IP Library Granted Patent US 7,700,810
Granted Patent B2
US 7,700,810 · App. 12/196,485 · Granted Apr 20, 2010

Catalytic conversion of ethanol to a 1-butanol-containing reaction product using a thermally decomposed hydrotalcite catalyst

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 7,700,810
App. No.
12/196,485
Granted
Apr 20, 2010
Kind
B2
Abstract

Hydrotalcites are partially or fully thermally decomposed to provide catalysts useful for the conversion of ethanol to a reaction product comprising 1-butanol.

Claims (26)

1. A process for making a 1-butanol-containing product, said process comprising:

contacting a reactant comprising ethanol with a catalyst at a reaction temperature and pressure sufficient to produce said product, wherein said catalyst is derived from a hydrotalcite of the formula:

(M 2+ 1−x M 3+ x (OH) 2 )(A n− x/n ). y H 2 O

wherein

M 2+ is divalent Mg, or a combination of divalent Mg and at least one divalent member selected from the group consisting of Zn, Ni, Pd, Pt, Co, Fe, and Cu;

M 3+ is trivalent Al, or a combination of trivalent Al and at least one trivalent member selected from the group consisting of Fe and Cr;

x is 0.66 to 0.1;

A n− is CO 3 2− with n=2 or OH − with n=1; and

y is 0 to 4;

wherein the hydrotalcite catalyst is partially decomposed.

2. The process of claim 1 , wherein the decomposition is achieved by heating for a time and at a temperature sufficient to cause a diminution in the hydrotalcite powder X-ray diffraction pattern peak intensities between 2θ angles of 10 degrees and 70 degrees using CuKα radiation.

3. The process of claim 1 , wherein M 2+ is divalent Mg.

4. The process of claim 1 , wherein M 3+ is trivalent Al.

5. The process of claim 1 , wherein A n− is CO 3 2− .

6. The process of claim 1 , wherein A n− is OH − .

7. The process of claim 1 , wherein M 2+ is Mg 2+ ; M 3+ is Al 3+ ; A n− is OH − ; n is 1; x is 0.247; and y is 0.5.

8. The process of claim 1 , wherein M 2+ is Mg 2+ ; M 3+ is Al 3+ ; A n− is CO 3 2− ; n is 2; x is 0.25; and y is 0.5.

9. The process of claim 1 , wherein said reaction temperature is from about 200° C. to about 500° C., and said pressure is from about 0.1 MPa to about 20.7 MPa.

10. The process for making the 1-butanol-containing product of claim 1 , said process comprising:

contacting a reactant comprising ethanol with a catalyst at a reaction temperature and pressure sufficient to produce said product, wherein said catalyst is made by a method comprising:

a) dissolving a soluble (i) sodium or potassium carbonate or sodium or potassium bicarbonate, or (ii) sodium, potassium or ammonium hydroxide, or (iii) a mixture of (i) and (ii), in water to form a first solution and heating the first solution to between 60° C. and 70° C.;

b) adjusting the pH of the first solution with hydroxide to a pH of approximately 10;

c) adding to the first solution (i) at least one magnesium salt and optionally salts of one or more divalent metals selected from the group consisting of Zn, Ni, Pd, Pt, Co, Fe, and Cu; and (ii) at least one aluminum salt and optionally salts of one or more trivalent metals selected from Fe or Cr, wherein (a) said salts are in one or more aqueous solutions, and (b) the magnesium and optional divalent metals of (i) and the aluminum and optional trivalent metals of (ii) are in a molar ratio between 0.5/1 and 9/1 inclusive, thereby forming a suspension whose pH is maintained at approximately 10;

d) optionally stirring the suspension and maintaining the suspension at a temperature between 60° C. and 70° C.;

e) aging the suspension of step (c) or step (d) to form a precipitate and separating the precipitate from the suspension; and

f) partially decomposing the precipitate by heating it for a time and at a temperature sufficient to cause a diminution in hydrotalcite powder X-ray diffraction pattern peak intensities between 2θ angles of 10 degrees and 70 degrees using CuKα radiation, thereby forming said catalyst.

Assignments (4)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 4, 2022
From: DUPONT US HOLDING, LLC
To: VIRIDIS CHEMICAL, LLC
Reel/Frame 058897/0129 →
CORRECTIVE ASSIGNMENT TO CORRECT THE DESIGNATION OF ASSIGNEE AS A DELAWARE CORPORATION TO A DELAWARE LIMITED LIABILITY COMPANY PREVIOUSLY RECORDED ON REEL 049880 FRAME 0001. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Aug 28, 2019
From: E. I. DU PONT DE NEMOURS AND COMPANY
To: DUPONT US HOLDING, LLC
Reel/Frame 051502/0610 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 26, 2019
From: E. I. DU PONT DE NEMOURS AND COMPANY
To: DUPONT US HOLDING, LLC
Reel/Frame 049880/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 24, 2008
From: KOURTAKIS, KOSTANTINOS; D'AMORE, MICHAEL B; MANZER, LEO ERNEST
To: E. I. DU PONT DE NEMOURS AND COMPANY
Reel/Frame 021730/0356 →