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10 th International Conference on Wood and Biofiber Plastic Composites 11-13 May 2009, Madison, USA Natural Fiber Composites Manufactured using Long Fiber Thermoplastic (LFT) Compounding and Compression Moulding Kristiina Oksman Niska and Aji P Mathew Division of Manufacturing and Design of Wood and Bionanocomposites, Luleå University of Technology, Sweden www.ltu.se
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10th International Conference on Wood and Biofiber Plastic Composites11-13 May 2009, Madison, USA

Natural Fiber Composites Manufactured using Long Fiber Thermoplastic (LFT) Compounding and

Compression Moulding

Kristiina Oksman Niska and Aji P Mathew

Division of Manufacturing and Design of Wood and Bionanocomposites,Luleå University of Technology,

Swedenwww.ltu.se

Outline

Composites ProcessingMaterials and Methods

−Reinforcing Fibers−Composites Manufacturing−Characterization

Results−Fiber Breakage During Process−Composites Mechanical Properties−Composites Microstructure

Conclusions

• Compounding of semi-manufactured materials− Pellets for injection moulding

or extrusion− Sheets for compression

moulding or thermoforming• Direct extrusion of profiles• Non-woven materials

− Compression moulding and thermoforming

Processing Methods

Limitations and Challanges

• Low bulk density, difficult to process

• Fiber length • Fiber damages due to process• Poor adhesion with plastics• Difficult to disperse• Thermal degradation• Moisture uptake

Aim of this Work

• Can we use long fibers in compoundingprocess?

• How does the process affect the fiber size and composites properties?

Long Fiber Thermoplastic (LFT) Process

• Long glass fibers are fed into the extruder and the compound is directly compression moulded (or injection moulded)

• Developed for structuralautomotive parts

• Common technology in Europe

Front end of LFT

Instrument panel of LFT

Schematic of the Process

F Mack, Coperion

1. Polymer2. Gravimetric feeding3. Fiber roving4-6. Co-rotating twin screw

extruder

7-8. Cutting and separation units9. Handling system10. Compression moulding

Plant for Long Fiber Thermoplastic (LFT)

ZSK Mc PLUS for the melting of the PP-compoundsAnd processing of the LFT-compounds

Separation unittaking-off belt

Roving supply

Die head and cutting unitSeparation unit

extrudate belt withforced air oven

Pellet conveyingand feeding system

Maintenanceplatform

F Mack, Coperion

Materials

Matrix: Polypropylene Adstiff 770 ADXP, MontelPolyolefines, MFI 45 g/10 min (230°C, 2.16 kg).Coupling agent: Maleated polypropylene (Epolene 43 WAX) from Eastman Chemicals was used as coupling agent, content 2 %wt.Reinforcing fibers: Banana, Sisal, Jute and Flax.All fibers were in the form of long fibers called rovings.Targeted fiber contents 30 and 40 wt-%

BANANA SISAL JUTE FLAX

Characterization

Fiber breakage• Fibers were extracted from PP with xylene. The lengths

were measured with optical microscopy and image analysis.

Mechanical properties• The flexural testing according to ASTM D790 standard. • Impact testing was performed according to ISO 179

unnotched Izod standard. • At least ten specimens were tested for every material.Microstructure• Composites fractured surfaces and fibers were studied

with a scanning electron microscope, Jeol JSM 5200.

Fibers

Banana

Jute

Sisal

Flax

Mechanical Properties

Ref. Satayanarayna et al 1990, Ilvessalo-Pläffi 1995, Bledzki et al 1996, Bismarck et al 2005, Maya and Rajesh 2008

28-1002.4345-1100Flax271.5393-773Jute123-5.8500-550Banana

9-205-14511-700Sisal1.6-28PP

E-modulus(GPa)

Elongation(%)

Tensile Strength(MPa)

Properties

Mechanical Properties

Bundle

Single fiber

Fiber Properties

264-715-1165033-7019Flax

12-1361-7281102-520Jute

563-5410150-80-250Banana

867-78221001-820Sisal

Lignin(%)

Cellulose(%)

Fibril angle(°)

l/dratio

Length(mm)

Diameter(μm)

Fibertype

Ref. Satayanarayna et al 1990, Ilvessalo-Pläffi 1995, Bledzki et al 1996, Bismarck et al 2005, Maya and Rajesh 2008

Processing of Long Natural Fiber Thermoplastics

• Twin Screw Extruder, Coperion W&P, ZSK 25 WLE, Stuttgart, Germany

• Constant screw speed 300 rpm in main extruder and varied speed in side extruder

• Total output 16 kg/h• The targeted fibre contents were predecided and the fibre feeding

rate was calculated

F

F

Continuous Feeding of Fibers

Example: Total throught put 16 kg/hTargeted 40% fiber content, 6.4 kg/h fibersRoving weight: 12 g/m

Screw speed for fiber feeding 296 rpm

Targeted weight of fibres

length/revolution x time x weight/lengthScrew speed =

6400 / (0.03 x 60 x 12) = 296

Compression Moulding

Load 600 kNPressure 70 MPaMould temperature 50°CPress time 40 s

Fjellman Press, Mariestad, 3100 ton

Fiber Lengths after Compounding

Composites Microstructure

Mechanical Properties

(kJ/m)

Improved Adhesion

Improved Adhesion

Conclusions

• Fiber roving feeding is an suitable way to feed natural fibers in to the extruder.

• Flax fibers were separated to single elementary fibers during the compounding process while all other fibers were in the form of fiberbundles.

• The fiber length measurements showed that flax and jute fiberswere shortest followed by banana and sisal. The typical sisal fiberlength was between 3-5.5 mm.

• Mechanical testing showed that highest stiffness was obtained byaddition of jute and flax fibers while sisal resulted in composites with the best impact behaviours.

• Fiber l/d ratio, microfibrillar angle, fiber properties had limited impact on the mechanical properties when the adhesion between the fiberand matrix was poor.

• MAPP coupling agent had positive effect on mechanical properties.

Acknowledgements

Runar Långström at Swerea SICOMP, Sweden and Joseph Kuruvilla at Indian Institute of Space Science and Technology, India for help with process and mechanicaltesting and MSc-students Laborde Laure and SimonetYann for the fibre length measurements.

Thank you all for listening!


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