Bulk polymerization of cycloolefins

Claim 2

A process comprising the steps of conveying a reactive liquid mix into a mold maintained at an elevated temperature whereby ring opening polymerization in bulk of said liquid mix is thermally initiated, and extracting a molded product from the mold; said liquid mix comprising an organoammonium catalyst selected from organoammonium molybdates and organoammonium tungstates, an alkoxyalkylaluminum halide or aryloxyalkylaluminum halide cocatalyst, and at least one norbornene-type monomer.

Claim 3

Process of claim 1 wherein said norbornene-type monomer is selected from the following monomers, and mixtures thereof: ##STR3## where R and R 1 are independently selected from hydrogen, alkyl, and aryl groups of 1 to 20 carbon atoms, and saturated and unsaturated cyclic groups containing 3 to 12 carbon atoms formed by R and R 1 and the two ring carbon atoms connected thereto; amount of said catalyst being 0.01 to 50 millimoles molybdenum or tungsten per mole of total norbornene-type monomer and the molar ratio of said cocatalyst as aluminum to said catalyst as molybdenum or tungsten is in the range of about 200:1 to 1:10.

Claim 4

Process of claim 2 wherein R and R 1 of said norbornene-type monomer are independently selected from hydrogen and alkyl groups of 1 to 2 carbon atoms; wherein said liquid mix has a pot life of at least about one hour at room temperature and is polymerized in less than 5 minutes after being thermally initiated; and wherein said catalyst is defined by the following formulas I and II: [R.sub.4 N].sub.(2y-6x) M.sub.x O.sub.y (I) [R.sup.1.sub.3 NH].sub.(2y-6x) M.sub.x O.sub.y (II) where each R and R 1 group is independently selected from hydrogen, alkyl, and alkylene groups each containing 1 to 20 carbon atoms, and cycloaliphatic groups each containing 5 to 16 carbon atoms, the sum of all carbon atoms represented by said R groups is 20 to 72 and the sum of all carbon atoms represented by said R 1 groups is 15 to 54; M is selected from molybdenum (VI) and tungsten (VI): and x and y represent the number of M and O atoms in the molecule.

Claim 5

Process of claim 3 wherein said cocatalyst is defined by the formula (RO).sub.a R'.sub.b AlX.sub.c where R is selected from alkyl and aryl groups containing 1 to 18 carbon atoms, R' is an alkyl group of 1 to 18 carbon atoms, X is a halogen, and (a), (b) and (c) represent equivalents of RO, R' and X, respectively, where (a) is about 1/2 to 21/2, (b) is about 1/4 to 2, and (c) is about 1/2 to 2.

Claim 6

Process of claim 3 wherein in reference to said cocatalyst the R group is an alkyl group of 2 to 4 carbon atoms and the R 1 group also contains 2 to 4 carbon atoms; said liquid mix is heated in the mold to a temperature above 50° C.

Claim 7

Process of claim 4 wherein said norbornene-type monomer is selected from substituted and unsubstituted 2-norbornenes, dicyclopentadienes, dihydrodicyclopentadienes, trimers of cyclopentadienes, tetracyclodoecenes, and mixtures thereof; and said liquid mix has a pot life of about 1 to 8 hours at room temperature and is polymerized in the mold at a mold temperature in the range of 60° to 200° C.

Claim 8

Process of claim 5 wherein said norbornene-type monomer is selected from norbornene, methylnorbornene, tetracyclododecene, methyltetracyclododecene, dicyclopentadiene, tricyclopentadiene, and mixtures thereof; pot life at room temperature of said liquid mix being about 1 hour to 8 hours and said liquid mix is polymerized in less than 2 minutes in a mold at a mold temperature in the range of 60° to 200° C.

Claim 9

Process of claim 2 including the steps of preparing said liquid mix from two monomer mixtures, one mixture containing said monomer and said catalyst and the second mixture containing said monomer and said cocatalyst, by mixing the two monomer mixtures in a predetermined proportion at a temperature at which polymerization reaction is essentially dormant for a period of at least one-half minute, conveying the resulting reactive liquid mix to a mold maintained at an elevated temperature at which polymerization is thermally initiated; and extracting a molded product from the mold.

Claim 10

Process of claim 5 wherein said catalyst is selected from tridodecylammonium, methyltricaprylammonium, tri(tridecylammonium) and trioctylammonium molybdates and tungstates; and (a), (b) and (c) of said cocatalyst are defined by the area ABCD in the plot of FIG. 1.

Claim 11

Process of claim 9 wherein said polymerization is conducted under a blanket of nitrogen, and said halide in said cocatalyst is selected from chlorine, bromine and iodine.

Claim 12

Product produced by the process of claim 1.

Claim 13

Product produced by the process of claim 10.