FIELD: chemistry.
SUBSTANCE: apparatus includes a reaction vessel and a degassing vessel. In the method, each of the first and second processes includes the following steps: (a) bringing a main olefin and a comonomer into contact with a catalyst in gas-phase polymerisation conditions in a reaction vessel to obtain a first polymer or a second polymer, respectively, wherein said first and second methods employ the same main olefin, the difference between the two methods being at least one of the following factors: (1) the comonomer used and (2) the reaction temperature at which the polymer is obtained, and (b) subsequently bringing the first or second polymer, respectively, into contact with a blowout gas in a degassing vessel. The transition method involves changing the flow rate of the blowout gas in the degassing vessel from a first value X1, which is used when degassing the first polymer, to a second value X2, which is used when degassing the second polymer. The second value is determined relative the flow rate Xi and temperature Ti used at earlier steps of producing the polymer during transitional polymerisation using the same comonomer as in the second process, and reaction temperature T2 in the second process. The method is characterised by that, (a) if T2 increases relative Ti, X2 is at least 1% lower than Xi when T2 is raised every 1°C compared to Ti, (b) if T2 drops relative Ti, X2 is at least 1% higher than Xi when T2 is decreased every 1°C compared to Ti, (c) if T2 is equal to Ti, X2 is equal to or greater than Xi, preferably equal to Xi.
EFFECT: if values Xi and Ti for earlier polymers are set for each comonomer to be used in successive polymerisation to obtain different polymers, the subsequent values of flow rate of the blowout gas X2 for other polymers to be obtained can easily be determined based on said values and temperature T2.
11 cl, 2 tbl, 1 ex
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Authors
Dates
2013-09-20—Published
2009-09-21—Filed