Field
[0001] This invention relates to activated carbon yarns (multi-fold activated carbon yarns).
Background
[0002] The use of activated carbon for sorption of toxic chemical vapors or gases is well-known.
The use of activated carbon in the form of activated carbon yarns for sorption of
toxic substances is also known. There have been several attempts to produce activated
carbon yarns which could be incorporated into fabrics that would provide the wearer
with protection from toxic chemical vapors or gases.
[0003] Several problems have been encountered in making these fabrics. These problems appear
to be due to the physical characteristics of the activated carbon yarn. After the
activation process, the activated carbon yarn has very low strength, such as low tensile
strength, and poor abrasion resistance. The low strength of the activated carbon yarn
results in a greater tendency of the yarn to break during commercial weaving processes
and results in fabrics that are susceptible to failure at stress points. This tendency
to break and to fail at stress points makes fabric production difficult.
[0004] U.S. 4,285,831 relates to a process for producing activated carbon fibers reportedly
having high adsorption capacity. This patent discloses that by adjusting the amount
of bonded oxygen in the oxidized fiber to a certain amount of oxygen, and by controlling
the shrinkage of the fiber during the oxidation to a limited value an activated carbon
fiber reportedly having excellent adsorption capacity and excellent mechanical properties
can be obtained. The oxidized fiber is activated by heating in a gas selected from
C0
2, NH
3, steam or a mixture thereof, at a temperature of about 200
oC to about 1000°C for 10 minutes to 3 hours while the fiber is allowed to shrink freely.
The activated carbon fiber produced has a specific surface area of from 300 m
2/g to 2,000 m
2 (B.E.T. method using nitrogen gas adsorption isotherm at 25°C). The activated carbon
fiber also has a tensile strength of about 20 to about 80 kg/mm
2, a tensile elongation of about 0.5 to 3% and a tensile modulus of about 1,500 to
about 5,000 kg/mm
2.
[0005] U.S. 4,412,937 relates to a method for manufacturing activated carbon fiber reportedly
having high strength, high adsorbing ability and high processability. The method disclosed
comprises preoxidation and activation steps. Before preoxidation, a treating agent,
selected from phosphorus and borax compounds, is incorporated with an acrylic fiber.
The acrylic fiber is then preoxidized in an oxidizing atmosphere. The concentration
of the phosphorous and/or borax in the oxidized fiber is adjusted and then the oxidized
fiber is activated. The temperature of activation is in the range of 900
0C to 1,300°C.
[0006] U.S. 4,362,646 discloses that the use of an acrylonitrile-based fiber containing
an iron compound prevents the coalescence of fibers at the oxidation step, markedly
shortens the oxidation time and provides a fibrous activated carbon reportedly having
excellent performance in high yields. The patent discloses that the activation processing
can be accomplished by physical activation or a method comprising impregnating the
fiber with an activating agent used in chemical activation and then applying physical
activation. The activation is generally carried out at a temperature of from about
600°C to 1,300°C, preferably about 800°C to about 1,300
0C for from about 6 seconds to 2 hours.
[0007] U.S. 4,256,607 relates to a process for producing. an activated carbon fiber reportedly
having excellent adsorption capacities and sufficient mechanical strength. The patent
discloses a process whereby an acrylonitrile based fiber is subjected to sufficient
oxidation in an oxidizing atmosphere at a temperature of about 200
oC to about 300°C while applying a tension until the amount of bonded oxygen reaches
about 50% to about 90% of the saturated amount of bonded oxygen. The fiber so obtained
is then subject to activation. The activation can be carried out by known methods.
The activation is generally carried out at a temperature of about 700
0 to about 1,000° for about 10 minutes to about 3 hours.
[0008] In fact, a variety of char forming synthetic polymers have been used as precursors
to activated carbon fibers and fabrics. Some examples of synthetic polymers which
form a char on pyrolysis are given in Jenkins, G.M. and Kawamura, K., Polymeric Carbons
- Carbon Fibre, Glass and Char, Cambridge University Press, New York, 1976--see for
example, page 14. A method of producing activated carbon fibers by subjecting the
fiber of a phenol resin to carbonization and activation processings is known and described,
for example, in Ling R. Y. and Ecomomy, J., "The Preparation and Properties of Activated
Carbon Fibers Derived From Phenolic Precursor," in Applied Polymer Symposium No. 21,
pp. 143-152 (John Wiley & Sons Inc, 1973).
[0009] U.S. patent 4,401,588 relates to making activated carbon fabric by heating an aramid
fabric of poly-(benzimidazole) or poly(p-phenylene terephthalamide) under a gaseous
stream containing a mixture of inert gas, preferably nitrogen and about 20% by volume
steam at a temperature in the range of 850-950
oC for at least 10 minutes.
[0010] It is also known in the art to use a continuous process for the activation of tow.
However, the activated yarn produced from such a process has low tensile strength
and poor abrasion resistance.
[0011] A translation of Japanese Applicantion No. 123784 filed July 17, 1982 and laid-open
(published) as No 59-015531-A on January 20, 1984 discloses an active carbon fiber
spun yarn which is composed of single fibers whose twist coefficient is 30 to 60.
The activated carbon fiber yarn is spun yarn of single yarn or at least two folded
yarn. In the case of single yarn that twist coefficient is of the yarn itself. In
the case of a two folded yarn the twist coefficient is of the primary twist or first
twist. If the twist coefficient surpasses 60, the tenacity of the yarn becomes high
but snarls will form easily and the processability will become bad; when less than
30, not only will the tenacity of the yarn drop to the extreme but clogging of yarn
scraps toward the yarn guide will occur frequently. When the spun yarn is at least
two folded yarn, it is best to cause the ratio of the final twist and the primary
twist to be 0.50 to 0.70. See also UK Patent Application GB 2,125,078A published February
29, 1984 which claims priority based on the aforementioned Japanese Application.
[0012] It is also known that non-carbon-containing precursor yarns can be intertwined together
to form a plied yarn having improved elasticity over the component yarns. However,
since these type of plied yarns are not activated carbon yarns they do not have and
therefore do not solve the problem associated with activated carbon yarns.
Summary of the Invention
[0013] This invention provides an activated carbon yarn comprising a plurality of carbon
containing precursor yarns, intertwined together to produce a multi-fold yarn and
then subjected to an activation process.
[0014] Another embodiment of this invention provides an activated carbon yarn comprising
a plurality of carbon containing precursor yarns, intertwined together to produce
a multi-fold yarn and then subjected to an activation process, said activated yarn
having a tenacity of greater than about 0.1 gram/denier (g/d) with about 1.0 g/d to
about 4 g/d being preferred and a carbon tetrachloride (CC1
4) sorptivity of greater than about 25% by weight, based on the weight of activated
carbon yarn, with about 25% to about 140% being preferred.
[0015] In yet another embodiment of this invention, there is provided an activated carbon
yarn comprising a plurality of oxidized yarns, intertwined together to produce a multi-fold
yarn and then subjected to an activation process, said activated carbon yarn having
a tenacity greater than about 1 g/d and a CC1
4 sorptivity of greater than about 60% by weight based on the weight of activated carbon
yarn. Preferably, the oxidized yarn is an oxidized acrylic yarn.
[0016] In still another embodiment of this invention there is provided an activated carbon
yarn made from a carbon containing yarn by a process comprising the steps of:
(1) longitudinally intertwining together a plurality of said carbon containing yarns
thereby forming a multi-fold yarn; and
(2) continuously pulling or feeding said multi-fold yarn through at least one heated
furnace zone while passing an oxidizing gas through said furnace
wherein the temperature of said furnace, the gas flow rate and the through-put rate
(i.e., the rate at which the yarn is pulled or fed through the furnace, feed rate)
are sufficient to produce an activated carbonized yarn having a tenacity greater than
about 0.1 g/d and a CC1
4 sorptivity of greater than about 25% by weight based on the weight of activated carbon
yarn.
[0017] Yet another embodiment of this invention provides articles of manufacture made from
the activated carbon yarns of this invention, in particular articles of manufacture
which are fabrics and the objects made therefrom --e.g. garments (clothing), tents,
masks, and the like.
[0018] Surprisingly it has been discovered that activated carbon material can be treated
with an aqueous dispersion of polymeric fluorocarbon resin particles to provide an
activated carbon material coated with a polymeric fluorocarbon. The polymeric fluorocarbon
coating provides the activated carbon material with increased abrasion resistance
without decreasing CC1
4 sorptivity. This is surprising and unexpected because one skilled in the art would
expect that a coating placed on the activated carbon material would occlude the activation
sites causing decreased sorptivity. However, contrary to expectations, activated carbon
materials do not exhibit a decreased sorptivity when coated with polymeric fluorocarbons.
[0019] Therefore, this invention in another embodiment provides an activated carbon material
coated with a polymeric fluorocarbon and having increased abrasion resistance comprising
an activated carbon material treated with an aqueous dispersion of polymeric fluorocarbon
resin particles.
[0020] In another embodiment this invention provides an activated carbon yarn comprising
a plurality of carbon containing precursor yarns, intertwined together to produce
a multi-fols yarn, and then subjected to an activation process, and then treated with
an aqueous dispersion of polymeric fluorocarbon resin particles.
[0021] In yet another embodiment this invention provides a process for making an abrasion
resistant activated carbon material comprising immersing or dipping an activated carbon
materia in, or spraying an activated carbon material with, an aqueous dispersion of
polymeric fluorocarbon resin particles and then drying said material.
[0022] In still another aspect, this invention provides an improved warp knitted activated
carbon fabric comprising a weft of a multi-fold activated carbon yarn and a warp of
a hydrophobic, monofilament yarn.
[0023] In another embodiment, a hydrophilic layer is incorporated on one side of the above
described warp knitted activated carbon fabric.
[0024] The fabrics of this invention may be used in clothing or fabric enclosures -- e.g.,
tents, window covers, and the like -- to protect individuals from toxic chemical vapors.
The invention may also be used as air filters and in water treatment as well as other
applications requiring the filtration of toxic chemical vapors, gases and liquids.
[0025] Preferably, the carbon containing precursors in the above embodiments are oxidized
acrylic yarns.
[0026] Surprisingly, the multi-fold activated carbon yarns of this invention can be activated
to a higher CC1
4 sorptivity on a weight for weight basis than a single ply yarn (of which the multi-fold
yarn is composed of) and still maintain high levels of tenacity. This is unexpected
because it appears that the multi-fold yarn.has less fiber surface exposed to the
activating gas stream due to the intertwining of the single plies. Thus, it would
be expected that the reduced surface area would result in reduced activation of the
yarn resulting in reduced sorptivity capabilities.
[0027] The multi-fold activated carbon yarns of this invention also have greater ability
to deform or distort in response to an applied force (such as that encountered during
a commercial weaving process). This ability to deform or distort is due to increased
elasticity resulting from intertwining the plies of yarn together before the activation
process.
[0028] Term "carbon containing yarn" as used herein means a yarn that has a char yield.
The term "char yield" means that a carbon residue remains after the yarn has been
pyrolyzed (usually at 1000°C).
[0029] The term "twist coefficient" refers to the primary yarn and as used herein means
the:
Twist Number Per Meter
[0030] Metric count of spun yarn
[0031] The term "twist ratio" as used herein means the ratio of the twist (final twist)
of the activated carbon yarn to the twist of the primary yarns.
[0032] The term "primary yarn" as used herein refers to the individual plies or the multi-fold
yarn.
Brief Description of the Drawings
[0033]
FIG. 1 is a schematic diagram of the activation Process.
FIG. 2 is a diagram of the yarn feed-through entrance.
FIG. 3 is a diagram of the yarn feed-through exit.
