The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Dec. 02, 2025

Filed:

Apr. 26, 2024
Applicant:

Exxonmobil Chemical Patents Inc., Baytown, TX (US);

Inventors:

Patrick C. Chen, Houston, TX (US);

Mark H. Li, Sugar Land, TX (US);

Jennifer L Rapp, Houston, TX (US);

Pramod J. Nandapurkar, Seabrook, TX (US);

Brian H. Wahn, Houston, TX (US);

Babak Lotfizadehdehkordi, New Hope, PA (US);

Craig J. Emett, Houston, TX (US);

Najeeb M. Kuzhiyil, League City, TX (US);

Jian Yang, Houston, TX (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08F 210/16 (2006.01); C07C 2/30 (2006.01); C07C 2/32 (2006.01); C07C 17/00 (2006.01); C08F 4/659 (2006.01); C08F 4/6592 (2006.01); C08F 110/14 (2006.01);
U.S. Cl.
CPC ...
C08F 210/16 (2013.01); C07C 2/30 (2013.01); C07C 2/32 (2013.01); C07C 17/00 (2013.01); C08F 4/65908 (2013.01); C08F 4/65912 (2013.01); C08F 4/65922 (2013.01);
Abstract

In at least one embodiment, a process to produce a poly alpha-olefin (PAO) includes introducing a first alpha-olefin to a first catalyst system comprising activator and a metallocene compound into a continuous stirred tank reactor or a continuous tubular reactor under first reactor conditions to form a first reactor effluent. The first alpha-olefin is introduced to the reactor at a flow rate of about 100 g/hr or more. The first reactor effluent includes at least 60 wt % of PAO dimer and 40 wt % or less of higher oligomers, where the higher oligomers are oligomers that have a degree of polymerization of 3 or more. The process includes introducing the first reactor effluent and a second alpha-olefin to a second catalyst composition including an acid catalyst in a second reactor to form a second reactor effluent comprising PAO trimer.


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