Table lists the polymer mass fractions (m) and ratios of propagation to chain transfer rates (KM,...
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Table lists the polymer mass fractions (m) and ratios of propagation to chain transfer rates (KM, KH, and K) for each active site type in a 5-site-type catalyst used to make polyethylene resins at 80 °C in a fluidized-bed gas phase reactor operated at steady state. These parameters are definided in Eq. (with kt = 0), T= KtM kp m KM Kx Kg (mol-L-¹) + kty [H₂] Ktg 1 + Kp [M] k, [M] = Table Polymerization kinetic parameters for a 5-site-type catalyst. Site 3 Site 1 0.1 Site 2 0.25 1 x 10-4 0.03 5 x 10-5 5 x 10-5 0.01 2.5 x 10-5 0.3 2.5 x 10-5 0.005 1.25 x 10-5 KM + KH where [M] and [H2] are the concentrations of ethylene and hydrogen at the active sites (dissolved in the amorphous polymer phase), respectively. M₁ = [H₂] [M] 1 mi Σ1 Μπι + KB [M] a) Plot the MWD of a polyethylene sample made at the following polymerization conditions: [M] = 0.6 mol/L and [H₂] = 0.04 mol/L. The molar mass of ethylene is 28 mol/g. Site 4 0.25 1.25 x 10-5 0.0025 6.25 x 10-6 b) If you need to make a resin with M₁ = 60,000 by changing only the concentration of hydrogen in the reactor, what would be the required [H₂]? What would be the values of the Mw and D at these conditions? 71 Hint: The average molecular weights, M₁ and Mw, of polymers made with a catalyst having n site types are, Site 5 0.1 6.25 x 10-6 0.00125 3.13 x 10-6 and Mw = [m.Mw₁ W i=1 You should be able to prove these relations based on your knowledge of how Mn and Mw of polymer populations are calculated. Table lists the polymer mass fractions (m) and ratios of propagation to chain transfer rates (KM, KH, and K) for each active site type in a 5-site-type catalyst used to make polyethylene resins at 80 °C in a fluidized-bed gas phase reactor operated at steady state. These parameters are definided in Eq. (with kt = 0), T= KtM kp m KM Kx Kg (mol-L-¹) + kty [H₂] Ktg 1 + Kp [M] k, [M] = Table Polymerization kinetic parameters for a 5-site-type catalyst. Site 3 Site 1 0.1 Site 2 0.25 1 x 10-4 0.03 5 x 10-5 5 x 10-5 0.01 2.5 x 10-5 0.3 2.5 x 10-5 0.005 1.25 x 10-5 KM + KH where [M] and [H2] are the concentrations of ethylene and hydrogen at the active sites (dissolved in the amorphous polymer phase), respectively. M₁ = [H₂] [M] 1 mi Σ1 Μπι + KB [M] a) Plot the MWD of a polyethylene sample made at the following polymerization conditions: [M] = 0.6 mol/L and [H₂] = 0.04 mol/L. The molar mass of ethylene is 28 mol/g. Site 4 0.25 1.25 x 10-5 0.0025 6.25 x 10-6 b) If you need to make a resin with M₁ = 60,000 by changing only the concentration of hydrogen in the reactor, what would be the required [H₂]? What would be the values of the Mw and D at these conditions? 71 Hint: The average molecular weights, M₁ and Mw, of polymers made with a catalyst having n site types are, Site 5 0.1 6.25 x 10-6 0.00125 3.13 x 10-6 and Mw = [m.Mw₁ W i=1 You should be able to prove these relations based on your knowledge of how Mn and Mw of polymer populations are calculated.
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Chemical Principles The Quest For Insight
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7th Edition
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