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New Methodology


       Heat Pipe Thermally
    Enhanced (HPTE) Mandrels
       In Filament Winding
           Applications
Heat pipes

    Well
Established in
 Automotive
   Tooling


                    1
Heat pipes

What value does heatpipe
    technology bring to
    mandrel design and
filament winding process
       optimization?
                           1
Heatpipe Operating Principles




                                2
Heatpipe Features & Benefits
   Heatpipes transfer large amounts of thermal energy rapidly.

   Heatpipes are intrinsically Isothermal.

   Heatpipes redistribute localized energy inputs.

   Heatpipes have an Intuitive, remediating response to locally
    generated energy deficit and surplus transients. (sinks and
    exotherms)

   Heatpipes require no electrical power or mechanical
    connections.

   Heatpipes are sealed systems.

                                                                   4
HPTE Mandrels


“In Oven” Convection
     Oven Curing of
 Filament Wound Tube
       Sections
                       3
Current “In Oven”
        Cure Challenges and Limitations


 The cure sequence usually occurs in a heated
  convection oven or radiant energy environment.

 Energy is provided to the surface of the
  resin/filament composite through the heated
  oven atmosphere at low watt density.

 A large percentage of energy produced by the
  oven is vented and not efficiently utilized.

                                                   3
Current “In Oven" Filament Winding
       Cure Challenges and Limitations

 The mandrel is not directly heated.

 The mandrel is the last component to be heated.

 The cure is initiated at the outside surface of the
  winding, sealing the outer surface of the tube
  section, trapping gasses and vapour liberated during
  the cure cycle.

 Trapped gasses and vapours contribute to
  delamination and porosity.

                                                         3
HPTE Mandrel Testing Cell




                            5
Traditional Mandrel Test Results

                                                             Transient Temperature Curves for the Hollow Mandrel


                        140
                                      Top (2")
                                      Mid (33")
                        120           Bottom(60")
                                      Delta T (bottom-top)

                        100
Surface Temp. (deg.F)




                        80



                        60



                        40                                                                                Date: Jan. 9, 09
                                                                                                          Sand Bath Temp. 350 Deg. F
                                                                                                          Heat Transfer Rate: ~12W.
                        20                                                                                Mandrel OD. 1.875".
                                                                                                          Mandrel Length: 72".
                                                                                                          TC location is the distance from the top.

                         0
                              0   5                 10           15            20                 25       30              35               40        45
                                                                                    Time (Min.)
                                                                                                                                                           6
HPTE Mandrel Test Results

                                                   Transient Temperature Curves for the Mandrel-Isobar


                               260

                               240

                               220

                               200

                               180
Surface Temperature (deg. F)




                               160

                               140
                                                           Top (2")
                               120
                                                                                                Date: Jan. 8, 09
                               100                         Mid (33")
                                                                                                Sand Bath Temp. 350 Deg. F
                               80                          Bottom (62")                         Heat Transfer Rate: ~210W.
                                                                                                Mandrel OD. 2".
                               60                          Delta T (bottom-top)                 Mandrel Length: 74".
                               40                                                               TC location is the distance from the top.

                               20

                                0

                               -20
                                     0   10   20    30           40               50      60             70           80             90     100
                                                                           Time (Min.)                                                      7
HPTE mandrels thermodynamic
                features in conventional
               oven curing applications

   Exposed surfaces of the HPTE mandrel absorb thermal energy
    from the oven and transfer it directly to the mandrel.

   This absorbed thermal energy is immediately redistributed
    throughout the HPTE mandrel.

   The redistributed thermal energy results in a dynamically
    isothermal mandrel.

   The heated isothermal mandrel provides an optimum uniform
    cure platform providing thermal energy from I.D. to O.D. of the
    tube section.




                                                                      8
HPTE mandrels in convection
                 oven curing applications
                 thermodynamic benefits
   The mandrel is now thermally uniform. (isothermal) and super
    thermally conductive and reactive to the ambient temperatures
    within the oven.

   Resident energy within the oven is absorbed through the
    exposed ends of the mandrel, heating the mandrel directly and
    efficiently.

   Because both the I.D. and O.D. surfaces of the winding are now
    actively heated, the cure cycle time is reduced.

   The heated mandrel draws resin to the I.D. of the winding
    resulting in a tube section with a homogeneous, resin rich,
    nonporous surface on the tube inner diameter.


                                                                     9
HPTE Mandrels

    “Out of Oven”
 Induction Curing of
Filament Wound Tube
     Sections After
       Winding
                       3
Induction cure sequence using
a HPTE Mandrel winding and curing a 3” I.D.
     Tube section with ½” wall using
       carbon fiber epoxy prepreg




                                              14
HPTE mandrels in induction
     heated “out of oven”curing applications

 The induction heating coil is situated proximate to the
  mandrel permitting unimpeded mandrel rotation.

 Induction heating is relatively instantaneous and intense.

 RF energy is invisible to the uncured resin and filament
  but fully sensed by the metal mandrel.

 Significant thermal energy per unit time can be provided
  to the mandrel which then intimately transfers that energy
  to the uncured composite resulting in significant energy
  efficiencies.