FIG. 4 is a graph of data showing "tenacity versus Twist Coefficient" for GB 2,125,078A
and the presently claimed invention.
FIG. 5 is a schematic diagram of the dipping process for coating an activated carbon
fiber.
FIG. 6 is a representative diagram of the testing method used to determine the abrasion
resistance of the activated carbon yarns both coated and uncoated.
FIG. 7 is a schematic diagram of the aparatus used to test the dynamic sorptivities
of both nonwoven and woven fabrics of Example 72.
FIG. 8 is a point diagram for a tricot or raschel type warp knit fabric as described
in Example 73.
FIG. 9 is a point diagram for a tricot or raschel type warp knit fabric with a backing
layer incorporated into the fabric.
Detailed Description of the Invention
[0034] Carbon containing yarns comprising one of the following precursors may prove useful
in producing the activated carbon yarns of this invention: phenolic, poly(benzimidazole),
poly(p-phenyleneterephthalamide), polyacrylonitrile, pitch (petroleum or coal tar),
and the like.
[0035] Examples of commercially available yarns are: KYNOL, a produce designation for a
phenolic-aldehyde yarn available from American Kynol, Inc.; KEVLAR
O 49, brand of aramid yarn from E. I. du Pont de Nemburs & Co., Inc.; PYRON
O brand of oxidized polyacrylonitrile yarn from Stackpole Fibers Co., Inc.; CELIOX
O brand of oxidized polyacrylonitrile yarn from Celanese Corporation, Celion Fiber
Division; GRAFIL '0', a product designation for an oxidized polyacrylonitrile yarn
from Hysol Grafil Limited; FORTAFIL® OPF brand of oxidized polyacrylonitrile yarn
from Great Lakes Carbon Corp.
[0036] Of these yarns, oxidized acrylic yarns are widely used with acrylonitrile oxidized
yarns being preferred. A preferred oxidized acrylonitrile based acrylic yarn is available
from Celanese Corporation, Celion Carbon Fiber Division under the trademark CELIOX®.
[0037] Production of acrylic yarns, as well as oxidation and activation processes are well
known in the art. For example, see U.S. 4,285,831, U.S. 4,412,937, U.S. 4,362,646
and U.S. 4,256,607.
[0038] Yarns made from fibers of acrylonitrile homopolymers and acrylonitrile copolymers
and then oxidized are suitable for use in this invention. Examples of such copolymers
may include copolymers containing not less than about 60% by weight, preferably not
less than 85% by weight, acrylonitrile.
[0039] It is also believed that mixtures of homopolymers and copolymers or mixtures of copolymers
themselves may be used to produce the fiber that will be used to make the yarn from
which the oxidized yarns are made. Copolymers containing less than about 60% by weight
acrylonitrile may be used in admixture with acrylonitrile polymers to produce the
fiber, if the amount of acrylonitrile in the ultimate fiber exceeds 60% by weight.
[0040] Comonomers which may be introduced into the above copolymers include addition-polymerizable
vinyl compounds such as vinyl chloride, vinylidene chloride, vinyl bromide, acrylic
acid, methacrylic acid, itaconic acid; the salts (e.g., the sodium salts) of these
acids; derivatives of these acids, e.g., acrylic acid esters (e.g., alkyl esters containing
1 to 4 carbon atoms in the alkyl moiety such as methyl acrylate, butyl acrylate, and
the like), methacrylic acid esters (e.g., alkyl esters containing 1 to 4 carbon atoms
in the alkyl moiety such as methyl methacrylate, and the like); acrylamide, N-methylolacrylamide;
allyl sulfonic acid, methallyl sulfonic acid, vinyl sulfonic acid, and the salts (e.g.,
the sodium salts) of these acids; vinyl acetate; 2-hydroxyethylacrylate; 2-hydroxyethylmethacrylate;
2-hydroxyethylacrylonitrile; 2-chloroethylacylate; 2-hydroxy-3-chloropropylacrylate;
vinylidene cyanide; alpha-chloroacrylonitrile; and the like. In addition, other compounds
which may be used maybe selected from among those described in U.S. 3,202,640.
[0041] The degree of polymerization of these polymers or polymer mixtures will be sufficient
if a fiber can be formed, and it is generally about 500 to about 3,000, preferably
1,000 to 2,000.
[0042] These acrylonitrile based polymers can be produced using hitherto known methods,
for example, suspension polymerization or emulsion polymerization in an aqueous system,
or solution polymerization in a solvent. These methods are described in, for example,
U.S. 3,208,962, U.S. 3,287,307 and U.S. 3,479,312.
[0043] Spinning of the acrylonitrile based polymer can be carried out by hitherto known
methods. Examples of spinning solvents which can be used include inorganic solvents
such as a concentrated solution of zinc chloride in water, concentrated nitric acid
and the like, and organic solvents such as dimethylformamide, dimethyl- acramide,
dimethyl sulfoxide, and the like. Examples of spinning methods which can be used are
dry spinning and wet spinning. In wet spinning, in general, steps such as coagulation,
waterwashing, stretching, shrinking, drying and the like are suitably combined. These
spinning methods are described in U.S. 3,135,812 and U.S. 3,097,053.
[0044] This stretching is carried out to the same extent as in a usual acrylonitrile based
fiber, and a suitable degree of stretching is generally about 5 to about 30 times
the original length.
[0045] It is believed that the conditions by which the yarn is oxidized effect the physical
properties of the resulting oxidized yarn. Depending on the polymers or copolymers
from which the yarn is made and the oxidation method used, it is believed that the
resulting oxidized yarn will vary in physical properties--e.g., stability. By stability
it is meant that the fiber structure is heat resistant and will not melt, nor will
neighboring fibers coalesce in the temperature range 200°C to 1000
oC. Without wishing to be bound by theory, it is believed that the physical properties
and the polymeric makeup of the oxidized yarn effect the activation conditions under
which the activated carbon yarns of this invention having optimum properties can be
obtained. By optimum properties it is meant a tenacity of at least about 1 g/d and
a CC1
4 sorptivity of greater than about 60% by weight, based on the weight of the activated
carbon yarn. Therefore, those skilled in the art can appreciate that oxidized yarns,
differing in polymeric makeup and/or method of oxidation, may have to be activated
under conditions-- e.g., temperature, gas flow rate, and through-put rate--which vary
from yarn to yarn in order to obtain activated carbon yarns having optimum properties.
However, such conditions may be determined by those skilled in the art without undue
experimentation.
[0046] In the activated carbon yarns of this invention a plurality of carbon containing
precusor yarns, preferably oxidized acrylic yarns, or a combination of different carbon
containing precusor yarns are brought together and arranged spatially by intertwining
to form a multi-fold yarn structure. Intertwining is defined as including any method
for making yarns including the art recognized methods for making yarns from staple
or continuous filaments--e.g., twisting or braiding. Methods for making yarns and
the configurations by which yarns are made--e.g., braided or twisted--are well known
in the art. Preferably, the multi-fold yarn for the activation process is made by
longitudinally twisting or braiding together a plurality of carbon containing precusor
yarns. The carbon containing precuror yarns generally have a twist coefficient greater
than about 65 and usually within the range of from about'65 to about 150. The multi-fold
yarn made by twisting generally has from about 0.5 to about 10 turns per inch. The
twist ratio is generally within the range of about 0.1 to about 0.5.
[0047] The multi-fold yarn is generally made from about 2 to about 20 carbon containing
yarns, preferably oxidized acrylic yarns, with about 3 to about 10 being preferred.
The yarns can be intertwined together at one time or a given number of yarns can be
intertwined together to form a unit and then a given number of units can be intertwined
together to form the multi-fold yarn for activation. For example, 2 oxidized acrylic
yarns can be intertwined to form a pair and then 3 pairs can be intertwined to form
the multi-fold yarn for activation.
[0048] Those skilled in the art will appreciate that the denier of the individual plies
and consequently the denier of the plied yarn are generally chosen to meet specific
requirements of the end product. Thus, as shown by the examples below, 6 oxidized
acrylic spun yarns of 10 worsted count (797 denier) were plied and activated to yield
a plied yarn of from about 20 to 6 worsted count (400 to 1300 denier).
[0049] The multi-fold yarn is then subjected to an activation process. For example, a continuous
activation process can be utilized. In a continuous process the multi-fold yarn is
continuously pulled or fed through at least one hot zone (furnace) while passing an
activating gas through the hot zone. The gas, for example, can be passed through the
hot zone counter current to the direction of the multi-fold yarn. Multiple hot zones,
for example 2, can be utilized--see for example FIG. I--to supply the energy requirements
of the process. The conditions of the temperature, gas flow rate, through-put rate
and the tension the yarn is held at during the process are such that an activated
carbon yarn is produced having a tenacity greater than about 0.1 g/d and a CC1
4 sorptivity of greater than about 25% by weight, based on the weight of the activated
carbon yarn. The activated carbon yarn produced preferably has a tenacity of about
0.1 g/d to about 4 g/d with about 1 to about 4 g/d being most preferred and greater
than about 2 g/d being even more preferred. Preferably, the yarn produced has a CC1
4 sorptivity of about 25% to about 140% by weight, based on the weight of activated
carbon yarn, with greater than about 60% being most preferable and greater than about
75% being even more preferable. The physical properties of the activated carbon yarn
obtained will have some variation based upon the denier of the precursor yarn and,
as discussed above, the denier is generally chosen for specific applications.
[0050] An example of activation conditions for a continuous process are as follows: the
temperature range of the furnace(s) is high enough to allow activation to occur under
the conditions of operation, but not so high as to cause unnecessary degradation of
the multi-fold yarn; thus the temperature is generally from about 700 to about 1300°C
with about 900 to about 1150 being preferred. Those skilled in the art can appreciate
that the gas flow rate, yarn through-put rate, and yarn tension can vary because they
are dependent on the precursor, the precursor's denier, and hot zone lengths, and
these parameters are interactive with each other. Thus, as indicated, some experimentation
may be required to determine the ranges for these parameters that will yield optimum
physical properties of the yarn.
[0051] The gases which are suitable for use in the activation process are well known in
the art. For example, C0
2, NH
3, steam or a mixed gas thereof--e.g., C0
2 and H
20--are used. The amount of allowable oxygen is such that the fiber does not burn,
and the concentration is generally not more than 3 vol %. One or more inert gases
such as N
2, Ar or He may be contained in an activation gas in an amount of up to about 50 vol
% of--e.g., C0
2 and N
2, and the like. Preferably, C0
2, which is bubbled through a gas washing bottle containing H
20 imparting a H
20 vapor content to the C0
2 is utilized.
[0052] A diagram showing an example of a continuous activation process scheme for the production
of an activated carbon yarn utilizing two furnaces is shown in FIG. 1. A precursor
spool (1) contains the carbon containing yarn (2). Tension is applied to the yarn
with a spring tension device (12) with the tension being monitored by a tension meter
(3). The yarn is pulled longitudinally, entering into a quartz reaction tube (4a)
which is heated in a furnace (5a), for example, a Lindberg furnace. The yarn exits
the quartz reaction tube (4a') and enters the second quartz reaction tube (4b) which
is in a furnace, (5b), for example, a Lindberg furnace. The yarn exits the quartz
reaction tube (4b') to take-up rolls (6) and then,to a precision winder (7), for example,
a Leesona winder. An oxidizing gas, flowing from a cylinder (9), passes through a
mass flow controller (10) into a gas washing bottle (8). From the gas washing bottle
the gas enters the furnace (5) countercurrent to the direction of yarn movement. A
digital thermometer monitors the temperature of entering gas. The equipment in processing
unit 14 is equivalent to the equipment in processing unit 13. If only one furnace
is used in the activation process then either unit 13 or unit 14 would be eliminated.
If more than two furnaces are utilized, other units equivalent to units 13 and 14
would be added.
[0053] Precursor yarns of this invention may be activated in furnace at 900
0-1300
0C containing a flowing activating gas. The residence time would determine the degree
of activation.
[0054] FIG. 2 is a schematic of the yarn feed-through entrance (4a and 4b of FIG. 1). FIG.
3 is a schematic of the yarn feed-through exit (4a' and 4b' of FIG. 1). The yarn enters
through 15 (FIG. 2) and exits through 17 (FIG. 3). The activating gas enters through
