BACKGROUND OF THE INVENTION
[0001] The invention relates generally to hygroscopic wicks and, more particularly, to bicomponent
fiber wicks that may be adapted for transmitting analyte fluids in assay devices.
[0002] Various assay devices are known for use in the home, office, clinic, hospital or
doctor's surgery for providing an analytical result which is rapid and which requires
a minimal degree of skill and involvement by the user. Examples of this are the test
devices or assays for pregnancy and fertile period (ovulation). Typically in such
devices the number of operations in getting the results should be minimized.
[0003] Typical assay devices comprise a housing, a reaction medium positioned in the housing,
upon which the assay chemistry occurs, and a wick for collecting the liquid to be
assayed and transferring it to the reaction medium. In general, the assay device should
merely require that a collection portion of the device be contacted with a sample
(e.g., a urine sample for pregnancy testing), and thereafter no further user actions
are required. The sample is carried from the collection portion to the reaction medium
via the wick. Observation of changes to the reaction medium or a substrate carrying
the reaction medium provide an analytical result. Ideally, the analytical result should
be observable within a matter of minutes following sampling.
[0004] The actual analytic techniques used to obtain the results typically determine the
presence or absence of and/or quantify the amount of various analytes in tissues and
fluids of organisms. Currently most diagnostic testing is done with blood, urine,
fecal material, saliva, or tissue biopsy. Testing based on these materials, however,
entails substantial invasion of privacy and poses a significant safety hazard (particularly
with the testing of blood). Improved assay devices are required that allow for greater
speed and control of the transport and analysis of the fluid sample. These devices
will depend on improved wick materials and structures.
[0005] The present invention provides wicks that make use of bicomponent fibers in which
at least one of the fiber components a polyamide material. An illustrative aspect
of the invention provides a bicomponent fiber wick for use in processing an analyte
fluid. The bicomponent fiber wick comprises a self-sustaining, fluid transmissive
body comprising a plurality of bundled, crimped, continious bicomponent fibers bonded
to each other at spaced apart contact points. Each bicomponent fiber has a fiber structure
comprising a first fiber component formed from a polyamide material and a second fiber
component. The fibers collectively define tortuous fluid flow paths through the fluid
transmissive body, the fiber structure being configured for controlling flow of the
analyte fluid through the fluid transmissive body with at least a portion of the first
fiber component in contact with the analyte fluid.
[0006] The invention can be more fully understood by reading the following detailed description
together with the accompanying drawing, in which like reference indicators are used
to designate like elements, and in which:
[0007] Figure 1 is a flow diagram of a process for manufacturing a bicomponent fiber wick
according to an embodiment of the invention:
[0008] Figure 2 is a cross-sectional view of a sheath-core bicomponent fiber that may be
used in embodiments of the invention; and
[0009] Figure 3 is a nOL-to-scale perspective view of a bicomponent fiber wick according
to an embodiment of the invention.
[0010] The present invention provides bicomponent fiber wicks that are particularly adapted
for use in devices requiring rapid, controlled transport of fluids. They are particularly
adaptable for use in assay devices requiring transport of analyte fluids. As used
herein the term analyte fluid means a fluid sample that is to be analyzed for the
presence of one or more analytes in the fluid sample and/or to quantify the amount
of one or more analytes present in the fluid sample.
[0011] The wicks of the present invention are formed from bicomponent fibers the structure
and material constituents of which may be tailored to provide specific fluid transport
properties for particular analytes and analyte fluids.
[0012] Bicomponent fibers have been used to some extent in wicks and medical assay devices.
Most prior art assay devices, however, are constructed from low cost mono-component
fibers formed from such materials as low density polyethylene (LDPE), polypropylene(PP)
high density polyethylene (HDPE), ultra-high molecular weight polyethylene (UHMW),
polypropylene (PP), polyvinylidene fluoride (PVDF), polytetrafluoroethylene (PTFE),
polyester, and polyethersulfone (PES). It has generally been found that certain materials
such as nylon 6 may be usable and, in fact may be desirable for their natural hydrophilic
behavior. However, the use of nylon materials have not been favored in such mono-component
applications in part due to their cost. It has also been found that non-woven hydrophilic
structures formed from nylon are often not self-sustaining. Further, nylon processing
often requires additional procedures to avoid inadvertent moisture absorption by the
nylon fibers. In some instances, this may require a dedicated drying process. Finally,
the physical and mechanical properties of spun nylon fibers are subject to changes
over time (aging effects).
