other embodiments, the thermoplastic resin may be ethylene-methyl
acrylate (EMA) based polymers. In other particular embodiments, the ethylene-alpha
olefin copolymer may be ethylene-butene, ethylene-hexene, or ethylene-octene copolymers
or interpolymers. In other particular embodiments, the propylene-alpha olefin copolymer
may be a propylene-ethylene or a propylene-ethylene-butene copolymer or interpolymer.
[0050] The thermoplastic polymer may have a crystallinity as determined by the observance
of at least one endotherm when subjected to standard differential scanning calorimetry
(DSC) evaluation. For ethylene-based polymers, a melt index ("MI") determined according
to ASTM D1238 at 190°C (375°F) with a 2.16 kg (4.75 lb.) weight of 30 g/10 minutes
or less in some embodiments; 25 g/10 minutes or less in other embodiments; 22 g/10
minutes or less in other embodiments; and 18 g/10 minutes or less in yet other embodiments.
In other embodiments, ethylene-based polymers may have a melt index (MI) of 0.1 g/10
minutes or greater, 0.25 g/10 minutes or greater in other embodiments; 0.5 g/10 minutes
or greater in other embodiments; and 0.75 g/10 minutes or greater in yet other embodiments.
[0051] Propylene-based polymers may have a Melt Flow Rate ("MFR") determined according to
ASTM D1238 at 230°C (446°F) with a 2.16 kg (4.75 lb.) weight of 85 g/10 minutes or
less in some embodiments; 70 g/10 minutes or less in other embodiments; 60 g/10 minutes
or less in other embodiments; and 50 g/10 minutes or less in yet other embodiments.
In other embodiments, propylene-based polymers may have a melt flow rate (MFR) of
0.25 g/10 minutes or greater; 0.7 g/10 minutes or greater in other embodiments; 1.4
g/10 minutes or greater in other embodiments; and 2 g/10 minutes or greater in yet
other embodiments.
[0052] Ethylene-based polymers may have a density of 0.845 g/cc or greater in some embodiments;
0.85 g/cc or greater in other embodiments; 0.855 g/cc or greater in other embodiments;
and 0.86 g/cc or greater in yet other embodiments. In other embodiments, ethylene-based
polymers may have a density of 0.97 g/cc or less; 0.96 g/cc or less in other embodiments;
0.955 g/cc or less in other embodiments; and 0.95 g/cc or less in yet other embodiments.
[0053] Propylene-based polymers may comprise 5 percent by weight comonomer or greater in
some embodiments. In other embodiments, propylene-based polymers may comprise 7 percent
by weight comonomer or greater. In other embodiments, propylene-based polymers may
contain 35 percent or less comonomer by weight; 25 percent or less comonomer by weight
in yet other embodiments.
[0054] One class of thermoplastic polymers useful in various embodiments are copolymers
of ethylene and 1-octene or 1-butene, where the ethylene copolymer contains 90 weight
percent or less ethylene; 85 weight percent or less ethylene in other embodiments;
50 weight percent or greater ethylene in other embodiments; and 55 weight percent
or greater ethylene in yet other embodiments. The ethylene copolymer may contain 1-octene
or 1-butene from 10 weight percent or greater in some embodiments; 15 weight percent
or greater in other embodiments; 50 weight percent or less in other embodiments; and
45 weight percent or less in yet other embodiments. Each of the above weight percentages
are based on the weight of the copolymer. In various embodiments, the ethylene copolymers
may have a Melt Index of 0.25 g/10 minutes or greater; 0.5 g/10 minutes or greater
in other embodiments; 30 g/10 minutes or less in other embodiments; and 20 g/10 minutes
or less in yet other embodiments.
[0055] Other polymers useful in embodiments may include copolymers of propylene and ethylene,
1-octene, 1-hexene or 1-butene, where the propylene copolymer contains from 95 weight
percent or less propylene; 93 weight percent or less in other embodiments; 65 weight
percent or greater in other embodiments; and 75 weight percent or greater in yet other
embodiments. The propylene copolymer may contain one or more comonomers, such as ethylene,
1-octene, 1-hexene or 1-butene, from 5 weight percent or greater in some embodiments;
7 weight percent or greater in other embodiments; 35 weight percent or less in other
embodiments; and 25 weight percent or less in yet other embodiments. In various embodiments,
the propylene copolymers may have a Melt Flow Rate of 0.7 g/10 minutes or greater;
1.4 g/10 minutes or greater in other embodiments; 85 g/10 minutes or less in other
embodiments; and 55 g/10 minutes or less in yet other embodiments.
[0056] Alternatively, instead of a single polymer, a blend of polymers may be employed that
has the physical characteristics described herein. For example, it may be desirable
to blend a first polymer with relatively high MI or MFR that is outside the range
described, with another of relatively low MI or MFR, so that the combined MI or MFR
and the averaged density of the blend fall within the described ranges. A more crystalline
alpha-olefin polymer may be combined with one of relatively lower crystallinity, such
as one having a significant amount of long chain branching, to provide a blend that
has substantially equivalent processing capability in preparing froths and foams described
herein. Where reference is made to a "polymer" in this specification, it is understood
that blends of olefin polymers with equivalent physical characteristics may be employed
with like effect and are considered to fall within our description of the various
embodiments.
[0057] In certain embodiments, the thermoplastic resin may be an ethylene-octene copolymer
or interpolymer having a density between 0.857 and 0.911 g/cc and melt index (190°C
with 2.16 kg weight) from 0.1 to 100 g/10 min. In other embodiments, the ethylene-octene
copolymers may have a density between 0.863 and 0.902 g/cc and melt index (190°C with
2.16 kg weight) from 0.8 to 35 g/10 min. The ethylene-octene copolymer or interpolymer
may incorporate 20-45 percent octene by weight of ethylene and octene.
[0058] In certain embodiments, the thermoplastic resin may be a propylene-ethylene copolymer
or interpolymer having an ethylene content between 5 and 20% by weight and a melt
flow rate (230°C with 2.16 kg weight) from 0.5 to 300 g/10 min. In other embodiments,
the propylene-ethylene copolymer or interpolymer may have an ethylene content between
9 and 12 percent by weight and a melt flow rate (230°C with 2.16 kg weight) from 1
to 100 g/10 min.
[0059] In certain other embodiments, the thermoplastic resin may be a low density polyethylene
having a density between 0.911 and 0.925 g/cc and melt index (190°C with 2.16 kg weight)
from 0.1 to 100 g/10 min.
[0060] In some embodiments, the thermoplastic resin may have a crystallinity of less than
50 percent. In other embodiments, the crystallinity of the resin may be from 5 to
35 percent. In yet other embodiments, the crystallinity may range from 7 to 20 percent.
[0061] In some embodiments, the thermoplastic resin is a semi-crystalline polymer and may
have a melting point of less than 110°C. In other embodiments, the melting point may
be from 25 to 100°C. In yet other embodiments, the melting point may be between 40
and 85°C.
[0062] In some embodiments, the thermoplastic resin is a glassy polymer and may have a glass
transition temperature of less than 110°C. In other embodiments, the glass transition
temperature may be from 20 to 100°C. In yet other embodiments, the glass transition
temperature may be from 50 to 75°C.
[0063] In certain embodiments, the thermoplastic resin may have a weight average molecular
weight greater than 10,000 g/mole. In other embodiments, the weight average molecular
weight may be from 20,000 to 150,000 g/mole; in yet other embodiments, from 50,000
to 100,000 g/mole.
[0064] The one or more thermoplastic resins may be contained within the aqueous dispersions
described herein in an amount from 1 percent by weight to 96 percent by weight polymer
solids. For instance, the thermoplastic resin may be present in the aqueous dispersion
in an amount from 10 percent by weight to 60 percent by weight in one embodiment,
and 20 percent to 50 percent by weight in another embodiment.
[0066] One embodiment of a polyurethane dispersion may include water and polyurethane and/or
a mixture capable of forming polyurethane, such as a polyurethane prepolymer, for
example. The polyurethane dispersion may also include one or more additives such as
surfactants, wetting agents, and viscosity modifiers. Polyurethane forming materials
may include, for example, polyurethane prepolymers that retain some minor isocyanate
reactivity for some period of time after being dispersed. Also, the terms polyurethane
prepolymer and polyurethane may encompass other types of structures such as, for example,
urea groups.
[0067] Polyurethanes useful in embodiments disclosed herein may include polyurethanes manufactured
from prepolymers based on any organic polyisocyanates, modified polyisocyanates, isocyanate
based prepolymers, and mixtures thereof. These may include aliphatic and cycloaliphatic
isocyanates, including multifunctional aromatic isocyanates such as 2,4- and 2,6-toluenediisocyanate
and the corresponding isomeric mixtures; 4,4'-, 2,4'- and 2,2'-diphenyl-methanediisocyanate
(MDI) and the corresponding isomeric mixtures; mixtures of 4,4'-, 2,4'- and 2,2'-diphenylmethanediisocyanates
and polyphenyl polyethylene polyisocyanates (PMDI); and mixtures of PMDI and toluene
diisocyanates.
[0068] In some embodiments, polyurethane polymers useful in embodiments of the composite
structure may be prepared by bringing and reacting together an aqueous phase with
an isocyanate-terminated prepolymer. The resulting polymer may have a foam or gel
structure. Suitable prepolymers are described in, for example
WO2004074343 (A1) and
WO2005097862 (A1)
[0069] In some embodiments, the prepolymer may be the reaction product of a polyether polyol
with a stoichiometric excess of an isocyanate mixture. The isocyanate mixture may
include methylene diphenylisocyanate, toluene diisocyanate, hexamethylene diisocyanate,
isophorone diisoayanate, polymethylene polyphenylisocyanate, carbodiimide or allophonate
or uretonimine adducts of methylene diphenylisocyanate and mixtures thereof. Isocyanates
used to make up the balance of the composition may include polymethylene polyphenylisocyanate,
carbodiimide or allophonate or uretonimine adducts of methylene diphenylisocyanate.
[0070] Prepolymer formulations in some embodiments may include a polyol component. Active
hydrogen containing compounds used in polyurethane production may include compounds
having at least two hydroxyl groups or amine groups. Those compounds are referred
to herein as polyols. Representatives of suitable polyols are generally known and
are described in such publications as
High Polymers, Vol. XVI, "Polyurethanes, Chemistry and Technology" by Saunders and
Frisch, Interscience Publishers, New York, Vol. I, pp. 32-42, 44-54 (1962) and
Vol. II, pp. 5-6, 198-199 (1964);
Organic Polymer Chemistry by K. J. Saunders, Chapman and Hall, London, pp. 323-325
(1973); and
Developments in Polyurethane, Vol. I, J. M. Burst, ed., Applied Science Publishers,
pp. 1-76 (1978). However, any active hydrogen containing compound may be used. Examples of such
materials include those selected from the following classes of compositions, alone
or in admixture: (a) alkylene oxide adducts of polyhydroxyalkanes; (b) alkylene oxide
adducts of non-reducing sugars and sugar derivatives; (c) alkylene oxide adducts of
phosphorus and polyphosphorus acids; and (d) alkylene oxide adducts of polyphenols.
Polyols of these types are referred to herein as "base polyols." Examples of alkylene
oxide adducts of polyhydroxyalkanes useful herein are adducts of ethylene glycol,
propylene glycol, 1,3-dihydroxypropane, 1,4-dihydroxybutane, and 1,6-dihydroxyhexane,
glycerol, 1,2,4-trihydroxybutane, 1,2,6-dihydroxyhexane, 1,1,1-trimethylolethane,
1,1,1-trimethylolpropane, pentaerythritol, polycaprolactone, xylitol, arabitol, sorbitol,
mannitol. Other useful alkylene oxide adducts include adducts of ethylene diamine,
glycerin, piperazine, water, ammonia, 1,2,3,4-tetrahydroxy butane, fructose, sucrose.
Also useful are poly(oxypropylene) glycols, triols, tetrols and hexols and any of
these that are capped with ethylene oxide. These polyols also include poly(oxypropyleneoxyethylene)polyols.
The oxyethylene content may comprise less than 80 weight percent of the total polyol
weight in some embodiments, and less than 40 weight percent in other embodiments.
The ethylene oxide, when used, may be incorporated in any way along the polymer chain,
for example, as internal blocks, terminal blocks, randomly distributed blocks, or
any combination thereof.
[0071] Polyester polyols may also be used to prepare the polyurethane dispersions. Polyester
polyols are generally characterized by repeating ester units which may be aromatic
or aliphatic and by the presence of terminal primary or secondary hydroxyl groups,
but any polyester terminating in at least two active hydrogen groups may be used.
For example, the reaction product of the transesterification of glycols with poly(ethylene
terephthalate) may be used to prepare polyurethanes disclosed herein.
[0072] The polyisocyanate components of the formulations disclosed herein may be prepared
using any organic polyisocyanates, modified polyisocyanates, isocyanate based prepolymers,
and mixtures thereof. These may include aliphatic and cycloaliphatic isocyanates,
including multifunctional aromatic isocyanates such as 2,4- and 2,6-toluenediisocyanate
and the corresponding isomeric mixtures; 4,4'-, 2,4'- and 2,2'-diphenyl-methanediisocyanate
(MDI) and the corresponding isomeric mixtures; mixtures of 4,4'-, 2,4'- and 2,2'-diphenylmethanediisocyanates
and polyphenyl polymethylene polyisocyanates (PMDI); and mixtures of PMDI and toluene
diisocyanates.
