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:
Jan. 31, 2006

Filed:

Aug. 19, 2004
Applicants:

Christopher Lobue, Montgomery, TX (US);

Gilbert Valdez, Pearland, TX (US);

Daniel Herndon, League City, TX (US);

C. Edward Baxter, Jr., League City, TX (US);

Russell E. Reid, Sr., Dayton, TX (US);

Inventors:

Christopher Lobue, Montgomery, TX (US);

Gilbert Valdez, Pearland, TX (US);

Daniel Herndon, League City, TX (US);

C. Edward Baxter, Jr., League City, TX (US);

Russell E. Reid, Sr., Dayton, TX (US);

Assignee:

Texas Petrochemicals LP, Houston, TX (US);

Attorneys:
Primary Examiner:
Int. Cl.
CPC ...
C08F 2/02 (2006.01);
U.S. Cl.
CPC ...
Abstract

Apparatus for olefin polymerization includes one or more shell and tube olefin polymerization reactors, each of which has an olefin polymerization reaction mixture inlet connection and a crude polyolefin product outlet connection. Each reactor is equipped with a recirculation system including a pump arranged to circulate a reaction mixture through the tube side of the reactor independently of the introduction of olefin polymerization reaction mixture into the reactor. The apparatus may also include an inlet reaction mixture distribution manifold and an outlet polymerization reaction mixture collection manifold interconnecting the reactors for operation in parallel. The apparatus also includes catalyst composition and catalyst modifier inlets for each reactor arranged such that a catalyst modifier to may be introduced into each reactor at a rate which is independent of the introduction of catalyst composition.


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