18 (FIG. 3). The yarn feed-througbs are connected to pyrex and caps, which in turn
are connected to the quartz reaction rube by ground glass joints, for example 24/40
around glass joints, (16 and 19, FIG. 2 and 3, respectively).
[0055] In an alternate embodiment, the present invention provides new and improved activated
carbon fiber yarns and cloths provided with a polyfluorocarbon coating which are characterized
by imprpoved abrasion resistance and weav- ability of the fibers, without adversely
affecting their toxic chemical sorbitivity.
[0056] The polymeric fluorocarbon resins utilized in this aspect of the invention are those
capable of being made into an aqueous dispersion and are well known to those skilled
in the art. Such polymeric fluorocarbons include for example: polytetraflurooethylene
and fluorinated ehtylenepropylene polymers, and the like. Polyhexa- fluoropropylene
may also prove useful. These polymeric fluorocarbon resins are available, for example,
from E. I. duPont de Nemours & Co., Inc. under the trademark TEFLON@. An example of
such a resin is TEFLON® 30B TFE.
[0057] It has been discovered that the polymeric fluorocarbon resin coating imrpoits the
abrasion resistance of activated carbon fibers, reduces the release of carbon fiber
particulates, i.e., fly, produced by abrasion, and creates a hydrophobic surface without
reducing the chemical sorptivity'of the cloth.
[0058] The activated carbon material can be immersed or dipped in an aqueous dispersion
of the fluorocarbon resin particles or can be sprayed with an aqueous dispersion of
the fluorocarbon resin particles. An example of such a resin is TEFLON
O 30B TFE which is a tetrafluoroethylene resin.
[0059] In general any commercially available aqueous dispersion of fluorocarbon resin particles
can be used, such as those available under the trademark TEFLON®. Thus, for example,
a suspension having particles ranging in size from about 0.05 microns to about 0.5
microns (available as TEFLON® 30B TFE) can be used.
[0060] The coated activated material is then dryed to remove the water at ambient temperatures
or with the application of heat, such as in an oven at a temperature of about 90 to
about 250°C.
[0061] The concentration of the aqueous dispersion can vary depending on the amount of coating
desired on the activated carbon material. In general, the amount of coating placed
on the activated carbon material will not effect sorptivity, but will effect the weight
of the activated carbon material. Thus, considerations of the desired weight of the
coated activated carbon material will basically determine the amount of coating placed
on the material. Therefore, any concentration of % solids of fluorocarbon resin in
an aqueous dispersion sufficient to coat the activated carbon material can be used.
For example, among the aqueous dispersions that can be used are those containing about
0.01% to about 10% solids (e.g., 0.01%, 0.1%, 0.5%, 1%, 5%, and 10% solids).
[0062] The use of this coating should allow activated fibers or yarns to be processed with
conventional textile equipment that would destroy or greatly reduce the properties
of uncoated fibers or yarns. Thus activated yarns or fibers may be woven or knit into
useful articles. The life of the garment, made from coated fibers or coated subsequent
to manufacture, should increase as a result of improved abrasion resistance. Less
fly is produced, which decreases safety hazards, when materials are coated. The coating
also creates a hydrophobic surface and repels water and chemical agents that might
be contained within an aqueous media.
[0063] The abrasion resistance of any activated carbon material can be increased by coating
with the fluorocarbon resin as described herein. However, it is desirable to coat
an activated carbon yarn or activated carbon material made from an activated carbon
yarn comprising a plurality of carbon containing precursor yarns, intertwined together
to produce a multi-fold yarn and then subject to activation process.
[0064] In still another embodiment, the invention provides and improved warp knitted activated
carbon fabric comprising a weft of a multi-fold activated carbon yarn and a warp of
a hydrophobic polymeric monofilament yarn wherein every course of said activated yarn
is inserted across the full width of said fabric with said monofilament being in the
wales and courses of said fabric.
[0065] The activated carbon fabrics of this invention, as those skilled in the art can appreciate,
can be produced by a variety of knitting designs known in the art e.g., tricot or
raschel knit fabric design.
[0066] A tricot knit fabric of this invention has a design pattern represented by the bar
movement pattern:
front guide bar: 1-0, 0-1
back guide bar: 1-0, 1-2 .
[0067] A raschel knit fabric having a design represented by the bar movement pattern:
front guide bar: 1-0, 0-1
back guide bar: 1-0, 1-2
may also be used to weave (knit) the fabrics of this invention.
[0068] Without wishing to be bound by theory, it is believed that the leakage encountered
with prior art fabrics is at least partially due to a "wicking effect." Since the
protective yarn is, for example, wrapped or braided along the entire length of the
activated carbon yarn a leakage path is established from outside to inside by a "wicking
effect" when, for example, the fabric gets wet. This wicking effect is overcome by
the use in this invention of a hydrophobic monofilament yarn as the warp. The monofilament
yarns suitable for use include for example: polyesters such as DENIER 20/1 SEMIDOLL
MONOFIL available from Hanover Mills Inc., NY, NY.
[0069] The monofilament generally has a denier of about 10 to about 100, with about 10 to
about 30 being preferred and about 15. to about 20 being most preferred.
[0070] The warp knit fabrics of this invention have monofilament yarn in the warp while
activated carbon yarn is weft inserted a selected number of courses per inch- i.e.,
from about 20 to about 60 courses per inch with about 24 to about 50 being preferred
and about 30 to about 40 being most preferred--to provide a warp knit fabric which
is flexible and has high sorptive capacity for toxic chemical vapors and gases and
liquids, is reasonably strong, and has sufficiently good abrasion resistance to retain
a large amount of sorptivity for toxic chemical vapors even after being subjected
to considerable abrasion. The warp knit fabrics may be produced on tricot type or
raschel type warp knitting machines modified so as to insert the unprotected activated
carbon yarn as weft while the monofilament yarn is being warp knitted. Such apparatuses
and methods are exemplified by U.S. Patent No. 3,364,701 and U.S. Patent No. 3,495,423.
[0071] Although the activated carbon yarn utilized has excellent tenacity, flexibility and
abrasion resistance, during experimental testing in a commercial weaving process,
it occasionally snags and is subject to a minimal amount of breakage around sharp
angle bends in the commercial weaving equipment. It is to be noted that the breakage
which occurs with these multi-fold activated carbon yarns is much less than that which
occurs with other activated carbon yarns. To overcome this, the knitting equipment
may be modified, for example, by placing plastic sleeves at sharp angle bends to guide
the yarn through.
[0072] It is preferred for the purposes of the invention that the warp knit fabric contain
at least 2 oz/yd
2 of the activated carbon yarn with about 3 oz/yd
2 to about 7 oz/yd
2 being most preferred. It is also preferred that the warp knit fabric have an ai"
permeability of at least 50 cubic feet/minute/square foot of fabric wiht about 200
ft
3/min/ft
2 to about 1000 ft
3/min/ft
2 being most preferred. Clothing constructed of warp knit fabric having the above-stated-preferred
characteristics will be effective for protecting the wearer of such clothing against
toxic chemical vapors or gasses for a reasonable length of time, depending on the
concentration of such vapors or gases in the atmosphere, and may be worn without experiencing
undue heat stress since the fabric breathes while sorbing the toxic chemical vapors
or gases and is relatively light weight due to the absence of multilayers and excessive
support yarns to protect the activated carbon yarn.
[0073] In another embodiment of this invention a layer of hydrophilic fiber is incorporated
on to one side of the warp knit fabric described above. This can be done by known
knitting methods as for example, in the manner described in FIG. 9 by, for example,
the addition of a third beam to a knitting machine of the Karl Mayer type. When the
added layer is placed toward the skin of the wearer it improves abrasion resistance,
protects the wearer against carbon fiber cut ends and serves to spread perspiration
for easy release through to the outside of the fabric Since this added layer is on
one side only and does not penetrate the activated carbon yarn layer, it does not
produce a leakage path for toxic liquid agents.
[0074] Hydrophilic fibers or yarns which are useful include but are not limited to: 50/50
polyester/cotton (polycotton), 100% cotton, 100% polyester, rayon, wool, and linen.
[0075] The hydrophilic yarns have a denier of about 100 to about 300 with about 150 to about
250 being preferred and about 175 to about 190 being most preferred. It is anticipated
that the addition of the second layer will add only about 1 to about 1.5 oz/yd
2 to weight of the warp knitted fabric described above.
[0076] While the invention has been described in terms of warp knit fabrics produced with
weft insertion of activated carbon yarn to provide toxic vapor sorptive capacity to
the fabrics, it is to be understood that similar results may be obtained employing
weft knitting machines in which warp yarns of activated carbon yarn are inserted and
held in place in the fabric by the knit weft monofilament yarn.
PROCEDURE FOR DETERMINING
ACTIVATED CARBON YARN'S STRENGTH
[0077] In the following examples, the tenacity of the activated carbon yarns was determined
by measuring the load required to break the multi-fold yarn. These loads were measured
with a tensile testing machine manufactured by Testing Machines, Inc. of New York.
Six-inch yarn lengths were gripped by two pairs of one-inch square rubber-faced jaws,
three inches apart. The loads were measured to the nearest 0.01 pound. Tenacities
were then calculated by dividing that load, in grams, by the denier of the yarn tested.
Yarn deniers (yarn weight per 9000 meters of yarn) were determined by weighing 20
cm. lengths of yarn.
PROCEDURE FOR DETERMINING ACTIVATED CARBON YARN'S CARBON TETRACHLORIDE SORPTIVITY
[0078] In the following examples, static sorption of carbon tetrachloride was used to evaluate
the level of activation in the samples produced. Fiber samples of approximately 500
mg. were placed in a vacuum desiccator which was then evacuated with a mechanical
vacuum pump for 0.5 hours. The desiccator was then back-filled with nitrogen. Each
sample was then weighed to the nearest 0.01 mg and quickly placed in a second desiccator,
saturated with carbon tetrachloride vapor,. for 4 hours. The samples were again weighed
immediately after their removal from the desiccator to determine the percentage weight
gain of carbon tetrachloride with respect to the initial sample weight.
EXAMPLE 1
CONTINUOUS PRODUCTION OF ACTIVATED CARBON YARN UTILIZING TWO FURNACES IN THE ACTIVATION
PROCESS
[0079] An oxidized acrylic yarn was activated in the system own in FIG 1. CELIOX
O brand of oxidized acrylic yarn, available from Celanese Corporation, was pulled through
two 5.4 cm (ID) by 120 cm long quartz reaction tubes. Each tube was placed within
a Lindberg Model 54352 tube furnace. The speed of the yarn through the system was
controlled by take-up rolls and tension in the yarn was monitored with a Tensilon
tension meter. Yarns entered and exited the reaction tube through pyrex end caps and
feed throughs. Flowing countercurrent to the fiber line was a stream of humidified
carbon dioxide. Humidificaticn was achieved by bubbling the gas through heated gas
washing bottles. The temperature of the gas was measured just prior to entering the
furnace. A Tylan mass flow controller was used to control and monitor the flow of
carbon dioxide into each washing bottle.
[0080] Six CELIOX® brand of oxidized acrylic yarns each having a 10 worsted count were twisted
to form a single plied yarn of about 4800 denier with about two turns per inch. The
temperature of the first furnace was held at about 1035
0C with a flow rate of about 3L/min (liters/miute) of carbon dioxide while the second
furnace was held at about 1015
0C with a flow rate of about 4L/min and a gas inlet temperature of about 30°C. A tension
of about 30 grams and a line speed of about 10 cm/min produced an activated carbon
yarn with a denier of 600, an average tenacity of 3.1 g/d and an average carbon tetrachloride
sorptivity of 83%.
[0081] The sample of activity carbon yarn for determining tenacity and CC1
4 sorptivated was taken from the end of about a 200 yard length of the activated carbon
yarn-- i.e., after about 200 yards of yarn had been subjected to the activation process,
a sampling was taken from the end of that length for testing.
[0082] Table 1 reports the results for the 19 samples from which the average tenacity and
average CC1
4 sorptivity was determined.