                                                               10
Testing Cell for Induction heating of
       both a HPTE Mandrel
     and a Traditional Mandrel




                                        11
3” Standard hollow mandrel:
      Thermographic study with induction heat



187.70 ºF




                                                12
3” HTPE mandrel: Thermographic
                study with induction heat


183.02 ºF




                                             13
Traditional hollow mandrel vs. HTPE mandrel
64” X 3” rotating at 100 RPM and heated by an
       induction coil providing 850 Watts




          Time lapse video sequences
HPTE Mandrels

    “Out of Oven”
 Induction Curing of
Filament Wound Tube
    Sections While
       Winding
                       3
Video of a cure while winding sequence using
    a HPTE Mandrel winding and curing
         a 3” I.D. tube section wound
        of carbon fiber epoxy prepreg




                                               15
HPTE mandrels in induction
     heated “out of oven” curing applications


 The mandrel now provides the uncured composite with
  100% of the thermal energy requirement. The cure begins
  at the mandrel surface and continues through to the tube
  section outside diameter.

 Curing from the inside diameter to the outside surface
  allows volatile vapours generated during the cure
  sequence to be liberated to atmosphere reducing porosity.

 Resin is drawn to the hottest surface during the cure
  resulting in a resin rich non porous I.D.


                                                              10
SAMPLE A Induction Cure vs. SAMPLE B Oven Cure
            CT Scan Defect Analysis
A: Induction Cure




                    Marker
B: Oven Cure
A: Induction Cure




 B: Oven Cure
Sample A: Induction Cure
       Volume: 1288.8789 mm3
       Defects: 2.7777 mm3
       Porosity: 0.21505 %




Defect Volume Distribution vs. Defect Count
Sample B: Oven Cure
      Volume: 1452.3339 mm3
      Defects: 2.7764 mm3
      Porosity: 0.19080 %




Defect Volume Distribution vs. Defect Count
Sample A: Induction Cure
Volume: 1288.8789 mm3
Defects: 2.7777 mm3
Porosity: 0.21505 %




Volume: 1452.3339 mm3            Sample B: Oven Cure
Defects: 2.7764 mm3
Porosity: 0.19080 %




           Defect Volume Distribution vs. Defect Count
Technology providers
                for this project

 Ameritherm Div of Ambrel Corp, Springfield NY
  Induction power supply and coil
 Chino Works America, Chicago Illinois
  Infrared sensor and process controller
 McClean Anderson, Schofield Wisconsin
  Filament winding machine and laboratory
 TCR Composites, Ogden Utah
  Prepreg epoxy filament materials
 Acrolab Ltd, Windsor Ontario, Canada
  HPTE mandrel



                                                  16
Thank you
       Joseph Ouellette
 Director, Advanced Research
        & Development
            Acrolab Ltd.




     Advanced Thermal Engineering /Research and Development
                   Windsor, Ontario, CANADA
                       www.acrolab.com

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Acrolabfinalisomandrelhptemandrelseptember72010 12863064458143-phpapp01

