IP Library Granted Patent US 10,099,988
Granted Patent B2
US 10,099,988 · App. 15/550,193 · Granted Oct 16, 2018

Process for production of acrylic acid

Inventors: Jay J. Farmer (Boston, MA); Peter Galebach (Madison, WI); Kyle Sherry (Rochester, NY); Sadesh H. Sookraj (Cambridge, MA)
Assignee: Novomer, Inc.
C07C51/09
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Quick Facts
Patent No.
US 10,099,988
App. No.
15/550,193
Granted
Oct 16, 2018
Kind
B2
Abstract

Provided are integrated processes for the conversion of beta propiolactone to acrylic acid. Systems for the production of acrylic acid are also provided.

Claims (21)

1. A method for producing acrylic acid, comprising:

(a) providing a feedstock stream comprising beta propiolactone;

(b) directing the feedstock stream to a reaction zone;

(c) contacting the feedstock stream with a polymerization catalyst in the reaction zone;

(d) polymerizing at least a portion of the beta propiolactone to poly(propiolactone) in the reaction zone, wherein the temperature of the reaction zone is at or above the pyrolysis temperature of poly(propiolactone);

(e) thermally decomposing the poly(propiolactone) in the reaction zone to produce acrylic acid; and

(f) withdrawing an acrylic acid product stream comprising the acrylic acid from the reaction zone;

wherein steps (b) and (e) occur in the same reaction zone.

2. The method of claim 1 , further comprising directing a return loop comprising a portion of the acrylic acid product stream to the reaction zone.

3. The method of claim 2 , wherein the return loop of acrylic acid is combined with the feedstock stream.

4. The method of claim 1 , wherein the polymerization catalyst is a salt of a compound of formula:

wherein p is 0 to 9.

5. The method of claim 1 , wherein the polymerization catalyst is a salt of a compound of formula:

where p is from 0 to 9 and IV is a non-volatile moiety.

6. The method of claim 1 , wherein the polymerization catalyst is heterogeneous.

7. The method of claim 1 , wherein after removal of all acrylic acid product stream, the polymerization catalyst remains as a salt or melt.

8. The method of claim 7 , further comprising recycling the salt or melt to the reaction zone.

9. The method of claim 1 , wherein the feedstock stream contains or is combined with a high boiling solvent.

10. The method of claim 9 , further comprising withdrawing a recycling stream of the polymerization catalyst from the reaction zone.

11. The method of claim 1 , further comprising directing a return loop of a portion of the acrylic acid product stream to the reaction zone.

12. The method of claim 1 , wherein the feedstock stream is neat.

Assignments (3)
CHANGE OF NAME Recorded Mar 24, 2026
From: NMER WINDDOWN, INC.
To: NOVOMER LLC
Reel/Frame 075187/0876 →
RELEASE OF SECURITY INTEREST Recorded Aug 5, 2022
From: TRUIST BANK
To: NOVOMER, INC.
Reel/Frame 061088/0116 →
SECURITY INTEREST Recorded Feb 1, 2022
From: NOVOMER, INC.
To: TRUIST BANK
Reel/Frame 058922/0803 →
Continuity (2)
Provisional Application 62116325 · Feb 13, 2015
Related Publication 20180016219A1 · Jan 18, 2018
Cited By (2)
US 12,377,405 US 12,606,667