COMPARATIVE EXAMPLE 1 ATTEMPT TO ACTIVATE SEPARATE 10 WORSTED COUNT YARNS
[0083] In an attempt to activate 6 separate 10 worsted count yarns, using the same conditions
as in Example 1, the yarns repeatedly failed in the oven, presumably as a result of
being over oxidized. The yarns similarly failed even after reducing the temperature
of both ovens 20
0C and lowering the total tension to 10 grams.
EXAMPLE 2
CONTINUOUS PRODUCTION OF ACTIVATED CARBON YARN UTILIZING TWO FURNACES IN THE ACTIVATION
PROCESS
[0084] Using the same procedure described in Example 1, 6 yarns of 6 ply 10 worsted count
CELIOX® brand of oxidized acrylic yarn with approximately 2 turns per inch were activated
with temperatures of about 1052
0C and about 1043°C and flow rates of about 4 and about 5 L/min in the first and second
furnaces, respectively. A line speed (through-put rate) of about 9.5 cm/min and line
tension of about 30 grams produced yarns with an average carbon tetrachloride static
sorptivity of 89% and an average tenacity of 3.0 g/d at a denier of about 670. The
tenacity and CC1
4 sorptivity averages were the result of six trials. The tenacity of these trials ranged
from 2.8 to 3.4 g/d and the CC1
4 sorptivity of these trials ranged from 75 to 96%.
EXAMPLES 3 - 6
[0085] A single furnace was used to activate 6 ply 10 worsted count CELIOX
O brand of oxidized acrylic yarn at various temperatures and flow rates as shown in
Table 2. Within the range examined increases in temperature increased carbon tetrachloride
sorptivity while an optimum B.E.T. surface area was obtained at a CC1
4 sorptivity of 63%. Tenacity appears uneffected by conditions until high carbon tetrachloride
sorptivities are reached when apparently the fibers become over oxidized.

