Methods for preparation of propylene polymers

Patent metadata

Field	Value
Publication number	US-9751965-B2
Application number	US-201314067289-A
Country	US
Kind code	B2
Filing date	Oct 30, 2013
Priority date	Oct 30, 2012
Publication date	Sep 5, 2017
Grant date	Sep 5, 2017

Abstract

Disclosed herein is a polymerization method of propylene, which can prepare a propylene homopolymer with both high fluidity and high rigidity as well as a propylene/α-define copolymer having both high fluidity and a good rigidity-toughness balance by, for example, control of polymerization steps and elevation of polymerization temperature, while the catalyst still maintains a relatively high polymerization activity.

First claim

What is claimed is:

1. A method for polymerization of propylene, comprising:
(1) performing pre-polymerization of propylene or an olefin mixture containing propylene and at least one another α-olefin comonomer in a gas phase or a liquid phase in the presence of a Ziegler-Natta catalyst at a temperature ranging from −10° C. to 50° C. and under a pressure ranging from 0.1 MPa to 10.0 MPa to obtain a propylene prepolymer, wherein the pre-polymerization multiplication is controlled within the scope ranging from 2 to 3000 g polymer/g catalyst; wherein the Ziegler-Natta catalyst comprises a reaction product of the following components:
(i) at least one titanium-containing solid catalyst component;
(ii) at least one alkyl aluminum compound; and
(iii) optionally, at least one external electron donor component,
and wherein the at least one titanium-containing solid catalyst component of the component (i) is a reaction product of contacting at least one alkoxy magnesium compound, at least one titanium compound and at least one internal electron donor compound,
wherein
the at least one titanium compound is selected from compounds of formula: Ti(OR) 4-n X n , in which R is selected from C 1 -C 14 aliphatic or aromatic hydrocarbonyl group, X is a halogen atom, n is an integer from 0 to 4 and in case of n being equal to or less than 2, the existing R groups can be same or different;
the at least one internal electron donor compound is selected from alkyl esters of aliphatic and aromatic monocarboxylic acids, alkyl esters of aliphatic and aromatic polycarboxylic acids, aliphatic ethers, cycloaliphatic ethers and aliphatic ketones; and
the at least one alkoxy magnesium compound is selected from the compounds of formula Mg(OR 1 ) 2-m (OR 2 ) m , wherein R 1 is ethyl, R 2 is (2-ethyl)hexyl, and 0.001≦m≦0.5;
(2) performing a homopolymerization of propylene or copolymerization of propylene and at least one another α-olefin comonomer in a gas phase in the presence of the propylene prepolymer as obtained in step (1) under conditions of 91-150° C. and 1-6 MPa to obtain a propylene polymer, wherein the polymerization time ranges from 0.5 h to 4 h;
(3) continuing the homopolymerization or copolymerization of propylene in a gas phase or a liquid phase in the presence of the product as obtained in step (2) under conditions of 50-150° C. and 1-6 MPa.

2. The method for polymerization of propylene according to claim 1 , wherein the pre-polymerization multiplication is controlled within the scope ranging from 3 to 2000 g polymer/g catalyst.

3. The method for polymerization of propylene according to claim 1 , wherein, in step (2), the temperature ranges from 91 to 130° C.

4. The method for polymerization of propylene according to claim 3 , wherein, in step (2), the temperature ranges from 91 to 110° C.

5. The method for polymerization of propylene according to claim 1 , wherein the individual steps are performed in one reactor for the batch polymerization operation, or performed in different reactors for continuation polymerization operation.

6. The method for polymerization of propylene according to claim 1 , wherein in step (1), the pre-polymerization temperature ranges from 0 to 30° C. and the pre-polymerization pressure ranges from 1.0 to 6.0 MPa.

7. The method for polymerization of propylene according to claim 6 , wherein, in step (1), the pre-polymerization temperature ranges from 10 to 25° C.

8. The method for polymerization of propylene according to claim 6 , wherein, in step (1), the pre-polymerization pressure ranges from 1.5 to 5.5 MPa.