[0013] The more typical, less expensive polymers such as polyolefins and polyesters that
are presently used to form assay device wicks have two disadvantages: (1) They often
require an additional material such as a surfactant in order to provide adequate fluid
transfer performance; and (2) unless functionalized, derivatized or modified, they
do not provide a reactive platform for other additives. As a result of these deficiencies,
the potential use of nylon as a naturally hydrophilic wick material was investigated.
The wick embodiments of the present invention make use of bicomponent fibers with
natural hydrophilic properties due to the use of polyamide materials in the fiber
structure. The structure of these fibers are adapted to provide an optimum polyamide
material amount while maintaining the desired flow characteristics for the final wick
product.
[0014] The use of bicomponent fibers in hydrophilic structures, generally, is well known
in the art. For example,
U.S. Pat. No. 5,607,766 issued Mar. 4, 1997,
U.S. Pat. No. 5,620,641 issued Apr. 15, 1997, and
U.S. Pat. No. 5,633,082 issued May 27, 1997 disclose the manufacture and use of bicomponent fibers comprising a core of a thermoplastic
material covered by a sheath of polyethylene terephthalate. These patents note that
such fibers are particularly useful in the production of elongated, highly porous
elements such as in the wicks used to transport bodily fluids to a test site in a
diagnostic device.
US-A-2002/0193030 and
EP-A-0171807 are disclosing bicomponent fiber wicks having a polyamide-based component.
[0015] The wick embodiments of the present invention are self-sustaining structures formed
from such fibers. The term "bicomponent" as used herein refers to the use of two polymers
of different chemical nature placed in discrete cross-sectional areas of a fiber structure.
The two polymers are arranged in substantially constantly positioned distinct zones
across the cross-section of the bicomponent fibers that extend continuously along
the length of the bicomponent fibers. While other forms of bicomponent fibers are
possible, the more common bicomponent fiber types are of the "side-by-side" and "sheath-core"
types. The first type is so-named because the two polymer materials literally form
a side-by-side cross-sectional configuration. In "sheath-core" bicomponent fibers,
a sheath of one polymer material is spun to completely cover and encompass a core
of another polymer material, typically a low shrinkage, high strength thermoplastic
polymeric material.
[0016] The wick structures of the present invention may be formed from either side-by-side
or sheath-core bicomponent fibers that include at least one polyamide fiber component.
The polyamide fiber component may be selected from the group consisting of nylon 6,
nylon 6,6, nylon 4, nylon 610, nylon 11, and nylon 12, or copolymers of any of the
various nylons with hydrophilic moieties, such as polyethylene glycol and/or poly(ethylene
oxide) diamines. In some instances, both bicomponent fiber components may be polyamides
selected from the group listed above.
[0017] The polymer or polymers of the second fiber component may depend on the bicomponent
fiber type. In side-by-side fibers, a first fiber component may be formed from a polyamide
material and a second fiber component may be formed from a material selected from
a group including but not limited to polyolefins, polyesters, polyamides, polysulfones,
etc. In sheath-core fibers, the sheath component may be formed from a polyamide material
while the core component may be formed from a thermoplastic polymer material selected
from a group including but not limited to polyamides (such as nylon 6, nylon 6,6 and
other nylons) polyesters (such as polyethylene terephthalate, polybutylene terephthalate,
polypropylene terephthalate and polylactic acid) and polyolefins (such as syndiotactic,
isotactic polypropylene and polyethylene).
[0018] It will be noted from the above that both side-by-side and sheath-core bicomponent
fiber types may have a first component of one polyamide material and a second component
of a another polyamide material. Thus, wick embodiments of the invention could, for
example, be formed from sheath-core fibers having a core component of nylon 6 and
a sheath component of nylon 6,6.
[0019] As will be discussed in more detail hereafter, it has been found that the fiber material
content and the fiber structure of both sheath-core and side-by-side fiber types has
a significant impact on certain properties of the final wick product. It has also
been found that fiber material content and fiber structure may be selected to provide
desired wick properties and, in fact, may be optimized based on various design criteria.
[0020] The bicomponent fibers used in embodiments of the invention may be produced by a
number of common techniques. Among such techniques are conventional melt spinning
processes in which molten polymer is pumped under pressure to a spinning head and
extruded from spinneret orifices into a multiplicity of continuous fibers. Melt spinning
is only available for polymers having a melting point temperature less than its decomposition
temperature, such as nylon, polypropylene and the like, whereby the polymer material
can be melted and extruded to fiber form without decomposing. Other polymers, such
as acrylics, cannot be melted without blackening and decomposing. Such polymers can
be dissolved in a suitable solvent (e.g., acetate in acetone) of typically 20% polymer
and 80% solvent. In a wet spinning process, the solution is pumped at room temperature
through the spinneret, which is submerged in a bath of liquid (e.g., water) in which
the solvent is soluble to solidify the polymeric fibers. It is also possible to dry
spin the fibers into hot air, rather than a liquid bath, to evaporate the solvent
and form a skin on the fiber surface. Other common spinning techniques may also be
used.
