FIELD OF THE INVENTION
[0001] The current invention relates to the field of splittable fibers and manufacturing
processes therefor. More particularly the current invention relates to the field of
splittable fibers formed of a multicomponent staple fiber and manufacturing processes
therefor.
BACKGROUND OF THE INVENTION
[0002] Artificial fibers are typically spun, drawn, and textured prior to being spun into
a yarn. Often such artificial fibers are textured by crimping prior to use as crimping
provides benefits such as processability (carding in particular), improved skin feel,
softness, stretch, fluffiness, etc. to the fibers. The fibers may be selected for
various properties, such as chemical resistance, fluffiness, surface area, hydrophobicity/hydrophilicity,
etc.
[0003] Carded fibers are known for use in filtration media and other uses, via mechanical
filtration principles such as diffusion, interception, inertial impaction and sieving
to capture and retain particles of various sizes. Splittable fibers having an increased
surface area are also known for use in filtration media, leading to a reduced pore
size with the same amount of material which leads to higher filtration efficiency
in the Z direction of the filter media.
[0004] Splittable fibers are known in the art to produce sub-fibers which have an increased
surface area, and therefore different properties than the original (single-strand)
splittable fiber itself. Such splittable fibers are typically produced from a multicomponent
fiber which is then split into multiple sub-fibers. The multicomponent fibers are
known to contain mixtures of polymers, a charge-enhancing additive, a filler, a finish
material, etc. to create the splittable fiber. See, e.g.,
US Patent No. 5,336,552 by Strack, et al., to Kimberly-Clark Corp., granted on August
9, 1994;
US 5,382,400 to Pike, et al., to Kimberly-Clark Corp.,granted on January 17, 1995;
US 2003/0203695 A1 by Polanco, et al., to Kimberly Clark Worldwide Inc., published
on October 30, 2003, all of which are hereby incorporated by reference in their entireties. Finish materials
are known to be added to splittable fibers to reduce the friction and heat generated
during further processing, such as during a carding process. Finish materials are
also employed to prevent static electricity from building up on the fibers during
such further processing.
[0005] Such splittable fibers and corresponding processes are known to produce fibers which
have a significantly larger surface are when split into sub-fibers. Either before
or after splitting, these fibers may be then formed into, for example, filters, filter
materials, nonwoven fabrics/materials, etc. Such splittable fibers are especially
useful in filters, filter materials, etc. where the splittability of the fibers can
significantly increase filtration efficiency. Similarly, higher water pressure during
hydroentanglement may lead to higher splitting, but may conversely also create "large"
apertures throughout the nonwoven fabric which then in turn decreases the filtration
efficiency. Furthermore, traditional hydroentanglement equipment is large, employing
high pressure water with many required safety features; these machines are therefore
very expensive to purchase and install, and yet often such high energy/high impact
processes are typically required in order to significantly split the current splittable
fibers used in nonwoven fabrics into their component sub-fibers.
[0006] Relatively gentle processes such as carding and needle punching will not (significantly)
split current splittable fibers, because they lack the physical force necessary to
significantly split current splittable fibers.
[0007] Additional methods of increasing filtration efficiency are also known, such as electret
charging of fibers. However, it has been found that current splittable fibers are
difficult to charge and/or quickly lose whatever charge they acquire. Typically, current
splittable fibers are multicomponent fibers that are split during a hydroentanglement
process. As a hydroentanglement process is a very energetic process the water jets
impart sufficient kinetic energy to break the multicomponent fibers into sub-fibers.
However such hydroentangled nonwoven fabrics suffer from specific drawbacks as the
hydroentanglement process itself causes large holes/pores in the nonwoven fabric which
decreases the potential filtration efficiency. Also, such nonwoven fabrics, and the
split fibers therein, are typically not chargeable, and certainly are not capable
of holding a durable charge, which also reduces their potential filtration efficiency.
Accordingly, the filtration efficiency of current splittable fibers is limited by
their lack of charge/chargeability. See, for example,
US 2015/0343455 A1 by Schultz, et al., to 3M Innovative Properties Co., published
on December 3, 2015, hereby incorporated by reference in its entirety.
[0008] Next Nano (nxtnano.com; Claremore, Oklahoma, USA) nano fiber-based filter media are
formed by depositing fine fibers onto the surface of a pleatable support layer making
a physical filtration structure that relies upon sieving only. The fibers are very
sensitive and it is difficult to get them to adhere to the surface of the support
layer. The fibers act as a high surface area membrane would, by basically surface
loading contaminant particles. As soon as the surface blinds off or builds a "dirt
cake" the resistance increases to maximum and the filter media has difficulty maintaining
airflow. Furthermore, such nano fiber-based filters are known to typically cost up
twice what other filters cost.
[0009] Conversely, structures that rely only on a high charge potential such as "Tribo electret
media" are designed to be of very low air resistance but have a very powerful surface
charge. The advantage from this type of media is that they "depth load" particulates
and possess a long life with only a small increase of resistance over many weeks or
even months. However, if a filter made with this fibers ingests an oily smoke from
cigarettes or forest fires, the charge is quickly masked, and the filter rapidly loses
efficiency. These filters have been mis-applied and placed in commercial buildings
where the filters prematurely fail due to the loss of charge when the building ventilation
system becomes contaminated with cigarette smoke. The EU has recognized this mis-application
and has initiated the new ISO 16890 standard, hereby incorporated by reference in
its entirety, where the filter is given a rating by averaging the beginning efficiency,
discharging the media and retesting. The results are quite dramatic for a media like
Tribo electret where it may have an initial efficiency of MERV 13 but after discharging
may end up with a MERV 6.
[0010] However, it has been found that as the finish materials currently used are intended
to reduce static build up in the nonwoven fabric, they also may cause the splittable
fiber to quickly lose the charge after, for example, electret charging via corona
processing. Thus, current splittable fibers are not known to be charged, or to durably
carry an electret charge. This in turn has been now found to limit their filtration
efficiency. Accordingly, there exists a need for a finish material for splittable
fibers which does not cause the splittable fiber to lose charge.
[0011] Accordingly, there exists a need for a splittable chargeable fiber capable of holding
a durable charge, especially for the production of filtration media, a nonwoven fabric
made therefrom, and processes for forming such a splittable chargeable fiber and nonwoven
fabric. There also exists the need for a process to manufacture a splittable chargeable
fiber capable of holding a durable charge. There also exists a need for a filtration
product which possesses the advantages of a nano fiber-based filter and a charged
filter to provide efficient and lasting filtration.
SUMMARY OF THE INVENTION
[0012] An embodiment herein relates to a process for forming a splittable fiber having the
steps of providing a multicomponent fiber; or a multicomponent staple fiber, providing
a finish material, and at least partially coating the multicomponent fiber with the
finish material to form a splittable fiber. The multicomponent fiber; or a multicomponent
staple fiber, contains a first thermoplastic segment comprising polymer component
A and a second thermoplastic segment comprising polymer component B. The finish material
has an evaporation point of less than about 160 °C.
[0013] An embodiment of the present invention relates to a process for forming a nonwoven
fabric having the steps of providing a splittable fiber by providing a multicomponent
fiber; or a multicomponent staple fiber as described herein, and forming the splittable
fiber into a nonwoven fabric.
