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• Gel-spun polyethylene fibres are ultra-strong, high-
  modulus fibres that are based on the simple and flexible
  polyethylene molecule.

• They are called high-performance polyethylene (HPPE)
  fibres, high-modulus polyethylene (HMPE) fibres or
  sometimes extended chain polyethylene (ECPE) fibres.

• The gel-spinning process uses physical processes to
  make available the high potential mechanical properties
  of the molecule.
• The chemical nature of polyethylene remains in the gel-
  spun fibre and this can both be positive and a limitation:
  abrasion, flexlife, etc. are very high but the melting point
  is sometimes too low for certain applications.
• Gel-spun high-performance polyethylene fibres are
  produced from poly-ethylene with a very high molecular
  weight (UHMW-PE).

• This material is chemically identical to normal high-
  density polyethylene (HDPE)
•



• In aramids and comparable fibres, the molecules tend to
  form rod-like structures and these need only be oriented
  in one direction to form a strong fibre.
• Polyethylene has much longer and flexible molecules and
  only by physical treatments can the molecules be forced
  to assume the straight (extended) conformation and
  orientation in the direction of the fibre.
polymer
• High performance polyethylene fibres are commercially
 produced under the trade names Dyneema by DSM High
 Performance Fibers in the Nether-lands and by the
 Toyobo/DSM joint venture in Japan, and Spectra by
 Honeywell (formerly Allied Signal or Allied Fibers) in the
 USA.
• To make strong fibres, the molecular chains must be
 stretched, oriented and crystallised in the direction of the
 fibre.

• Furthermore, the molecular chains must be long to have
 sufficient interaction and for this reason polyethylene with
 an ultra-high molecular weight (UHMW-PE) is used as
 the starting material.
• spinning these fibres from the melt is almost impossible
 due to the extremely high melt viscosity.
• Furthermore, the drawing of a melt-processed UHMW-PE
 is only possible to a very limited extent owing to the very
 high degree of entanglement of the molecular chains.


• Melt-processed UHMW-PE can be drawn up to five times
 only.
•
(disentanglement)

                        •
                    -

                        •
Dyneema                            •




• The production of Dyneema fibres demands relatively
 little energy and uses no aggressive chemicals. The
 product can easily be recycled so environmental pollution
 from product and process is minimal.
• PE with Mw = 1.5 • 106 was stabilized with 0.5% by
  weight di-t-butyl-p-cresol (DBPK) at 150 0C, then
  dissolved with 2% by weight in decaline at 130 0C, and
  spun through spinneret holes of 0.5 mm diameter
  according to the air gap process into a bath of decaline
  and water at 10 0C, extracted over a long distance, and
  drawn at 140 0C in a hot air oven.
• After a draw ratio of 1:32 the multifilament has an elastic
  modulus of 90 GPa, a tenacity of 3.0 GPa (=36.5 g/dtex)
  and 6% breaking elongation.
• The draw ratio is also dependent on the temperature and
 the type of drawing: Wet drawing is limited to about 1:60,
 while hot air drawing has achieved ratios of 1:90.
• While the better solvent is decaline, paraffin oil is
 technically preferred, especially for working around 180..
 .200 0C. Then the drawing is divided into a first stage of
 1: (2. . .4) directly following the coagulation bath, a
 second stage of up to 1 :12 after extraction, and a third
 stage after drying at 180.. .200 0C in hot air with drawing
 over a long heated plate at > 130 0C.
In the autoclave (10) the solvent
(11) and the stabilizer (12) are
mixed and heated for the paraffin
oil to 140.. .170 0C. In the high
shear mixer (15) the PE powder is
pasted with this and homogenized
in the twin screw extruder (18).
This gel is then extruded by the
spin pump through the spin head
(23) into an air gap before the
filaments enter into the coagulation
bath (30). During take-up there is a
hot air drawing zone between the
godets (54) and (59). A long
distance extraction (37) follows and
so does hot air drying (45). This
yarn can either be wound (52) and
taken up from this bobbin, or it can
be hot drawn
•




    •



-   •
HDPE                   •

   -       HDPE        •
       -      UHMWPE
•



• these two factors together result in a solution that has a
  viscosity that is far too high to spin.