[0021] After spinning, the fibers are commonly attenuated by withdrawing them from the spinning
device at a speed faster than the extrusion speed. The fibers may be attenuated by
taking them up on nip rolls rotating at a speed faster than the rate of extrusion
or between nip rolls operating at different speeds. Depending on the nature of the
polymer, drawing the fibers in this manner can make them stronger by making them more
crystalline.
[0022] Attenuation can also be effected through the use of a melt blowing process. In this
process, the fibers are attenuated by contacting them with a fluid such as high velocity
air as they emanate from the spinneret orifices. The effect of the fluid is to draw
the fibers into fine filaments. These filaments may be collected as an entangled web
of fibers on a continuously moving surface such as a conveyor belt or a drum surface,
for subsequent processing. This process, known as "melt blowing," is of particular
commercial importance in the production of many products because of its ability to
attenuate the fibers while they are still molten.
[0023] Any of the above processes may be used to produce bicomponent fibers for use in wicks
of the present invention. It will be understood by those of ordinary skill in the
art that the actual process used for a given fiber may depend on the fiber components
and configuration. Regardless of the manner of forming the bicomponent fibers, they
are subsequently gathered together and passed through one or more processing stations
in which the fibers are bonded and formed to produce a continuous, self-sustaining,
porous wick element of constant cross-section.
[0024] The wick element may then be further treated and/or divided into individual wick
elements, each wick element being a self-sustaining structure formed as a network
of continuous, bonded fibers. This network of fibers provides a tortuous interstitial
path for passage of fluids by capillary action and for interstitial entrapment of
loaded substances and/or substances entrained in fluids passing therethrough.
[0025] With reference to Figure 1, a manufacturing process for forming bicomponent fiber
wick elements according to an embodiment of the invention will now be discussed in
more detail. The process begins at S 100 and at S110, a plurality of bicomponent fibers
having at least one polyamide fiber component are provided. Individual fibers are
typically provided on separate bobbins from which they may be drawn through a feed
roll. The fibers may alternatively be provided as a tow, or as a melt blown, spun
bond, or combination non-woven roving. At S120, the fibers may be drawn through a
temperature and humidity controlled draw box where the fibers are heated and stretched
using a predetermined draw ratio. In an illustrative embodiment, the predetermined
draw ratio may be in a range of about 1.5 to 1 to about 6 to 1 and is preferably in
a range of about 2.5 to 1 to about 3.5 to 1.
[0026] At S 130, a crimp may be established in the fibers. Prior to crimping, the gathered
fibers form a plurality of continuous, linear fiber elements. Crimping the fibers
causes them to become multidimensional and has the effect of increasing the bulk and
loft of the final wick product. Moreover, crimping increases the uniformity of the
wick body structure and, in particular, the capillaries that make up the tortuous
fluid paths through the wick product. Crimping may be accomplished by mechanical means
or, with certain bicomponent fiber configurations, by inducing a self-crimping action.
Mechanical crimping can be applied to any fiber type and tends to produce a zigzag
or sawtooth-shaped pattern as viewed from the side and/or from above the fiber. Any
suitable mechanical crimping process may be used in the practice of the present invention.
[0027] Self-crimping fibers are generally bicomponent fibers in which the two fiber components
have different shrinkage/expansion characteristics. Usually, one of the fiber components
(typically the core component in sheath-core fibers) has a higher melt temperature,
lower shrinkage and higher strength than the second component. When a self-crimping
fiber is heated and then allowed to relax, the difference in behavior of the two components
causes the fiber to deform, or crimp, in a predictable manner. Through selection of
the component materials and the cross-sectional geometry of the two fiber components,
a desired three-dimensional deformation may be introduced.
[0028] In both side-by-side and sheath-core bicomponent fibers, the self-crimping action
of the fiber will be affected by the materials used in the fiber components and by
the relative cross-sectional areas of the two components. A cross-section of a particularly
preferred form of self-crimping fiber is illustrated in Figure 2. As shown, the fiber
10 is a sheath-core fiber in which the cross-sections of the core component 12 and
the sheath component 14 are both substantially circular (with outer radii R
1 and R
2, respectively) but are not concentric. Such fibers may be referred to as eccentric
sheath-core fibers. The eccentricity of the fiber may be defined as the ratio of the
offset X between the centers of the two components and the outer radius of the fiber,
which is equal to the outer radius R
1 of the sheath component. The degree of eccentricity and the relative cross-sectional
areas of the two components may be varied to change the degree of deformation when
the fibers are allowed to crimp. Fibers used in the wicks of the present invention
typically have an eccentricity in a range from about 0.1 to about 0.5.
