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:
Jul. 11, 2017

Filed:

Aug. 11, 2014
Applicants:

Gene W. Bachman, Baton Rouge, LA (US);

Raymond M. Jones, Pearland, TX (US);

Michael D. Cloeter, Lake Jackson, TX (US);

Charles W. Lipp, Lake Jackson, TX (US);

Mark J. Bartel, Baton Rouge, LA (US);

Brady J. Coomes, Drochtersen-Assel, DE;

Scott J. Daigle, Lake Jackson, TX (US);

Steve F. Janda, Lake Jackson, TX (US);

Inventors:

Gene W. Bachman, Baton Rouge, LA (US);

Raymond M. Jones, Pearland, TX (US);

Michael D. Cloeter, Lake Jackson, TX (US);

Charles W. Lipp, Lake Jackson, TX (US);

Mark J. Bartel, Baton Rouge, LA (US);

Brady J. Coomes, Drochtersen-Assel, DE;

Scott J. Daigle, Lake Jackson, TX (US);

Steve F. Janda, Lake Jackson, TX (US);

Assignee:

Dow Global Technologies LLC, Midland, MI (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B23P 19/00 (2006.01); B01J 19/24 (2006.01); B01F 3/04 (2006.01); B01F 3/08 (2006.01); B01F 5/00 (2006.01); B01F 5/02 (2006.01); B01F 15/00 (2006.01); B01F 5/04 (2006.01);
U.S. Cl.
CPC ...
B01F 5/0275 (2013.01); B01F 3/0446 (2013.01); B01F 3/0865 (2013.01); B01F 5/048 (2013.01); B01F 5/0463 (2013.01); B01F 5/0475 (2013.01); B01J 19/2405 (2013.01); B23P 19/00 (2013.01); B01F 15/00844 (2013.01); B01F 2005/0017 (2013.01); B01F 2215/0036 (2013.01); Y10T 29/49826 (2015.01);
Abstract

A mixer for a continuous flow reactor and methods for forming the mixer and the operation thereof. The mixer allows for segmentation of a primary reactant flow through a plurality of ports into many smaller flows that are injected as jets into a secondary reactant flow in channels of the mixer. The channel has a constant width dimension to enhance even flow distribution and local turbulence of the primary and secondary reactant flows. The constant width dimension of the channel and the size and number of the ports of the mixer can be configured to ensure the primary reactant flow injected into the channel directly impinges on a surface of the channel that is opposite the injection point at normal operating conditions.


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