September
24-27, 2007
• Renaissance Waverly Hotel
•Atlanta, Georgia USA
Meltblown & Spunbond Technology II
Tuesday,
September 25
2:30 p.m.—5:00 p.m.
Moderator: Marshall Hutten,
Hollingsworth & Vose Co.
Production and Evaluation
of Meltblown Poly (phenylene
sulfide)
Roy Broughton, Jr., Auburn University
- Thermal shrinkage of MB PPS has
been successfully minimized.
- Causes and steps to control thermal
shrinkage presented.
[Open
Abstract] [Close
Abstract]
Manufacturers are currently supplying poly(phenylene sulfide) (PPS)
for use in continuous melt production of nonwoven fabrics by spunbond and meltblowing
(MB) processes. Aside from a preliminary study made by these authors
in a paper presented on MB PPS at the INDA Filtration Conference in November
2006, little evaluation of the products which might be produced has been reported. The
significant thermal shrinkage problem with MB PPS was noted and it was thought
that shrinkage might be minimized by slowing the PPS fiber cooling rate hopefully
to allow polymer crystallization to occur during the melt blowing process. In
this second paper, this approach was successfully implemented and a better understanding
of the causes and control of thermal shrinkage was achieved. Japanese authors
have also reported that extensive annealing is necessary to produce a nonwoven
PPS fabric with low shrinkage. The authors have altered the extrusion,
quench and collection conditions in an effort to reduce the thermal shrinkage,
and report on the effectiveness of this approach.
Technical Aspects of Halar
Meltblown Nonwovens
Rowland Griffin, Monadnock Non-Wovens LLC
- Difficulties extruding Halar or
ETCFE aside, its properties offer
new opportunities and technical
solutions to long-standing problems.
- Learn what opportunities exist and
how they can be translated into
financial rewards.
[Open
Abstract] [Close
Abstract]
Outside the difficulties encountered in processing Halar or ETCFE as
a meltblown nonwoven, its properties offer new opportunities and technical solutions
to long standing problems.
The Role of Sheath and Core with Bicomponent Filament Nonwovens
Jaap Frijlink, Colbond Nonwovens
- Importance of the sheath in
bond formation, fabric strength,
deformation and breakage.
- Bicomponent webs made with
numerous combinations of polymers
examined and results if sheath/core
remains the same.
[Open
Abstract] [Close
Abstract]
Bicomponent nonwovens hold strong positions in durable nonwovens markets for
years, with emphasis on commercial carpeting, automotive and roofing applications.
A well known brand (Colback®) is based on PET core and PA6 sheath. In the
2-step Colback process (spinning and web formation-bonding) properties are tuned
by varying sheath percentage and draw ratio, among others. We compared
bicomponent webs with cores of PET, PA6, PBT, PP all with the same sheath polymer.
The stress-strain curves are completely different, reflecting properties of core
polymers and draw ratio. We also compared different sheath polymers (PA,
PBT, others) with two draw ratios of the same core (PET). Again we see little
influence of sheath on stress-strain properties. Nevertheless, the contribution
of the bond forming sheath is unique and manifold: without bonds we would not
have any web properties
Considering sheath perspectives:
- The sheath consolidates the lay down pattern and enables transfer of stresses
via numerous bonds between filaments. Although bonds are much weaker than filaments,
their numbers are so huge that they can transfer high loads when yielding
simultaneously.
- The sheath enables some tuning of the E-modulus: high density and strength
of bonds restrict macroscopic fabric deformation and shift emphasis fully on
straining of filaments, leading to a high E-modulus. The opposite -low density
and strength of bonds- provokes more macroscopic fabric deformation, being the
lowest strain energy solution to an imposed strain.
- The sheath polymer controls the process of break. Bicomponent nonwovens mostly
collapse at strains well below the breaking strain of filaments. Application
dependent, the sheath is designed such that delamination of the consolidated
structure initiates break. Keeping a fixed core-sheath ratio and bonding temperature,
Load at Break appears to be proportional to the specific mass of the nonwoven.
Swirl Dies for Use in Melt Blowing
Robert Shambaugh, University of
Oklahoma
- Typically used to apply glue, polymer
was extruded through a swirl die;
process arameters were examined.
- Fiber characteristics were measured
and found to compare with
mathematical models; results shared.
[Open
Abstract] [Close
Abstract]
For melt blowing with a conventional slot (“Exxon”) die or a multi-row
Schwarz die, air is injected parallel to or at an angle to the molten fiber. However,
the air is never injected off-center with respect to the fiber orifice. This
is not the case with a swirl die. In a swirl die, the molten polymer
stream is attenuated and directed (swirled) by a concentric ring of air jets. This
type of die is commonly used as a glue applicator. However, it is a type
of melt blowing die, and as such it could potentially be used to produce melt
blown fibers.
With polypropylene, experiments were run wherein the effects of air flowrate,
polymer flowrate, air temperature, and polymer temperature were examined. The
fiber diameter, swirl pattern diameter, and swirl frequency were measured. The
experimental results favorably compared to results predicted by a mathematical
model. Experiments were also run wherein hollow fibers were produced with
the swirl die. The swirl frequency increased with increasing hollowness,
a result that could be commercially exploited for increasing line speed or improving
fiber laydown pattern.
