diss_SCHWAIGER.pdf - OPUS Bayreuth - Universität Bayreuth

A.3 Polystyrol-Toluol-Mischungen
c T/ K D th /10 −4 m 2 s −1 c T/ K D th /10 −4 m 2 s −1
0.01 293.15 8.564 0.4643 293.15 8.769
0.01 303.15 8.258 0.4643 303.15 8.710
0.01 313.15 8.082 0.4643 313.15 8.473
0.01 323.15 7.761 0.4643 323.15 8.217
0.01 333.15 7.535 0.4643 333.15 8.120
0.01 343.15 – 0.4643 343.15 7.945
0.0315 293.15 8.563 0.5743 293.15 8.271
0.0315 303.15 8.239 0.5743 303.15 8.191
0.0315 313.15 8.061 0.5743 313.15 8.018
0.0315 323.15 7.851 0.5743 323.15 7.807
0.0315 333.15 7.614 0.5743 333.15 7.719
0.0315 343.15 7.397 0.5743 343.15 7.609
0.1044 293.15 8.413 0.7575 293.15 2.643
0.1044 303.15 – 0.7575 303.15 5.943
0.1044 313.15 8.203 0.7575 313.15 7.365
0.1044 323.15 7.927 0.7575 323.15 7.618
0.1044 333.15 7.722 0.7575 333.15 7.625
0.1044 343.15 7.517 0.7575 343.15 –
Tabelle A.6: Konzentrations- und Temperaturabhängigkeit der thermischen Diffusivität
in PS(90 kgmol −1 )/Toluol-Mischungen
103