[0073] The aqueous non-ionic hydrophilic polyurethane dispersions may include the reaction
product of a non-ionic hydrophilic prepolymer, water, optionally an external surfactant,
and optionally a chain-extending reagent. The hydrophilic prepolymer may include the
reaction product of a first component and a second component. The first component
may include aromatic polyisocyanate, an aliphatic polyisocyanate, and combinations
thereof. The second component may include hydrophilic alkylene oxide polyol, a non-ionic
hydrophilic alkylene oxide monol, or a mixture of hydrophilic and hydrophobic alkylene
oxide polyols or monols or combinations thereof. The aqueous non-ionic hydrophilic
polyurethane dispersion may optionally include one or more surfactants.
[0075] Other Substrate Components
[0076] In some embodiments, substrates may be formed from or may include other polymeric
and non-polymeric components, including natural or synthetic materials. Other components
may include, for example, polyolefins, such as, polyethylene, polypropylene, polybutylene,
and the like; polyesters, such as polyethylene terephthalate, poly(glycolic acid)
(PGA), poly(lactic acid) (PLA), poly(β-malic acid) (PMLA), poly(ε-caprolactone) (PCL),
poly(p-dioxanone) (PDS), poly(3-hydroxybutyrate) (PHB), and the like; polyamides,
such as nylons (nylon-6, nylon-6,6, nylon-6,12, and others); polyaramids, such as
KEVLAR®, NOMEX®, and the like, TEFLON®, and polyester nylons (EP); cellulosic esters;
cellulosic ethers; cellulosic nitrates; cellulosic acetates; cellulosic acetate butyrates;
ethyl cellulose; regenerated cellulose, such as viscose, rayon, and the like; cotton;
flax; silk; hemp; and mixtures thereof. In other embodiments, substrates may include
polymers such as ethylene-vinyl acetate (EVA), ethylene/ vinyl alcohol copolymers,
polystyrene, impact modified polystyrene, ABS, styrene/butadiene block copolymers
and hydrogenated derivatives thereof (SBS and SEBS), and thermoplastic polyurethanes.
Suitable polyolefins may include linear or low density polyethylene, polypropylene
(including atactic, isotactic, syndiotactic and impact modified versions thereof)
and poly (4-methyl-1-pentene). Suitable styrenic polymers may include polystyrene,
rubber modified polystyrene (HIPS), styrene/acrylonitrile copolymers (SAN), rubber
modified SAN (ABS or AES) and styrene maleic anhydride copolymers.
[0077] In other embodiments, substrates may be formed from or may include any natural or
synthetic pulp or cellulosic fibers including, but not limited to, nonwoody fibers,
such as cotton, abaca, kenaf, sabai grass, flax, esparto grass, straw, jute hemp,
bagasse, milkweed floss fibers, and pineapple leaf fibers; and woody fibers such as
those obtained from deciduous and coniferous trees, including softwood fibers, such
as northern and southern softwood kraft fibers; hardwood fibers, such as eucalyptus,
maple, birch, and aspen. Woody fibers may be prepared in high-yield or low-yield forms
and can be pulped in any known method, including kraft, sulfite, high-yield pulping
methods and other known pulping methods. Pulp and fibers prepared from organosolv
pulping methods may also be used, including the fibers and methods disclosed in
U.S. Patent No. 4,793,898, issued Dec. 27, 1988 to Laamanen et al.;
U.S. Patent No. 4,594,130, issued June 10, 1986 to Chang et al.; and
U.S. Patent No. 3,585,104. Useful pulp and fibers may also be produced by anthraquinone pulping, exemplified
by
U.S. Patent No. 5,595,628 issued Jan. 21, 1997, to Gordon et al. Other examples of useful cellulose-based compositions useful in the present invention
include those disclosed in
U.S. Patent Nos. 6,837,970,
6,824,650,
6,863,940 and in U.S. Patent Application Nos.
US20050192402 and
20040149412 .
[0078] Cellulose-based compositions and polymers may also be used, including methylcellulose
(
i.e. METHOCEL), hydroxyethyl cellulose (HEC) (
i.e. CELLOSIZE), ethylcellulose (
i.e. ETHOCEL), cationic HEC, and other cellulose derivatives. Polyoxyethylene (such as
POLYOX) may also be used in some embodiments. Each of the above indicated trademarked
products is available from The Dow Chemical Company, Midland, MI. Other cellulose-based
compositions and polymers may also include hydroxypropylmethyl cellulose, hydroxypropyl
cellulose, hydroxypropylmethyl cellulose phthalate, hydroxypropylmethyl cellulose
acetate succinate, carboxymethylethyl cellulose, cellulose acetate phthalate, polyvinylacetal
diethylaminoacetate, aminoalkyl methacrylate copolymer, hydroxypropylmethyl cellulose
acetate succinate, methacrylic acid copolymers including methacrylic acid - methyl
methacrylate copolymers, cellulose acetate trimellitate (CAT), polyvinyl acetate phthalate,
shellac, carboxymethyl cellulose, calcium carboxymethyl cellulose, sodium carboxymethyl
cellulose, croscarmellose sodium A-type (Ac-di-sol), starch, crystalline cellulose,
hydroxypropyl starch, partly pregelatinized starch, polyvinylpyrrolidone, gelatin,
gum arabic, ethyl cellulose, polyvinyl alcohol, pullulan, pregelatinized starch, agar,
tragacanth, sodium alginate, propyleneglycol alginate, cellulose derivatives, starch
derivatives, pectins, polyacrylates, polyvinyl acetate phthalate, oxidized regenerated
cellulose, polyacrylates, modified starches (including water-soluble polymers derived
from a starch (e.g., corn starch, potato starch, tapioca starch) such as by acetylation,
halogenation, hydrolysis (e.g., such as which an acid), or enzymatic action, or any
type of water-soluble modified starch, including but not limited to oxidized, ethoxyolated,
cationic, lypophilic and pearl starch, may be used), polyvinyl alcohol, polyethylene
glycols, natural and synthetic gums like guar gum, xanthan gum, cellulose gum, acacia
gum, polycarbophil, polyolefin oxides such as polyethylene oxide, locust bean gum,
bentonite, scheroglucan, polyacrylic acids such as carbopol, polycarbophil, poly(methyl
vinyl ether-co-methacrylic acid), poly(2-hydroxyethyl methacrylate), poly(methylmethacrylate),
poly(isobutylcyanoacrylate), poly(isohexycyanoacrylate) and polydimethylaminoethyl
methacrylate, hydrolytically unstable polyesters containing derivatizable groups,
alginate, carrageenan, guar gum derivatives, karaya gum, dextran, hyaluronic acid,
pullulan, amylose, high amylose starch, hydroxypropylated high amylose starch, dextrin,
pectin, chitin, chitosan, levan, elsinan, collagen, gelatin, zein, gluten, soy protein
isolate, polysaccharides, whey protein isolate, and casein. In other embodiments combinations
of the above described compositions may be used.
[0079] Those having ordinary skill in the art will recognize that the above lists are a
non-comprehensive listing of suitable polymers. It will be appreciated that the scope
of the present disclosure is restricted by the claims only.
[0080] Dispersion Stabilizing Agent
[0081] Embodiments of the present disclosure use a stabilizing agent to promote the formation
of a stable dispersion or emulsion. In selected embodiments, the stabilizing agent
may be a surfactant, a polymer (different from the thermoplastic polymers detailed
above), or mixtures thereof In other embodiments, the thermoplastic resin may be a
self-stabilizer, so that an additional exogenous stabilizing agent may not be necessary.
For example, a self-stabilizing system may include a partially hydrolyzed polyester,
where by combining polyester with an aqueous base, a polyester resin and surfactant-like
stabilizer molecule may be produced. In particular, the dispersion stabilizing agent
may be used as a dispersant, a surfactant for frothing the dispersion, or may serve
both purposes. In addition, one or more stabilizing agents may be used in combination.
[0082] In certain embodiments, the dispersion stabilizing agents used for the polyolefin
and polyurethane dispersions herein may be a polar polymer, having a polar group as
either a comonomer or grafted monomer. In preferred embodiments, the dispersion stabilizing
agent may include one or more polar polyolefins, having a polar group as either a
comonomer or grafted monomer. Typical polymers include ethylene-acrylic acid (EAA)
and ethylene-methacrylic acid copolymers, such as those available under the trademarks
PRIMACOR™ (trademark of The Dow Chemical Company), NUCREL™ (trademark of E.I. DuPont
de Nemours), and ESCOR™ (trademark of ExxonMobil) and described in
U.S. Patent Nos. 4,599,392,
4,988,781, and
5,938,437. Other suitable polymers include ethylene ethyl acrylate (EEA), ethylene methyl methacrylate
(EMMA), and ethylene butyl acrylate (EBA) copolymers. Other ethylene-carboxylic acid
copolymer may also be used. Those having ordinary skill in the art will recognize
that a number of other useful polymers may also be used.
[0083] If the polar group of the polymer is acidic or basic in nature, the dispersion stabilizing
polymer may be partially or fully neutralized with a neutralizing agent to form the
corresponding salt. The salts may be alkali metal or ammonium salts of the fatty acid,
prepared by neutralization of the acid with the corresponding base, e.g., NaOH, KOH,
and NH
4OH. These salts may be formed in situ in the dispersion step, as described more fully
below. In certain embodiments, neutralization of the dispersion stabilizing agent,
such as a long chain fatty acid or EAA, may be from 25 to 200% on a molar basis; from
50 to 110% on a molar basis in other embodiments. For example, for EAA, the neutralizing
agent is a base, such as ammonium hydroxide or potassium hydroxide, for example. Other
neutralizing agents may include lithium hydroxide or sodium hydroxide, for example.
Those having ordinary skill in the art will appreciate that the selection of an appropriate
neutralizing agent depends on the specific composition formulated, and that such a
choice is within the knowledge of those of ordinary skill in the art.
[0084] Other dispersion stabilizing agents that may be used in the polyolefin and polyurethane
dispersions may include long chain fatty acids or fatty acid salts having from 12
to 60 carbon atoms. In other embodiments, the long chain fatty acid or fatty acid
salt may have from 12 to 40 carbon atoms.
[0085] Additional dispersion stabilizing agents include cationic surfactants, anionic surfactants,
or non-ionic surfactants. Examples of anionic surfactants include sulfonates, carboxylates,
and phosphates. Examples of cationic surfactants include quaternary amines. Examples
of non-ionic surfactants include block copolymers containing ethylene oxide, propylene
oxide, butylene oxide, and silicone surfactants. Surfactants useful as a dispersion
stabilizing agent may be either external surfactants or internal surfactants. External
surfactants are surfactants that do not become chemically reacted into the polymer
during dispersion preparation. Examples of external surfactants useful herein include
salts of dodecyl benzene sulfonic acid and lauryl sulfonic acid salt. Internal surfactants
are surfactants that do become chemically reacted into the polymer during dispersion
preparation. An example of an internal surfactant useful herein includes 2,2-dimethylol
propionic acid and its salts or sulfonated polyols neutralized with ammonium chloride.
A surfactant may be included in formulations disclosed herein in an amount ranging
from 0.01 to 8 parts per 100 parts by weight of polyurethane component.
[0086] In particular embodiments, the dispersing agent or stabilizing agent may be used
in an amount ranging from greater than zero to 60% by weight based on the amount of
thermoplastic resin (or thermoplastic resin mixture) used. With respect to the thermoplastic
resin and the dispersion stabilizing agent, in some embodiments, the thermoplastic
resin may comprise between 30% to 99% (by weight) of the total amount of polymer and
dispersion stabilizing agent in the composition. In other embodiments, the thermoplastic
resin may comprise between 50% and 80% (by weight) of the total amount of polymer
and dispersion stabilizing agent in the composition. In yet other embodiments, the
thermoplastic resins may comprise about 70% (by weight) of the total amount of polymer
and dispersion stabilizing agent in the composition. For example, long chain fatty
acids or salts thereof may be used from 0.5 to 10% by weight based on the amount of
thermoplastic resin. In other embodiments, ethylene-acrylic acid or ethylene-methacrylic
acid copolymers may be used in an amount from 0.5 to 60% by weight based on the amount
of the thermoplastic resin. In yet other embodiments, sulfonic acid salts may be used
in an amount from 0.5 to 10% by weight based on the amount of thermoplastic resin,
[0087] Currently most commercially available polyurethane dispersions contain DMPA (depot
medroxyprogesterone acetate) as an internal surfactant and can be utilized in this
invention. In contrast, a family of polyurethane dispersions which does not contain
DMPA, rather incorporating non-ionic modifiers based on ethylene oxide as internal
surfactants are equally suitable and may provide other technical and commercial advantages.
See for example
U.S. Patent No. 6,271,276.
[0088] As discussed above, more than one dispersion stabilizing agent may be used, and combinations
may be used as a dispersion stabilizing agent and as a frothing surfactant, for example.
One of ordinary skill in the an will recognize that the dispersants used to create
a relatively stable aqueous dispersion may vary depending on the nature of the thermoplastic
resin employed.
[0089] Dispersion Formulations
[0090] Dispersion formulations in accordance with embodiments disclosed herein may include
a liquid medium, such as water, a thermoplastic resin, a dispersion stabilizing agent,
and optionally frothing surfactants, additives, and fillers. In some embodiments,
the aqueous dispersions may include polyolefin and/or polyurethane resin particles
ranging in size from 0.02 to 10 µm (microns) from 0.05 to 5 µm (microns) in another
embodiment; and from 0.1 to 2 µm (microns) in yet other embodiments.