[0014] An embodiment of the present invention relates to a split multicomponent fiber comprising
a durable charge.
[0015] An embodiment of the present invention relates to a nonwoven fabric, a filter and/or
a spun yarn formed by the fibers and processes described herein.
[0016] Without intending to be limited by theory, it is believed that the present invention
may provide a splittable fiber which is capable of receiving and maintaining / holding
a durable charge. This splittable fiber may then be further formed into, for example,
a filtration media possessing significant advantages over existing filtration media.
[0017] Without intending to be limited by theory, it is also believed that the present invention
may provide surprising benefits by combining the best advantages of nano fiber-based
filters and electret-charged filters by incorporating high surface area physical filtration
and electret charge to enhance fine particle retention. The present invention is believed
to provide both depth load filtration and to maintain long-lasting performance with
little or no resistance spikes. It is believed that the present invention significantly
reduces the chances of prematurely failure due to, for example, cigarette smoke, while
also providing significant manufacturing and cost advantages. The invention herein
may provide one or more benefits such as improved filter loading, improved filter
life, improved MERV rating, improved resilience/scuff resistance, etc.
BRIEF DESCRIPTION OF THE DRAWINGS
[0018]
Fig. 1a shows a cross-sectional views of an embodiment of a splittable multicomponent
fiber;
Fig. 1b shows a cross-sectional views of an embodiment of a splittable multicomponent
fiber;
Fig. 1c shows a cross-sectional views of an embodiment of a splittable multicomponent
fiber;
Fig. 2 shows a partial side view of an embodiment of a splittable fiber of the present
invention after splitting;
Fig. 3 shows a partial side view of an embodiment of a splittable fiber of the present
invention after splitting; and
Fig. 4 shows a cross-sectional view of a hollow multicomponent fiber containing a
plurality of alternating thermoplastic segments.
[0019] The figures herein are for illustrative purposes only and are not necessarily drawn
to scale.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0020] Unless otherwise specifically provided, all tests herein are conducted at standard
conditions which include a room and testing temperature of 25 °C, sea level (1 atm.)
pressure, pH 7, and all measurements are made in metric units. Furthermore, all percentages,
ratios, etc. herein are by weight, unless specifically indicated otherwise. It is
understood that unless otherwise specifically noted, the materials, compounds, chemicals,
etc. described herein are typically commodity items and/or industry-standard items
available from a variety of suppliers worldwide.
[0021] As used herein, the terms "a", "an", and "the" are interchangeable with "at least
one" to mean one or more of the elements as described.
[0022] As used herein, the term "durable charge" indicates an electret charge that retains
at least 90% of the original charge after at least about 1 year; or at least about
2 years; or at least about 3 years, in normal conditions of packaging, storage and
handling. A simple hand held static measuring device can be used to measure the initial
charge after electret charging, and the retained charge after the above period of
time, and the percentage retention is easily calculated.
[0023] As used herein, "electret" refers to a material that exhibits a quasi-permanent electric
charge.
[0024] As used herein the phrase "multicomponent fiber" indicates a fiber that has been
formed from a plurality of component polymers, or the same polymer having different
properties and/or additives, and extruded as separate sub-fibers (i.e., strands) from
separate extruders. Typically the multicomponent fiber will be made from a plurality
of different component copolymers; or each sub-fiber is made from a different polymer
from that of the adjacent sub-fiber(s). The sub-fibers are then combined to form a
single fiber, for example, by spinning. Typically the sub-fibers are arranged in consistently-positioned
positions across the cross-section of the multicomponent fiber. The relative positions
of the sub-fibers may be in, for example, pie-wedges such as seen in Figs 1a-1c, stripes,
etc. as known in the art. See, for example,
US Patent No. 5,108,820 to Kaneko, et al., assigned to Mitsubishi Petrochemical Industries,
granted on April 28, 1992, hereby incorporated herein by reference in its entirety.
[0025] As used herein the term "nonsplittable fiber" indicates a fiber having a single,
relatively fixed and constant denier along substantially its entire length even after
processing, including, for example, carding, hydroentanglement, etc., into a nonwoven
web. In an embodiment herein, the nonsplittable fiber is a fiber having a roughly
circular cross-sectional shape in which the entire fiber surface comprises a single
polymer to a depth of at least 10% of the fiber's maximum radius; or for a non-circular
cross sectional fiber, such as a trilobal fiber, wherein a single polymer comprises
substantially the entire fiber surface.
[0026] As used herein "splittable fiber" indicates that a multicomponent fiber having a
given width and cross-sectional configuration may be changed after fiber extrusion,
substantially as part of the nonwoven fabric formation process, typically through
physical disruption of the attachment between individual sub-fibers by the application
of mechanical energy. Typically, a splittable fiber herein will split into at least
2 sub-fibers for about 20% or more; or for about 30% or more of its length; or for
about 40% or more of its length after a typical carding process having a main cylinder
: worker roll speed ratio of 20:1; or 15:1; or 10:1 at a given output speed.
[0027] As used herein the term "staple fiber" indicates a fiber; typically an extruded fiber,
which may be from about 1.25 cm to about 16 cm in length typically, due to cutting.
Staple fibers are typically then formed into a nonwoven fabric via one or more forming
processes such as carding, air laying, adhesive bonding, thermal bonding, etc.
[0028] An embodiment of the present invention relates to a process for forming a splittable
fiber having the steps of providing a multicomponent fiber; or a multicomponent staple
fiber, providing a finish material, and at last partially coating the multicomponent
fiber, or the multicomponent staple fiber, with the finish material. The multicomponent
staple fiber contains a first thermoplastic segment containing polymer component A,
and a second thermoplastic segment containing polymer component B. The finish material
has an evaporation point of less than 160 °C.
[0029] The polymer component A and polymer component B are typically useful herein when
a carded web made from a pie wedge fiber made from the polymer pair is observed to
contain at least 20% of the pie wedge fibers that have split to any degree after carding.
This typically means that polymer component A and polymer component B have different
empirical chemical formulas. Without intending to be limited by theory, it is believed
that, for example, two different grades of polypropylene with different molecular
weights would have the same empirical chemical formula and would not be sufficiently
different for 20% or more of the pie wedge fibers to split during carding. Similarly,
it is believed that a polyethylene terephthalate (PET) and an isophthalic acid/terephthalic
acid coPET would have identical empirical chemical formulas (but not identical chemical
structures) and would thus it would be unlikely for 20% or more of the pie wedge fibers
to split during carding. In contrast, for example, PET and polypropylene have different
chemical formulas and are sufficiently different so as to function in the invention.
Thus, without intending to be limited by theory, it is believed that the present invention
is operable and may provide a splittable fiber so long as the empirical chemical formula
of polymer component A is significantly different from; or different from, polymer
component B.
