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filingDate 2008-08-29-04:00^^<http://www.w3.org/2001/XMLSchema#date>
inventor http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_a96ff9fa44aa797ed0b101a8ff8c579d
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publicationDate 2010-06-04-04:00^^<http://www.w3.org/2001/XMLSchema#date>
publicationNumber KR-20100059833-A
titleOfInvention Slurry Phase Polymerization Method
abstract 20 to 80% by weight of the first polymer in the first reactor is prepared as a suspension, 80 to 20% by weight of the second polymer is prepared as a suspension in the second reactor in the presence of the first polymer and the stream or slurry containing the polymer obtained is At least 50 mole percent of the liquid component of the slurry, or non-polymeric component of the stream, exiting the reactor and entering the flash tank is transported to a flash tank operated at a pressure and at a temperature such that the flash is discharged from the flash tank. The concentration of components with a molecular weight of less than 50 g / mol in the stream or slurry entering the tank C lights (mol%) is given by the formula: C lights <7 + 0.07 (40-T c ) + 4.4 (P c -0.8)-7 ( C H2 / C Et) [wherein, T c and P c are respectively the temperature (℃) and pressure (MPa g) at the location where the vapor is condensed to be discharged from the flash tank, C H2 and C Et are hydrogen and Process for producing a multimodal polyethylene in the respective flash ethylene molar Im] more than one reactor, connected in series to meet in the tank.
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