EXAMPLES 7-23
[0086] Table 3, Examples 7-23, lists the % CC1
4 sorptivity and the tenacity (Example 12 only) for activated carbon yarns made from
CELIOX
O brand of oxidized acrylic yarn. Following the procedure of Examples 3-6, six oxidized
yarns each having a worsted count of 10 were intertwined by twisting to form a single
plied yarn (multi-fold yarn). The multi-fold yarn was activated in a single furnace
at the conditions listed in Table 3, using carbon dioxide as the oxidizing gas. One
multi-fold yarn was activated at a time and line tensions are approximate.

EXAMPLES 24-26
[0087] Table 4, Examples 24-26, lists the % CC1
4 sorptivity and the tenacity for activated carbon yarns made from CELIOX® brand of
oxidized acrylic yarn.
[0088] Following the procedure of Example 1, six oxidized yarns each having a worsted count
of 10 were intertwined by twisting to form a single plied yarn (multi-fold yarn).
The multi-fold yarn was activated using two furnaces at the conditions listed in Table
4 using carbon dioxide as the oxidizing gas. One multi-fold yarn was activated at
a time and gas temperature and line tensions are approximate.

EXAMPLES 27-34
[0089] Table 5, Examples 27-34, lists the % CC1
4 sorptivity and the tenacity for activated carbon yarns made from CELIOX
O brand of oxidized acrylic yarns.
[0090] Following the procedure of Example 1, six oxidized yarns each having a worsted count
of 10, were intertwined together by twisting to form a single plied yarn (multi-fold
yarn). The multi-fold yarn was activated using two furnaces at the conditions listed
in Table 5. Nitrogen gas was used in the first furnace and carbon dioxide gas was
used in the second furnace. One multi-fold yarn was activated at a time and gas temperatures
are approximate.