[0030] The multicomponent fiber; or multicomponent staple fiber, useful herein is a fiber
having a plurality of thermoplastic segments; typically a first thermoplastic segment
and a second thermoplastic segment, although additional thermoplastic segments may
also be included, such as a third thermoplastic segment, a fourth thermoplastic segment,
etc. The multicomponent fiber typically contains at least 4 distinct thermoplastic
segments; or from about 4 to about 128 distinct thermoplastic segments; or from about
8 to about 64 distinct thermoplastic segments, or from about 16 to about 32 distinct
thermoplastic segments. Each thermoplastic segment may be formed of polymer component
A or polymer component B as desired, as long as at least one thermoplastic segment
in the multicomponent fiber is formed of polymer component A, and at least one thermoplastic
segment in the multicomponent fiber is formed of polymer component B. Typically, in
order to promote the desired splitting of the multicomponent fiber into the desired
sub-fibers, each segment will be of a different polymer than the adjacent segment(s).
[0031] It is further understood that in a multicomponent fiber, the thermoplastic segments
are typically arranged in the fiber such that they define a specific spatial arrangement
within the fiber's cross section. Furthermore, this specific spatial arrangement typically
does not vary significantly along the entire length of the multicomponent fiber prior
to splitting. See, for example, embodiments of the multicomponent fiber herein containing
multiple thermoplastic segments in Figs. 1a-1c., showing cross-sectional views of
various multicomponent fiber embodiments, where the multicomponent fiber, 10, contains
a plurality of thermoplastic segments, 12, 12a, 12b, 12c, 12d, etc. each of which
may correspond to a sub-fiber (see Fig. 2 at 14). The various thermoplastic segments
are typically coextruded together to form a single multicomponent fiber, although
they may be separately extruded and then combined, typically quickly combined (before
the individual thermoplastic segments harden), to form the multicomponent fiber. Each
thermoplastic segment has the potential to form its own sub-fiber (see Fig. 2 at 14)
upon splitting.
[0032] In an embodiment herein, a process for forming a nonwoven fabric includes the steps
of providing a splittable fiber, and forming the splittable fiber into a nonwoven
fabric. The splittable fiber is provided by providing a multicomponent fiber; or a
multicomponent staple fiber, containing a first thermoplastic segment containing a
polymer component A, and a second thermoplastic segment containing a polymer component
B, providing a finish material having an evaporation point of less than 160 °C and
at least partially coating the multicomponent staple fiber with the finish material.
[0033] In an embodiment herein, the step of forming the splittable fiber into a nonwoven
fabric may be, for example, forming step is selected from the group consisting of
carding, thermal bonding, needle punching, spunbonding/spinbonding, air laying, hydroentanglement,
melt blowing, hydro pulping, refining, wet laying, passing thorough air oven, cross-lapping,
and a combination thereof; or thermal bonding, needle punching, hydropulping, wet-laying,
chemical bonding (e.g., for acrylic latex), melt blowing, air laying, carding, needling,
hydroentanglement, and a combination thereof; or thermal bonding, needlepunching,
hydropulping, wet laying, and a combination thereof. Typically carding, spunbinding/spunbonding,
air-laying, melt blowing and melt laying are considered processes for initially forming
a nonwoven web, while thermal bonding, needle punching, hydroentanglement, chemical
bonding, and cross-lapping are processes that consolidate the initially-formed nonwoven
web into a nonwoven web which is typically possesses increased strength, rigidity,
etc. as compared to the initially-formed nonwoven web. Hydro pulping and refining
are used prior to wet-laying to condition the water-borne fibers. Accordingly, as
used herein, the term "forming step" includes all different phases of the physical
forming process, from the point that fibers are extruded, to the final production
of the nonwoven fabric. However, the forming process as used herein does not necessarily
include the electret charging step.
[0034] It is understood that when the multicomponent fiber splits apart into sub-fibers,
they do so in a distribution of splitting at any specific location along the multicomponent
fiber (see, e.g., Fig. 2 and Fig. 3). That is, for example, at a certain location,
a multicomponent fiber comprising 16 thermoplastic segments may split entirely into
16 separate sub-fibers, with each sub-fiber containing a single thermoplastic segment.
Alternatively a multicomponent fiber (or even the same multicomponent fiber at a different
location) may split into 6 sub-fibers each containing one thermoplastic segment each,
2 sub-fibers comprising 2 thermoplastic segments each (not split apart from each other),
and one sub-fiber comprising 6 thermoplastic segments that remain adhered to each
other in a single sub-fiber. In other fibers, or even along the same multicomponent
fiber, the distribution of single-segment and multiple segment sub-fibers may be different.
[0035] Fig. 2 shows a partial side view of an embodiment of a splittable fiber, 20, of the
present invention after splitting. The multicomponent fiber, 10, contains 8 different
thermoplastic sub-fibers, 12a-12h from top to bottom respectively, to form the splittable
fiber, 20. At point A-A, along the multicomponent fiber, 10, thermoplastic segments
12a, 12b, 12c, 12d, and 12e are joined together in a sub-fiber 14a, while thermoplastic
segments 12f, 12g and 12h are joined together in a sub-fiber, 14b. The split distribution
can be measured using, for example, the BET test, the Micronaire test, SEM analysis,
etc. as described herein.
[0036] However, at point B-B along the same multicomponent fiber, thermoplastic segment
12a has split from thermoplastic segments 12b and 12c which are still joined together.
Thermoplastic segment 12d and thermoplastic segment 12e are split as well as single
sub-fibers, 14, while thermoplastic segments 12f, 12g, and 12h are still joined together
in sub-fiber 14b.
[0037] At point C-C, all of the 8 thermoplastic segments 12, have split apart, so thermoplastic
segments 12a, 12b, 12c, 12d, 12e, 12f, 12g and 12h can all be seen and identified
separately as individual sub-fibers.
[0038] At point D-D, all of the 8 thermoplastic segments are joined together as a single
multicomponent fiber. One skilled in the art understands that additional combinations
and arrangements of the thermoplastic segments to form various sub-fibers are also
possible as well, either in different multicomponent fibers, or at different places
in the same multicomponent fiber.
[0039] Without intending to be limited by theory it is believed that such a splittable fiber
having a variable split distribution is useful as it allows the production of various
nonwoven fabrics having different physical features and properties such as fluffiness,
thickness, insulation levels, air/water resistance, filtration levels, etc. from the
same multicomponent fiber. Furthermore, it is believed that the split distribution
can be increased by changing the process, for example, more vigorous carding leads
to a higher splitting of the splittable fibers, both along the same fiber as well
as in different fibers.
[0040] Fig. 3 shows a partial side view of an embodiment of a splittable fiber of the present
invention after splitting. Specifically, the splittable fiber, 20, can be shown split
into thermoplastic segments, 12a, 12b, 12c, 12d, 12e, 12f, 12g, and 12h, for a majority
of its length. As can be seen on the right side of the figure, the splittable fiber,
20, is split into thermoplastic segments, 12a, 12b, 12c, 12d, 12e, 12f, 12g, and 12h,
each of which corresponds to a sub-fiber, 14a, 14b, 14c, 14d, 14e, 14f, 14g, and 14h.
[0041] Fig. 4 shows a cross-sectional view of a hollow multicomponent fiber, 10, containing
a plurality of alternating thermoplastic segments, 12a and 12b. Specifically, the
multicomponent fiber, 10, contains a hollow center, 16. Each segment 12a is formed
of polypropylene and in the embodiment of Fig. 4 each segment 12b is formed of polymethylpentene,
which would normally bind together too strongly to be split when formed into a shape
such as Fig. 1a. However, due to the lower adjoining surface area, 18, between the
different segments, 12a and 12b, due to the hollow center, 16, in the multicomponent
fiber, 10, these segments, 12a and 12b, may still be split from each other during
a carding process. Thus, in an embodiment herein, the multicomponent fiber is a hollow
fiber. In an embodiment herein, the polymer component A is polypropylene and polymer
component B is polymethylpentene.