9. The method for polymerization of propylene according to claim 1 , wherein the at least another α-olefin comonomer has the carbon atom number of 2 to 6 but not 3.

10. The method for polymerization of propylene according to claim 1 , wherein the gas phase polymerization of propylene in step (2) is performed in a horizontal reaction kettle having a horizontal agitating shaft and a stirring speed of 10-150 rpm, in which the agitating blade is selected from T-shape, rectangle shape, inclined paddle, door shape, wedge-shape and any combination thereof, and the reaction kettle uses a quench liquid to remove heat.

11. The method for polymerization of propylene according to claim 1 , wherein the polymer obtained in step (2) has a melt flow rate MFR of 20-1000 g/10 min, as measured according to ISO1133 under 230° C. and 2.16 kg load.

12. The method for polymerization of propylene according to claim 1 , wherein the gas phase homopolymerization or copolymerization of propylene in step (3) is performed at the polymerization temperature of 55-110° C., and the polymer obtained in step (3) has a melt flow rate MFR of 1-500g/10min, as measured according to ISO1133 under 230° C. and 2.16 kg load.

13. The method for polymerization of propylene according to claim 1 , wherein a liquid phase bulk pre-polymerization of propylene is performed at 0-30° C. in step (1); a gas phase homopolymerization of propylene is performed at 91-110° C. in step (2); and the gas phase homopolymerization or copolymerization of propylene is continued in the presence of the product as obtained in step (2) at 55-110° C. in step (3), wherein the weight ratio of the polymers obtained in steps (2) and (3) ranges from 0.3:1 to 3:1.

14. The method for polymerization of propylene according to claim 13 , wherein the weight ratio of the polymers obtained in steps (2) and (3) ranges from 1.0:1 to 2.0:1.

15. The method for polymerization of propylene according to claim 1 , wherein a homopolymerization of propylene is performed in steps (1) and (2), while a copolymerization of propylene and at least one another α-olefin comonomer is performed in step (3).

16. The method for polymerization of propylene according to claim 1 , wherein the at least one another α-olefin comonomer is selected from ethylene, butylene and hexylene.

17. The method for polymerization of propylene according to claim 15 , wherein in step (3) the copolymerization is performed using ethylene in an amount ranging from 4 to 40 wt % relative to the weight of propylene homopolymer as obtained in step (2).

18. The method for polymerization of propylene according to claim 17 , wherein in step (3) the copolymerization is performed using ethylene in an amount ranging from 6 to 30 wt % relative to the weight of propylene homopolymer as obtained in step (2).

19. The method for polymerization of propylene according to claim 1 , wherein 0.001≦m≦0.25.

20. The method for polymerization of propylene according to claim 19 , wherein 0.001≦m≦0.1.

21. The method for polymerization of propylene according to claim 1 , wherein the at least one internal electron donor compound is selected from alkyl esters of C 1 -C 4 saturated aliphatic carboxylic acids, alkyl esters of C 7 -C 8 aromatic carboxylic acids, C 2 -C 6 aliphatic esters, C 3 -C 4 cyclic ethers, C 3 -C 6 saturated aliphatic ketones, and 1,3-diether compounds.

Assignees

• China Petroleum & Chem Corp
• Beijing Res Inst Chemical Ind China Petroleum & Chemical Corp

Inventors

• Yu Luqiang
• Yang Zhichao
• Chen Jiangbo
• Zhang Jianxin
• Du Yafeng
• Tong Qinyu
• Sun Kang
• Liu Yang
• Zou Jie
• Wang Lusheng
• Dai Zengyue
• Tan Zhong

Classifications

• C08F4/16

  of silicon, germanium, tin, lead, titanium, zirconium or hafnium · CPC title

• C08F2500/12

  Melt flow index or melt flow ratio · CPC title

• C08F4/022

  Magnesium halide as support anhydrous or hydrated or complexed by means of a Lewis base for Ziegler-type catalysts · CPC title

• C08F210/06 Primary

  Propene · CPC title

• C08F10/06 Primary

  Propene · CPC title