[0091] The foregoing examples demonstrate the production of activated carbon yarns having
excellent tenacity and sorptivity. Those skilled in the art will appreciate that there
are many parameters -- e.g., furnace temperature, gas flow rate, through-put rate
(feed rate), and the like -- subject to variation. It can be appreciated that, in
trying initially to determine the conditions which would yield an activated carbon
yarn with optimum properties, several experiments yielded yarns with less than optimum
properties. Possible explanations for these variants involve the parameters either
individually or in some combination, e.g., unrecorded temperature differences (fluctuations),
a gas flow rate that is too slow, a temperature that is too low, a feed rate that
is too fast or too slow, a gas flow rate that is too low in combination with a temperature
that is too low, and the like.
[0092] Set forth below are examples of experiments which did not yield activated carbon
yarns having optimum properties.
EXAMPLES 35 - 49
[0093] Table 6, Examples 35 to 49, lists the results of experiments which provided yarns
with less than optimum properties when the single furnace technique was used. The
oxidized yarns used, their ply, worsted count and the procedure followed was the same
as for Examples 7-23 except as follows:
- Example 35: utilized PYRONe brand of acrylonitrile based oxidized yarn available from Stackpole Fibers Co. Inc.
The yarn was supplied as a 20 ply yarn (plied yarn), made by intertwining (by twisting)
20 oxidized yarns having a worsted count of 10.
- Example 36: utilized PYRONe brand of acrylonitrile based oxidized yarn as in Example 35 except that 2 oxidized
yarns having a worsted count of 10 were twisted together.
- Example 40: two multi-fold yarns, made of six CELIOXO brand of oxidized acrylic yatn having a worsted count of 10 were drawn through the
furnace parallel to each other. The multi-fold yarn was activated in a single furnace
at the conditions listed in Table 6 using carbon dioxide as the oxidizing gas and
line tensions are approximate.