[0091] The thermoplastic resin and the dispersion stabilizing agent may be dispersed in
a liquid medium, which in some embodiments is water. In some embodiments, sufficient
base is added to neutralize the resultant dispersion to achieve a solution having
a pH in the range from 6 to 14. In particular embodiments, sufficient base is added
to maintain a pH between 9 to 12. Water content of the dispersion may be controlled
so that the combined content of the thermoplastic resin and the dispersion stabilizing
agent (solids content) may be between 1% to 74% (by volume). In another embodiment,
the solids content may range between 25% to 74% (by volume). In yet another embodiment,
the solid content may range between 30% to 50% (without filler, by weight). In yet
another embodiment, the solids content may range from 40% to 55% (without filler,
by weight).
[0092] Dispersions formed in accordance with some embodiments may be characterized in having
an average particle size of between 0.02 to 5.0 µm (microns) In other embodiments,
dispersions may have an average particle size from 0.04 to 2.0 µm (microns) "Average
particle size" as used herein refers to the volume-mean particle size. In order to
measure the particle size, laser-diffraction techniques may be employed for example.
A particle size in this description refers to the diameter of the polymer in the dispersion.
For polymer particles that are not spherical, the diameter of the particle is the
average of the long and short axes of the particle. Particle sizes can be measured
on a Beckman-Coulter LS230 laser-diffraction particle size analyzer or other suitable
device.
[0093] In a specific embodiment, a thermoplastic resin and a stabilizing agent may be melt-kneaded
in an extruder along with water and a neutralizing agent, such as ammonia, potassium
hydroxide, or a combination of the two, to form a dispersion. Those having ordinary
skill in the art will recognize that a number of other neutralizing agents may be
used. In some embodiments, filler may be added before, during, or after blending the
thermoplastic resin and stabilizing agent.
[0094] Any melt-kneading means known in the art may be used. In some embodiments, a kneader,
a BANBURY® mixer, single-screw extruder, or a multiscrew extruder is used. A process
for producing the dispersions in accordance with the present disclosure is not particularly
limited. Processes for melt-kneading the above-mentioned components are disclosed
in
U.S. Patent No. 5,756,659 and
U.S. Patent Publication No. 20010011118, for example.
[0095] Figure 2 schematically illustrates an extrusion apparatus that may be used in embodiments
of the disclosure. An extruder 20, in certain embodiments a twin screw extruder, is
coupled to a back pressure regulator, melt pump, or gear pump 30. Embodiments also
provide a base reservoir 40 and an initial water reservoir 50, each of which includes
a pump (not shown). Desired amounts of base and initial water are provided from the
base reservoir 40 and the initial water reservoir 50, respectively. Any suitable pump
may be used, but in some embodiments a pump that provides a flow of about 150 cc/min
at a pressure of 240 bar is used to provide the base and the initial water to the
extruder 20. In other embodiments, a liquid injection pump provides a flow of 300
cc/min at 200 bar or 600 cc/min at 133 bar. In some embodiments, the base and initial
water are preheated in a preheater.
[0096] Generally, any method known to one skilled in the art of preparing thermoplastic
polymer (polyolefin and polyurethane) dispersions may be used. A suitable storage-stable
polyurethane dispersion as defined herein is any polyurethane dispersions having a
mean particle size of less than 5 µm (microns) Polyurethane dispersions that are not
storage-stable may have a mean particle size of greater than 5 microns. For example,
a suitable dispersion may be prepared by mixing a polyurethane prepolymer with water
and dispersing the prepolymer in the water using a mixer. Alternatively, a suitable
dispersion may be prepared by feeding a prepolymer into a static mixing device along
with water, and dispersing the water and prepolymer in the static mixer. Continuous
methods for preparing aqueous dispersions of polyurethane are known and may be used
in embodiments disclosed herein, For example,
U.S. Patent Nos. 4,857,565,
4,742,095,
4,879,322,
3,437,624,
5,037,864,
5,221,710,
4,237,264, and
4,092,286 all describe continuous processes useful for preparing polyurethane dispersions.
In addition, a polyurethane dispersion having a high internal phase ratio can be prepared
by a continuous process such as is . described in
U.S. Patent No. 5,539,021.
[0097] Other types of aqueous polymer dispersions may be used in combination with the polyolefin
and polyurethane dispersions useful in embodiments disclosed herein. Suitable dispersions
useful for blending with polyurethane dispersions include: styrene-butadiene dispersions;
styrene-butadiene-vinylidene chloride dispersions; styrene-alkyl acrylate dispersions;
ethylene vinyl acetate dispersions; polychloropropylene latexes; polyethylene copolymer
latexes; ethylene styrene copolymer latexes; polyvinyl chloride latexes; or acrylic
dispersions, like compounds, and mixtures thereof.
[0098] In producing embodiments of the polyurethane dispersions, the surfactants may be
added to the polyurethane dispersion along with antioxidants, bactericides, etc.,
when viscosity is low and good mixing may be obtained. The dispersion stabilizing
agent may then be added followed by any inorganic filler, slowly enough to ensure
good dispersion and avoid clumping/lumping of the filler. Finally the thickener may
be added to obtain the desired viscosity. It is believed that the addition of ammonium
stearate after the filler and thickener addition avoids swelling of the polyurethane
dispersion particle, resulting in a lower viscosity during mixing.
[0099] Frothing Surfactants
[0100] Surfactants useful for preparing froths are referred to herein as frothing surfactants.
A frothing surfactant allows the gas, commonly air, used in frothing to disperse homogenously
and efficiently into the formulated foamed dispersion. Preferably, the frothing surfactant
produces a non-sudsing composite foam product after drying.
[0101] Embodiments of the present disclosure may use a frothing surfactant to promote the
formation of a stable dispersion and to aid in frothing. Creating and stabilizing
the froth during the frothing and drying steps may be accomplished by addition of
a froth stabilizing surfactant to the aqueous dispersion of the polyolefin resin when
initially creating the froth. In addition, these surfactants may also be used to improve
aqueous wetting of dried foams, if desired. Suitable frothing surfactants may be selected
from cationic, nonionic and anionic surfactants: In some embodiments, frothing surfactants
may include the stabilizing agents as described above.
[0102] In some embodiments, the frothing surfactant may be an alkylcellulose ethers, hydroxyalkyl
cellulose ethers, hydroxyalkyl alkylcellulose ethers, guar gum, xanthan gum, and polyoxyethylene
resins of at least 20,000 molecular weight, or combinations thereof. Other suitable
frothing surfactants may be selected from cationic surfactants, anionic surfactants,
or non-ionic surfactants. Examples of cationic surfactants include quaternary amines,
primary amine salts, diamine salts, and ethoxylated amines. Examples of non-ionic
surfactants include block copolymers containing ethylene oxide, silicone surfactants,
alkylphenol ethoxylates, and linear and secondary alcohol ethoxylates of alkyl group
containing more than 8 carbon atoms.
[0103] Examples of cationic surfactants include quaternary amines, primary amine salts,
diamine salts, and ethoxylated amines. Examples of non-ionic surfactants include block
copolymers containing ethylene oxide, silicone surfactants, alkylphenol ethoxylates,
and linear and secondary alcohol ethoxylates of alkyl group containing more than 8
carbon atoms.
[0104] Examples of anionic surfactants include sulfonates, carboxylates, and phosphates.
In one embodiment, anionic surfactants useful in preparing the froth from the aqueous
dispersion may be selected from carboxylic acid salts and ester amides of carboxylic
fatty acids, preferably fatty acids comprising from 12-36 carbon atoms, e.g., stearic
or lauric acid, palmitic, myristic, oleic, linoleic, ricinoleic, erucic acid and the
like.
[0105] In some embodiments, the surfactant may include amphoteric surfactants such as aminopropionates,
amphoteric sulfonates, betaines, imidazoline based amphoterics, and sultaines, among
others. For example, the surfactant may be derived from an imidazoline and can either
be the acetate form (containing salt) or the propionate form (salt-free). Examples
of suitable amphoteric surfactants include surfactants such as lauramidopropyl betaine,
sodium laurimino dipropionate, cocoamidopropyl hydroxyl sultaine, alkylether hydroxypropyl
sultaine, sodium capryloampho hydroxypropyl sulfonate, disodium capryloampho dipropionate,
sodium cocoamphoacetate, disodium cocoamphodiacetate, sodium cocoamphopropionate,
disodium octyl iminodipropionate, sodium cocoampho hydroxypropyl sulfonate, disodium
lauryl iminodipropionate, sodium stearoampho acetate, and disodium tallow iminodipropionate,
among others. Other amphoteric surfactants known in the art may also be used.
[0106] In one embodiment, when a good "hand" or fabric-like feel is desired in the finished
foam, a saturated fatty acid derivative (e.g., the salt of stearic or palmitic acid)
may be used. Other suitable anionic surfactants include alkylbenzene sulfonates, secondary
n-alkane sulfonates, alpha-olefin sulfonates, dialkyl diphenylene oxide sulfonates,
sulfosuccinate esters, isothionates, linear alkyl (alcohol) sulfates and linear alcohol
ether sulfates. It is understood that the froth stabilizing surfactants may or may
not be different than those used to prepare the dispersion. These surfactants serve
both to assist in froth formation and help to stabilize the froth. In a particular
embodiment, the surfactant may be selected from at least one of alkali metal, mono-,
di- and tri-alkanol amine (mono-, di- or triethanol amine, for example), and ammonium
salts of lauryl sulfate, dodecylbenzene sulfates, alcohol ethoxy sulfates, and isothionates,
the dibasic salt of N-octyldecylsulfosuccinimate, and mixtures thereof. In other embodiments,
the froth stabilizing agent may include cellulose.
[0107] In some embodiments, the frothing surfactant may be used in an amount such that the
resulting froth, as described below, may contain from 0.01 to 10.0 weight percent
frothing surfactant based on the dry weight of the thermoplastic polymer. In other
embodiments, the froth may contain from 0.02 to 3.0 weight percent frothing surfactant
based on the dry weight of the thermoplastic polymer; from 0.03 to 2.5 weight percent
based on the dry weight of the thermoplastic polymer in other embodiments; and from
0.05 to 10.0 weight percent based on the dry weight of the thermoplastic polymer in
yet other embodiments. In various other embodiments, the frothing surfactant may be
present in the froth in an amount ranging from a lower bound of 0.01, 0.02, 0.03,
0.04, or 0.05 weight percent based on the dry weight of the thermoplastic polymer
to an upper bound of 2.0, 2.5, 3.0, 4.0, 5.0, or 10.0 weight percent based on the
dry weight of the thermoplastic polymer, in any combination of given upper and lower
bounds.
[0108] In addition to the above listed surfactants, other surfactants may be used which
do not detrimentally affect the frothing or stability of the froth. In particular
additional anionic, zwitterionic, or nonionic surfactants may be used in combination
with the above listed surfactants.
[0110] The polymers, dispersions, froths, and foams disclosed herein may optionally contain
fillers in amounts, depending on the application for which they are designed, ranging
from 2-100 percent (dry basis) of the weight of the thermoplastic resin. These optional
ingredients may include, for example, calcium carbonate, titanium dioxide powder,
polymer particles, hollow glass spheres, fibrillated fibers, polymeric fibers such
as polyolefin based staple monofilaments and the like. Foams designed for use in the
absorbent articles may contain bulk liquid-absorbing material, such as short cotton
fiber or other cellulose fiber evenly distributed throughout the polymer foam.
[0111] Additives may be used with the thermoplastic polymers, dispersion stabilizing agents,
frothing surfactants, or fillers without deviating from the scope of the present disclosure.
For example, additives may include a wetting agent, surfactants, antistatic agents,
antifoam agent, anti block, wax-dispersion pigments, a neutralizing agent, a thickener,
a compatibilizer, a brightener, a rheology modifier, a biocide, a fungicide, and other
additives known to those skilled in the art.
[0112] Additives and adjuvants may be included in any formulation comprising the thermoplastic
polymers. Suitable additives include fillers, such as organic or inorganic particles,
including clays, talc, titanium dioxide, zeolites, powdered metals, organic or inorganic
fibers, including carbon fibers, silicon nitride fibers, steel wire or mesh, and nylon
or polyester cording, nano-sized particles, clays, and so forth; tackifiers, oil extenders,
including paraffinic or napthelenic oils; and other natural and synthetic polymers,
including other polymers according to embodiments of the invention.
[0113] The compositions disclosed herein may contain processing oils, plasticizers, and
processing aids (collectively referred to as processing oils). Processing oils having
a certain ASTM designation and paraffinic, napthenic or aromatic process oils are
all suitable for use. In some embodiments, from 0 to 150 parts processing oils per
100 parts of total polymer may be employed; from 0 to 100 parts in other embodiments;
and from 0 to 50 parts of oil per 100 parts of total polymer are employed in yet other
embodiments. Higher amounts of processing oil may tend to improve the processing of
the resulting product at the expense of some physical properties. Additional processing
aids include conventional waxes, fatty acid salts, such as calcium stearate or zinc
stearate, (poly)alcohols including glycols, (poly)alcohol ethers, including glycol
ethers, (poly)esters, including (poly)glycol esters, and metal salts, especially Group
1 or 2 metal salts or zinc salt derivatives thereof.
[0114] Compositions, including thermoplastic blends, may also contain anti-ozonants or anti-oxidants.
