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:
Sep. 01, 2015

Filed:

May. 28, 2014
Applicant:

Clearwaterbay Technology, Inc., Pomona, CA (US);

Inventors:

Vaibhav V. Kelkar, Chino Hills, CA (US);

Drow Lionel O'Young, Walnut, CA (US);

Christianto Wibowo, Chino Hills, CA (US);

Madhura Kelkar, Chino Hills, CA (US);

Hok Chung Chan, Hong Kong, CN;

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C07C 45/73 (2006.01); B01J 8/00 (2006.01); B01J 19/00 (2006.01);
U.S. Cl.
CPC ...
C07C 45/73 (2013.01); B01J 19/0046 (2013.01); B01J 2219/00006 (2013.01); B01J 2219/00306 (2013.01);
Abstract

Embodiments of the present invention describe systems and methods for production of methyl isobutyl ketone (MIBK) from acetone and hydrogen in a two-step process. In a first step, acetone is converted to a product stream containing mesityl oxide (MO) at a temperature in the range of about 0-120° C. and a pressure in the range of about 1-3 atm. The composition of the product stream from the first reaction step is adjusted so that the resulting stream can undergo a favorable liquid-liquid separation in a decanter, and an MO rich product stream can be recovered. The composition of the feed to the decanter is controlled by choosing the number of reactor stages for the first reaction step and their operating temperatures, and/or by recycling some MIBK to the decanter feed. The method does not require a substantially complete conversion of acetone in the first reaction step, nor does it require a removal of DAA from the product of the first reaction step by separation.


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