  • 1. New Methodology Heat Pipe Thermally Enhanced (HPTE) Mandrels In Filament Winding Applications
  • 2. Heat pipes Well Established in Automotive Tooling 1
  • 3. Heat pipes What value does heatpipe technology bring to mandrel design and filament winding process optimization? 1
  • 5. Heatpipe Features & Benefits  Heatpipes transfer large amounts of thermal energy rapidly.  Heatpipes are intrinsically Isothermal.  Heatpipes redistribute localized energy inputs.  Heatpipes have an Intuitive, remediating response to locally generated energy deficit and surplus transients. (sinks and exotherms)  Heatpipes require no electrical power or mechanical connections.  Heatpipes are sealed systems. 4
  • 6. HPTE Mandrels “In Oven” Convection Oven Curing of Filament Wound Tube Sections 3
  • 7. Current “In Oven” Cure Challenges and Limitations  The cure sequence usually occurs in a heated convection oven or radiant energy environment.  Energy is provided to the surface of the resin/filament composite through the heated oven atmosphere at low watt density.  A large percentage of energy produced by the oven is vented and not efficiently utilized. 3
  • 8. Current “In Oven" Filament Winding Cure Challenges and Limitations  The mandrel is not directly heated.  The mandrel is the last component to be heated.  The cure is initiated at the outside surface of the winding, sealing the outer surface of the tube section, trapping gasses and vapour liberated during the cure cycle.  Trapped gasses and vapours contribute to delamination and porosity. 3
  • 10. Traditional Mandrel Test Results Transient Temperature Curves for the Hollow Mandrel 140 Top (2") Mid (33") 120 Bottom(60") Delta T (bottom-top) 100 Surface Temp. (deg.F) 80 60 40 Date: Jan. 9, 09 Sand Bath Temp. 350 Deg. F Heat Transfer Rate: ~12W. 20 Mandrel OD. 1.875". Mandrel Length: 72". TC location is the distance from the top. 0 0 5 10 15 20 25 30 35 40 45 Time (Min.) 6
  • 11. HPTE Mandrel Test Results Transient Temperature Curves for the Mandrel-Isobar 260 240 220 200 180 Surface Temperature (deg. F) 160 140 Top (2") 120 Date: Jan. 8, 09 100 Mid (33") Sand Bath Temp. 350 Deg. F 80 Bottom (62") Heat Transfer Rate: ~210W. Mandrel OD. 2". 60 Delta T (bottom-top) Mandrel Length: 74". 40 TC location is the distance from the top. 20 0 -20 0 10 20 30 40 50 60 70 80 90 100 Time (Min.) 7
  • 12. HPTE mandrels thermodynamic features in conventional oven curing applications  Exposed surfaces of the HPTE mandrel absorb thermal energy from the oven and transfer it directly to the mandrel.  This absorbed thermal energy is immediately redistributed throughout the HPTE mandrel.  The redistributed thermal energy results in a dynamically isothermal mandrel.  The heated isothermal mandrel provides an optimum uniform cure platform providing thermal energy from I.D. to O.D. of the tube section. 8
  • 13. HPTE mandrels in convection oven curing applications thermodynamic benefits  The mandrel is now thermally uniform. (isothermal) and super thermally conductive and reactive to the ambient temperatures within the oven.  Resident energy within the oven is absorbed through the exposed ends of the mandrel, heating the mandrel directly and efficiently.  Because both the I.D. and O.D. surfaces of the winding are now actively heated, the cure cycle time is reduced.  The heated mandrel draws resin to the I.D. of the winding resulting in a tube section with a homogeneous, resin rich, nonporous surface on the tube inner diameter. 9
  • 14. HPTE Mandrels “Out of Oven” Induction Curing of Filament Wound Tube Sections After Winding 3
  • 15. Induction cure sequence using a HPTE Mandrel winding and curing a 3” I.D. Tube section with ½” wall using carbon fiber epoxy prepreg 14
  • 16. HPTE mandrels in induction heated “out of oven”curing applications  The induction heating coil is situated proximate to the mandrel permitting unimpeded mandrel rotation.  Induction heating is relatively instantaneous and intense.  RF energy is invisible to the uncured resin and filament but fully sensed by the metal mandrel.  Significant thermal energy per unit time can be provided to the mandrel which then intimately transfers that energy to the uncured composite resulting in significant energy efficiencies. 10
  • 17. Testing Cell for Induction heating of both a HPTE Mandrel and a Traditional Mandrel 11
  • 18. 3” Standard hollow mandrel: Thermographic study with induction heat 187.70 ºF 12
  • 19. 3” HTPE mandrel: Thermographic study with induction heat 183.02 ºF 13
  • 20. Traditional hollow mandrel vs. HTPE mandrel 64” X 3” rotating at 100 RPM and heated by an induction coil providing 850 Watts Time lapse video sequences
  • 21. HPTE Mandrels “Out of Oven” Induction Curing of Filament Wound Tube Sections While Winding 3
  • 22. Video of a cure while winding sequence using a HPTE Mandrel winding and curing a 3” I.D. tube section wound of carbon fiber epoxy prepreg 15
  • 23. HPTE mandrels in induction heated “out of oven” curing applications  The mandrel now provides the uncured composite with 100% of the thermal energy requirement. The cure begins at the mandrel surface and continues through to the tube section outside diameter.  Curing from the inside diameter to the outside surface allows volatile vapours generated during the cure sequence to be liberated to atmosphere reducing porosity.  Resin is drawn to the hottest surface during the cure resulting in a resin rich non porous I.D. 10
  • 24. SAMPLE A Induction Cure vs. SAMPLE B Oven Cure CT Scan Defect Analysis
  • 27. A: Induction Cure B: Oven Cure
  • 28. Sample A: Induction Cure Volume: 1288.8789 mm3 Defects: 2.7777 mm3 Porosity: 0.21505 % Defect Volume Distribution vs. Defect Count
  • 29. Sample B: Oven Cure Volume: 1452.3339 mm3 Defects: 2.7764 mm3 Porosity: 0.19080 % Defect Volume Distribution vs. Defect Count
  • 30. Sample A: Induction Cure Volume: 1288.8789 mm3 Defects: 2.7777 mm3 Porosity: 0.21505 % Volume: 1452.3339 mm3 Sample B: Oven Cure Defects: 2.7764 mm3 Porosity: 0.19080 % Defect Volume Distribution vs. Defect Count
  • 31. Technology providers for this project  Ameritherm Div of Ambrel Corp, Springfield NY Induction power supply and coil  Chino Works America, Chicago Illinois Infrared sensor and process controller  McClean Anderson, Schofield Wisconsin Filament winding machine and laboratory  TCR Composites, Ogden Utah Prepreg epoxy filament materials  Acrolab Ltd, Windsor Ontario, Canada HPTE mandrel 16
  • 32. Thank you Joseph Ouellette Director, Advanced Research & Development Acrolab Ltd. Advanced Thermal Engineering /Research and Development Windsor, Ontario, CANADA www.acrolab.com