The anti-ozonants may be physical protectants such as waxy materials that come to
the surface and protect the thermoplastic from oxygen or ozone or they may be chemical
protectors that react with oxygen or ozone. Suitable chemical protectors include styrenated
phenols, butylated octylated phenol, butylated di(dimethylbenzyl) phenol, p-phenylenediamines,
butylated reaction products of p-cresol and dicyclopentadiene (DCPD), polyphenolic
anitioxidants, hydroquinone derivatives, quinoline, diphenylene antioxidants, thioester
antioxidants, and blends thereof. Some representative trade names of such products
are WINGSTAY™ S antioxidant, POLYSTAY™ 100 antioxidant, POLYSTAY™ 100 AZ antioxidant,
POLYSTAY™ 200 antioxidant, WINGSTAY™ L antioxidant, WINGSTAY™ LHLS antioxidant, WINGSTAY™
K antioxidant, WINGSTAY™ 29 antioxidant, WINGSTAY™ SN-1 antioxidant, and IRGANOX™
antioxidants. In some applications, the anti-oxidants and anti-ozonants used will
preferably be non-staining and non-migratory.
[0115] For providing additional stability against UV radiation, hindered amine light stabilizers
(HALS) and UV absorbers may be also used. Suitable examples include TINUVIN™ 123,
TINUVIN™ 144, TINUVIN™ 622, TINUVIN™ 765, TINUVIN™ 770, and TINUVIN™ 780, available
from Ciba Specialty Chemicals, and CHEMISORB™ T944, available from Cytex Plastics,
Houston TX, USA. A Lewis acid may be additionally included with a HALS compound in
order to achieve superior surface quality, as disclosed in
U.S. Patent No. 6,051,681.
[0116] For some compositions, additional mixing processes may be employed to predisperse
the anti-oxidants, anti-ozonants, carbon black, UV absorbers, and/or light stabilizers
to form a masterbatch, and subsequently to form polymer blends there from.
[0117] Suitable crosslinking agents (also referred to as curing or vulcanizing agents) for
use herein include sulfur based, peroxide based, or phenolic based compounds. Examples
of the foregoing materials are found in the art, including in
U.S. Patents No.: 3,758,643,
3,806,558,
5,051,478, 4,104,210,
4,130,535,
4,202,801,
4,271,049,
4,340,684,
4,250,273,
4,927,882,
4,311,628 and
5,248,729.
[0118] Other prepolymers may also include a chain extender or crosslinker. A chain extender
may be used to build the molecular weight of the polyurethane prepolymer by reaction
of the chain extender with the isocyanate functionality in the polyurethane prepolymer,
that is, chain extend the polyurethane prepolymer. A suitable chain extender or crosslinker
is typically a low equivalent weight active hydrogen containing compound having 2
or more active hydrogen groups per molecule. Chain extenders typically have 2 or more
active hydrogen groups while crosslinkers have 3 or more active hydrogen groups. The
active hydrogen groups may be hydroxyl, mercaptyl, or amino groups. An amine chain
extender may be blocked, encapsulated, or otherwise rendered less reactive. Other
materials, particularly water, may function to extend chain length and, therefore,
may be chain extenders.
[0119] Polyamines chain extenders may be selected prom amine terminated polyethers such
as, for example, JEFFAMINE® D-400 from Huntsman Chemical Company, aminoethyl piperazine,
2-methyl piperazine, 1,5-diamino-3-methylpentane, isophorone diamine, ethylene diamine,
diethylene triamine, aminoethyl ethanolamine, triethylene tetraamine, triethylene
pentaamine, ethanol amine, lysine in any of its stereoisomeric forms and salts thereof,
hexane diamine, hydrazine and piperazine. In some embodiments, the chain extender
may be used as an aqueous solution.
[0120] In the formation of polyurethane dispersions, a chain extender may be employed in
an amount sufficient to react with from zero to 100 percent of the isocyanate functionality
present in the prepolyxner, based on one equivalent of isocyanate reacting with one
equivalent of chain extender. It may be desirable to allow water to act as a chain
extender and react with some or all of the isocyanate functionality present. A catalyst
may optionally be used to promote the reaction between a chain extender and an isocyanate.
When chain extenders have more than two active hydrogen groups, they may also concurrently
function as crosslinkers.
[0121] Thermoplastic compositions according to embodiments of the invention may also contain
organic or inorganic fillers or other additives such as starch, talc, calcium carbonate,
glass fibers, polymeric fibers (including nylon, rayon, cotton, polyester, and polyaramide),
metal fibers, flakes or particles, expandable layered silicates, phosphates or carbonates,
such as clays, mica, silica, alumina, aluminosilicates or aluminophosphates, carbon
whiskers, carbon fibers, nanoparticles including nanotubes, wollastonite, graphite,
zeolites, and ceramics, such as silicon carbide, silicon nitride or titania. Silane
based or other coupling agents may also be employed for better filler bonding.
[0122] Examples of conventional fillers include milled glass, calcium carbonate, aluminum
trihydrate, talc, bentonite, antimony trioxide, kaolin, fly ash, or other known fillers.
A suitable filler loading, in a polyurethane dispersion for example, may be from 0
to 200 parts of filler per 100 parts of dispersion solids (pphds). Fillers may be
loaded in an amount of less than 100 pphds in some embodiments, and less than 80 pphds
in other embodiments. Addition of inorganic fillers may enhance the production of
the foam composite by faster drying speeds on the production line because the percentage
of water to be removed on drying is lower.
[0123] Optionally a filler wetting agent may be used. A filler wetting agent may improve
the compatibility of the filler and the polyolefin or polyurethane dispersions. Useful
wetting agents include phosphate salts such as sodium hexametaphosphate. A filler
wetting agent may be included at a concentration of at least 0.5 pphds.
[0124] Thickeners may be useful to increase the viscosity of polyurethane and polyolefin
dispersions. For example, suitable thickeners include ALCOGUM
™ VEP-II (a trade designation of Alco Chemical Corporation) and PARAGUM
™ 241 (a trade designation of Para-Chem Southern, Inc.). Other suitable thickeners
may include cellulose derivatives such as METHOCEL
™ products (a trade designation of The Dow Chemical Company). Thickeners may be used
in any amount necessary to prepare a dispersion of desired viscosity.
[0125] Thickening agents may be used when it is desired to control the viscosity of the
aqueous phase and facilitate the transportation and distribution of, for example,
fillers or fibers. Fillers may include clays, diatomaceous earth, calcium carbonate,
and mineral fibers such as wallastonite; aqueous, latexes such as for example a styrene-butadiene.
Thickening agents may include natural products such as xanthan gums, or chemical agents
such as polyacrylamide polymers and gels. Other additives include mixing aids and
emulsifiers.
[0126] The aqueous phase may also be used to introduce to other substances, such as fatty
oils and functional additives, besides fibers and fillers when desiring to modify
physical properties of the resulting polymer. Also present may be fragrances or perfumes
or other such substances that can be detected by scent should this be required for
the end application. If the end application requires a polymer that has some physiological
active properties, the aqueous phase can also be used to introduce active molecules
such as for example, pesticides, insecticides, herbicides, attractants, pheromones,
growth promoting or regulating substances or plant or animal nutrients. If the resulting
polymer is to be used in end applications where electrical or luminescent properties
are required, the aqueous mixture may be used to introduce electrolytes so as to render
the polymer electro-conductive, or fluorescent or phosphorescent additives so as to
render the polymer luminescent. While generally such additional substances are introduced
via the aqueous phase, the isocyanate-terminated prepolymer can also be utilized in
the same manner when no adverse reactions or process conditions prevail.
[0127] While optional for purposes of the present invention, some components can be highly
advantageous for product stability and durability during and after the manufacturing
process. For example, inclusion of antioxidants, biocides, and preservatives may be
highly advantageous in some embodiments.
[0129] For preparing froths from the above described dispersions, a gaseous frothing agent
is generally used. Examples of suitable frothing agents include: gases and/or mixtures
of gases such as, for example, air, carbon dioxide, nitrogen, argon, helium. Frothing
agents are typically introduced by introduction of a gas above atmospheric pressure
into a dispersion to form a homogeneous froth by mechanical shear forces during a
predetermined residence time. In preparing froths, all components of the dispersion
may be mixed and then the gas may be blended into the mixture, using equipment such
as an OAKES
™, COWIE & RIDING
™, or FIRESTONE® frother.
[0130] Froths may be prepared from the dispersion/surfactant/optional additives mixtures
by using a mechanical method such as a high shear, mechanical mixing process under
atmospheric conditions to entrain air or other gases in the aqueous phase of the dispersion
or optionally injecting gas into the system while mixing. The amount of air or other
gas (where a gas in addition to or other than air is desirable) that may be incorporated
in the froth may comprise at least 80% by volume in one embodiment, at least 85% by
volume in another embodiment, and at least 90% by volume of the resultant froth in
yet another embodiment. Initially, all components to be used in making the froth may
be mixed together with mild agitation to avoid entrapping air.
[0131] Once all of the ingredients are well mixed, the mixture may be exposed to high shear
mechanical mixing. During this step, the bulk viscosity of the mixture may increase
as more air is entrapped within the continuous aqueous phase until a non-flowable,
stiff froth is formed. The mixing time necessary to obtain a froth with the desired
density may vary with amount and type of froth stabilizing surfactant and the amount
of mechanical shear. Any mechanical mixing device capable of whipping air into a thickened
aqueous dispersion, such as a kitchen blender/hand mixer, Hobart mixer fitted with
a wire whip, or, on a larger scale, a COWIE-RIDING
™ Twin Foamer (Cowie Riding Ltd.) may be used. The commercial foamers may also allow
one to inject air into their high shear mixing head to obtain very low (less than
50 g/L) density froth.
[0132] Froth density may be measured, for example, by drawing off samples of the froth in
cups of predetermined volume and weight, weighing the froth-filled cup, and then calculating
the density of the sample. In commercial frothers, air can be added directly into
the mixing head to assist in development of low density froth. The speed of the frothing
device may be increased or decreased to attain a desired froth density. In one embodiment,
the froth density may be in a range of 0.04 to 0.15 g/cc, and from 0.07 to 0.10 g/cc
in another embodiment. In other embodiments, the froth density may be in from 0.05
g/cc to 0.09 g/cc. Once a desired density of the froth is obtained, the froth may
be optionally spread on a substrate prior to conversion of the froth into foam.
[0133] Frothed foams comprising the polymers may also be formed as disclosed in PCT Application
PCT/US2004/027593, filed August 25, 2004, and published as
WO2005/021622. In other embodiments, the polymers may also be crosslinked, preferably after forming
the foam, by any known means, such as the use of peroxide, electron beam, silane,
azide, gamma irradiation, ultraviolet radiation, or other crosslinking techniques.
The polymers may also be chemically modified, such as by grafting (for example by
use of maleic anhydride (MAH), silanes, or other grafting agent), halogenation, amination,
sulfonation, or other chemical modification.
[0134] Drying and Recovery Steps
[0135] In one embodiment, the foam may be prepared from the froth by removing at least a
portion of the liquid/aqueous element of the froth prepared as disclosed herein. In
other embodiments, the foam may be prepared from the froth by removing at least a
majority of the liquid/aqueous element of the froth. In yet other embodiments, the
foam may be prepared by removing substantially all of the liquid/aqueous element.
In various embodiments, greater than 30 weight percent, greater than 50 weight percent,
greater than 80 weight percent, greater than 90 weight percent, greater than 95 weight
percent, greater than 98 weight percent, or greater than 99 weight percent of the
liquid/aqueous element may be removed. The means by which the liquid portion is removed
may be selected to minimize the amount of froth volume collapse. In one embodiment,
the froths may be dried and converted to foams by heating in a forced air drying oven,
at temperatures selected for optimum drying. In one embodiment, the froth may be heated
to a temperature between 60°C and 120°C.
[0136] As the nature of the thermoplastic resin permits, processing may be conducted at
the highest temperature feasible to remove water as rapidly as possible from the froth
without destroying the viscosity of the polyolefin resin particles on the surface
of the bubbles of the froth or causing significant (e.g., more than 75-80 volume percent)
collapse of the partially dried froth. In another embodiment, the drying temperature
may be selected so as to not exceed, the melting point temperature of the thermoplastic
fibers. In one embodiment, it may be desirable to dry the froth at a temperature that
approaches, but does not exceed the melting range of the thermoplastic resin. In another
embodiment, it may be desirable to attain a temperature where the amorphous regions
in the thermoplastic resin begin to coalesce while pseudo-crosslinking with the fibers
and avoid or at least minimize collapse of the froth before the foam has become fully
"dried" in its ultimate form and dimension and at least 95 weight percent of the water
in the froth has been driven out. The resulting "dried" foam may has a density of
0.03 to 0.07 g/cc ; and from about 0.03 to 0.05 g/ce in other embodiments. In other
embodiments, the foams may have a density within the range of 0.03 g/cc to 0.06 g/cc.
[0137] Some embodiments of the dried foam may have an average thickness ranging from 0.5
mm to 300 mm or more; from 1 mm to 6 mm in other embodiments; and from 0.01 cm to
2.5 cm in yet other embodiments. Other embodiments of the dried foam may have an average
thickness ranging from 0.05 cm to 2.0 cm; and from 1 to 1.5 cm in yet other embodiments.
Articles comprising embodiments of the dried foam may include at least one layer of
foam having an average thickness ranging from 0.1 cm to 2.5 cm; from 0.5 cm to 2.0
cm in other embodiments; and from 1.0 cm to 1.5 cm in yet other embodiments. In some
embodiments, two or more foams may be laminated together; in various embodiments,
the two or more foams may have the same or different densities, the same or different
cell sizes, or the same or different structures (fibrillated, open-celled, closed-celled,
etc.). Open-cell foams have interconnected pores or cells, whereas closed-cell foams
do not have interconnected pores or cells. In other embodiments, one or more foams
may be laminated to a substrate, such as film.
