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Characterization of Exxon Mobil
Escorene and Achieve Polypropylene
Resins



Stephen Whitson
11/23/2011
Materials
Exxon Mobil Chemical Inc.

 Escorene # PP3546                      Escorene
     Isotactic homopolymer
     Contains Peroxide
     Fine granules (homogenous)
     MFR - 1200 g/10 min


 Achieve # 6936G1
     Metallocene based homopolymer
     Peroxide Free
     Large distribution of granular sizes
     MFR - 1550 g/10 min

                                             Achieve
Melt-Blowing




                             Schematic of MB process




 Hopper and screw extruder                             Die To Collector
                                   Die Assembly
Processing

 Industrial Melt Blowing Line
   Haake Twin Screw Extruder
   Zenith Metering Pump
   Ingersol-Rand Air Compressor SSR-2000
   Collector
   6 in. die – 120 holes – 0.01in. hole diameter
Processing Parameters

     Parameters        Escorene® PP3546      Achieve® 6936G1

     Air Pressure:           10 psi                10 psi
        DCD:                   20                    20
   Colllector Speed:   137 rpm (4.9 m/min)   137 rpm (4.9 m/min)
   Extruder Speed:           57 rpm                69 rpm
  Extruder Pressure:      160-180 psi            370-380 psi
   Pump Pressure:            11 psi                14 psi
    Pump Speed:             8.5 rpm               8.5 rpm
      Air Temp:              500 ᵒF                500 ᵒF
     Web Weight             100 g/m²              100 g/m²
Characterization
 Fiber Diameter
    6 samples
                                                                TMI 49-70

 Web Thickness (ASTM D5729)
    TMI 49-70
    10 samples

 Air Permeability (ASTM D737)
    TexTest FX 3300
    7 Samples

 Tensile (ASTM D5035)                                                      TexTest FX 3300
    EJA Tensile Tester -10 lb load cell
    8 (1” gauge) Samples CD
    5 (1” gauge) Samples MD

 Elmendorf Tear (ASTM D5734)              EJA Tensile Tester
    TexTest FX 3750
    5 (2.5” x 4”) Samples CD & MD

                                                       TexTest FX 3750
Web Properties
                             Fiber Diam.   Thickness Air Perm
      Polymer
                                (µm)         (mm)      (cfm)

     Escorene®    Mean          1.95         1.15     27.57
                 Std. Dev.     0.595         0.09      1.01
      Achieve®    Mean          2.28         1.31     24.59
                 Std. Dev.      0.67         0.07      0.89




   Escorene®                                            Achieve®
Load vs. Elongation
               2000


               1800


               1600


               1400


               1200


               1000                                                               Escorene MD
Load (gms)
                                                                                  Achieve MD
                                                                                  Escorene CD
                800
                                                                                  Achieve CD

                600


                400


                200


                  0
        -0.1          0     0.1   0.2   0.3        0.4    0.5   0.6   0.7   0.8
                                        Elongation (in)
Mechanical Properties


                                     Peak Load      Peak Elongation Modulus       Elmendorf
             Polymer                 (gms)          (% in)          (gms/in²)     (cN)
                         Mean              1403.0               5.40 1,283,755          51.7
             Escorene®
 Machine                 Std. Dev.          164.3               0.90    288,090         15.8
 Direction
                         Mean              1894.6               5.07 1,758,291          49.4
             Achieve®
                         Std. Dev.          228.7               0.42    158,099         11.9


                         Mean               605.6              18.45    244,525         79.6
             Escorene®
Transverse               Std. Dev.           39.4               2.55     14,633         18.8
 Direction
                         Mean               619.7               8.39    347,856         68.6
             Achieve®
                         Std. Dev.           17.3                0.8     18,948          6.6
Conclusion

 The Achieve Resin (MB Web)
    Higher Melt Flow Rate
    Lower Molecular Weight
    Peroxide Free/Cleaner
    Better Tensile Properties
                                          Achieve Web

 The Escorene Resin (MB Web)
    Higher Molecular Weight
    Better Ductility and Tear Strength




                                          Escorene Web

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Characterization of Exxon Mobil Escorene and Achieve Polypropylene Melt Blown Nonwovens

