Branched Low and Medium Density Polyethylene
The invention relates to a long chain branched medium and low density polyethylene having a combination of the following properties: a) a density of from 0.910 to 0.945 g/cm 3 ; b) an HLMI of from 2 to 150 dg/min and an MI 2 of from 0.01 to 2 dg/min; c) a polydispersity index (PDI) Mw/Mn of at least 7, wherein Mw is the weight average molecular weight and Mn is the number average molecular weight of the polyethylene; and d) and a minimum amount of long chain branching measured by a value selected from one of g rheo and LCBI. The invention also relates to a process for obtaining said polyethylene comprising the following steps: a) injecting ethylene, one or more alpha-olefinic comonomers comprising 3 to 10 carbon atoms and an activated chromium-based catalyst into a gas phase polymerisation reactor; b) copolymerising said ethylene and comonomer in said reactor in the gas phase; and c) retrieving an ethylene copolymer having a density of from 0.910 to 0.945 g/cm 3 from said reactor; said activated catalyst having a chromium concentration of at least 0.1 wt-% and of at most 1.0 wt-% based on the weight of the titanated chromium-based catalyst and a titanium concentration of from 1 wt-% to 5 wt-% based on the weight of the titanated chromium-based catalyst, whereby the catalyst was titanated with vaporised titanium compound and activated at a temperature of at least 500° C.
1 - 22 . (canceled)
23 . A polyethylene comprising:
a density of from 0.910 to 0.945 g/cm 3 ;
an HLMI of from 2 to 150 dg/min and an MI 2 of from 0.01 to 2 dg/min;
a polydispersity index (PDI) Mw/Mn of at least 7, wherein Mw is the weight average molecular weight and Mn is the number average molecular weight of the polyethylene; and
a long chain branching value selected from one of:
a g rheo fulfilling the following equation:
g rheo <1.1/(3.73+6.08*10 −7 ( M w ) 2.5 +0.144/(ln(ρ)))
an LCBI fulfilling the following equation:
LCBI>3.5*(1−(1/3.73+6.08*10 −7 ( M w ) 2.5 +0.144/(ln(ρ)))) 2
wherein in both equations Mw is the weight average molecular weight of the polyethylene expressed in kDa and ρ is the density of the polyethylene expressed in g/cm 3 .
24 . The polyethylene of claim 23 , wherein the polyethylene has a long chain branching value selected from one of:
a g rheo less than 0.65; and
an LCBI greater than 0.56.
25 . The polyethylene of claim 23 , wherein the HLMI is from 2 to 100 dg/min and the MI 2 is from 0.01 to 1 dg/min.
26 . The polyethylene of claim 23 , wherein the density is from 0.915 to 0.935 g/cm 3 .
27 . A polymerisation process:
injecting ethylene, one or more alpha-olefinic comonomers comprising 3 to 10 carbon atoms and an activated chromium-based catalyst into a gas phase polymerisation reactor;
copolymerising said ethylene and comonomer in said reactor in the gas phase; and
retrieving an ethylene copolymer having a density of from 0.910 to 0.945 g/cm 3 from said reactor;
said activated catalyst being previously obtained by:
providing a silica-based support having a specific surface area of at least 250 m 2 /g and of less than 400 m 2 /g and comprising a chromium compound deposited thereon so that the chromium concentration is at least 0.1 wt-% and at most 1.0 wt-% based on the weight of the titanated chromium-based catalyst;
dehydrating the titanated chromium-based catalyst;
titanating the dehydrated titanated chromium-based catalyst in an atmosphere of dry and inert gas containing at least one vaporised titanium compound of the general formula selected from R n Ti(OR″) m and (RO) n Ti(OR′) m , wherein R and R′ are the same or different hydrocarbyl groups containing from 1 to 12 carbon atoms, and wherein n is 0 to 3, m is 1 to 4 and m+n equals 4, to form a titanated chromium-based catalyst having a titanium concentration of from 1 wt-% to 5 wt-% based on the weight of the titanated chromium-based catalyst; and
activating the titanated chromium-based catalyst at a temperature of at least 500° C.
28 . The process of claim 27 , wherein the activated catalyst has a support with a specific surface area of from 250 to 380 m 2 /g.
29 . The process of claim 27 , wherein the activated catalyst has a ratio of specific surface area of the support to chromium content of at least 25000 m 2 /g Cr.
30 . The process of claim 29 , wherein the activated catalyst has a ratio of specific surface area of the support to chromium content of at least 50000 m 2 /g Cr.
31 . The process of claim 27 , wherein the activated catalyst has a ratio of specific surface area of the support to titanium content of from 5000 to 25000 m 2 /g Ti.
32 . The process of claim 31 , wherein the activated catalyst has a ratio of specific surface area of the support to titanium content of from 5000 to 20000 m 2 /g Ti.
33 . The process of claim 27 , wherein the activated titanated chromium-based catalyst is activated at a temperature of from 500 to 850° C.
34 . The process of claim 27 , wherein the activated titanated chromium-based catalyst is activated at a temperature of from 500 to 750° C.
35 . The process of claim 27 , wherein the polymerisation process is carried out in a fluidised bed gas phase polymerisation reactor.
36 . Polyethylene formed by the process of claim 27 .
37 . The polyethylene of claim 36 comprising:
an HLMI of from 2 to 150 dg/min and an MI 2 of from 0.01 to 2 dg/min;
a polydispersity index (PDI) MW/Mn of at least 7, wherein Mw is the weight average molecular weight and Mn is the number average molecular weight of the polyethylene; and
a long chain branching value selected from one of
a g rheo fulfilling the following equation:
g rheo <1.1/(3.73+6.08*10 −7 ( M w ) 2.5 +0.144/(ln(ρ)))
an LCBI fulfilling the following equation:
LCBI>3.5*(1−(1/3.73+6.08*10 −7 ( M w ) 2.5 +0.144/(ln(ρ)))) 2
wherein in both equations Mw is the weight average molecular weight of the polyethylene expressed in kDa and ρ is the density of the polyethylene expressed in g/cm 3 .
38 . An article formed by the polyethylene of claim 36 selected from foamed extruded articles and cable coatings.
39 . A modified polymer comprising:
the polyethylene of claim 36 ; and
a second polyethylene selected from a metallocene-based polyethylene, a Ziegler-Natta-based polyethylene or a chromium-based polyethylene using a chromium-based catalyst different from the catalyst used for the polyethylene of claim 36 , wherein the modified polymer has improved processability when compared to the processability of the second polyethylene alone.