[0138] Drying of the froth to form the desired foam of the disclosure may be conducted in
batch or continuous mode. Devices including, for example, conventional forced air
drying ovens or banks of infrared heating lamps or dielectric heating devices, e.g.,
radio (typically operated at permitted frequency bands in the range between 1-100
MHz) and microwave (typically operated at permitted frequency bands in the range between
400 to 2500 MHz) frequency energy generating sources, lining a tunnel or chamber in
which the froth may be placed or conveyed through, in a continuous fashion, may be
employed for drying. A combination of such drying energy sources may be used, either
simultaneously or sequentially applied, to dry a froth to form a foam. In one embodiment,
the drying includes the simultaneous use of a dielectric device and a forced air drying
oven. For foam having a thickness of 0.25 to 0.6 cm, the drying may be achieved as
quickly as 45 to 90 seconds when the forced air oven is operated at approximately
75°C and a radio frequency generator heats the froth to an internal temperature of
45 to 50°C. The temperature of the drying operation may be selected according to the
nature and the melting range of the polyolefin resin (as determined by DSC) employed
to prepare the foam. The dielectric heating frequency bands, permitted for industrial
use in various countries, are designated in greater detail in the reference "Foundations
of Industrial Applications of Microware and Radio Frequency Fields," Rousy, G and
Pierce, J. A. (1995).
[0139] In one embodiment, the absorbent structure (the foam) may have a non-cellular, fibrillated
morphology. As used herein, a "non-cellular, fibrillated structure" refers to a foam
having an open, random, non-cellular, morphology composed of or having fibrils or
thread-like filaments. The non-cellular, fibrillated structure, for example, may be
non-uniform and non-repeating, such as where the fibrils form a non-woven fibrous-like
web and where a majority of the struts are not interconnected.
[0140] In other embodiments, the foams disclosed herein may be open-cell foams, wherein
the cell size of the majority of cells of the foam ranges between 5 and 1000 micrometers.
In other embodiments, the foam may be characterized by having a majority of its cells
being substantially ellipsoidal in shape.
[0141] The foams described herein may adhere to a substrate. In some embodiments, the adhesive
force between the foam and the substrate may be 17.5 N/m (0.1 lb
f/in) or greater. In other embodiments, the adhesive force between the foam and the
substrate may be 26.3N/m (0.15 lb
f/in) or greater; and 32N/m (0.2 lb
f/in) or greater in yet other embodiments.
[0143] Substrates that may be used in embodiments of the composite structures disclosed
herein may include non-wovens, elastic non-wovens, and soft non-wovens. Non-woven
textiles are those that are neither woven nor knit. Non-wovcns are typically manufactured
by putting small fibers together in the form of a sheet or web, and then binding them
mechanically, with an adhesive, or thermally. In other embodiments, substrates may
include fabrics or other textiles, porous films, and other non-wovens, including coated
substrates. In certain embodiments, the substrate may be a soft textile, such as a
soft or elastic non-woven, such as an elastomeric polyolefin or a polyurethane, for
example. Wovens and/or knits made from microdenier fibers may also provided the desired
substrate performance.
[0144] In some embodiments, the non-wovens may be based on polyolefin monocomponent fibers,
such as polyethylene. In other embodiments, bicomponent fibers may be used, for example
where the core is based on a polypropylene and the sheath may be based on polyethylene.
It should be understood that the fibers used in embodiments of the composite structure
may be continuous or non-continuous, such as staple fibers.
[0145] One example of a suitable soft non-woven is described in
WO20051111282A1, disclosing a non-woven material having a fuzz/abrasion resistance of less than 0.5
mg/cm2, and a flexural rigidity of less than or equal to 0.043 * Basis Weight - 0.657
mN-cm. The non-woven material may have a basis weight greater than 15 grams/m
2, a machine direction (MD) tensile strength of more than 25 N/5cm in MD (at a basis
weight of 20 grams/m
2), and a consolidation area of less than 25%. In other embodiments, a spun-bond non-woven
fabric may be made using fibers having a diameter in a range of from 0.1 to 50 denier.
[0146] An additional specific example of a suitable soft non-woven is described in
WO2005111291A1, disclosing a non-woven material having a fuzz/abrasion resistance of less than 0.7
mg/cm2 and a flexural rigidity of less than 0.15 mN.cm. The non-woven material may
have a basis weight greater than 15 grams/m
2, a tensile strength of more than 10 N/5cm MD and 7 N/5cm cross direction (CD) (at
a basis weight of 20 GSM), and a consolidation area of less than 25%. In other embodiments,
a fiber from 0,1 to 50 denier may be formed from a polymer blend, wherein the polymer
blend includes a) from 40 weight percent to 80 weight percent by weight of the polymer
blend of a first polymer which is a homogeneous ethylenela/α-olefin interpolymer having:
1) a melt index of from 1 to 1000 grams/10 minutes, and 2) a density of from 0.87
to 0.95 grams/cc, and b) from 60 to 20 percent by weight of a second polymer which
may be an ethylene homopolymer or an ethylene/a-olefin interpolymer having: 1) a melt
index of from 1 to 1000 grams/10 minutes, and 2) a density which is at least 0.01
grams/cc greater than the density of the first polymer. Homogeneous ethylene/α-olefin
polymers are those having a composition distribution breadth index (CDBI) of at least
70% in some embodiments, at least 80% in other embodiments, and as high as 100% in
yet other embodiments. CDBI is defined herein as described in
U.S. Patent No, 5,246,783 and
WO 93/04486, using the apparatus described in
U.S, Patent No. 5,008,204.
[0147] Additionally, a web having similar physical properties to those described above may
also be utilized. The web structure may be formed from individual fibers, filaments,
or threads which are interlaid, but not in an identifiable manner. Non-woven fabrics
or webs have been formed from many processes such as melt blowing, spun-bonding, electrospun,
and bonded carded web processes. The basis weight of the non-wovens ranges from 15
to 250 g/m
2 in some embodiments; 20 to 250 g/m
2 in other embodiments .
[0148] In some embodiments, elastic non-wovens, such as described in
U.S. Patent No 6,994,763 may be used. The elastic non-woven may be based on bicomponent fibers, where the
core component may an elastomeric polymer and the sheath component may a polyolefin.
Representative examples of commercially available elastomers for the core component
of the bicomponent fiber may include the following polymers: KRATON® Polymers, ENGAGE
™ polymers, VERSIFY
™ elastomers, INFUSE
™ olefin block copolymers, VISTAMAXX
™ polyolefin elastomers, VECTOR
™ polymers, polyurethane elastomeric materials ("TPU"), and heterophasic block copolymers.
Representative materials for the sheath component may include polyolefin based homo-
and co- polymers. The polyolefin polymers may include polypropylene homopolymer, polypropylene
random copolymers, polypropylene impact copolymers, and polyethylenes. In some embodiments,
the polyethylenes may have a density ranging from 0.925g/cm
3 to 0.965g/cm
3.
[0149] In other embodiments, suitable elastic non-wovens may be formed from one or more
"elastomeric" polymers. The term "elastomeric" generally refers to polymers that,
when subjected to an elongation, deform or stretch within their elastic limit. For
example, spun-bonded fabrics formed from elastomeric filaments typically have a root
mean square average recoverable elongation of at least 75% based on machine direction
and cross direction recoverable elongation values of the fabric after 30% elongation
of the fabric and one pull. Advantageously, spun-bonded fabrics formed from elastomeric
filaments typically have a root mean square average recoverable elongation of at least
65% based on machine direction and cross direction recoverable elongation values of
the fabric after 50% elongation of the fabric and one pull.
[0150] In some embodiments, substrates include non-woven fibrous webs. In other embodiments,
the above mentioned substrates may be coated with the above mentioned polyolefin and
polyurethane dispersions to form polyolefin- or polyurethane-coated substrates useful
in embodiments of the composite structures disclosed herein.
[0151] In other embodiments, apertured films may be utilized as a layer(s) of the composite
structures or laminates described herein. Use of apertured films may increase the
strength of the structure. Additionally the apertured films may provide a suitable
feel for applications not requiring contact with the face or other sensitive skin.
[0152] Descriptions of apertured films may be found in
WO200080341A1 and
U.S. Patent Nos. 3,929,135 and
4,324,246. Apertured films may include thin polymeric films with small openings space uniformly
across the width of the film. Apertured films are commonly used for use in body contacting
absorbent and non-absorbent articles such as baby diapers, adult incontinent articles,
sanitary napkins or panty liners, facial wipes, body wipes, articles of clothing,
hospital bed sheets and the like.
[0153] In other embodiments, the composite structures described herein may include substrates
coated with the polyurethane dispersions and/or polyolefin dispersions, such as described
above, or similar coatings for increased durability of the substrate and improved
softness.
[0154] Non-woven substrates used in the composite structures may include mono- and bi- component
fibers having a basis weight ranging from 15 to 2509 g/m
2 in some embodiments; 20 to 250 g/m
2 in other embodiments; and a basis weight ranging from 25 to 60 g/m
2 in other embodiments. Basis weight may be determined by measuring the weight of a
known area of fabric. For example, basis weight may be determined according to ASTM
D 3776.
[0155] In other embodiments, the composite structures described herein may be formed from
a substrate having an abrasion loss of less than 0.7 mg/cm
2; less than 0.6 mg/cm
2 in other embodiments; and less than 0.5 mg/cm
2 in yet other embodiments. Abrasion loss, or the amount of fuzz generated during abrasion,
may be measured by the rub test. The rub test is performed by rubbing sandpaper of
a defined grit across the surface of the sample with a controlled force. The sample
is weighed before and after the test and weight loss is measured to determine the
amount of fuzz formed and removed from the surface by the sandpaper.
[0157] Composite structures formed from one or more of the above described substrates, including
foam and fabric substrates may have a balance of softness, weight, and other properties
which may include bending rigidity, coefficient of friction, fuzz resistance, loft,
volume, and others.
[0158] Composite structures include at least one substrate layer and at least one open-cell
foam layer. The substrate includes non-wovens, fabrics, and the like. Incorporation
of open-cell foams with a substrate (e.g., non-wovens, fabrics, etc.) into wipes or
other articles may impart additional softness, loft, and volume to the article. The
additional loft and volume may be achieved while enhancing and/or maintaining the
desired, pre-existing surface feel, of the substrate alone. The incorporation of the
open-cell foam may also increase the available void volume and/or surface area for
the inclusion and delivery of active agents when compared to the fabric or non-woven
layer alone.
[0159] In other embodiments, composite structures may include an open-cell foam layer, a
substrate layer, and optionally at least one cleaning surfactant, active agent, or
enhancing filler. Embodiments of the composite structure may exhibit a desired combination
of performance properties, including high softness and high loft, and/or excellent
resistance to surface abrasion. The soft, high loft composite structure may be useful
for disposable and semi-disposable applications related to personal care, medical,
shipping and household markets. The composite structure may also be capable of delivering
wet active agents or dry active agents requiring wetting for cleansing, polishing
or medical applications.
[0160] In other embodiments, the composite structure may include an impervious substrate
layer. For example, a thermoplastic film or thermoplastic impregnated paper layer
may provide a barrier between layers of the composite structure. Impervious substrate
layers may be advantageously used where one side of the structure is used for delivering
wet or dry active agents, and where a second side is to remain free of the wet or
dry active agents. For example,
EP0951228 discloses use of an impervious layer in a pad having handles that may be used for
application of fingernail polish remover (acetone) while limiting skin contact with
the polish remover. Impervious layers may also be advantageously used where the formation
of a wet/dry wipe is desired.
[0161] The composite structures disclosed herein may be used for cleaning wipes for skin
contact, and may include wet and/or dry active agents. The composite structures disclosed
herein may also be used for other applications including baby wipes, hand wipes, hard
surface cleaners for home use, and industrial cleaning wipes.
[0162] Enhanced softness or a more cloth-like feel are also desirable for applications beyond
skin cleansing wipes. These applications may include, but are not limited to, applicator
pads, polishing cloths, medical cleansing, shipping/packaging material for sensitive
components, and an application pad for topical medicines. Additionally these articles
may be used as a means for the temporary storage of measured amounts liquid materials.
[0163] The above foams and/or coatings (dispersions and/or froths) may be used in combination
with the substrates (foams and/or fabrics) also defined above. The following process/technologies
may be used in the manufacture of these various combinations. Methods described below
are typical and detailed descriptions of the techniques can be found in standard texts.
[0164] In one embodiment, a substrate (foams and/or fabrics) may be contacted with a fluid,
such as an active compound described below, to form a composite structure. The resulting
composite structure may have desired properties, such as basis weight, rigidity, coefficient
of friction, and fuzz resistance.
[0165] In some embodiments, the composite structures may be formed by extrusion coating.
The froth, such as a polyolefin froth may be extruded directly onto the desired substrate.
A second substrate may be applied to the top of the froth or foam. Layers may be repeated
as necessary. The sandwiched composite may then be heated to dry the foam and to adhere
the layers together.
[0166] In other embodiments, the composite structures may be formed by roll coating (doctor
blade). The wet foam or froth may be applied to a continuous belt of substrate using
a doctor blade a fixed height above the substrate. Wet foam continuously fed to one
side of the blade creates a constant pool of material. The moving substrate below
the blade pulls from this pool of material with the thickness of the resultant coating
to be fixed by the blade height. Additional layers of substrate or foam may be added
as required. The resultant structure may then be dried to remove moisture and to aid
in adhesion.
[0167] In other embodiments, the composite structures may be formed by adhesive lamination.
The dried foam may be adhesively laminated onto the desired substrate
[0168] In other embodiments, the composite structures may be formed by spray coating. The
froth or wet foam may be sprayed onto desired substrate and subsequently dried.