[0029] If self-crimping fibers are used in the process of Figure 1, the action of establishing
crimps in the gathered fibers may include passing the fibers through a drawing section
to stretch the fibers and then through the turbulent region of an air jet where they
are allowed to relax and take on a typical self-crimped fiber pattern. This multi-dimensional
fiber deformation results in intermingling of the gathered fibers, which is desirable
in the downstream formation of a self-sustaining wick.
[0030] At S 140, the intermingled, crimped fibers are drawn through an oven or other heating
device in which the temperature is at or near the melt temperature of at least one
of the two fiber components. In a preferred embodiment in which the fiber is a sheath-core
fiber, the oven temperature is set at or near the melt temperature of the polyamide
sheath material to at least partially melt the sheath material. The environment within
the oven is carefully controlled to assure even heating of the fibers. At S 150, the
intermingled fibers are drawn through a heated sizing die, which causes the intermingled,
crimped fibers to make contact with one another at various spaced-apart points along
the length of the melted fiber component. Upon cooling at S160, the fibers remain
bonded at these contact points, thereby producing a self-sustaining fiber structure.
The fibers may be allowed to cool under ambient conditions or may be cooled by passing
the drawn fiber structure through a subsequent cooling die, by applying chilled air,
or by applying a cooler fluid, depending on the specifics of the process. In a preferred
embodiment in which the fibers are sheath-core fibers, the fiber structure bonds are
formed at various interspersed points along the polyamide sheath portions of the fibers.
[0031] At this point in the process, the crimped bicomponent fibers have been formed into
a continuous wick body structure. Though typically rectangular, it will be understood
that the cross-section of the continuous wick body may be of any geometric shape.
The continuous wick body structure may be cut into desired lengths to form discrete
wick bodies at S170. An exemplary final product wick 100 is represented in Figure
3 (not to scale). The wick 100 has a rectangular fluid transmissive wick body 110
formed from generally aligned but three dimensionally intermingled, bonded, crimped,
bicomponent fibers 120. The process ends at S190.
[0032] In some instances, it may be desirable that the final wick product be loaded or coated
with an additive material. Typical additive materials may include, for example, blocking
agents, surfactants and reactive agents. Additives may be incorporated by coating
or immersing the wick body structure with an additive solution before or after cutting.
In a particular embodiment, a pump may be used to apply an additive in a solution
to the formed wick element. The amount of an additive applied to the wick may be controlled
through the concentration of the additive in the solution, the pump rate and the speed
of the wick through the solution. A stripping die may be used to remove excess additives.
The wick structure may then be dewatered by means generally known in the art.
[0033] Like all wick embodiments of the invention, the final product of the method described
above is a self-sustaining network of bonded bicomponent fibers. This network defines
a tortuous flow path for passage of fluids through the wick. As is known, a structure
so-formed may provide a means of transporting a fluid with no flow impetus other than
capillary action. The degree of capillary action, and thus, the flow rate for a given
fluid is determined by the degree of surface energy at the boundaries of the interstitial
capillaries through the fiber structure. Absent the use of enhancing additives such
as surfactants, capillary surface energy will be determined by the polymer materials
used in the fibers. The overall fluid transfer performance of the wick may also be
affected by the uniformity of the intermingled fiber structure established by crimping
the fibers.
[0034] As previously noted, polyamide materials--and in particular, nylon--are naturally
hydrophilic (i.e., have a naturally high surface energy when compared to other common
fiber forming materials such as polyolefins and polyesters). Accordingly, it can be
seen that the use of nylon fiber components in wick structures can provide relatively
high fluid flow rates without the use of enhancing additives. In the bicomponent fiber
structures of the present invention, at least some of the exposed fiber surfaces that
form capillary boundaries are provided by the polyamide fiber component of the bicomponent
fibers. In wicks formed from sheath-core fibers with polyamide sheath components and
wicks formed from side-by-side fibers having both components formed from polyamide
materials, all of the exposed surfaces are provided by polyamides. In wicks formed
from side-by-side fibers in which only one fiber component is a polyamide, the degree
of natural capillary flow potential may be determined by the relative surface area
presented by the polyamide component as compared to the surface area presented by
the non-polyamide component.
