IP Library Granted Patent US 9,109,056
Granted Patent B2
US 9,109,056 · App. 12/676,264 · Granted Aug 18, 2015

Method of preparation of spherical support for olefin polymerization catalyst

Inventors: Eun-Il Kim (Daejon, KR); Young-Joo Lee (Inchon, KR); Hoe-Chul Jung (Seosan, KR); Joon-Ryeo Park (Seoul, KR)
Assignee: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
C08F10/00
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Quick Facts
Patent No.
US 9,109,056
App. No.
12/676,264
Granted
Aug 18, 2015
Kind
B2
Abstract

Provided is a method of preparation of a spherical support for an olefin polymerization catalyst. Specifically, provided is a method of preparation of a support which can be used in preparation of an olefin polymerization catalyst, wherein, MgX(I) (X=halogen atom) is prepared by reacting a reaction initiator, nitrogen halide, and magnesium metal, and then magnesium metal and alcohol are reacted in the presence of the MgX, thereby resulting a smooth-surfaced spherical dialkoxy magnesium support having a uniform particle size distribution.

Claims (23)

1. A method of preparation of a spherical support for an olefin polymerization catalyst, comprising:

i) preparing MgX(I), where X is halogen atom, and (I) refers to an oxidation state number by reacting a halogenated nitrogen compound and magnesium metal at a same ratio in equivalent weight; and

ii) reacting magnesium metal and alcohol in the presence of the MgX obtained from the step i),

wherein the halogenated nitrogen compound is at least one selected from the group consisting of the following structures (1), (2), (3), and (4):

(1) N-halide succinimides

where X is a halogen atom, and R 1 , R 2 , R 3 and R 4 are independently hydrogen or C 1 -C 12 alkyl or C 6 -C 20 aryl,

(2) trihaloisocyanuric acids

where X is a halogen atom,

(3) N-halophthalimides

where X is a halogen atom, and R 1 , R 2 , R 3 or R 4 are independently hydrogen, or C 1 -C 12 alkyl or C 6 -C 20 aryl, and

(4) hydantoins

where X is a halogen atom, and R 1 and R 2 are independently hydrogen, or C 1 -C 12 alkyl or C 6 -C 20 aryl.

2. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the alcohol is at least one selected from the group consisting of aliphatic alcohols represented as a general formula of ROH where R is alkyl having C 1 -C 6 and aromatic alcohols.

3. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein, in the reaction of magnesium metal and alcohol, the magnesium metal and the alcohol are used in a ratio of magnesium metal by weight:alcohol by volume=1:5-1:50.

4. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the X in MgX is Cl, Br or I.

5. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the magnesium metal is a powder having a particle size of 10-300 μm.

6. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the magnesium metal is a powder having a particle size of 50-200 μm.

7. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the alcohol is at least one selected from the group consisting of methanol, ethanol, propanol and butanol.

8. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the alcohol is ethanol.

9. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein in the reaction of magnesium metal and alcohol, the magnesium metal and the alcohol are used in a ratio of magnesium metal by weight:alcohol by volume=1:7-1:20.

10. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the reacting the magnesium metal and the halogenated nitrogen compound is performed at a temperature of 25-110° C.

11. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the reacting the magnesium metal and the halogenated nitrogen compound is performed at a temperature of 25-75° C.

12. The method of preparation of a spherical support for an olefin polymerization catalyst according to claim 1 , wherein the reacting magnesium metal and alcohol in the presence of the MgX is performed at a temperature of 75-90° C.

Assignments (5)
CHANGE OF NAME Recorded Dec 1, 2022
From: HANWHA TOTAL PETROCHEMICAL CO., LTD.
To: HANWHA TOTALENERGIES PETROCHEMICAL CO., LTD.
Reel/Frame 062034/0926 →
CORRECTIVE ASSIGNMENT TO CORRECT THE RECEIVING PARTY ADDRESS PREVIOUSLY RECORDED AT REEL: 036548 FRAME: 0271. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Nov 9, 2015
From: SAMSUNG ATOFINA CO., LTD.; SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: HANWHA TOTAL PETROCHEMICAL CO., LTD.
Reel/Frame 037071/0433 →
CHANGE OF NAME Recorded Sep 3, 2015
From: SAMSUNG ATOFINA CO., LTD.; SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: HANWHA TOTAL PETROCHEMICAL CO., LTD.
Reel/Frame 036548/0271 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 10, 2015
From: KIM, EUN-LL; LEE, YOUNG-JOO; JUNG, HOE-CHUL; PARK, JOON-RYEO
To: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
Reel/Frame 036054/0480 →
CHANGE OF ADDRESS OF ASSIGNEE Recorded Jul 14, 2014
From: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
To: SAMSUNG TOTAL PETROCHEMICALS CO., LTD.
Reel/Frame 033312/0388 →
Priority Claims (1)
KR 10-2007-0128627 · Dec 12, 2007 · national
Continuity (1)
Related Publication 20100172820A1 · Jul 8, 2010