EXAMPLES 50-59
[0094] Table 7, Examples 50-59, lists the results of experiments which provided yarns with
less than optimum properties. The procedure and oxidized yarns used were the same
as in Examples 1 and 24-26. The multi-fold yarn was activated at the conditions listed
in Table 7 using carbon dioxide as the oxidizing gas and gas temperatures and line
tesions are approximate.

EXAMPLES 60-68
[0095] Table 8, Examples 60-68, lists the results of experiments which provided yarns with
less than optimum properties. The procedures and oxidized yarns used were the same
as in Examples 27-34. The multi-fold "arn was activated at the conditions listed in
Table 8 using carbon dioxide as the oxidizing gas. The gas temperatures are approximate.

[0096] As of the date of filing of this application, there has been limited testing on various
fibers, including an oxidized acrylic fiber, KEVLAR
O 49 brand of Aramid fiber, and a phenolic-aldehyde fiber available under the product
designation KYNOL in the form of continuous tows with no twist which however have
not been adequate to suggest conditions which would result in an activated carbon
yarn with optimum properties. As indicated, it is desirable to use fibers with either
a twisted continuous tow or spun yarn for the yarns of this invention.
[0097] It will be appreciated by those skilled in the art that commercial applications of
the multi-fold yarns of this invention, such as fabric weaving operations, will be
subject to quality control constraints as to processability of the yarns. Thus, as
of the date of filing of this application, experimental testing of the multi-fold
yarns of this invention, such as those exemplified by Example 2, in a commercial weaving
process have been about 95% successful. That is, when tested in a Karl Meyer commercial
knitting process there was only about 5% breakage of the yarn. Possible reasons for
such breakage may include over oxidation of the multi-fold yarn during activation
causing weak spots (areas) in the yarn from variations in process procedures, such
as variation in gas flow rates during activation and non-uniformity of the carbon
containing yarns from batch to batch. It will be further appreciated that this level
of breakage, while low in magnitude, may be additionally reduced to essentially negligible
levels through suitable quality control adjustments in the multi-fold yarn manufacturing
process and/or commercial weaving process.
PROCEDURE FOR DETERMINING ACTIVATED CARBON YARN'S CARBON TETRACHLORIDE SORPTIVITY
[0098] Static sorption of carbon tetrachloride was used to evaluate the level of sorptivity
in coated and uncoated samples. Samples were placed in a vacuum desiccator which was
then evacuated with a mechanical vacuum pump for 0.5 hours. The desiccator was then
back-filled with nitrogen. Each sample was then weighed to the nearest 0.01 mg and
quickly placed in a second desiccator, saturated with carbon tetrachloride vapor,
for 4 hours. The samples were again weighed immediately after their removal from the
desiccator to determine the percentage weight gain of carbon tetrachloride with respect
to the initial sample weight. For coated materials the sorptivity can be based on
the weight of the activated material or the weight of the activated material plus
the coating weight.
Example 69
[0099] Six ply activated carbon fiber yarns of approximately 600 denier were cut to about
1 meter lengths. The yarns were placed in a vacuum desiccator which was evacuated
with a mechanical pump for 0.5 hours. The desiccator was then backfilled with nitrogen
and each yarn was weighed to obtain a base weight. Each yarn was then dipped into
a dispersion of TEFLON
O 30B TFE resin particles 0.05 to 0.5 microns in size suspended in water. Concentrations
of 0.01%, 0.1%, 0.5%, 1%, 5%, and 10% solids were used and were prepared by mixing
TEFLON® 30B TFE resin with varying amounts of deionized water. Each yarn was left
in one of the above suspensions for about 10 seconds. The yarns were then laid on
aluminum foil and were dried at 115
0C for 1 hour. To determine the percentage weight gain of TEFLON
O 30B TFE resin, the yarns were evacuated for 1 hour, backfilled with nitrogen and
reweighed. Each yarn was then tested to determine CC1
4 sorptivity. The results are shown in Table 9.
[0100] The same concentrations of solids in suspensions were used to continuously coat the
same activated carbon yarns for mechanical testing. As shown in FIG. 5, the activated
carbon yarn contained on a spool (1) was pulled through a dip tank containing the
suspension (2) and then through an 18 inch hot zone (3), at about 170°C, with take-off
rolls (4) at a speed of about 20 inches/minute.
[0101] FIG. 6 represents how the abrasion resistance of the yarn was tested by drawing a
weighted yarn over a yarn hook/guide (1) from a Karl Meyer Weftamatic Warp Knit Machine.
The yarn was pulled down one inch and released up one inch (2) with a 50 gm weight
(3) attached to the other end of the yarn. This down-up motion comprised one cycle.
This was repeated until the yarn broke. The number of cycles to failure was noted
and are listed in Table 9.