[0035] It can thus be seen that the wick structures of the invention can provide a high
degree of fluid flow potential. It can also be seen that, in embodiments incorporating
sheath-core fiber types, the degree of flow potential is essentially independent of
the volume of polyamide in the fiber sheath, as long as a sufficient fiber surface
area of nylon is maintained. Accordingly, the amount of the polyamide material in
the fiber may be minimized relative to a less expensive core material. Thus, the sheath-core
fiber configuration can provide a significant advantage in that all of the exposed
fiber surface may be established by a nylon sheath that forms only a fraction of the
total fiber material. If surface energy were the only consideration, the wick fibers
could be formed with the minimum polyamide material required for complete coverage
of the core component.
[0036] There are, however, other considerations in selecting the amount and configuration
of the polyamide fiber component. For example, for a given polyamide material, the
ability of the bicomponent fibers to bond to form the self-sustaining wick bodies
of the invention may be related to the amount of polyamide material used. This is
particularly true for sheath-core fibers having a polyamide sheath. Also, as previously
discussed, the use of crimped fibers and, in particular, self-crimped fibers, affects
the flow transport properties of the wick because of its effect on uniformity of the
bonded fiber structure and the tortuous flow paths formed thereby. As noted above,
the crimping behavior of self-crimping fibers is generally a function, not only of
the relative expansion (or contraction) behavior of the two fiber components, but
also of the relative cross-sectional areas--and thus, the relative material amounts--of
those components.
[0037] As a result, there may be, in some circumstances, an incentive to increase the amount
of polyamide material in the bicomponent fiber beyond the minimum required to produce
a particular polyamide material surface area. The amount of polyamide material used
may thus be based on multiple design constraints including parameters based on surface
energy requirements, structural uniformity and bondability. However, there is also
likely to be a desire to minimize the amount of polyamide material required to meet
these constraints. The present invention provides for tailoring the fiber geometry
to meet one or more of these design criteria.
[0038] For a given polyamide material and fiber type, the flow surface area is essentially
determined by the required fluid transfer performance. The remaining performance parameters
may be related to the polyamide component ratio of the bicomponent fibers. As used
herein, the term "polyamide component ratio" means the ratio of the weight per unit
length (or volume) of polyamide material providing a polyamide surface for the capillaries
of the wick to the overall weight per unit length (or volume) of the bicomponent fiber.
It can be readily seen that in bicomponent fibers having a polyamide first fiber component
and a non-polyamide second fiber component, the polyamide component ratio will be
the ratio of the first component weight per unit length divided by the overall fiber
weight per unit length. It can also be readily seen that a bicomponent fiber having
a given polyamide sheath material and having a high polyamide component ratio may
have a degree of surface energy and bondability but may also have a relatively high
cost due to the high percentage of polyamide material. On the other hand, a fiber
with a low polyamide component ratio may have a lower cost but may have bonding problems
and may not provide a sufficient polyamide surface area. It should be noted that because
some bicomponent fibers may have both components formed from polyamide materials,
the polyamide component ratio may be as high as 1.0.
[0039] For a given bicomponent fiber type, the actual cross-sectional geometry of the fiber
may be determined from a combination of the polyamide surface area requirements and
the polyamide component ratio. If a self-crimping fiber is used, the crimping behavior
may also be factored in.
[0040] Based on the above, it can be seen that a bicomponent fiber wick of the present invention
may be optimally tailored for a particular combination of wick performance properties.
The fluid transmissive body of the bicomponent fiber wick may be formed from a plurality
of bicomponent fibers bonded to each other at spaced apart contact points. As in all
the wicks of the invention, the fibers collectively define tortuous three dimensional
fluid flow paths through the wick body. The bicomponent fibers have a fiber structure
comprising first and second fiber components each having discrete cross-sectional
areas extending continuously along the length of the bicomponent fiber. The fiber
includes at least one polyamide material. Typically, the fiber will have a first component
formed from polyamide material and a second component that is not, although in some
embodiments, the second component may also be a polyamide material having different
properties from the polyamide of the first component. The bicomponent fiber geometry
may be specifically adapted to provide a polyamide component ratio that provides a
final wick structure adapted to meet predetermined design requirements.
[0041] Although there may be some variation depending on the particular polyamide material
being used, it has been determined that acceptable wicks may be produced from crimped
bicomponent fibers having a polyamide component ratio in a range of about 0.10 to
about 0.50. In a preferred embodiment, wicks may be produced from crimped bicomponent
fibers having a polyamide component ratio in a range of about 0.20 to about 0.35.