[0169] In other embodiments, the composite structures may be formed by curtain coating.
Wet foam or froth may be applied via direct deposition onto a moving belt or substrate.
The coating thickness is controlled by the froth or wet foam feed rate and the speed
of the substrate below coating curtain.
[0170] In other embodiments, the composite structures may be formed by batch application.
The froth or wet foam may be manually applied to a substrate surface. The surface
may then be leveled using a knife blade and metering bars of desired thickness. The
knife moves across the metering bars removing wet foam from the surface creating a
uniform height.
[0171] In other embodiments, it may be desirable to form an article having two or more foam
layers. In some embodiments, the foam layers may be of the same or different density.
In other embodiments the two or more foam layers may be laminated.
[0172] Additional processing techniques may include thermoforming; embossing, hydroentaglement,
air lacing, exposure to infrared heat, and addition of surface fibers, such as flocking
techniques.
[0173] The resulting composite structures may have one or more desired physical properties.
In some embodiments, the resulting composite structures may have an advantageous combination
of the desired physical properties.
[0174] The composite structure is formed from substrates having a basis weight of 15 to
250 g/m
2. In other embodiments, the composite structure may be formed from substrates having
a basis weight of 20 to 250 g/m
2; from 20 to 80 g/m
2; and from 25 to 50 g/m
2 in yet other embodiments. Basis weight may be determined by measuring the weight
of a known area of fabric, where the area is no smaller than 50 mm
2. For example, basis weight may be determined according to ASTM D 3776.
[0175] In some embodiments, composite structures may be formed by incorporating a liquid,
such as an active, with a foam substrate. In other embodiments, composite structures
may include one or more foam layers. Foams and foam substrates may have a thickness
of from 0.5 to 300 mm in some embodiments, and from 1 to 6 mm in yet other embodiments.
Polyolefin foams and foam substrates may have a density from 0.025 to 0.1 g/cc in
some embodiments, and from 0.03 to 0.06 g/cc in other embodiments. Polyurethane foams
and foam substrates may have a density from 0.025 g/cc to 0.5 g/cc in some embodiments,
and from 0.05 to 0.1 g/cc in other embodiments. Foam density may be measured by weighing
a dried foam sample of known dimensions (volume).
[0176] In some embodiments, the composite structures may have a Kawabata Evaluation System
(KES) coefficient of friction ranging from 0.1 to 1.0 MIU. In other embodiments, the
composite structures may have a KES coefficient of friction ranging from 0.3 to 1.0
MIU; from 0.4 to 0.9 MIU in other embodiments; and from 0.5 to 0.8 MIU in yet other
embodiments. The composite structure may have a KES surface roughness, in either the
machine direction or the cross direction, of less than 4.0 µm (microns) in some embodiments.
In other embodiments, the composite structure may have a KES surface roughness of
less than 3.5 µm (microns); less than 3.25 µm (microns) in other embodiments; and
less than 3.0 µm (microns) in yet other embodiments. Surface properties (resistance
/ drag / friction) and surface contour (roughness) values are as determined using
a KES-FB4 surface tester, where a tension load of 20 gf/cm is applied to the sample.
MIU is a measure of the coefficient of friction on a scale of 0 to 1, where a higher
MIU value corresponds to a greater friction or resistance and drag. Regarding KES
surface roughness, measured in microns, a higher value corresponds to a geometrically
rougher surface.
[0177] In some embodiments, the composite structures may have Kawabata Evaluation System
(KES) compression resilience from 30% to 50%. In other embodiments, the composite
structures may have a KES compression resilience ranging from 35% to 45%; and from
37% to 43% in yet other embodiments. KES compression resilience is as determined using
a KES-FB3 compression tester, measured by applying a varied load from 0-10 gf/cm
2 to a 2 cm
2 area of the samples. Compression resilience is the percent recovery of the material
thickness after the applied load is removed. Higher compression resilience numbers
are favorable and indicate a greater percent recovery after being compressed.
[0178] The composite structures may have a bending (flexural) rigidity of less than 1000
mN·cm in some embodiments, for both the cross direction and machine direction. In
other embodiments, the composite structures may have a bending rigidity of less than
900 mN·cm; less than 800 mN·cm in other embodiments; and less than 700 mN·cm in yet
other embodiments. Bending rigidity is a measure of the energy required to bend the
fabric to a 41.5° decline, where the energy is given per unit fabric width. To measure
bending rigidity, the substrate sample is cut into a piece of 25.4 mm by 152.4 mm
and is set onto a raised platform allowing a 41.5° angle below the horizontal of the
platform to be formed. The sample is then moved forward at a constant rate off the
platform until the unsupported end of the sample flexes to contact the 41.5° angle.
The bending length is one half the measured sample overhang length. Additionally,
the sample basis weight is calculated as outlined above. The bending rigidity is calculated
by G = m x C
3 10
-3 (mN-cm), where m is the basis weight of the sample (g/m
2) and C is the bending length of the sample in cm. The acceleration due to gravity
(9.81 m/s
2) has been rounded to 10 m/s
2 in determining this equation. The bending rigidity of the non-woven fabric was also
measured in both the longitudinal direction and the transverse direction.
[0179] In some embodiments, the composite structures may have a machine direction tensile
strength of greater than 10 N/5cm; greater than 12 N/5cm in other embodiments; and
greater than 15 N/5cm in yet other embodiments. Tensile strength of a fabric may be
measured, for example, using test method DIN53354. Tensile strength is measured by
cutting the fabric into a piece 5 cm by 10 cm, where the long edge is in the machine
direction, holding the fabric in the chucks of a tensile tester and measuring for
tensile strength at a pull rate of 100 mm/min.
[0180] In some embodiments, the composite structures may have a cross direction tensile
strength of greater than 10 N/5cm; greater than 12 N/5cm in other embodiments; and
greater than 15 N/5cm in yet other embodiments. Tensile strength of a fabric may be
measured, for example, using test method DIN53354. Tensile strength is measured by
cutting the fabric into a piece 5 cm by 10 cm, where the long edge is in the cross
direction, holding the fabric in the chucks of a tensile tester and measuring for
tensile strength at a pull rate of 100 mm/min.
[0181] In some embodiments, the composite structure may have a good fuzz resistance. The
composite may have a Rub Test fuzz generation of 0.7 mg/cm
2 or less in some embodiments, 0.6 mg/cm
2 in other embodiments; and 0.5 mg/cm
2 in yet other embodiments. The rub test fuzz generation is a weight measure of fibers
per unit area removed from a sample after abrasion with a rough surface. To determine
fuzz generation, an 11 cm by 4 cm sample is weighed, placed into a Sutherland Ink
Rub Tester. A piece of 320 grit sandpaper of suitable size is adhered to a 2 pound
weighted holder within the tester. The weighted holder is then placed onto the specimen,
and the rub tester is then started with a speed of 42 cycles per minute. The tester
is then run for a total of 20 cycles. The weighted holder is then removed from the
sample. Any loose fibers remaining on the specimen surface are removed with gentle
application and removal of adhesive tape. The weight of the sample after abrasion
is then recorded. The fuzz generation value is calculated as the weight loss of the
sample per unit area of the sample. Lower fuzz generation values are considered desirable.
[0182] In some embodiments, the composite structure may have a good "hand" quality. The
composite structure may have a "hand" value, normalized for sample volume, of 25 gf/cm
3 or less in some embodiments; 14 gf/cm
3 or less in other embodiments; 13 gf/cm
3 or less in other embodiments; and 11 gf/cm
3 or less in yet other embodiments. Additionally, the composite structures may have
a "hand" quality, normalized for sample weight, of 220 gf/g or less in some embodiments;
160 gf/g or less in other embodiments; 158 gf/g or less in other embodiments; and
118 gf/g or less in yet other embodiments. The "hand" quality is considered to be
the combination of resistance due to surface friction, flexibility, and compressibility
of a fabric material. As described in INDA 1
st 90.3 (95), a Handle-O-Meter tester (manufactured by Thwing-Albert Instrument Co.,
West Berlin, NJ) measures the above factors using a Linear Variable Differential Transformer
(LVDT) to detect the resistance that a blade encounters when forcing a specimen of
material into a slot of parallel edges. A 3/2 digital voltmeter (DVM) indicates the
resistance directly in grams. Samples of the composites were cut into three 50cm
2 circle specimens and were conditioned at 50% relative humidity and 21.1 °C (70°F)
prior to testing. The Handle-O-Meter slot width was set at 20 mm. Measurements were
taken in each of four positions per specimen as required by the instrument manufacturer's
test manual, and the four measurements were summed to give the total hand for a single
specimen in grams-force, with the total hand being averaged for the three specimens.
This averaged hand was then normalized to the specimen weight and volume.
[0183] In some embodiments, the composite structure may have a balance of softness and strength.
For example, a composite structure formed by contacting a fluid, such as an active,
with a foam or fabric substrate may have a dry basis weight of 25 to 150 g/m
2, a flexural rigidity of less than 1000 mN·cm, and a coefficient of friction within
the range from 0.4 to 0.9 MIU. In other embodiments, the composite structure may also
have a Rub Test fuzz level of 0.7 mg/cm
2 or less. And in other embodiments, the composite structure may also have a surface
roughness of less than 3.5 SMD. In yet other embodiments, the composite structure
may also have a hand of less then 25 gf/cm
3
[0184] Where the composite structure includes two or more layers, the layers may be adhered
together with or without adhesives In some embodiments, the adhesion of a first layer
to an adjoining second layer may be 17.5 cm N/m (0.1 lb
f/in) or greater. In other embodiments, the adhesive strength may be 26.3 N/m (lb
f/in) or greater; 32 N/m (0.2 lb
f/in) or greater in yet other embodiments. Adhesive strength, or laminate peel strength,
is a measure of the energy required to separate the layers per unit area. Adhesive
strength is the average load per unit width of bond line required to part bonded materials,
where the angle of separation is 180 degrees and separation rate is 6 in/min (ASTM
D-903).
[0186] The composite structures described using the above foam technologies, substrates
and application techniques may also include wet or dry active agents for increased
performance within specific end use applications. Active agents for direct or post
introduction may include: additives for cleaning, such as surfactants, enhancing fillers
(such as exfoliates for abrasion or skin peeling additives), alcohols or oils; wellness
additives such as oils moisturizing agents; additives for skin cleaning like make-up
removing oils; additives which help to recover stressed skin, like zinc salts, camomile,
marigold, aloe vera, vitamins and minerals; skin care actives, such as proteins (hydrolized
collagen, elastin, keratin, soy, corn, wheat, oats, silk, and synthetic peptides,
for example), botanicals (green tea, grape seed, and the like), polysaccharides (such
as hyaluronic acid, phycopolysaccharides, b-1, 3-glucans, chitosan), and enzymes (bromelain,
papain, superoxide dismutase, subtilisin). Additional active agents may include moisture/odor
absorbing compounds such as silica gel, activated carbon, zeolites, etc.
[0187] These active agents, such as surfactants, emollients, soaps, inorganics, moisturizers,
fragrance, cleaner, antimicrobial, vitamins and fillers may be introduced into the
structure via multiple mechanisms. Incorporation of actives may be achieved using
some or all of the techniques described below.
[0188] In other embodiments, the active agent may be added to a polyolefin dispersion prior
to frothing. In other embodiments, the active agent may be added to the composite
structure, either to the surface of the foam or into the pores of the foam, via post-treatment
or standard coating techniques. In other embodiments, the active agent may be added
to a non-woven substrate using standard coating techniques. In yet other embodiments,
the active agent may be added as an additional layer or a pocket within the composite
structure.
[0191] A first substrate layer of DREAMEX® (a polyethylene copolymer based elastic non-woven
having a basis weight of 50 g/m
2, available from Corovin GmbH Corporation, Germany) is placed on silicone release
paper. A template measuring 200 mm x 400 mm x 3.0 mm is then placed on the substrate.
[0192] A froth formed from an AFFINITY
™ based dispersion is prepared by the following procedure. An aqueous dispersion of
a polyolefm plastomer is formed in accordance with the procedures as described in
W02005021638. The dispersion is formed using AFFINITY
™ EG 8200 (an ethylene-alpha olefin copolymer having an MI2 of about 5 dg/min, and
a density of about 0.87 g/cc). The dispersion surfactant system includes UNICID® 350
(a linear carboxylic acid available from Baker Petrolite), HYSTRENE® 4516 (a fatty
acid available from Crompton Corp., Greenwich, Connecticut), and METHOCEL® (a water-soluble
methylcellulose and hydroxypropyl methylcellulose polymer available from The Dow Chemical
Company), used at a loading of 2 weight percent, 1 weight percent, and 0.35 weight
percent, respectively, based on the combined weight of the ethylene copolymer and
the surfactant system. The aqueous dispersion produced has a solids content of approximately
53 weight percent: To produce a foam, the above described dispersion is then mixed
with 1 weight percent sodium lauryl sulfate (STEPANOL® WAT-K, available from Stepan
Co.), based on polymer solids.
[0193] Approximately 160 grams of the aqueous dispersion is added to a mixing bowl. The
dispersion is mixed using a Hobart bench top mixer on high setting for 3 minutes,
targeting a froth density of 0.06g/cc. The froth is then spread evenly over the template
and substrate using a spatula, and the template removed. A second substrate layer
of DREAMEX
™ is then placed on top of the just applied froth. The composite structure is then
placed in an oven at 75°C for 25-30 minutes or until surface temperature reaches 70-75°C.
The sample is then cooled to room temperature and cut into 50 cm
2 sample disks using a circular die.
[0195] The procedures of Example 1 are repeated with a 200 mm x 400 mm x 4.4 mm template.
