IP Library Granted Patent US 9,555,404
Granted Patent B2
US 9,555,404 · App. 14/135,674 · Granted Jan 31, 2017

Catalyst composition and process for di-, tri- and/or tetramerization of ethylene

Inventors: Peter M. Fritz (Unterhaching, DE); Heinz Bölt (Wolfratshausen, DE); Anina Wöhl (Pullach, DE); Wolfgang Müller (Munich, DE); Florian Winkler (Munich, DE); Anton Wellenhofer (Munich, DE); Uwe Rosenthal (Lambrechtshagen, DE); Bernd H. Müller (Rostock, DE); Marko Hapke (Rostock, DE); Normen Peulecke (Rostock, DE); Mohammed Hassan Al-Hazmi (Riyadh, SA); Vugar O. Aliyev (Riyadh, SA); Fuad Mohammed Mosa (Riyadh, SA)
Assignees: SAUDI BASIC INDUSTRIES CORPORATION; LINDE AG
B01J31/2495B01J31/143B01J31/189B01J31/1885C07C2/32C07C2/36C07F9/224C07F9/46C07F9/4883C07F9/6587C07F9/65848B01J2231/20B01J2531/0258B01J2531/62C07C2531/14C07C2531/24Y02P20/52
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,555,404
App. No.
14/135,674
Granted
Jan 31, 2017
Kind
B2
Abstract

A catalyst composition and a process for di-, tri- and/or tetramerization of ethylene, wherein the catalyst composition comprises a chromium compound, a ligand of the general structure R 1 R 2 P—N(R 3 )—P(R 4 )—N(R 5 )—PR 6 R 7 , or any cyclic derivatives thereof, wherein at least one of the P or N atoms of the PNPNP-unit is member of a ring system, the ring system being formed from one or more constituent compounds of the ligand by substitution, and a co-catalyst or activator.

Claims (27)

1. A catalyst composition comprising:

(a) a chromium compound;

(b) a ligand of the general structure R 1 R 2 P—N(R 3 )—P(R 4 )—N(R 5 )—PR 6 R 7

wherein R 1 , R 2 , R 3 , R 4 , R 5 , R 6 and R 7 are independently selected from halogen, amino, trimethylsilyl, C 1 -C 10 -alkyl, phenyl, benzyl, tolyl and xylyl; and

(c) an activator or co-catalyst;

wherein the concentration of the chromium compound is from 0.1 to 10 mmol/l;

wherein the chromium compound is CrCl 3 (THF) 3 , Cr(III)acetylacetonate, Cr(III)octanoate, chromium hexacarbonyl, Cr(III)-2-ethylhexanoate or (benzene)tricarbonyl-chromium.

2. The catalyst composition according to claim 1 , wherein R 1 , R 2 , R 3 , R 4 , R 5 , R 6 and R 7 are selected from chloro, amino, methyl, ethyl, isopropyl, and tert-butyl.

3. The catalyst composition according to claim 1 , wherein the activator or co-catalyst is selected from trimethylaluminum, triethylaluminum, tri-isopropylaluminum, tri-isobutylaluminum, ethylaluminumsesquichloride, diethylaluminum chloride, ethylaluminumdichloride, methylaluminoxane (MAO) or mixtures thereof.

4. The catalyst composition according to claim 1 , further comprising a solvent, wherein the solvent is an aromatic hydrocarbon, a straight-chain aliphatic hydrocarbon, a cyclic aliphatic hydrocarbon, a straight-chain olefin, an ether, or mixtures thereof.

5. The catalyst composition according to claim 4 , wherein the solvent is selected from toluene, benzene, ethylbenzene, cumene, xylene, mesitylene, hexane, octane, cyclohexane, methylcyclohexane, hexene, heptene, octene, diethylether, tetrahydrofuran or mixtures thereof.

6. The catalyst composition according to claim 1 , wherein the ligand/Cr ratio is 0.8 to 2.0.

7. The catalyst composition according to claim 3 , wherein the Al/Cr ratio is from 10:1 to 200:1.

8. A catalyst composition; obtained by combining at least;

(a) a chromium compound;

(b) a ligand of the general structure

R 1 R 2 P—N(R 3 )—P(R 4 )—N(R 5 )—PR 6 R 7 ,

wherein R 1 , R 2 , R 3 , R 4 , R5, R 6 and R 7 are independently selected from halogen, amino, trimethylsilyl, C 1 -C 10 -alkyl, phenyl, benzyl, tolyl and xylyl; and

(c) an activator or co-catalyst;

wherein the concentration of the chromium compound is from 0.1 to 10 mmol/l;

wherein the chromium compound is CrCl 3 (THF) 3 , Cr(III)acetylacetonate, Cr(III)octanoate, chromium hexacarbonyl, Cr(III)-2-ethylhexanoate or (benzene)tricarbonyl-chromium.

9. A process for di-, tri- or tetramerization of ethylene, comprising contacting ethylene with the catalyst composition of claim 1 under ethylene oligomerization conditions.

10. The process according to claim 9 , wherein said contacting is carried out at a pressure of 10 to 50 bar.

11. The process according to claim 9 , wherein said contacting is carried out at a temperature of from 20° C. to 100° C.

12. The process according to claim 9 , wherein the process is carried out continuously with a mean residence time of from 1 to 4 hours.

13. The process according to claim 9 comprising subjecting the catalyst to a gas phase of ethylene.

14. The process according to claim 9 , wherein said contacting is carried out in a reactor.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 1, 2019
From: LINDE AG
To: SABIC GLOBAL TECHNOLOGIES B.V.
Reel/Frame 049634/0310 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 8, 2014
From: FRITZ, PETER M.; BÖLT, HEINZ; WÖHL, ANINA; MÜLLER, WOLFGANG; WINKLER, FLORIAN; WELLENHOFER, ANTON; ROSENTHAL, UWE; MÜLLER, BERND H.; HAPKE, MARKO; PEULECKE, NORMEN; AL-HAZMI, MOHAMMED HASSEN; ALIYEV, VUGAR O.; MOSA, FUAD MOHAMMED
To: SAUDI BASIC INDUSTRIES CORPORATION; LINDE AG
Reel/Frame 032851/0486 →
Priority Claims (1)
EP 07013543 · Jul 11, 2007 · regional
Continuity (2)
Continuation 12452594
Related Publication 20140179970A1 · Jun 26, 2014