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Old MathJax webview fast.. . Shear Rate (s) 0.100 0.2154 0.4641 1.00 2.154 4.641 10.0 Viscosity (Pa-s) 170C 7.801 E02 7.608 E02 7.049 E02 6.396E02
Old MathJax webview
fast..
.
Shear Rate (s) 0.100 0.2154 0.4641 1.00 2.154 4.641 10.0 Viscosity (Pa-s) 170C 7.801 E02 7.608 E02 7.049 E02 6.396E02 5.908E02 5.207E02 4.336E02 Viscosity (Pa-s) 180C 6.649 E02 6.657 E02 6.111 E02 5.689 E02 5.138 E02 4.535 E02 3.922 E02 Viscosity (Pa-s) 190C 5.575 E02 5.390 E02 4.846 E02 4.561 E02 4.139 E02 4.267 E02 3.705 E02 (c) Based on your solution from part (b) above, what is the net impact on M, for the polystyrene polymer produced? (d) Based on your solution from part (b) above, how would you change your initial styrene monomer concentration in order to match your original Mo value? Counterion Na+ K+ Rb+ CS+ for dioxane ko [L/ (mol s)] 0.94 3.4 19.8 21.5 24.5 for tetrahydrofuran kp [L/ (mol s)] 160 80 60 50 22Step by Step Solution
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