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:
Jun. 19, 2018

Filed:

Apr. 27, 2016
Applicant:

Anellotech, Inc., Pearl River, NY (US);

Inventors:

Charles Sorensen, Haverstraw, NY (US);

Ruozhi Song, Maple Valley, WA (US);

Zachary Goodman, Rochester, MA (US);

Collin Schmidt, Nyack, NY (US);

Scott Johnstone, Peekskill, NY (US);

Kevin Dolan, New City, NY (US);

Megan Wagner, Nyack, NY (US);

Assignee:

ANELLOTECH, INC., Pearl River, NY (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C10B 53/02 (2006.01); C10B 49/22 (2006.01); C10B 57/06 (2006.01); C10G 3/00 (2006.01); C10G 1/08 (2006.01);
U.S. Cl.
CPC ...
C10B 53/02 (2013.01); C10B 49/22 (2013.01); C10B 57/06 (2013.01); C10G 1/083 (2013.01); C10G 1/086 (2013.01); C10G 3/44 (2013.01); C10G 3/57 (2013.01); Y02E 50/14 (2013.01); Y02E 50/32 (2013.01); Y02P 20/145 (2015.11);
Abstract

The present invention provides an improved catalytic fast pyrolysis process for increased yield of useful and desirable products, while greatly reducing or eliminating fouling of various critical process lines which are likely to transfer heavy hydrocarbons, aromatics and oxygenates. The process comprises steps including feeding a fluid solvent stream having a Snyder Polarity Index of at least 2.4 to one or more of i) the raw fluid product stream from a catalytic fast pyrolysis process fluidized bed reactor to a first separation system, ii) the fluid product stream from the first separation system to a quench vapor/liquid separation system, iii) the vapor phase stream from the quench vapor/liquid separation system to a product recovery system, and, optionally, to the spent catalyst steam stripping system upstream of the catalyst regeneration system.


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