IP Library Granted Patent US 10,898,887
Granted Patent B2
US 10,898,887 · App. 16/326,872 · Granted Jan 26, 2021

Selective solid catalyst for tail end of olefin-epoxidation flow reactor

Inventors: Alexander Okrut (Oakland, CA); Alexander Katz (Richmond, CA)
Assignee: THE REGENTS OF THE UNIVERSITY OF CALIFORNIA
B01J29/89B01J19/0053B01J35/02C07D301/19B01J2219/0004B01J2219/00051B01J2219/308B01J2219/30207B01J2219/30433B01J2219/30475
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 10,898,887
App. No.
16/326,872
Granted
Jan 26, 2021
Kind
B2
Abstract

In one example, a method for converting a first compound into a second compound is provided. The method includes providing the first compound in an entrance of a flow through reactor, wherein the entrance comprises a first catalyst and an oxidant, converting the first compound and the oxidant into the second compound as the first compound and the oxidant contact the first catalyst in the entrance of the flow through reactor while moving towards a tail end of the flow through reactor, and converting the first compound and the oxidant into the second compound via a solid catalyst comprising a white crystalline solid with a titanium content of about 0.5 to about 1.5 weight percent (wt %) in the tail end of the flow through reactor.

Claims (8)

1. A method for converting an olefin into an epoxide, comprising:

providing the olefin in an entrance of a flow through reactor, wherein the entrance comprises a first catalyst and an oxidant, wherein the first catalyst comprises titanium grafted on an amorphous silica support or molybdenum napthenate;

converting the olefin and the oxidant into the epoxide as the olefin and the oxidant contact the first catalyst in the entrance of the flow through reactor while moving towards a tail end of the flow through reactor; and

converting the olefin and the oxidant into the epoxide via a solid catalyst comprising a white crystalline solid with a titanium content of about 0.5 to about 1.5 weight percent (wt %) in the tail end of the flow through reactor.

2. The method of claim 1 , wherein a temperature of the entrance of the flow through reactor is approximately 40 degrees Celsius.

3. The method of claim 1 , wherein conversion of the oxidant in the tail end is greater than 80% at temperatures greater than 110 degrees Celsius.

4. The method of claim 1 , wherein the oxidant comprises an organic hydroperoxide.

5. The method of claim 1 , wherein the converting occurs with a residence time of at least one hour in the tail end of the flow through reactor.

Assignments (2)
CONFIRMATORY LICENSE Recorded Feb 3, 2025
From: UNIVERSITY OF CALIFORNIA BERKELEY
To: NATIONAL SCIENCE FOUNDATION
Reel/Frame 070095/0854 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 11, 2019
From: OKRUT, ALEXANDER; KATZ, ALEXANDER
To: THE REGENTS OF THE UNIVERSITY OF CALIFORNIA
Reel/Frame 050692/0859 →
Continuity (2)
Provisional Application 62378977 · Aug 24, 2016
Related Publication 20200009543A1 · Jan 9, 2020