Process for the polymerization of ethylene

Patent metadata

Field	Value
Publication number	US-10077322-B2
Application number	US-201515533856-A
Country	US
Kind code	B2
Filing date	Dec 1, 2015
Priority date	Dec 9, 2014
Publication date	Sep 18, 2018
Grant date	Sep 18, 2018

Abstract

The present disclosure provides a gas-phase polymerization process for preparing polyethylene, wherein halogenated alcohols in combination with a Ti based catalyst component and aluminum alkyls as co-catalyst suppress ethane formation or increase polymerization activity.

First claim

What is claimed is:

1. A method for reducing ethane generation in the preparation of an ethylene (co)polymer comprising:
polymerizing a gaseous mixture comprising;
(a) ethylene,
(b) hydrogen,
(c) an inert fluidizing gas, and
(d) optionally one or more alpha olefins CH 2 ═CHR where R is a C 1 -C 10 hydrocarbon group,

in the presence of
(i) a catalyst system comprising
(A) a pre-polymerized solid catalyst component comprising a titanium (Ti) compound supported on magnesium dichloride further comprising an internal donor (ID) selected from the group consisting of ethers, esters, amines and ketones, and
(B) an aluminum alkyl compound, and
(C) a halogenated alcohol of the general formula AOH,

where A is a C 1 -C 10 saturated or unsaturated hydrocarbon group wherein at least one of the hydrogen atoms is replaced by chlorine,
wherein the molar ratio of AOH to Ti is about 0.5 to about 8.

2. The method of claim 1 , wherein the A group has up to 8 carbon atoms.

3. The method of claim 1 , wherein the A group is a saturated linear hydrocarbon group having up to four carbon atoms.

4. The method of claim 1 , wherein the chlorine atom replaces one or more hydrogen atoms linked on the carbon atom in alpha position with respect to the hydroxyl group.

5. The method of claim 1 , wherein at least two atoms of hydrogen are replaced by chlorine atoms.

6. The method of claim 1 , wherein the gas mixture comprises the alpha-olefins and the R group is selected among C 1 -C 5 linear alkyl groups.

7. The method of claim 1 , wherein the compound (C) is 2,2,2,-trichloroethanol.

8. The method of claim 1 , wherein the halogenated alcohol (C) is used in an amount such as to give a molar ratio (C)/Ti ranging from about 0.1 to about 10, where Ti is the titanium molar amount within component (A).

9. The method of claim 8 , wherein the (C)/Ti molar ratio ranges from about 0.5 to about 8.

10. The method of claim 9 , wherein the ID is used in an amount such as to give a ID/Ti ratios from about 0.1 to about 8.

11. The method of claim 1 , wherein the process is carried out at a temperature of about 60 to about 130° C. and at total gas phase from about 10 to about 40 bar.

12. The method of claim 1 , further comprising the following steps in any mutual order:
a) polymerizing ethylene, optionally together with one or more comonomers, in a gas-phase reactor in the presence of a first amount of hydrogen and a catalyst system comprising (A) a pre-polymerized solid catalyst component comprising a titanium compound supported on magnesium dichloride, (B) an aluminum alkyl compound, and (C) a halogenated alcohol of the general formula AOH, where A is a C 1 -C 10 saturated or unsaturated hydrocarbon group in which at least one of the hydrogen atoms is replaced by a chlorine atom;
b) copolymerizing ethylene with one or more comonomers in a second gas-phase reactor in the presence of (i) a second amount of hydrogen less than the first amount of hydrogen in step a) and (ii) the catalysts system as defined in step (a);
wherein, in at least one of the gas-phase reactors, the growing polymer particles flow upward through a first polymerization zone (riser) under fast fluidization or transport conditions, leave the riser and enter a second polymerization zone (downcomer) through which the particles flow downward under the action of gravity, leave the downcomer and are reintroduced into the riser, thereby establishing a circulation of polymer between two polymerization zones.

13. The method of claim 1 , wherein the molar ratio of AOH to Ti is about 0.5 to about 6.

Assignees

• Basell Poliolefine Italia Srl

Inventors

• Baita Pietro
• DALL'OCCO Tiziano
• Di Diego Maria
• Liguori Dario
• Marturano Lorella
• Maus Andreas
• Mei Gabriele
• Meier Gerhardus
• Morini Giampiero
• Pica Roberta
• Schueller Ulf

Classifications

• C08F2/34 Primary

  Polymerisation in gaseous state · CPC title

• C08F2500/12

  Melt flow index or melt flow ratio · CPC title

• C08F4/6494

  containing oxygen · CPC title

• C08F110/02 Primary

  Ethene · CPC title

• C08F4/6543

  halides of magnesium · CPC title