• Already at 2% PE concentration in paraffin oil viscosities
  of up to 20,000 Pa- s can occur.
Gelation and crystallization
• The solvent used in the polyethylene gel-spinning
  process should be a good solvent at high temperatures
  (>100 °C) but at lower temperatures (<80 °C) the polymer
  should easily crystallize from the solution.
• After the spinneret, the solution is cooled in the quench,
  the solvent is removed and a gel fibre is formed. This can
  be done by evaporation or by extraction of the solvent.
• From a diluted solution, polyethylene crystallizes in the
  form of flat crystals of about 20 nm thickness, in which
  the chains are neatly folded.

• In these crystals the C-axis or chain axis is perpendicular
  to the crystal (lamella) surface.

• The crystal structure is orthorhombic, which implies that
  the crystal axes are at right angles, two by two.
• Dyneema and Spectra are produced as a multifilament
  yarn.

• The titre of the monofilaments varies from about 0.3
  denier per filament (dpf) (0.44 dtex) to almost 10 dpf (11
  dtex).

• Tenacity of one filament may well be over 5 N/tex, and
  the modulus can be over 120 N/tex.

• Most fibre grades have a more or less circular cross-
  section. The fibre skin is smooth.
•
•
           -
PBO



• In contrast to the high tensile strength, the gel-spun fibre
  has a low compressive yield strength, approximately 0.1
  N/tex.
• HPPE fibres are the first high-performance fibres that not
  only have a high tenacity but that also have tension and
  bending fatigue properties comparable with the
  commonly used polyamide and polyester grades in
  ropes.

• Fatigue is very    important   in,   for   example,   rope
  applications.
• Carbon fibres and glass fibres have a high modulus and
 a brittle breaking mode, but Dyneema and Spectra fibres
 have a high modulus but still are flexible and have a long
 flex life,
• This fiber has a very low coefficient of friction; is self-
  lubricating; and is highly resistant to abrasion, in some
  forms being 15 times more resistant to abrasion than
  carbon steel.
• Its coefficient of friction is significantly lower than that of
  nylon and acetal, and is comparable to that of
  polytetrafluoroethylene (PTFE, Teflon), but UHMWPE
  has better abrasion resistance than PTFE.
• It is odorless, tasteless, and nontoxic.

• HPPE fibres are produced from polyethylene and do not
  contain any aromatic rings or any amide, hydroxylic or
  other chemical groups that are susceptible to attack by
  aggressive agents.

• The result is that polyethylene and especially highly
  crystalline, high molecular weight polyethylene is very
  resistant against chemicals.
Gel spun high-performance polyethylene fibres
Gel spun high-performance polyethylene fibres

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Gel spun high-performance polyethylene fibres