[0042] As mentioned above, polymer component A and polymer component B have different empirical
chemical formulas. In an embodiment herein, the polymer component A includes a polymer;
or a polymer selected from the group consisting of a polyamide, a sulfur-containing
polymer, an aromatic polyester, an aliphatic polyester, a polyolefin, and a combination
thereof; or a polyamide, a polyphenylene sulfide, a polyarylene terephthalate, a polyarylene
isopthalate, a polylactic acid, a polyhydroxyalkanoate an aliphatic polyester, a polypropylene,
a polyethylene, a polymethylpentene, and a combination thereof; or nylon, polyphenylene
sulfide, polyethylene terephthalate, polylactic acid, poly propylene, and a combination
thereof; or PET, polylactic acid polymer, polypropylene, and a combination thereof.
As used herein with respect to the polymers, the term "a combination thereof' specifically
includes copolymers, homopolymers, and blends thereof.
[0043] In an embodiment herein, the polymer component B includes a polymer; or a polymer
selected from the group consisting of a polyamide, a sulfur-containing polymer, an
aromatic polyester, an aliphatic polyester, a polyolefin, and a combination thereof;
or a polyamide, a polyphenylene sulfide, a polylactic acid, a polyarylene terephthalate,
a polyarylene isopthalate, a polyhydroxyalkanoate an aliphatic polyester, a polypropylene,
a polyethylene, a polymethylpentene, and a combination thereof; or a nylon, a polyphenylene
sulfide, a polylactic acid, a polyethylene terephthalate, a poly propylene, and a
combination thereof; or a PET, a polylactic acid polymer, a polypropylene, and a combination
thereof.
[0044] In an embodiment herein, the polymer component A and/or the polymer component B contains
a polyolefin; or a polyolefin selected from the group consisting of a polypropylene,
a polyethylene, and a combination thereof. Without intending to be limited by theory,
it is believed that polyolefins; or polypropylene, polyethylene, and the combination
thereof are especially useful for acquiring and holding an electret charge.
[0045] In an embodiment herein, the polymer component A contains a polyolefin polymer, and
polymer component B contains a non-polyolefin polymer. In an embodiment herein, the
polymer component A contains a polylactic acid polymer, and polymer component B contains
a non-polylactic acid polymer.
[0046] The finish material herein is applied to the surface of the splittable fiber to aid
in lubricating the splittable fiber to reduce heat generation and to reduce static
during further processing, such as carding, etc. Generally in the art, traditional
finish materials contain mineral oils or synthetic oils with anti-static additives.
Sometimes these traditional finish materials may contain animal fats, or fatty acids.
However, it has now been found that these traditional finish materials reduce or eliminate
the charge induced or added on to the splittable fiber, during, for example, electret
charging; or electret charging via corona charging. Accordingly, an embodiment of
the invention herein includes the step of removing the finish material from the splittable
fiber prior to electret charging; or removing the finish material from the splittable
fiber during the electret charging process. In an embodiment herein, the finish material
is removed during, for example, the dwell time in an oven, etc.
[0047] A finish material may be required for increasing lubrication during further processing,
to reduce static charge build up, etc. Thus, in an embodiment herein, the finish material
has an evaporation point of less than about 160 °C; or from about 30 °C to about 160
°C; or from about 40 °C to about 150 °C; or from about 50°C to about 100 °C.
[0048] The finish material herein may be a substantially water-soluble; or water-soluble
finish material, which is especially intended to wash away during, for example, washing,
a hydroentanglement process, etc. In an embodiment herein, the finish material is
a water-soluble finish material, and the forming process includes the step of hydroentangling
the splittable fiber while coated with the finish material.
[0049] Without intending to be limited by theory, it has been found that when the evaporation
temperature is in the range above, then most; or substantially all, of the finish
material is removed; or evaporated, during the thermal bonding process to form the
nonwoven web. In an embodiment herein, the process herein includes the step of removing,
by weight, at least a portion; or from about 50% to about 100% of the finish material;
or from about 75% to about 100% of the finish material; or form about 80% to about
100% of the finish material, from the nonwoven fabric, the multicomponent fiber, and/or
the splittable fiber; or from the splittable fiber, during or after the forming step
when the splittable fiber is formed into a nonwoven fabric and prior to the electret
charging process. In an embodiment herein, the nonwoven fabric forming process removes
at least a portion of the finish material; or from about 50% to about 100% of the
finish material; or from about 75% to about 100% of the finish material; or form about
80% to about 100% of the finish material; or substantially all of the finish material,
by weight from the nonwoven fabric.
[0050] In an embodiment herein, the finish material comprises water, a lubricant, and an
emulsifier. In an embodiment herein, the lubricant is a selected from a plant-based
oil, a natural oil, a synthetic oil, a water-soluble lubricant, and a combination
thereof; or a vegetable oil, a mineral oil and a combination thereof; or a light vegetable
oil, a light mineral oil, and a combination thereof; or a coconut oil, a corn oil,
and a combination thereof. It is preferred that the lubricant herein possess a low
molecular weight, a high viscosity, and few, or no molecular byproducts when exposed
to heat, and no residue after evaporation. In an embodiment herein the finishing material
and/or the lubricant are compliant with the United States Federal Drug Administration
guidelines regarding GRAS (Generally Regarded As Safe) list (See, for example, https://www.fda.gov/food/food-ingredients-packaging/generally-recognized-safe-gras;
and US Code of Federal Regulations: 21 CFR 177.2800; 21 CFR 176.210; 21 CFR 178.3400),
all hereby incorporated by reference in its entirety.
[0051] In an embodiment herein, the finish material is a water-soluble finish material;
typically containing a water-soluble lubricant; or containing sufficient emulsifier
to fully emulsify any and all oil in the finish material, or is a fully water-soluble
finish material, so that during, for example, a hydroentanglement process, the finish
material washes away; or substantially washes away, from the splittable fiber.
[0052] In an embodiment herein, the emulsifier acts as an antistatic compound; or an antistatic
compound having an evaporation point of less than about 160 °C; or from about 30 °C
to about 160 °C; or from about 40 °C to about 150 °C; or from about 50°C to about
100 °C. In addition, the finish material may contain a specific antistatic material
other than the emulsifier.
[0053] In an embodiment herein, the finish material may also contain a stabilizer, a thickener,
a thinner, an anticoagulant, an antimicrobial compound and a combination thereof.
These compounds are well-known in the art and available from multiple well-known suppliers
worldwide.
[0054] The multicomponent fiber is at least partially coated; or coated, in a coating step
with the finish material to form a splittable fiber. The coating step may include,
for example, spraying the finish material onto the multicomponent fiber, immersing
the multicomponent staple fiber in the finish material, contacting the fiber and a
film of liquid finish material on the surface of a transfer roll (for example, a kiss-roll
application process), contacting the fiber with a bead of the finish material as the
fiber passes through a grooved applicator (e.g., using a metered-finish application
process), and a combination thereof.