In a most preferred embodiment, wicks may be produced from crimped bicomponent fibers
having a polyamide component ratio in a range of about 0.25 to about 0.30.
EXAMPLE
[0042] Wick structures were successfully formed from bicomponent fibers having different
polyamide content levels and geometries. The processing methods previously discussed
were used to produce wicks from self-crimped sheath-core bicomponent fibers in which
the core fiber component was polyethylene terephthalate (Dupont 4441) and the sheath
fiber component was nylon 6 (Ultramid BASF BS403N). The fibers were formed using conventional
bicomponent melt spinning techniques using a spin pack with 288 individual filaments.
The filaments were spun to 25 dpf (denier per filament) and individual packages were
creeled to provide a final wick product of sufficient density. The collected yarns
were drawn at a 3.5 draw ratio at 150-160°C to induce a self-crimped fiber structure.
The yarns were then passed through an oven at 200-235°C and drawn through a heated
die to form a self-sustaining wick structure having a 2.45 mm by 11.5 mm rectangular
cross-section. The continuous wick structure was then cut in 44 mm lengths.
[0043] Two sets of wicks were produced, both having an outer fiber diameter of 38 microns.
In the first set, the wick fibers were formed with a core diameter of 29.4 microns
and an eccentricity of 0.45, in order to produce a polyamide component ratio of 0.40.
In the second set, the wick fibers were formed with a core diameter of 32.9 microns
and an eccentricity of 0.27, in order to produce a polyamide component ratio of 0.25.
Both wick sets provided fully bonded self-sustaining, fluid transmissive bodies with
substantially similar fluid transmission properties far in excess of conventional
untreated bicomponent fiber wicks.
[0044] The wicks of the invention have a wide applicability and may be used in any fluid
transfer application. They are particularly adapted for use in assay devices such
as may be used in medical applications. Thus, for example, the wicks of the present
invention can be used for the transport of virtually any analyte fluid, including
biological analyte fluids such as urine, blood, and saliva. Moreover, the wicks of
the invention may be used in assay devices for detecting one or more analytes including,
but not limited to, hormones such as human chorionic gonadotropin (hCG) frequently
used as a marker for pregnancy, antigens, enzymes, antibodies to HIV, antibodies to
HTLV, antibodies to Helicobacter pylori, antibodies to hepatitis, antibodies to measles,
hepatitis antigens, antibodies to terponemes, antibodies to host or infections agents,
cellular markers of pathology including, but not limited to, cardiolipin, lecithin,
cholesterol, lipopolysaccaride and sialic acid, antibodies to mumps, antibodies to
rubella, cotinine, cocaine, benzoylecgonine, benzodizazpines, tetrahydrocannabinol,
nicotine, ethanol theophylline, phenytoin, acetaminophen, lithium, diazepam, nortriptyline,
secobarbital, phenobarbital, theophylline, testosterone, estradiol, 17-hydroxyprogesterone,
progesterone, thyroxine, thyroid stimulation hormone, follicle stimulating hormone,
luteinizing hormone, transforming growth factor alpha, epidermal growth factor, insulin-like
growth factor I and II, growth hormone release inhibiting factor, IGA and sex hormone
binding globulin; and other analytes including glucose, cholesterol, caffeine, cholesterol,
corticosteroid binding globulin, PSA, or DHEA binding glycoprotein.
1. A bicomponent fiber wick (100) for use in processing an analyte fluid, the bicomponent
fiber wick comprising a self-sustaining, fluid transmissive body (110) comprising
a plurality of bicomponent fibers (10, 120) bonded to each other as spaced apart contact
points, each bicomponent fiber having a fiber structure comprising a first fiber component
(14) formed from a polyamide material and a second fiber component (12), wherein the
fibers are bundled and crimped continuous fibers, collectively defining tortuous fluid
flow paths through the fluid transmissive body, the fiber structure being configured
for controlling flow of the analyte fluid through the fluid transmissive body with
at least a portion of the first fiber component in contact with the analyte fluid.
2. A bicomponent fiber wick according to claim 1 wherein the polyamide material is selected
from nylon 6, nylon 6,6, nylon 4, nylon 6,10, nylon 11, and nylon 12, and copolymers
thereof.
3. A bicomponent fiber wick according to claim 1 or claim 2 wherein the second fiber
component (12) comprises at least one of nylon 6, nylon 6,6, polyethylene terephthalate,
polybutylene terephthalate, polypropylene terephthalate, polylactic acid, polypropylene
and polyethylene.
