IP Library Granted Patent US 10,647,625
Granted Patent B2
US 10,647,625 · App. 15/837,382 · Granted May 12, 2020

Single step conversion of ethanol to butadiene

Inventors: Vanessa Dagle (Richland, WA); Robert A. Dagle (Richland, WA)
Assignee: BATTELLE MEMORIAL INSTITUTE
C07C1/24C07C1/20C07C2521/06C07C2521/08C07C2523/42C07C2523/46C07C2523/50
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Quick Facts
Patent No.
US 10,647,625
App. No.
15/837,382
Granted
May 12, 2020
Kind
B2
Abstract

A process for producing 1,3-butadiene (BD) from ethanol in a single step by s7passing a mixture containing ethanol in a gas phase over a multifunctional catalyst having a transition metal dispersion of at least 30% on a silica metal oxide support. In some examples the multifunctional catalyst comprises a silica metal oxide having a surface area of at least 200 m{circumflex over ( )}2/g. The multifunctional catalyst can include a transition metal oxide, a silica metal oxide made from a high purity silica gel, mesoporous silica and fumed silica, such as high purity SBA16, SBA15, or Davisil grade 646.

Claims (14)

1. A method for producing 1,3-butadiene (BI)) from ethanol the method comprising:

passing a gaseous feed containing the ethanol over a multi-functional catalyst to produce the 1,3-butadiene (BD); wherein

the multifunctional catalyst comprises a silica support, said silica support comprises 1-10 wt % ZrO2 and has a Lewis Acid site concentration of 10-35 μmole/gram; and the multifunctional catalyst comprises silver (Ag) or copper (Cu) having a dispersion of at least 40% on the silica metal oxide support.

2. The process of claim 1 wherein the silica ZrO2 support comprises a silica selected from the group consisting of a high purity silica gel, mesoporous silica and fumed silica.

3. The process of claim 2 wherein the silica ZrO2 is a high purity SBA16.

4. The process of claim 2 wherein the silica ZrO2 is high purity SBA15.

5. The process of claim 2 wherein the silica ZrO2 is Davisil grade 646.

6. The process of claim 1 wherein hydrogen is added to the feed.

7. The process of claim 1 wherein the feed is 100% ethanol.

8. The process of claim 1 wherein the feed is a mixture containing at least 30% ethanol and includes water and wherein the process produces a yield that is at least 30% butadiene.

9. The process of claim 1 wherein the step of passing the feed containing ethanol in a gas phase is performed at a temperature between 200° C. and 375° C.

10. A process for producing 1,3-butadiene (BD) from ethanol in a single step, comprising the step of passing a feed containing ethanol in gas phase over a 1% Ag/4% ZrO 2 /SiO 2 -SBA-16 catalyst having a Ag dispersion of at least 40% on the SiO 2 -SBA-16 support.

11. The process of claim 10 wherein the step of passing a feed containing ethanol is performed in operating conditions including a temperature of 325° C., pressure of 1 atm, and a flow rate of 0.23 hr −1 .

12. The process of claim 10 wherein the feed contains at east 30 percent water by weight.

Assignments (2)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 7, 2018
From: DAGLE, VANESSA; DAGLE, ROBERT A.
To: BATTELLE MEMORIAL INSTITUTE
Reel/Frame 044854/0440 →
CONFIRMATORY LICENSE Recorded Jan 10, 2018
From: BATTELLE MEMORIAL INSTITUTE, PACIFIC NORTHWEST DIVISION
To: U.S. DEPARTMENT OF ENERGY
Reel/Frame 044583/0232 →
Continuity (2)
Provisional Application 62455768 · Feb 7, 2017
Related Publication 20180222813A1 · Aug 9, 2018
Cited By (1)
US 12,599,897