[0055] In an embodiment herein, where the invention employs a multicomponent staple fiber,
the process herein may further include the step of cutting a multicomponent fiber
to form a multicomponent staple fiber, crimping a multicomponent staple fiber to a
length of from about 1.25 cm to about 16 cm, and a combination thereof.
[0056] Once the multicomponent fiber is formed into the splittable fiber, then the splittable
fiber is typically formed into a nonwoven fabric by, for example, by the forming processes
described herein. Such forming processes are known in the art.
[0057] In an embodiment herein, the splittable fiber is fully split into a plurality of
sub-fibers. In an embodiment herein, the smallest sub-fibers have a linear density
of less than about 5 denier; or less than about 2 denier; or less than about 1 denier;
or less than about 0.8 denier; or less than about 0.4 denier.
[0058] In an embodiment herein, the nonwoven web includes a nonsplittable fiber having a
linear density of greater than about 1 denier; or from about 1.5 denier to about 4
denier; or from about 1.5 denier to about 3 denier. In an embodiment herein, the nonwoven
fabric herein further contains an additional nonsplittable fiber having a linear density
of from about 1 denier to about 20 denier to provide additional properties such as
stiffness, the ability to hold a shape or a crease/fold, etc.
[0059] An embodiment of the present invention further includes a split multicomponent fiber
having a durable charge as described herein.
[0060] In an embodiment herein, the nonwoven fabric also contains a nonsplittable fiber
in addition to the splittable fiber. Thus, in an embodiment of the nonwoven fabric
formation process herein, the process includes the step of providing a nonsplittable
fiber. The nonwoven web is then formed from the splittable fiber and the nonsplittable
fiber. In an embodiment herein the nonwoven fabric contains from about 1% to about
100%; or from about 3% to about 97%; or from about 5% to about 95%; or from about
10% to about 90% splittable fibers by weight of the nonwoven fabric. It is believed
that a blend of both splittable fibers and nonsplittable fibers may provide benefits
such as strength, shape retention, filtering, etc. In an embodiment herein, the nonwoven
fabric contains at least 20% nonsplittable fibers, especially if it is thermal bonded
during the forming step.
[0061] In an embodiment herein the finish material is removed after the forming step; or
after the splittable fiber is split. Without intending to be limited by theory, it
is believed that by removing the finish material from the splittable fiber, the nonwoven
fabric, the split multicomponent fiber, etc. the resulting individual split multicomponent
fiber's ability to acquire and hold a durable charge will not be significantly abated
or reduced by the antistatic properties of the finish material.
[0062] In an embodiment herein, the process for forming a nonwoven web includes the step
of splitting the multicomponent fiber; or the multicomponent staple fiber; or the
splittable fiber, into a split fiber. In an embodiment herein, the splitting step
includes a needle punching process, a hydroentanglement process, a carding process,
a flexing process, a twisting process, a stretching process, a drawing process, a
scraping process, a crushing process, a rolling process, a hydropulping process, a
stitchbonding/stitchbinding process, and a combination thereof; or a carding process,
a needle punching process, a hydropulping process, and a combination thereof. In an
embodiment herein the splitting step is the same as the forming step.
[0063] In an embodiment herein, the electret charging process charges a thermoplastic component
in the splittable fiber, the split fiber, the multicomponent fiber, the multicomponent
staple fiber, the nonwoven fabric, and/or etc. selected from the group of the first
thermoplastic component, the second thermoplastic component, and a combination thereof;
or the split fiber, the multicomponent fiber, the split multicomponent fiber, and/or
the nonwoven fabric. In an embodiment herein, the electret charging process useful
herein is selected from the group of corona charging, ion bombardment, atmospheric
plasma deposition (APD), other charging methods, and a combination thereof; or corona
charging, ion bombardment, APD and a combination thereof; or corona charging, APD,
and a combination thereof. Corona charging is known in the art and has its roots in
the foil and film lamination process. Early research in nonwoven media started in
the 1990's when Dr. Peter Tsai from University of Tennessee developed and patented
a system to enhance melt blown polypropylene with a similar technology designed to
give films a normalized surface energy for secondary processing. Dr. Tsai found that
by applying a strong polarity of charge to a polypropylene melt blown structure that
the surface energy attracted, removed and held fine particles (> 1.0 micron) enhancing
an otherwise low efficiency filtration media.
[0064] In an embodiment herein, the electret charging process includes the process of APD.
In an embodiment herein, the electret charging process first employs an atmospheric
plasma deposition process and subsequently a corona charging process. Without intending
to be limited by theory, it has been found that in addition to including an electret
charge in the fibers, APD may can also remove oligomers and other low molecular weight
by-products, such as the finish material, from thermoplastic polymeric fibers as well
as providing a nano-etched finish giving the fibers a more suitable surface. It is
further believed that the APD process may actually clean and functionalize the fiber
surface such that when the APD process is followed by a corona charging process, the
corona charge may be stronger, and/or may last an even longer time; i.e., is even
more durable.
[0065] In an embodiment herein, the electret charging; or the corona charging process, ion
bombardment, the APD process, other charging methods, and a combination thereof; or
the heat from the corona charging process, the APD process, and a combination thereof,
helps to remove finish material from the splittable fiber, the nonwoven fabric, the
multicomponent fiber, the multicomponent staple fiber, the split fiber, and/or sub-fiber.
In an embodiment herein, the electret charging; or the corona charging, imparts a
negative charge to the outer surface of the splittable fiber, the nonwoven fabric,
the split fiber, the multicomponent fiber, the multicomponent staple fiber, and/or
sub-fiber. Without intending to be limited by theory, it is believed that this negative
surface energy on the outer surface of the splittable fiber, the nonwoven fabric,
the split fiber therefore attracts positively-charged particles from the air or other
media passing through the filter, thereby significantly increasing filtration efficacy.
The electret charging may impart either a net negative charge or a net positive charge
on the nonwoven fabric, the multicomponent fiber, multicomponent staple fiber, and/or
the split fiber. An electric charge allows the nonwoven fabric, the multicomponent
fiber, the multicomponent staple fiber, and/or the split fiber to attract oppositely-charged
particles when being used as, for example, a filtration matrix.
[0066] In an embodiment herein, a charge-enhancing additive added is included into the multicomponent
fiber; or the polymer component A; or the polymer component B. The charge-enhancing
additive enhances the development and/or retention of an electret charge; or a static
electrical charge. In an embodiment herein, the charge-enhancing additive is selected
from the group of stearate salts; phosphate metal salts, benzoic acid salts, zinc,
and a combination thereof; or the charge-enhancing additive is selected from the group
of calcium stearate, magnesium stearate, sodium phosphate, sodium benzoate, zinc salts,
and a combination thereof; or the charge-enhancing additive is selected from the group
of calcium stearate; magnesium stearate, sodium phosphate, and a combination thereof.
