## Abstract A first‐order Markovian terpolymer model is used to describe the arrangement of ethylene (1), inverted propylene (2), and normal propylene (3) units in an ethylene‐propylene chain by means of chain propagation probabilities (__P__ set) and corresponding reactivity ratios (__r__ set). Fr
Chain structure of homogeneous ethylene-propylene copolymers showing inversion, described on the basis of 13C-NMR data. II. Application
✍ Scribed by V. B. F. Mathot; Ch. C. M. Fabrie; G. P. J. M. Tiemersma-Thoone; G. P. M. Van Der Velden
- Publisher
- John Wiley and Sons
- Year
- 1990
- Tongue
- English
- Weight
- 808 KB
- Volume
- 28
- Category
- Article
- ISSN
- 0887-6266
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✦ Synopsis
Abstract
For a series of homogeneous ethylene‐propylene copolymers with mole fraction ethylene (x~1~) ranging between 0.40 and 0.85, the inversion (I) independent propagation probabilities (P~ij~s) and reactivity ratios ( r~ij~s) and the methylene, ethylene, and propylene sequence length distributions have been determined from ^13^C nuclear magnetic resonance (NMR) data, using a first‐order Markovian terpolymer [ethylene (1), inverted propylene (2), and normal propylene (3)] model. For each sample, the limiting values of I (I~min~, I~max~) are given. Calculations of the common parameters for 19 samples show that the polymerization direction characterized by the r set and I is statistically more probable than the opposite direction, which is characterized by the r′ set and I′. Further, I = I~min~ appears to be close to the most probable value of I. The resulting r set is r~12~ = 119, r~13~ = 19.7 and, for I = I~min~, r~21~ = 0, r~31~ = 0.034, r~32~ = 2.98. In the limited range 0.60 < x~1~ < 0.85, there appears to be no preference for either polymerization direction, so that the solutions characterized by the r set and I = I~min~ and by the r′‐set and I = I′~max~, respectively, are about equally probable. If the copolymer reactivity ratios r~e~ and r~p~ are defined in the usual manner, it follows that for the limited range r~e~ = 17. In the model used here, r~p~ is found to be dependent on the ethylene‐propylene ratio in the reactor. Nevertheless, it can be stated that r~p~ ≅ 0.029 and r~e~ r~p~ ≅ 0.50.
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