[0197] The procedures of Example 1 are repeated with a 200 mm x 400 mm x 5.5 mm template.
[0199] The procedures of Example 1 are repeated with a 200 mm x 400 mm x 4.4 mm template,
and the mixing is performed using a Hobart bench top mixer on high setting for 1.5
minutes, targeting a froth density of 0.091 g/cc.
[0201] The procedures of Example 1 are repeated with a 200 mm x 400 mm x 5.5 mm template,
the first substrate is a polyethylene copolymer based elastic non-woven having a basis
weight of 50 g/m
2, and the second substrate is a polyethylene copolymer based elastic non-woven having
a basis weight of 25 g/m
2.
[0203] The procedures of Example 1 were repeated with a 200 mm x 400 mm x 4.4 mm template;
the mixing is performed using a Hobart bench top mixer on high setting for 1.5 minutes,
targeting a froth density of 0.091 g/cc; the first substrate is a polyethylene copolymer
based elastic non-woven having a basis weight of 50 g/m
2; and the second substrate is a polyethylene copolymer based elastic non-woven having
a basis weight of 25 g/m
2.
[0205] The procedures of Example 1 were repeated with a 200 mm x 400 mm x 4.4 mm template,
the first substrate is a polyethylene copolymer based soft non-woven having a basis
weight of 19.3 g/m
2, and the second substrate is a polyethylene copolymer based soft non-woven having
a basis weight of 19.3 g/m
2.
[0206] Wipes samples with cleaning agent
[0207] A cleaning agent is prepared by mixing components as follows. The first component
includes 225 grams de-ionized water and 6 grams Stepanquat ML (Quaternium 82). The
second component includes 6 grams Ciba Salicare SC-95 (Polyquaternium-37, Mineral
Oil, PPG-1 Trideceth-6), 60 grams Stepan Octyl Isonanoate (ethylhexyl isononanoate),
and 3 grams Goldschmidt Abil EM-9 (cetyl dimethicone copolyol). The third component
includes 0.03 grams Herbal lavender Q-12672, a fragrance, and 1.2 grams Lonza Glydant,
a preservative. Component 1 is added to Component 2, and is mixed for about 20 minutes,
after which Component 3 is added and the solution is homogenized.
[0209] The cleaning agent is added to
Example 3 to meet a cleaning agent to substrate volume of 0.15 g cleaning agent per 1 cm
3 substrate.
[0211] The cleaning agent is added to
Example 5 to meet a cleaning agent to substrate volume of 0.15 g cleaning agent per 1 cm
3 substrate.
[0213] The cleaning agent is added to Example 7 to meet a cleaning agent to substrate volume
of 0.15 g cleaning agent per 1 cm
3 substrate.
[0215] A soft non-woven substrate is formed using the AFFINITY
™ based 2-1-1 dispersion described above diluted with deionized water to yield about
5% solids content (approximately 90 grams water to 10 grams POD dispersion). A soft
non-woven (Haberer/386 ELITE 5600) utilizing a polyethylene-based copolymer and having
a basis weight of 20 g/m
2 is submerged in the diluted dispersion, removed, and is allowed to air dry for 24
hrs, resulting in a polyolefin coated substrate having a dry coat weight of approximately
0.22 grams solid per gram non-woven.
[0216] A first substrate layer of the polyolefin coated soft non-woven substrate is placed
on silicone release paper. 4.7 mm thickness bars are then placed 300 mm apart on the
substrate that was placed on release paper.
[0217] A froth formed from the AFFINITY
™ based dispersion is prepared by the following procedure. Approximately 100 grams
of the dispersion is added to a mixing bowl. The dispersion is mixed using a Hobart
bench top mixer on high setting for 3 minutes, targeting a froth density of 0.095g/cc.
The froth is then spread evenly over the substrate using a spatula, and the bars removed.
A second substrate layer of the polyolefin coated non-woven is then placed on top
of the just applied froth. The composite structure is then placed in an oven at 75°C
for 25-30 minutes or until surface temperature reaches 70-75°C. The sample is then
cooled to room temperature and cut into 50 cm
2 sample disks using a circular die.
[0219] A hydrophilic aqueous poly(urea/urethane) dispersion (HYPOL), available from The
Dow Chemical Company, Midland, Michigan), prepared using a continuous mechanical dispersion
process such as described in
U.S. Patent Nos. 5,339,021,
5,688,842,
5,959,027, and
6,087,440, is diluted with deionized water to yield about 5% solids content (approximately
75 grams water to 25 grams poly(urea/urethane) dispersion). A soft non-woven (Haberer/386
ELITE 5600) utilizing a polyethylene-based copolymer and having a basis weight of
20 g/m
2 is submerged in the dilute dispersion, removed, and is allowed to air dry for 24
hrs, resulting in a polyurethane coated substrate having a dry coat weight of approximately
0.27 grams solid per gram non-woven.
[0220] A first substrate layer of the polyurethane coated soft non-woven substrate is placed
on silicone release paper. 4.7 mm thickness bars are then placed 300 mm apart on the
substrate that was placed on release paper.
[0221] A froth formed from an AFFINITY
™ based dispersion is prepared by the following procedure. Approximately 100 grams
of the dispersion is added to a mixing bowl. The dispersion is mixed using a Hobart
bench top mixer on high setting for 3 minutes, targeting a froth density of 0.095g/cc.
The froth is then spread evenly over the substrate using a spatula, and the bars removed.
A second substrate layer of the polyurethane coated non-woven is then placed on top
of the just applied froth. The composite structure is then placed in an oven at 75°C
for 25-30 minutes or until surface temperature reaches 70-75°C. The sample is then
cooled to room temperature and cut into 50 cm
2 sample disks using a circular die.
[0223] Polyolefin foam samples are made by frothing 150 grams of the AFFINITY
™ based 2-1-1 dispersion described above. The dispersion is mixed for 3 minutes on
high using a Kitchen Aid mixer utilizing a Hobart brand wire whisk, resulting in a
froth having a density of 0.10 g/cc. The resulting froth is applied to silicon release
paper using a 20.2 cm x 20.2 cm x 0.5 cm template. The shaped froth layer is then
dried for 30 minutes at 75°C.
[0224] The resulting foam is then cut into 10.16 cm x 10.16 cm (4" x 4") samples and is
placed onto spunbond, hydrophilic, PGI non-woven substrate. An additional layer of
non-woven is placed on top of the foam. The edges of the samples are then crimped
using a heat sealer, forming a square pouch with foam on the interior.
[0225] In one sample, the non-woven is heat crimped directly to the interior foam layer,
in another example, the non-woven is heat crimped around the foam on the interior.
In this latter sample, the foam is not adhered to the non-woven but is encased by
the non-woven. In the earlier sample the foam is bound to the non-woven around the
perimeter with the center of the foam not being adhered to the non-woven.
[0227] The procedures of Example 1 are repeated with a 200 mm x 400 mm x 4.4 mm template,
where the first substrate is a polyethylene copolymer based elastic non-woven having
a basis weight of 50 g/m
2, and the second substrate is a polyethylene copolymer based elastic non-woven having
a basis weight of 25 g/m
2.
[0228] Comparison Products
[0229] Products existing in the marketplace were identified and compared to samples generated
in Examples 1-16. The five identified products are referenced as Comparative Samples
1-5. Specifically, the products are: Comparative Sample 1) NEUTROGENA® Pure Glow Daily
Cleansing Cushion; Comparative Sample 2) OLAY® Daily Facials Deep Cleansing Cloths;
Comparative Sample 3) PONDS® Clean Sweep Cleansing & Makeup Removing Towlettes; Comparative
Sample 4) DOVE® Gentle Exfoliating Daily Facial Cleansing Pillows; and Comparative
Sample 5) BIROE™ Pore Perfect Daily Deep Pore Cleansing Cloths.
[0230] Comparative Samples and samples generated from the above described examples were
tested for physical properties. The resulting data is discussed in three sections
below: Sensory Panel Testing, Physical Property Tests, and Kawabata Evaluation System
(KES) Testing. The various test methods provide a mechanism to describe the advantages
that the composite structures disclosed herein have over existing products.
[0231] Sensory Panel Testing
[0232] Sensory Panel Testing provides a system of forced ranking to compare the Examples
to the Comparative Samples by human touch. Within these data the following attributes
were compared; hand friction, depression depth, fullness/volume, stiffness, and thermal.
These attributes are important to the perception of softness. It is desirable to provide
a product that is low in hand friction, high in depression depth, high in fullness/volume,
low in stiffness and high in thermal (or "warmest feeling").
[0233] These results show that the dry Examples are higher in depression depth, high fullness/volume,
lower in warmth, and comparable to higher in hand friction than the Comparative Samples.
The results also show that the Examples are low in stiffness compared to the bulkier,
higher volume Comparative Samples.
[0234] These trends hold for Examples that have a cleaning solution incorporated i.e. wet
samples with the exception of the warmth and hand friction. These attributes shift
to being comparable in both attributes to the wet Comparative Samples. The data, for
wet and dry samples, show that, overall, the Examples have more desirable softness
attributes then the Comparative Samples, especially balance of loft and flexibility.
[0235] A human sensory panel was used to evaluate article attributes believed to be associated
with the perception of softness. The attributes are defined as follows. Twenty-four
trained panelists evaluated the samples, with a random order of presentation, and
random three-digit labeling for the samples. The samples were evaluated for hand friction
or slipperiness, depression depth, fullness and volume, stiffness, thermal characteristics.
[0236] Hand friction is evaluated by moving one's hand across the surface of the composite
structure. The sample is placed flat on a table, evaluation side up. Using the weight
of the hand and forearm, the hand is moved horizontally across the surface in all
four directions parallel to the edges. Slipperiness is evaluated based on a no drag
to drag scale from 1 to 6, where 1 equals the least amount of drag (most slip), and
6 equals the most drag.
[0237] Depression depth is characterized by evaluating the amount of the sample depression
when downward force is applied. The sample is placed flat on the table. Finger tips
are used to press down gently on the center of the sample. The downward force is then
released. Depression depth is evaluated based on a 1 to 6 scale, where 1 equals the
least amount of depression and 6 equals the most depression.
[0238] Fullness and volume are evaluated based upon the amount of material sample felt in
the hand during manipulation. The sample is placed flat on the table. Then, one's
dominant hand is placed on top of the sample, positioned so the fingers are pointing
toward the top of the sample. The fingers are then closed, gathering the composite
sample with fingers toward palm. The non-dominant hand is then used to press the sample
into the cupped dominant hand. The dominant hand is then closed slightly and the sample
manipulated by rotating the sample in the palm. Fullness and volume are also measured
on a scale from 1 to 6, where 1 is the least full (low volume), and 6 is the most
full (high volume).
[0239] Stiffness evaluates the degree to which the sample feels pointed, ridged, or cracked.
The sample is placed flat, and one's dominant hand is placed on top of the sample;
position so the fingers are pointing toward the top of the sample. The fingers are
then closed, gathering the composite sample with fingers toward palm. The non-dominant
hand is then used to press the sample into the cupped dominant hand. The dominant
hand is then closed slightly and the sample manipulated by rotating the sample in
the palm. Stiffness is also measured on a scale from 1 to 6, where 1 is the least
stiff (most pliable), and 6 is the stiffest (least pliable).
[0240] Thermal characteristics evaluate the difference in the heating or cooling effect
felt when the sample is placed against skin. The sample is held flat in the palm of
one's hand. One's other hand is placed on top of the hand, and the temperature effect
evaluated. Thermal characteristics are evaluated on a scale of 1 to 6, where 1 is
the coolest feel, and 6 is the wannest feel
[0241] The samples evaluated are shown in Table 2, along with the panel results (averaged).
Depression depth, fullness/volume, and stiffness were evaluated on the above mentioned
scales. The sample thickness was quantitatively measured with applied force of 0.00035
Mpa (0.05 psi) onto 2.54 cm (1") diameter area using a linear gauge. These thickness
measurements are included for reference.
Table 2.
| Sample |
Sample Description |
Sample Thickness (mm) |
Hand Friction |
Depression Depth |
Fullness/ Volume |
Stiffness |
| Example 2 |
Elastic nonwoven, Low Density PFF |
3.1 |
3.75 |
3.13 |
3.13 |
2.75 |
| Example 4 |
Elastic nonwoven, High Density PFF |
3.5 |
3.63 |
3.38 |
3.96 |
4.54 |
| Example 1 |
Elastic nonwoven, Low Density PFF |
1.9 |
3.58 |
1.29 |
1.54 |
2.33 |
| Example 3 |
Elastic nonwoven, Low Density PFF |
4.3 |
2.83 |
4.83 |
4.63 |
2.63 |
| Example 7 |
Soft nonwoven, Low Density PFF |
1.3 |
1.21 |
2.38 |
1.75 |
2.75 |
[0242] The elastic non-woven (Examples 1, 2, 3, and 4) resulted in increased hand friction
(more drag) (>2.8) feel than the soft non-woven (1.2). Thicker foam layers resulted
in more depression depth, indicating a more "cushion-like" feel. For example, the
5.5 mm sample (Example 3) rated 4.83 whereas the 3.0 mm sample (Example 1) rated 1.29.
[0243] The high density foam (Example 4) resulted in a stiffer feel. For example, the low
density foam rated 2.75 whereas the high density foam rated 4.54. Fullness/volume
correlated with foam thickness and density, but the non-woven also had a small influence.
[0244] Samples described above were compared to commercially available articles. The commercially
available wipes were laundered to remove surfactants and other agents, and then air
dried. The samples were then cut into 8 cm diameter circles when possible. Samples
not large enough for cutting were evaluated in the size received. Composite samples
were also cut into 8 cm diameter circles. The commercially available samples were
also assessed, with the results given in Table 3.