Without intending to be limited by theory, it is believed that stearate salts; or
calcium stearate and magnesium stearate particles; or calcium stearate particles having
a diameter of 5 microns (µ) or less and magnesium stearate particles having a diameter
of 5µ or less are especially desirable if the multicomponent fiber and/or a sub-fiber
contains polypropylene. Without intending to be limited by theory it is believed that
once the multicomponent fiber and/or the sub-fiber contains and/or is coated with
the charge-enhancing additive(s), the charge-enhancing additive(s) may form a capacitor-like
structure which may enhance the electret charge density and/or durability as compared
to when no charge-enhancing additive is present.
[0067] In an embodiment herein, the charge-enhancing additive is an organic acid metal salt
composed of at least a C
10 carbon-chain organic acid and a metal ion work function of 4eV or more. Examples
of the organic acid useful herein include C
10 or higher carbon chain length carboxylic acids, organic phosphoric acids, organic
sulfonic acids, and the like, especially lauric acid, linolenic acid, t-butylbenzoic
acid, di-(t-butylphenyl) phosphoric acid, and/or stearic acid. The metal salt ions
useful herein include, for example, aluminum ions, iron ions, nickel ions, cobalt
ions, tin ions, copper ions, lead ions, cadmium ions, etc., especially aluminum ions.
See
JP H06-254319A by Tokuda, et al., to TOYOBO Co., Ltd., published on September 13,
1994 hereby incorporated by reference in its entirety.
[0068] In an embodiment herein, the charge-enhancing additive is selected from the group
of triphenylmethanes; ammonium compounds and immonium compounds; intensely fluorinated
ammonium and immonium compounds; biscationic acid amide and acid imide derivatives;
polymeric ammonium compounds; diallylammonium compounds; arylsulfide compounds; phenolic
compounds (respectively compounds of the
CAS-No. 41481-66-7 and 13288-70-5); phosphonium compounds; highly fluorine-substituted phosphonium compounds;
calix(n)arene compounds; metal complex compounds like chromium-, cobalt-, iron-, zinc-
or aluminum azocomplexes or chromium-, cobalt-, iron-, zinc- or aluminum salicyclic
acid complexes (such as described by
CAS-Numbers 31714-55-3, 104815-18-1, 84179-68-8, 110941-75-8, 32517-36-5, 38833-00-00, 95692-86-7, 85414-43-3,
136709-14-3, 135534-82-6, 135534-81-5, 127800-82-2, 114803-10-0, 114803-08-6 and the
like); benzimidazolon compounds; and/or azines of the following Color Index numbers,
C. I Solvent Black 5, 5:1, 5:2, 7, 31, 50; C.I. Pigment Black 1, C. I. Basic Red 2
and C. I. Basic Black 1 and 2. See,
EP 623941A2 to Groh, et al., published on March 5, 1994, assigned to Hoechst Celanese Corp., hereby incorporated by reference in its entirety.
[0069] In an embodiment herein, the charge-enhancing additive contains an arylamino-substituted
benzoic acid and/or an arylamino-substituted benzoic acid salt. The salts useful herein
may be metal-containing salts and may be salts of monovalent, divalent or trivalent
metals. Alternatively, the charge-enhancing additive useful herein may contain phenolate
salts; or triazine phenol salts; or a triazine phenolate anion and a metal cation.
See
US 2016/0067717 A1 by Schultz, et al., to 3M Innovative Properties Co., published
on March 10, 2016; and
US 2019/0336896 A1 by Schultz, et al., to 3M Innovative Properties Co., published
on November 7, 2019, all of which are hereby incorporated by reference in their entireties.
[0070] The charge-enhancing additive may be present in any suitable level as known in the
art; or in an amount up to about 10%; or from about 0.02% to about 5%, by weight of
the polymer component.
[0071] Fillers useful herein are typically particulate materials added into the polymer
component to provide bulk and to reduce the overall material cost and are extruded
together. The particles are typically from about 0.5µ to 5µ in diameter, although
they may not have a regular shape. Non-limiting examples of fillers useful herein
include inorganic fillers such as calcium carbonate, titanium dioxide, talc, barium
carbonate, magnesium carbonate, magnesium sulfate, mica, clays, kaolin, diatomaceous
earth, and the like. Organic fillers include chitin, carbon black, wood and cellulose
powders, etc.
[0072] In an embodiment herein, a pigment, whether liquid, solid, etc., may be added to
any of the fibers herein to provide a color to the fiber.
[0073] Without intending to be limited by theory it is believed that once the splittable
fibers herein are split into split fibers, and further provided with an electret charge,
the filter material's MERV (Minimum Efficiency Reporting Values) rating will very
likely increase, indicating that the filter is better at removing particulates, especially
charged particulates. See, for example, https://www.epa.gov/indoor-air-quality-iaq/what-merv-rating-1,
hereby incorporated by reference in its entirety, which explains MERV ratings and
that it is derived from the American Society of Heating, Refrigerating, and Air Conditioning
Engineers (ASHRAE) [see www.ashrae.org].
[0074] In an embodiment herein the splittable fiber, the split fiber, the multicomponent
fiber, the multicomponent staple fiber, and/or the nonwoven fabric is formed into
a filter, such as an air filter for removing particulates from the air; or a face
mask; or a HEPA filter; or a filter having a MERV rating of at least 8; or a filter
having a MERV rating of at least 10; or a filter having a MERV rating of at least
14; or a filter having a MERV rating to at least 16.
[0075] In an embodiment herein, the splittable fiber, the split fiber, the multicomponent
fiber, the multicomponent staple fiber, and/or the nonwoven fabric is formed into
a filter; or an air filter; or a vehicle air filter; or an automotive engine air filter,
an automotive cabin air filter, an HVAC air filter, a face mask/respirator filter;
and a combination thereof; or a cigarette filter. In an embodiment herein, the splittable
fiber, the split fiber, the multicomponent fiber, the multicomponent staple fiber,
and/or the nonwoven fabric is formed into an insulator; or a heat insulator; or a
sound insulator; or a thermal insulator. In an embodiment herein, the splittable fiber,
the split fiber, the multicomponent staple fiber, and/or the multicomponent fiber
is included or formed into a spun yarn. In an embodiment herein, the splittable fiber,
the split fiber, the multicomponent fiber, the multicomponent staple fiber, and/or
the nonwoven fabric is included in a wipe.
TESTING PROCEDURES AND EQUIPMENT:
[0076] The TSI 8130A automated filter tester (see: https://www.tsi.com/products/filter-testers/automated-filter-tester-8130a/
by TSI Incorporated, Shoreview, Minnesota, USA) can be used to test the filtration
efficiency herein. The TSI 8130A creates 0.3µ particles which are injected into an
airstream and passed through a filter sample. See: https://youtu.be/HSngoNqKXvI, which
shows how the filter tester works. The 0.3 µ particles are measured both upstream
and downstream of the filter sample. As charge (or lack thereof) greatly impacts such
small particles, it this device and the associated test can easily show whether the
filter sample has an electret charge and/or show its efficiency as measured in % penetration.
The % penetration is calculated as: (downstream particle concentration) / (upstream
particle concentration) × 100.
[0077] A high % penetration indicates low filtration efficiency - i.e., many particles are
passing through the filter. Conversely, a low % penetration indicates a high filtration
efficiency where many particles are caught and held by the filter. As the particles
build up on the filter sample, the filter tester continuously monitors the flow rate
and the resulting pressure drop across the filter.