4. A bicomponent fiber wick according to any preceding claim wherein the bicomponent
fibers are self-crimped.
5. A bicomponent fiber wick according to any preceding claim wherein the fiber structure
is adapted to provide a predetermined polyamide component ratio.
6. A bicomponent fiber wick according to claim 5 wherein the predetermined polyamide
component ratio is in a range of 0.10 to 0.50.
7. A bicomponent fiber wick according to claim 6 wherein the predetermined polyamide
component ratio is in a range of 0.20 to 0.35.
8. A bicomponent fiber wick according to claim 7 wherein the predetermined polyamide
component ratio is in a range of 0.25 to 0.30.
9. A bicomponent fiber wick according to any preceding claim wherein the first fiber
component (14) forms a continuous bicomponent fiber sheath along the length of the
bicomponent fiber and the second fiber component (12) forms a continuous bicomponent
fiber core surrounded by the sheath.
10. A bicomponent fiber wick according to any preceding claim wherein the first and second
fiber components each have discrete cross-sectional areas extending continuously along
the length of the bicomponent fiber, the fiber structure being adapted to provide
a predetermined polyamide component ratio equal to a ratio of first fiber component
weight per unit volume to overall fiber weight per unit volume.
11. A method of collecting an analyte fluid sample wherein the fluid sample is drawn up
by means of a bicomponent fiber wick according to any preceding claim.
12. A method according to claim 11 wherein the analyte fluid is one of urine, blood, serum
and saliva.
1. Bikomponenten-Faserdocht (100) zur Verwendung bei der Verarbeitung einer Analytflüssigkeit,
wobei der Bikomponenten-Faserdocht einen selbsttragenden flüssigkeitsdurchlässigen
Körper (110) umfasst, der eine Vielzahl von Bikomponentenfasern (10, 120) enthält,
die an beabstandeten Kontaktpunkten miteinander verbunden sind, wobei jede Bikomponentenfaser
eine Faserstruktur hat, die eine erste Faserkomponente (14), die aus einem Polyamidmaterial
gebildet ist, und eine zweite Faserkomponente (12) umfasst, wobei die Fasern gebündelte
und gekräuselte durchgehende Fasern sind, die zusammen verschlungene Flüssigkeitsfließpfade
durch den flüssigkeitsdurchlässigen Körper bilden, wobei die Faserstruktur dazu konfiguriert
ist, ein Fließen der Analytflüssigkeit durch den flüssigkeitsdurchlässigen Körper
zu kontrollieren, wobei mindestens ein Teil der ersten Faserkomponente mit der Analytflüssigkeit
in Kontakt ist.
2. Bikomponenten-Faserdocht gemäß Anspruch 1, wobei das Polyamidmaterial aus Nylon 6,
Nylon 6,6, Nylon 4, Nylon 6,10, Nylon 11 und Nylon 12 und deren Copolymeren ausgewählt
ist.
3. Bikomponenten-Faserdocht gemäß Anspruch 1 oder Anspruch 2, wobei die zweite Faserkomponente
(12) mindestens Nylon 6, Nylon 6,6, Polyethylenterephthalat, Polybutylenterephthalat,
Polypropylenterephthalat, Polymilchsäure, Polypropylen oder Polyethylen umfasst.
4. Bikomponenten-Faserdocht gemäß einem der vorhergehenden Ansprüche, wobei die Bikomponentenfasern
selbst-gekräuselt sind.
5. Bikomponenten-Faserdocht gemäß einem der vorhergehenden Ansprüche, wobei die Faserstruktur
so ausgelegt ist, dass sie ein vorbestimmtes Polyamid-Komponenten-Verhältnis aufweist.
6. Bikomponenten-Faserdocht gemäß Anspruch 5, wobei das vorbestimmte Polyamid-Komponenten-Verhältnis
im Bereich von 0,10 bis 0,50 liegt.
7. Bikomponenten-Faserdocht gemäß Anspruch 6, wobei das vorbestimmte Polyamid-Komponenten-Verhältnis
im Bereich von 0,20 bis 0,35 liegt.
8. Bikomponenten-Faserdocht gemäß Anspruch 7, wobei das vorbestimmte Polyamid-Komponenten-Verhältnis
im Bereich von 0,25 bis 0,30 liegt.
9. Bikomponenten-Faserdocht gemäß einem der vorhergehenden Ansprüche, wobei die erste
Faserkomponente (14) entlang der Länge der Bikomponentenfaser einen durchgehenden
Bikomponenten-Fasermantel bildet und die zweite Faserkomponente (12) einen von dem
Mantel umgebenen durchgehenden Bikomponenten-Faserkern bildet.
