Process for the recovery of amorphous devaporized polyalphaolefin

Claim 1

A process for the production of a polyalphaolefin in fluid form which comprises: (a) withdrawing from a bulk polymerization zone maintained at a temperature between about 130° F. and about 175° F. and at a pressure between about 400 psig and about 550 psig through a valve a reactor effluent comprised of amorphous polyalphaolefin and liquid unreacted monomer; (b) directly contacting said effluent immediately upon withdrawal through said valve with a heated devaporized amorphous polyalphaolefin obtained in step (f) below and having a temperature in the range from about 350° F. to about 425° F.; (c) passing the resulting mixture from step (b) to a flash zone maintained at a pressure from about 40 to about 80 psig and a temperature between about 300° F. and about 375° F.; (d) withdrawing a vapor stream of unreacted monomer from said flash zone; (e) withdrawing devaporized amorphous polyalphaolefin from said flash zone; (f) heating a portion of said devaporized polyalphaolefin from step (e) by indirect heat exchange and passing the heated portion to step (b) above, and (g) recovering the remaining portion of said devaporized polyalphaolefin from Step (e) as the product of the process.