[0078] All MERV tests herein are conducted according to ASHRAE MERV Standard 52.2-2017 from
the American Society of Heating, Refrigerating and Air-Conditioning Engineers (ASHRAE),
hereby incorporated by reference in its entirety, available from the ASHRAE website
at: https://ashrae.iwrapper.com/ASHRAE_PREVIEW_ONLY_STANDARDS/STD_52.2_2017.
[0079] The TOPAS Flat Sheet Filter Media Test System (Model # AFC132; "TOPAS") quickly tests
small discs of filter media according to the ASHRAE Standard 52.2-2017, hereby incorporated
by reference in its entirety. TOPAS has proprietary software that creates potassium
chloride particles from 0.3 microns to 10.0 microns in diameter. The horizontal duct
holds the sample and challenges the media per the ASHRAE Standard 52.2-2017 at the
filter design velocity (Residential furnace filters are 110 fpm). Upstream and downstream
particle counters determine the size and number of particles which are trapped and
pass through the media giving each particle range (E1 0.3 - 1 micron, E2 1.0 - 3 micron,
E3 3.0 - 10 micron) and correlating the efficiency in each group with the ASHRAE Standard
52.2 MERV rating chart.
[0080] Although flat sheet accuracy is reasonably close to that of a pleated filter, the
dynamics of air flow, size of actual filter, pleat geometry etc. can have small effects
on the filter performance vs. a flat sheet. See below comparison of flat sheet data
to outside test lab of full filter. Resistance is nearly doubled due to this filter
being a wire back design where the wire holds the pleat form but also adds resistance
because of the blind area of the metal mesh. The filter frame also reduces the available
media exposed to flow causing the TOPAS design to result in a slightly higher velocity
than the flat sheet test per ASHRAE Standard 52.2:
Sample Description |
IR (in w.g.) |
E1 |
E2 |
E3 |
MERV |
Velocity fpm |
Flat sheet |
0.20 |
32.2 |
65.5 |
91.3 |
11 |
110 |
Filter |
0.40 |
21.8 |
71 |
93 |
11 |
113 |
IR = Initial resistance
in w.g. = inches water gauge
fpm = feet per minute (1 fpm = 1828.8 cm/min) |
[0081] Calculating the Area of a Pleated Filter:
Width in inches |
Pleat height (in inches) |
Please count |
Pleat Length (in feet) |
Pleated area (in sq. inches) |
Pleated area (in square feet) |
Volumetric air flow (in CFM) |
Volumetric Air Flow Rate (in cubic meters/hour) |
Media Velocity (in feet/min) |
Media Velocity (in cm/sec) |
23.75 |
0.9 |
35 |
5.51 |
1571.06 |
10.91 |
1968 |
3343.65 |
180.38 |
91.63 |
23.75 |
1.75 |
29 |
8.88 |
2531.16 |
17.58 |
1968 |
3343.65 |
111.96 |
56.88 |
[0082] The SIMCO-ION Electrostatic Fieldmeter (specifically model # FMX-003) is a commercially-available
(see: https://www.simco-ion.com/) fieldmeter which measures the static charge of a
material such as a fiber, a nonwoven fabric, etc.
[0083] In an embodiment herein, the split distribution of the splittable fiber (and/or the
multicompoenent splittable fiber, the multicomponent splittable staple fiber, the
nonwoven fabric, etc.) is determined with a Braunauer-Emmett-Teller (BET) test (see,
for example, https://en.wikipedia.org/wiki/BET_theory) according to ISO 9277:2010
"Determination of the specific surface area of solids by gas absorption - BET method"
(see, https://www.iso.org/standard/44941.html), hereby incorporated by reference in
its entirety. The BET test measures the physical absorption of gas molecules onto
the fiber (or sub-fiber) surface and therefore an increase in the BET test indicates
an increase in surface area which corresponds to a higher split distribution/more
splitting of the splittable fiber into sub-fibers as compared to a sample which does
not contain split fibers.
[0084] That being said, it is recognized that the BET test only measures the total surface
area (increase) and does not specifically distinguish between, for example, a single
fiber which is split entirely into sub-fibers, and a plurality of fibers that are
split only once to give the same total surface area.
[0085] In an embodiment herein, the splittable fiber; or the multicompoenent splittable
fiber; or the multicomponent splittable staple fiber; or the nonwoven fabric, herein
possess a surface area after splitting; or after carding, of from about 115% to about
800%; or from about 125% to about 700%; or from about 135% to about 650%; or from
about 150% to about 600% of the surface area of a comparable sample; or of substantially
the same sample, before splitting; or carding. In an embodiment wherein the splittable
fiber constitutes about 50% of the total fiber mass, then the splittable fiber; or
the multicompoenent splittable fiber; or the multicomponent splittable staple fiber;
or the nonwoven fabric, herein possess a surface area after splitting; or after carding,
of from about 115% to about 400%; or from about 125% to about 350%; or from about
135% to about 325%; or from about 150% to about 300% of the surface area of a comparable
sample; or of substantially the same sample, before splitting; or carding.
[0086] In an embodiment herein, the split distribution of the splittable fiber (and/or the
multicompoenent splittable fiber, the multicomponent splittable staple fiber, the
nonwoven fabric, etc.) is determined with a Micronaire test (MIC) which is a Cotton
industry standard measurement of a sample's air permeability and is used as an indication
of fiber fineness and maturity (see, https://barnhardtcotton.net/blog/what-is-a-micronaire-in-cotton-and-why-does-it-matter/
and also https://www.cotton.org/journal/2005-09/2/upload/jcs09-081.pdf), all hereby
incorporated by reference in their entireties. The MIC may be measured via, for example,
the Uster
® HVI 1000 (https://www.uster.com/en/instruments/cotton-classing/uster-hvi-2/), available
from Uster Technologies AG, Sonnenbergstrasse 10, CH-8610 Uster, Switzerland. When
comparing a sample containing unsplit fibers with a sample containing split fibers,
the sample containing split fibers should have a higher air resistance. Thus, for
a single (or otherwise substantially identical) sample, measuring the MIC before and
after splitting (for example, before and after carding) would indicate whether or
not the splittable fiber(s) have actually split, and provide an indication of the
split distribution.
[0087] The scaling of a Micronaire instrument is by gauging known fiber sizes over a range
of 0.2 denier (100% opened fibers) to 3 denier (100% un-opened fibers). The scale
is accentually aligned with known fiber sizes across the expected range of opening
to determine a 0% - 100% scale. Once the scale is established, then a nonwoven fabric
sample containing splittable fibers having an original known denier can be tested
both before and after splitting to determine the split distribution.
[0088] In an embodiment herein, the split distribution of the splittable fiber (and/or the
multicompoenent splittable fiber, the multicomponent splittable staple fiber, the
nonwoven fabric, etc.) is determined via visual and/or computer analysis of, for example,
one or more scanning electron micrographs (SEMs). In such a method, identical; or
substantially identical, samples may be compared before and after the splitting step
(for example, by carding), to determine the split distribution.