EXAMPLE 70
[0102] A TEFLON® 30B TFE suspension containing about 1% solids was used to dip and spray
coat activated carbon fiber yarns described in Example 69. A glass atomizer similar
to Kontes Model Number 42250 Thin Layer Chromatography Sprayer was used to spray the
suspension. Samples were dried at about 135
0C for about 0.5 hours. The yarns were tested for CCL
4 sorptivity and abrasion resistance as described in Example 69. CC1
4 sorptivities are based on the yarn plus coating weight. The results are shown in
Table 10.

EXAMPLE 71
[0103] Activated carbon yarn, in the form of continuous untwisted tow, was dipped into a
TEFLON® 30B TFE suspension containing about 1% solids. The tow was then dried at 135°C
for about 0.5 hours. The coating weight was found to be about 2% based on the weight
of the uncoated fiber. CC1
4 sorptivity and abrasion resistance were determined as in Example 69 and the.results
are shown in Table 11.

EXAMPLE 72
[0104] Nonwoven sheets containing 14.8 mg of activated carbon fiber, 1.64 mg of acrylic
fiber, and 0.5 ml of MAGNIFLOC® 1839A brand of flocculant available from American
Cyanamid Co., were made by a wet paper making process as described in copending Application
Serial No 531,366, filed September 12, 1983. One sheet was dipped into a suspension
containing about 1% of TEFLON® 30B TFE solids and was dried at 135
0C to yield a coating weight of about 15% based on the initial fabric weight.
[0105] Similarly, a plain weave fabric of Kuractive activated carbon fiber cloth (available
from Kuraray Chemical Co., Ltd., Japan) was dipped into a suspension containing about
1% of TEFLON® 30B TFE solids and was dried at 135
0C. The coating weight was determined to be about 6% based on the initial fabric weight.
Water was found to bead up on the TEFLON® 30B TFE coated Kuractive woven cloth whereas
water was quickly absorbed into the uncoated cloth.
[0106] Dynamic sorptivities of both fabrics, nonwoven and woven were tested with the apparatus
shown in FIG. 7. This aparatus is a modification of the MIL-C-43858 test specification
apparatus. Purified nitrogen (1) was preheated (2) and was bubbled through CC1
4 (3). The saturated gas was then passed into a mixing manifold (4). The flow of nitrogen
was controlled by a mass flow controller (5). By adjusting the flow of a second source
of nitrogen (6) into the manifold, a concentration of 5 mg of CC1
4 per liter of gas was established. This gas was then pulled through the activated
cloth, contained in a sample cup (7), and a Foxboro MIRAN Model 973 Infrared Analyzer
(8) by a vacuum pump (9). The analyzer was tuned to the 12.6 micron absorbance band
of CC1
4. Calibration of the analyzer was achieved prior to the run by injecting known amounts
of CC1
4 into a recirculating air pump. At a flow of one 1/min, as establizhed by a rotometer
(10), the breakthrough concentration of CC1
4 downstream from the filler was set at 0.5 mg/l as specified in MIL-C-43558. Excess
gas was vented through (11). Apparatus (2), (3), (4), and (7) were maintained at a
constant temperature of 32.5 ±1°C in an oven (12). The dynamic CC1
4 adsorption was calculated as follows:

where t
b is the breakthrough time in minutes. The military specification for chemical protective
clothing is 1.8 mg/cm
2. The results of these tests are shown in Table 12.

EXAMPLE 73
Tricot Warp Knit Activated Carbon Fabric
[0107] A six-ply CELIOX
O oxidized stabilized yarn having a worsted count of 6/10 was activated using the single
furnace technique described in copending Application Serial No. (Case 29,733), filed
(herewith). The multi-fold yarn had a twist coefficient of about 87.5 and a twist
ratio of about 0.2. The activated carbon yarn has a tenacity of 1.3 g/d, weight 1300
denier and static sorption to CC1
4 greater than 80% by weight, based on the weight of the activated carbon yarn. The
yarn was knitted into fabric using a Karl Mayer Weftamatic Warp Knit Machine and a
2 bar chain stitch plus tricot. Monofilament polyester of 20 denier was machine fed
in the warp while-the activated carbon yarn was fed in the weft. Testing yielded the
following characteristics:

[0108] Static and Dynamic sorption of CC1
4 was tested according to the standard method for Military Clothing Material.
[0109] Static CC1
4 sorption by weight gain in saturated vapor of CC1
4 for 4 hours minimum was 70%.
[0110] Dynamic sorption testing using the standard 5 mg/L CC1
4 threat oncentration in nitrogen at 1 L/min rate through 100 cm sample cup area to
a downstream limit of 0.5 mg/L resulted in 43 minutes test time to the end point (2.15
mg/cm2).
[0111] This data is significantly better than the requirements of a U.S. specified military
laminate for chemical protection which describes a carbon powder loaded polyurethene
foam system. MIL-C-43858 (GL) lists the following requirements:

[0112] It is anticipated that when the fabric exemplifiec by this Example is laminated to
a "body side" fabric, the overall laminate weight will be under about 5.5 oz/yd
2. This is a significant reduction in weight compared to existing prior art fabrics.
[0113] A tensile test of this fabric using a TMI tensile tester gave the following resilts:

[0114] This data demonstrates satisfactory strength for clothing applications.