  • 1. Characterization of Exxon Mobil Escorene and Achieve Polypropylene Resins Stephen Whitson 11/23/2011
  • 2. Materials Exxon Mobil Chemical Inc.  Escorene # PP3546 Escorene  Isotactic homopolymer  Contains Peroxide  Fine granules (homogenous)  MFR - 1200 g/10 min  Achieve # 6936G1  Metallocene based homopolymer  Peroxide Free  Large distribution of granular sizes  MFR - 1550 g/10 min Achieve
  • 3. Melt-Blowing Schematic of MB process Hopper and screw extruder Die To Collector Die Assembly
  • 4. Processing  Industrial Melt Blowing Line  Haake Twin Screw Extruder  Zenith Metering Pump  Ingersol-Rand Air Compressor SSR-2000  Collector  6 in. die – 120 holes – 0.01in. hole diameter
  • 5. Processing Parameters Parameters Escorene® PP3546 Achieve® 6936G1 Air Pressure: 10 psi 10 psi DCD: 20 20 Colllector Speed: 137 rpm (4.9 m/min) 137 rpm (4.9 m/min) Extruder Speed: 57 rpm 69 rpm Extruder Pressure: 160-180 psi 370-380 psi Pump Pressure: 11 psi 14 psi Pump Speed: 8.5 rpm 8.5 rpm Air Temp: 500 ᵒF 500 ᵒF Web Weight 100 g/m² 100 g/m²
  • 6. Characterization  Fiber Diameter  6 samples TMI 49-70  Web Thickness (ASTM D5729)  TMI 49-70  10 samples  Air Permeability (ASTM D737)  TexTest FX 3300  7 Samples  Tensile (ASTM D5035) TexTest FX 3300  EJA Tensile Tester -10 lb load cell  8 (1” gauge) Samples CD  5 (1” gauge) Samples MD  Elmendorf Tear (ASTM D5734) EJA Tensile Tester  TexTest FX 3750  5 (2.5” x 4”) Samples CD & MD TexTest FX 3750
  • 7. Web Properties Fiber Diam. Thickness Air Perm Polymer (µm) (mm) (cfm) Escorene® Mean 1.95 1.15 27.57 Std. Dev. 0.595 0.09 1.01 Achieve® Mean 2.28 1.31 24.59 Std. Dev. 0.67 0.07 0.89 Escorene® Achieve®
  • 8. Load vs. Elongation 2000 1800 1600 1400 1200 1000 Escorene MD Load (gms) Achieve MD Escorene CD 800 Achieve CD 600 400 200 0 -0.1 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 Elongation (in)
  • 9. Mechanical Properties Peak Load Peak Elongation Modulus Elmendorf Polymer (gms) (% in) (gms/in²) (cN) Mean 1403.0 5.40 1,283,755 51.7 Escorene® Machine Std. Dev. 164.3 0.90 288,090 15.8 Direction Mean 1894.6 5.07 1,758,291 49.4 Achieve® Std. Dev. 228.7 0.42 158,099 11.9 Mean 605.6 18.45 244,525 79.6 Escorene® Transverse Std. Dev. 39.4 2.55 14,633 18.8 Direction Mean 619.7 8.39 347,856 68.6 Achieve® Std. Dev. 17.3 0.8 18,948 6.6
  • 10. Conclusion  The Achieve Resin (MB Web)  Higher Melt Flow Rate  Lower Molecular Weight  Peroxide Free/Cleaner  Better Tensile Properties Achieve Web  The Escorene Resin (MB Web)  Higher Molecular Weight  Better Ductility and Tear Strength Escorene Web

Editor's Notes

  1. Polypropylene resins may be melt-blown for a variety of applications; the most common being filtersEscorene is a typical PP Melt-blownResinMetallocene catalyst basedNote: large distribution of granular sizes allow the resin to flow more freelyAchieve, achieves higher Melt Flow Rate, while being peroxide free; cleaner which is good for filters
  2. Melted through extruderPressurized through gear pumpHot hair forces polymer through dieMolten fibers solidify in air from die and hit spinning collectorWeb is then wound
  3. Parameters kept the same.Pressure increased (Achieve) to maintain 100 g/m^2 web; this is due to the lower density Achieve resin
  4. From the fiber diameter: Achieve less dense; more free volumeAchieve web more permeable/breathable
  5. Machine Direction = direction of spinning collector beltCross direction = direction transverse to the machine directionUnlike most other polymers PP attains better tensile properties with decrease in MWThis is because crystal formation is more difficult at higher MW’s for PPDuctility increases with increasing MWCan really be seen in the transverse direction, since here we bend the fibers/chains
  6. Achieve stiffer and higher strength; characteristic of lower molecular weight PPEscorene has slightly better tear resistance in the transverse direction, because of higher MW i.e. better ductility
  7. Higher MFI = lower MWCleaner, more permeable, better tensile properties (with the exception of ductility)Achieves this without peroxideMost likely due to type or technique of Metallocene based catalyst