  • 1.
  • 2. • Gel-spun polyethylene fibres are ultra-strong, high- modulus fibres that are based on the simple and flexible polyethylene molecule. • They are called high-performance polyethylene (HPPE) fibres, high-modulus polyethylene (HMPE) fibres or sometimes extended chain polyethylene (ECPE) fibres. • The gel-spinning process uses physical processes to make available the high potential mechanical properties of the molecule.
  • 3. • The chemical nature of polyethylene remains in the gel- spun fibre and this can both be positive and a limitation: abrasion, flexlife, etc. are very high but the melting point is sometimes too low for certain applications.
  • 4. • Gel-spun high-performance polyethylene fibres are produced from poly-ethylene with a very high molecular weight (UHMW-PE). • This material is chemically identical to normal high- density polyethylene (HDPE)
  • 5. • • In aramids and comparable fibres, the molecules tend to form rod-like structures and these need only be oriented in one direction to form a strong fibre.
  • 6. • Polyethylene has much longer and flexible molecules and only by physical treatments can the molecules be forced to assume the straight (extended) conformation and orientation in the direction of the fibre.
  • 8. • High performance polyethylene fibres are commercially produced under the trade names Dyneema by DSM High Performance Fibers in the Nether-lands and by the Toyobo/DSM joint venture in Japan, and Spectra by Honeywell (formerly Allied Signal or Allied Fibers) in the USA.
  • 9. • To make strong fibres, the molecular chains must be stretched, oriented and crystallised in the direction of the fibre. • Furthermore, the molecular chains must be long to have sufficient interaction and for this reason polyethylene with an ultra-high molecular weight (UHMW-PE) is used as the starting material.
  • 10. • spinning these fibres from the melt is almost impossible due to the extremely high melt viscosity. • Furthermore, the drawing of a melt-processed UHMW-PE is only possible to a very limited extent owing to the very high degree of entanglement of the molecular chains. • Melt-processed UHMW-PE can be drawn up to five times only.
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  • 14. Dyneema • • The production of Dyneema fibres demands relatively little energy and uses no aggressive chemicals. The product can easily be recycled so environmental pollution from product and process is minimal.
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  • 16. • PE with Mw = 1.5 • 106 was stabilized with 0.5% by weight di-t-butyl-p-cresol (DBPK) at 150 0C, then dissolved with 2% by weight in decaline at 130 0C, and spun through spinneret holes of 0.5 mm diameter according to the air gap process into a bath of decaline and water at 10 0C, extracted over a long distance, and drawn at 140 0C in a hot air oven.
  • 17. • After a draw ratio of 1:32 the multifilament has an elastic modulus of 90 GPa, a tenacity of 3.0 GPa (=36.5 g/dtex) and 6% breaking elongation.
  • 18. • The draw ratio is also dependent on the temperature and the type of drawing: Wet drawing is limited to about 1:60, while hot air drawing has achieved ratios of 1:90.
  • 19. • While the better solvent is decaline, paraffin oil is technically preferred, especially for working around 180.. .200 0C. Then the drawing is divided into a first stage of 1: (2. . .4) directly following the coagulation bath, a second stage of up to 1 :12 after extraction, and a third stage after drying at 180.. .200 0C in hot air with drawing over a long heated plate at > 130 0C.
  • 20. In the autoclave (10) the solvent (11) and the stabilizer (12) are mixed and heated for the paraffin oil to 140.. .170 0C. In the high shear mixer (15) the PE powder is pasted with this and homogenized in the twin screw extruder (18). This gel is then extruded by the spin pump through the spin head (23) into an air gap before the filaments enter into the coagulation bath (30). During take-up there is a hot air drawing zone between the godets (54) and (59). A long distance extraction (37) follows and so does hot air drying (45). This yarn can either be wound (52) and taken up from this bobbin, or it can be hot drawn
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  • 22. HDPE • - HDPE • - UHMWPE
  • 23. • • these two factors together result in a solution that has a viscosity that is far too high to spin. • Already at 2% PE concentration in paraffin oil viscosities of up to 20,000 Pa- s can occur.
  • 25. • The solvent used in the polyethylene gel-spinning process should be a good solvent at high temperatures (>100 °C) but at lower temperatures (<80 °C) the polymer should easily crystallize from the solution.
  • 26. • After the spinneret, the solution is cooled in the quench, the solvent is removed and a gel fibre is formed. This can be done by evaporation or by extraction of the solvent.
  • 27. • From a diluted solution, polyethylene crystallizes in the form of flat crystals of about 20 nm thickness, in which the chains are neatly folded. • In these crystals the C-axis or chain axis is perpendicular to the crystal (lamella) surface. • The crystal structure is orthorhombic, which implies that the crystal axes are at right angles, two by two.
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  • 29. • Dyneema and Spectra are produced as a multifilament yarn. • The titre of the monofilaments varies from about 0.3 denier per filament (dpf) (0.44 dtex) to almost 10 dpf (11 dtex). • Tenacity of one filament may well be over 5 N/tex, and the modulus can be over 120 N/tex. • Most fibre grades have a more or less circular cross- section. The fibre skin is smooth.
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  • 32. - PBO • In contrast to the high tensile strength, the gel-spun fibre has a low compressive yield strength, approximately 0.1 N/tex.
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  • 36. • HPPE fibres are the first high-performance fibres that not only have a high tenacity but that also have tension and bending fatigue properties comparable with the commonly used polyamide and polyester grades in ropes. • Fatigue is very important in, for example, rope applications.
  • 37. • Carbon fibres and glass fibres have a high modulus and a brittle breaking mode, but Dyneema and Spectra fibres have a high modulus but still are flexible and have a long flex life,
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  • 39. • This fiber has a very low coefficient of friction; is self- lubricating; and is highly resistant to abrasion, in some forms being 15 times more resistant to abrasion than carbon steel. • Its coefficient of friction is significantly lower than that of nylon and acetal, and is comparable to that of polytetrafluoroethylene (PTFE, Teflon), but UHMWPE has better abrasion resistance than PTFE.
  • 40. • It is odorless, tasteless, and nontoxic. • HPPE fibres are produced from polyethylene and do not contain any aromatic rings or any amide, hydroxylic or other chemical groups that are susceptible to attack by aggressive agents. • The result is that polyethylene and especially highly crystalline, high molecular weight polyethylene is very resistant against chemicals.