10. Bikomponenten-Faserdocht gemäß einem der vorhergehenden Ansprüche, wobei die erste
und die zweite Faserkomponente jeweils diskrete Querschnittsbereiche haben, die sich
durchgehend entlang der Länge der Bikomponentenfaser erstrecken, wobei die Faserstruktur
so ausgelegt ist, dass sie ein vorbestimmtes Polyamid-Komponenten-Verhältnis aufweist,
das gleich einem Verhältnis des Gewichts der ersten Faserkomponente pro Volumeneinheit
zum Gewicht der gesamten Faser pro Volumeneinheit ist.
11. Verfahren zum Sammeln einer Analytflüssigkeitsprobe, wobei die Flüssigkeitsprobe mittels
eines Bikomponenten-Faserdochts gemäß einem der vorhergehenden Ansprüche hochgezogen
wird.
12. Verfahren gemäß Anspruch 11, wobei die Analytflüssigkeit Urin, Blut, Serum oder Speichel
ist.
1. Mèche en fibres bicomposant (100) destinée à être utilisée dans le traitement d'un
fluide de substance à analyser, la mèche en fibres bicomposant comprenant un corps
autonome transmissif de fluide (110) comprenant une pluralité de fibres bicomposant
(10, 120) collées les unes aux autres en tant que points de contact espacés, chaque
fibre bicomposant ayant une structure de fibres comprenant un premier composant de
fibre (14) formé à partir d'un matériau en polyamide et un second composant de fibre
(12), dans laquelle les fibres sont des fibres continues liées et serties, définissant
collectivement des chemins d'écoulement de fluide tortueux à travers le corps transmissif
de fluide, la structure de fibres étant configurée pour commander l'écoulement du
fluide de substance à analyser à travers le corps transmissif de fluide avec au moins
une portion du premier composant de fibre en contact avec le fluide de substance à
analyser.
2. Mèche en fibres bicomposant selon la revendication 1, dans laquelle le matériau en
polyamide est sélectionné parmi du nylon 6, du nylon 6,6, du nylon 4, du nylon 6,10,
du nylon 11 et du nylon 12, et des copolymères de ceux-ci.
3. Mèche en fibres bicomposant selon la revendication 1 ou la revendication 2, dans laquelle
le second composant de fibre (12) comprend au moins un composé parmi le nylon 6, le
nylon 6,6, le polyéthylène téréphtalate, le polybutylène téréphtalate, le polypropylène
téréphtalate, l'acide polylactique, le polypropylène et le polyéthylène.
4. Mèche en fibres bicomposant selon l'une quelconque des revendications précédentes,
dans laquelle les fibres bicomposant sont automatiquement serties.
5. Mèche en fibres bicomposant selon l'une quelconque des revendications précédentes,
dans laquelle la structure de fibres est adaptée à fournir un rapport de composant
de polyamide prédéterminé.
6. Mèche en fibres bicomposant selon la revendication 5, dans laquelle le rapport de
composant de polyamide prédéterminé est dans une plage de 0,10 à 0,50.
7. Mèche en fibres bicomposant selon la revendication 6, dans laquelle le rapport de
composant de polyamide prédéterminé est dans une plage de 0,20 à 0,35.
8. Mèche en fibres bicomposant selon la revendication 7, dans laquelle le rapport de
composant de polyamide prédéterminé est dans une plage de 0,25 à 0,30.
9. Mèche en fibres bicomposant selon l'une quelconque des revendications précédentes,
dans laquelle le premier composant de fibre (14) forme une gaine de fibres bicomposant
continue le long de la longueur de la fibre bicomposant et le second composant de
fibre (12) forme un noyau de fibres bicomposant continu entouré par la gaine.
10. Mèche en fibres bicomposant selon l'une quelconque des revendications précédentes,
dans laquelle les premier et second composants de fibre ont chacun des sections transversales
discrètes s'étendant en continu le long de la longueur de la fibre bicomposant, la
structure de fibres étant adaptée à fournir un rapport de composant de polyamide prédéterminé
égal à un rapport entre le poids du premier composant de fibre par volume unitaire
et le poids de fibres global par volume unitaire.
11. Procédé de recueil d'un échantillon de fluide de substance à analyser, dans lequel
l'échantillon de fluide est prélevé au moyen d'une mèche en fibres bicomposant selon
l'une quelconque des revendications précédentes.
12. Procédé selon la revendication 11, dans lequel le fluide de substance à analyser est
un fluide parmi l'urine, le sang, le sérum et la salive.