[0089] In an embodiment herein, the split distribution is characterized by analyzing scanning
electron micrographs (SEMs) to estimate and/or calculate the split distribution. SEMs
may also be used herein to estimate/calculate the increase in surface area after splitting;
or carding. It is recognized herein that counting microfibers and sub-fibers in a
SEM image has one advantage over counting them in a cross section image, in that there
is no ambiguity introduced by splitting that might occur in cutting the fiber for
the cross section image. However, the cross section image also has an advantage over
the SEM, which is that in the cross section image there is no uncertainty whether
a microfiber comprises one, two, or three segments, or 7, 8, or 9 segments, etc. In
an SEM image, even discerning between fibers that might comprise 3, 4, or 5 segments
from those that might contain 6, 7, or 8 segments, for instance, is also a difficult
judgment call. For this reason, counting the split and unsplit fibers in a cross section
image is more reliable than counting fibers in an SEM image.
EXAMPLE 1
[0090] Control media is formed from 100% 3 dpf (denier per fiber) fibers. Splittable fibers
according to the invention of the same (initial) size are formed into a nonwoven web
and then split into a nonwoven fabric containing split fibers. This nonwoven fabric
is formed into a comparable filter, and then charged and left uncharged. All three
structures are the same. The MERV test is conducted according to ASHRAE MERV Standard
52.2-2017 and the data recorded below.
Sample Description |
BW (gsy) |
Thickness (mils) |
Air Perm (CFM) |
IR (PA) |
IR (in w.g.) |
E1 |
E2 |
E3 |
MERV |
Velocity fpm |
Control |
98.1 |
48.6 |
280.4 |
40 |
0.16 |
-0.6 |
26.6 |
79.9 |
8 |
110 |
Uncharged Split fibers |
99.2 |
43.6 |
167.6 |
82 |
0.33 |
16.9 |
56.3 |
85.4 |
10 |
110 |
Charged Split fibers |
99.2 |
43.6 |
167.6 |
73 |
0.29 |
59.8 |
82.1 |
95.6 |
12 |
110 |
BW = basis weight
gsy = grams per square yard [1 gsy X 1.196 = GSM (grams per square meter)]
Air perm = air permeability]
CFM = cubic feet per minute as measured by Frazier Precision Instrument per ASTM D737
(1
CFM = 28.32 liters per minute)
IR = Initial resistance
PA = Pascals
in w.g. = inches water gauge
fpm = feet per minute (1 fpm = 30.48cm/min) |
[0091] From the above it can be seen that the uncharged split fiber sample increases in
efficiency for E1, E2 and E3 as compared to the control sample. The charged split
fiber sample increases in efficiency E1, E2, and E3 with respect to both the control
sample and the uncharged split fiber sample. The control sample achieves a rating
of MERV 8, while the uncharged split fiber sample achieves a rating of MERV 10, and
the charged split fiber sample achieves a rating of MERV 12. In addition, the lower
CFM of the split fiber samples also indicates an increased surface area compared to
the control due to fibers due to the splitting.
EXAMPLE 2
[0092] A commercially available nano fiber-based media from Next Nano (Product Number NP048.
Web Address: https://nxtnano.com/products/hvac/) is purchased. Nano fiber-based filtration
media are typically fibers less than 200 nano meters (nm) in diameter and are not
typically charged. The pure physical filtration (through sieving) does not allow for
depth filtration and larger particles can build up on the surface of the media causing
premature high resistance. Nano fiber-based filtration media are also to be used for
a typical residential furnace filter. Below is an internal flat sheet test of such
media compared to the invention which uses depth filtration, physical filtration and
electro statics to balance the filtration media allowing adequate filtration.
Sample |
IR (in w.g) |
E1 |
E2 |
E3 |
MERV |
Velocity fpm |
Velocity m3/hr |
Next Nano |
0.26 |
45.0 |
78.8 |
97.1 |
12 |
110 |
35.4 |
Invention |
0.29 |
59.8 |
82.1 |
95.6 |
12 |
110 |
35.4 |
IR = Initial resistance
in w.g. = inches water gauge
fpm = feet per minute (1 fpm = 30.48 cm/min) |
[0093] As can be seen the present invention provides similar measurements as the Next Nano
sheet; however, in a different technical manner.
EXAMPLE 3
[0094] In an embodiment herein, nonwoven fabric samples with various split distributions
are compared.
[0095] Control Sample is a nonwoven fabric containing 100% nonsplittable fibers (3 dpf)
is measured by the BET test, and compared to Samples 1-3. The Control Sample is not
carded.
[0096] Sample 1 contains, by weight, 50% nonsplittable fibers and 50% splittable fibers.
Both the splittable fibers and the nonsplittable fibers are initially of the same
denier (3 dpf) as the control sample and thus the fabric sample (prior to splitting)
is essentially identical to the Control Sample. Sample 1 is then "slightly" carded
in order to split the splittable fibers into sub-fibers.
[0097] Sample 2 is essentially identical to Sample 1, except that Sample 2 is "normally"
carded to split the splittable fibers into sub-fibers.
[0098] Sample 3 is essentially identical to Sample 2, except that Sample 3 contains a charge-enhancing
additive is added to the splittable fiber and Sample 3 is charged via Corona Charging.
Without intending to be limited by theory it is believed that the significant increase
in surface area between Sample 3 and Sample 2 is due to the charged fibers repelling
each other and thereby increasing the overall surface area.
[0099] The BET test results for these samples are show in the table below.
Sample |
BET test surface area measurement (square meters surface area / gram of sample) |
Surface area after carding (as % of Control) |
Control Sample |
0.145 |
100 |
Sample 1 |
0.209 |
144 |
Sample 2 |
0.267 |
184 |
Sample 3 |
0.303 |
209 |
[0100] Accordingly, it can be seen that carding significantly increases the surface area
of the samples according to the present invention with a surface are ranging from
144% to 209% of the Control Sample which is substantially the same as the Samples
before splitting.
EXAMPLE 4
[0101] In an embodiment of the present invention a conventional charge is applied to the
formed nonwoven fabric after a thermal bonding process. The charge polarity is negative
30Kv @ 2.5 mA but can range from 0.5 KV @ 1 mA to 50Kv @ 3.0 mA. A SIMCO-ION FMX-003
Electrostatic Fieldmeter is used to measure the charge after the formation to the
nonwoven fabric and before electret charging. The same electrostatic fieldmeter is
used to measure the charge after electret charging and the results are shown below.
Sample |
Charge (in kV) |
Nonwoven fabric before charging |
0.0 |
Nonwoven web after charging |
-7.7 kV |
[0102] Charge retention is a function of applied voltage, dwell time under the applicator
bar (i.e., line speed in a continuous process), fiber density (surface area and basis
weight), base fiber polymer, charge-enhancing additives and atmospheric conditions.
[0103] It should be understood that the above only illustrates and describes examples whereby
the present invention may be carried out, and that modifications and/or alterations
may be made thereto without departing from the spirit of the invention.
[0104] It should also be understood that certain features of the invention, which are, for
clarity, described in the context of separate embodiments, may also be provided in
combination in a single embodiment. Conversely, various features of the invention
which are, for brevity, described in the context of a single embodiment, may also
be provided separately, or in any suitable subcombination.
[0105] All references specifically cited herein are hereby specifically incorporated by
reference in their entireties. However, the citation or incorporation of such a reference
is not necessarily an admission as to its appropriateness, citability, and/or availability
as prior art to/against the present invention.