Table 3.
| Sample |
Sample Description |
Sample Thickness (mm) |
Hand Friction |
Depression Depth |
Fullness/ Volume |
Stiffness |
| Comparative 1 |
NEUTROGENA® |
3.4 |
4.25 |
3.92 |
4.04 |
3.58 |
| Comparative 2 |
OKAY® |
0.9 |
3.58 |
2.92 |
3.08 |
3.58 |
| Comparative 3 |
PONDS® |
0.6 |
2.17 |
2.25 |
1.79 |
1.46 |
| Comparative 4 |
DOVE® |
2.8 |
2.54 |
4.29 |
4.71 |
4.83 |
| Comparative 5 |
BIROE'™ |
0.5 |
2.46 |
1.63 |
1.34 |
1.54 |
[0245] The commercially available samples showed a wide variation in results. The Competitive
Samples 1 and 4 had higher values for depression depth, fullness/volume, and stiffness
and therefore were compared directly to the samples evaluated above (Table 2). Comparative
Sample 3 was also included as this represented a more typical structure available
commercially. The results from this comparison are shown in Table 4.
Table 4.
| Sample |
Sample Description |
Thickness (mm) |
Hand Friction |
Depression Depth |
Fullness/ Volume |
Stiffness |
| Example 4 |
Elastic nonwoven, High Density PFF |
3.5 |
5.33 |
4.88 |
4.83 |
3.92 |
| Example 3 |
Elastic nonwoven, Low Density PFF |
4.3 |
5.29 |
5.79 |
5.54 |
2.88 |
| Example 7 |
Soft nonwoven, Low Density PFF |
1.3 |
2.29 |
4.13 |
3.08 |
2.54 |
| Comparative 1 |
NEUTROGENA® |
3.4 |
3.25 |
2.25 |
2.92 |
4.92 |
| Comparative 3 |
POUNDS® |
0.6 |
2.75 |
1.17 |
1.00 |
1.42 |
| Comparative 4 |
DOVE® |
2.8 |
2.25 |
2.79 |
3.63 |
5.33 |
[0246] An additional study was also conducted to include evaluation of a a lower basis weight
elastic non-woven on the polyolefin foam (Example 5). In this study the characterization
of the "warmth" property was included in the evaluation of the samples, with the results
shown in Table 5.
Table 5.
| Sample |
Sample Description |
Sample Thickness (mm) |
Hand Friction |
Depression Depth |
Thermal |
Fullness/ Volume |
Stiffness |
| Example 3 |
Elastic nonwoven (50gms), Low Density, 5.5mm |
4.3 |
3.76 |
4.33 |
2.38 |
5.29 |
3.57 |
| Example 5 |
Elastic nonwoven (25gms), Low Density, 5.5mm |
3.5 |
3.62 |
4.67 |
1.76 |
4.67 |
3.14 |
| Comparative 1 |
NEUTROGENA® |
3.4 |
2.81 |
2.19 |
4.14 |
2.43 |
4.95 |
| Comparative 3 |
PONDS® |
0.6 |
2.71 |
1.14 |
5.10 |
1.24 |
1.38 |
| Comparative 4 |
DOVE® |
2.8 |
2.10 |
2.67 |
4.86 |
2.90 |
5.81 |
[0247] The laminated composite structures (Examples 3, 4, 5, and 7) and the resulted in
higher rankings for depression depth and fullness/volume relative to the commercial
samples. And, in spite of the increased volume and loft of these samples, they scored
better on the stiffness ranking than the commercial competitive samples. Increasing
stiffness is perceived to be a negative attribute for softness. Thus, the data demonstrates
enhanced volume/loft without increasing stiffness, resulting in an overall softer
feel for the composite structures.
[0248] A study was also performed to evaluate the hand feel properties of the samples with
the inclusion of a liquid surfactant system. The results are shown in Table 6. All
of these samples had a standard facial cleaning formulation incorporated into the
wipe. The competitive samples were laundered and air dried to remove any existing
cleaning agent. The cleaning formulation was incorporated into all of the samples
to the same loading on a volume basis of 0.15 grams cleaning agent per 1 cm
3 substrate. This was done to minimize hand feel variation due to cleaning agent loading.
Table 6.
| Sample |
Sample Description |
Sample Thickness (mm) |
Hand Friction |
Depression Depth |
Thermal |
Fullness/ Volume |
Stiffness |
| Comparative 1 |
NEUTROGENA® |
3.4 |
5.00 |
2.14 |
5.36 |
2.77 |
5.27 |
| Comparative 3 |
PONDS® |
0.6 |
4.36 |
1.09 |
5.32 |
1.18 |
1.73 |
| Comparative 4 |
DOVE® |
2.8 |
3.50 |
3.27 |
5.68 |
4.14 |
6.14 |
| Examples 8 |
Elastic non-woven (50gms), Low Density |
4.3 |
4.68 |
5.36 |
1.86 |
5.59 |
3.77 |
| Example 9 |
Elastic non-woven (25gms), Low Density |
3.5 |
3.32 |
5.50 |
2.05 |
6.00 |
3.77 |
| Example 10 |
Sort non-woven, Low Density |
1.3 |
1.73 |
3.95 |
2.55 |
3.50 |
3.45 |
[0249] The inclusion of a cleaning formulation reduced the degree of perceived difference
in some of the attributes evaluated, such as with the hand friction attribute. However,
the same trends are evident between the dry and wet samples, specifically the Samples
measured higher in the loft characteristics while maintaining a degree of flexibility
than the Competitive Samples.
[0250] Physical Property Testing
[0251] Physical property tests are included to describe the physical attributes of the inventive
sample in comparison to Comparative Samples; included are bending stiffness; fuzz
level, hand, compression recovery, and tensile tear strength. Specifically the bending
stiffness is a measure of the products flexibility, fuzz level is a measure of the
products ability to resist wear or not to generate lint, hand is the cumulative measure
of the products surface friction, compressibility, and flexibility, compression recovery
is a measure of the products ability to retain loft/thickness after compression, and
tensile tear strength is a measure of the strength of the product to withstand use
and removal from packaging. It is desirable within the application to have a low bending
stiffness; low fuzz generation, low hand on a sample volume and weight basis, high
compression recovery, and good tensile tear strength.
[0252] A number of physical/mechanical property tests were performed to provide additional
comparative data between the Examples and the Comparative Samples. Literature studies
have shown correlations between physical properties such as tensile strength, coefficient
of friction, drape, and crush measurements to correlate with the perception of softness.
In addition, a rub test was performed to determine if the sample surface pills when
rubbed. While this property is not associated with a soft feel, it is a negative attribute.
[0253] The bending rigidity test is a measure of stiffness, as it measures how long of a
sample strip can hang over an edge before the strip bends. Unfortunately, several
of the commercially available Competitive Samples were not of sufficient size for
the bending rigidity test. Comparative Sample 3 (PONDS@) is a more simple non-woven
design that is very flexible, but has low volume/fullness. Results of the bending
rigidity test are shown in Figure 4. Data for the samples made from the composites
of Examples 2 and 4 show that the concept with low density foam is less stiff than
that with high density foam, which is in agreement with the sensory panel results
given above. There is also a difference in the stiffness in the machine direction
(MD) and cross direction (CD).
[0254] The rub test gives an indication of whether or not the surface of an article will
pill when rubbed. Again, adequate sample size was not possible for many of the most
relevant commercial samples. The rub test is performed by rubbing sandpaper of a defined
grit across the surface of the sample with a controlled force. The sample is weighed
before and after the test and weight loss is measured to determine the amount of fuzz
formed and removed from the surface by the sandpaper.
[0255] The results of the fuzz resistance test are shown in Figure 5, and indicate an improvement
in the resistance of the surface to pilling with the use of an elastic non-woven substrate
on the high density foam (Example 4). The Competitive Sample evaluated is a spun-laced
PET. The spun-lacing process relies on mechanically intertwining the fibers to form
the non-woven sheet, and no chemical or melting binders are utilized to tie fibers
together. As such, these fibers are more susceptible to abrasion and to being removed
from the matrix, causing a higher fuzz level measurement. The elastic non-woven utilized
as described within
U.S. Patent No. 6,994,763 employs melted tie points to bind the fibers of the non-woven. These bind points
reduce the release of fibers during the rub test, generating a lower fuzz level, which
for this type non-woven is typically 0.35 to 0.4 mg/cm
2. As shown, the fuzz level of this non-woven is only slightly increased to 0.44 mg/cm
2 when included as a laminate within the high density foam sample (Example 4). The
fuzz level increases more significantly when the elastic non-woven is used in combination
with the low density foam, having a fuzz level of 0.91 mg/cm
2. This indicates that the rigidity and/or density of the underlying material has an
affect on the fuzz level of the surface substrate and that higher density foam results
in a better fuzz performance, more closely approximating the performance of the base
non-woven.
[0256] This data shows that the improved rub performance of the elastic non-woven compared
to the spun-laced non-woven may be maintained while increasing the loft or thickness
as measured in the hand panel above of the overall structure. Maintenance of this
improvement is dependent on the density of the underlying material.
[0257] The measurement of "hand" is considered to be the combination of resistance due to
the surface friction, flexibility, and compressibility of a fabric material. This
measurement of hand has also been used to describe softness of non-woven articles
(such as in
U.S. Patent Nos. 6,241,780 and
6,779,718 and
WO2006065563A1). The hand of a specimen is the sum of the force required to move the specimen through
a slot of a fixed width in each of the four orientations as described by the instrument
manufacturer. The total hand of a sample is based on an average of three specimens
of the sample. This resultant total hand, in gram-force, is what is typically reported,
however this assumes a level of uniformity between sample weights per unit area and
volume in the comparison. Increases in total sample volume compared to a constant
fixed slot width will have an effect on the total hand reported for a sample. Additionally,
changes between sample weights per unit area will affect the total hand reported for
a sample. To account for variation in sample volume and/or sample weight per unit
area a better measure for comparison is the total hand reported for the sample on
a normalized basis to these factors, volume and weight per unit area. It is desirable
to have lower hand per unit volume and per unit weight per area.
[0258] Figures 6 and 7 show the measured hand per cubic centimeter of sample and measured
hand per basis weight (grams per square meter, gsm), respectively. These data show
that the Examples provide lower hand values per sample basis weight and .per sample
volume than the Comparative Samples. This softness/flexibility per volume/fullness
is also seen in the hand panel data.
[0259] The KES compression resilience provides a measure of a materials ability to return
to its original loft after compression. The higher the compression resilience the
better the material can maintain loft and the perception of softness during use. Results
from KES compression resilience are shown in Figure 8. The data indicates that the
Examples provide similar to improved performance when compared to Comparative Samples.
This improved compression resilience is achieved with higher loft, as seen in the
hand panel results.
[0260] The PPT tear test provides a measure of the tear strength of the non-woven system;
measured as total load, average peak load, and the average load. Results of the PPT
tear test are shown in Figures 9-11. The data indicates that the Examples provide
a greater overall PPT tear strength then that of the Comparative samples evaluated.
A greater overall PPT tear strength is indicative of an advantage of durability within
use when compared to the competitive samples. This durability advantage is achieved
with greater loft, as seen in the hand panel results.
[0261] Surface properties (coefficient of friction) and surface contour (roughness) values
of several Examples and Comparative samples are determined using a KES-FB4 surface
tester, where a tension load of 20 gf/cm is applied to the sample. The coefficient
of friction is given in MIU, a measure of the coefficient of friction on a scale of
0 to 1, where a higher MIU value corresponds to a greater friction or resistance and
drag. Regarding KES surface roughness, measured in microns, a higher value corresponds
to a geometrically rougher surface.
[0262] Results of the surface property tests are given in Figures 12 and 13. Figure 12 is
a graphical representation of the results for Kawabata Evaluation System measurements
for geometric roughness for embodiments of the composite structures disclosed herein
as compared to commercially available comparative samples. Figure 13 is a graphical
representation of the results for Kawabata Evaluation System measurements for coefficient
of friction for embodiments of the composite structures disclosed herein as compared
to commercially available comparative samples. The data indicate that the Examples
are comparable to lower in surface roughness while having a greater coefficient of
friction.
[0263] Advantageously, embodiments disclosed herein may provide for composite structures
that have one or more substrate layers, including foams and/or non-wovens. The composite
structures may advantageously allow for the softness, loft and functionality of each
component to be realized in a singular or composite structure.
[0264] Advantages of embodiments disclosed herein may include increased softness, increased
loft, increased toughness and the balance of these conflicting requirements. Additionally,
these advantages may be met along with a greater capability to contain and deliver
and active component such as a cleaning agent. Additional benefits may include the
retention and reduced separation of cleaning agent during shipping and storage within
the container, increase in the frothing of the surfactant in a wet system, and controlled
delivery of actives.
[0265] Embodiments of the composite structures disclosed herein, including "dry" samples,
may advantageously exhibit high depression depth and high fullness/volume, and low
stiffness compared to higher volume comparative samples. The data for wet and dry
samples indicated that embodiments of the composite structures disclosed herein may
have more desirable softness attributes then comparative samples. Additionally, embodiments
disclosed herein may advantageously combine a high tensile tear strength and low fuzz
generation.
[0266] While the invention has been described with respect to a limited number of embodiments,
those skilled in the art, having benefit of this disclosure, will appreciate that
other embodiments can be devised which do not depart from the scope of the invention
as disclosed herein. Accordingly, the scope of the invention should be limited only
by the attached claims.