Appeal No. 2007-0111 Reexamination 90/006,297 1 2 91. In addition, the ‘097 specification stated (page 6): 3 It has been found, also, that even when ethylene is 4 polymerized with the aid of the special promoters 5 obtained by reaction of the heavy metal and metal alkyl 6 compounds, in the ratios proposed for promoting 7 ethylene polymerization, the presence of any substantial 8 amount of the higher olefines inhibits polymerization of 9 the ethylene, while the higher olefines, if they react at all, 10 do so only at very low reaction rates and, in any case, 11 without yielding polymers of the type with which this 12 invention is concerned. [Emphasis added.] 13 14 92. The ‘097 specification states (page 12): 15 The method of this invention may be used for 16 polymerizing vinyl hydrocarbons of the formula given 17 including propylene, butene-1, pentene-1, hexene-1, 18 styrene, and so on, as well as mixtures thereof and 19 mixtures of the vinyl hydrocarbon with small amounts of 20 ethylene. [Emphasis added.] 21 22 93. Application 03/710,840 contained the following (specification, page 23 1): 24 This invention relates to a process for polymerizing 25 unsaturated hydrocarbons of the formula 26 CH2 = CHR 27 in which R is a saturated aliphatic, an alicyclic or an 28 aromatic radical, alone, in mixture with one another, or in 29 mixture with small amounts, up to about 5%, of a 30 monomer polymerizable therewith. 31 Uniquely, the initial polymerization products obtained by 32 the present method are mixtures of linear, head-to-tail 33 amorphous and crystalline polymers having no branches 34 longer than R. The polymers can be separated from the 35 polymerizate by fractional dissolution. The crystalline 30Page: Previous 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 Next
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