IP Library Granted Patent US 12,264,355
Granted Patent B2
US 12,264,355 · App. 17/286,372 · Granted Apr 1, 2025

Process for producing ammonium (meth-) acrylate

Inventors: Diego Ghislieri (Ludwigshafen, DE); Peter Oedman (Saint Joseph, MO); Tobias Joachim Zimmermann (Ludwigshafen, DE); Anna-Corina Schmidt (Trostberg, DE)
Assignee: BASF SE
C12P7/40C12M29/18C12M41/18C12N9/78C12Y305/05001
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 12,264,355
App. No.
17/286,372
Granted
Apr 1, 2025
Kind
B2
Abstract

The present invention relates to a process for preparing ammonium (meth-) acrylate, aqueous ammonium (meth-) acrylate solutions obtainable by such process, and (meth-) acrylic acid homopolymers or copolymers obtainable by polymerizing such ammonium (meth-) acrylate. The invention furthermore relates to a modular, relocatable bioconversion unit for manufacturing aqueous ammonium (meth-) acrylate solutions.

Claims (19)

1. A process for producing ammonium (meth-) acrylate, said process comprising the following steps:

(a) adding the following components (i) to (iii) to a reactor to obtain a composition for bioconversion:

(i) a biocatalyst capable of converting (meth-) acrylonitrile to ammonium (meth-) acrylate;

(ii) (meth-) acrylonitrile;

(iii) aqueous medium; and

(b) performing a bioconversion on the composition obtained in step (a) in a reactor;

wherein the reactor is a relocatable bioconversion unit, the unit comprising:

a single walled reaction vessel, the vessel having;

a volume from 10 m 3 to 150 m 3 ;

means for mixing the composition of step (a); and

means for controlling the temperature of the composition of step (a).

2. Process according to claim 1 , wherein the (meth-) acrylonitrile concentration of the composition at the end of the bioconversion is below 10.0% (w/w) by weight of the (meth-) acrylonitrile in the aqueous medium.

3. Process according to claim 1 , wherein the concentration of ammonium (meth-) acrylate at the end of the bioconversion is at least 10% (w/w) by weight of the ammonium (meth-) acrylate monomers in the aqueous medium.

4. Process according to claim 1 , wherein the biocatalyst is an enzyme having nitrilase activity.

5. Process according to claim 1 , wherein the biocatalyst having nitrilase activity is one selected from the group consisting of an isolated nitrilase, a recombinant construct, a recombinant vector comprising the recombinant construct, a recombinant microorganism comprising the recombinant construct, and a recombinant microorganism comprising the recombinant vector.

6. Process according to claim 1 , wherein the biocatalyst is a recombinant microorganism selected from the group consisting of Bacillus licheniformis, Bacillus pumilus, Bacillus subtilis, Escherichia coli, Saccharomyces cerevisiae, Rhodococcus rhodocrous , and Pichia pastoris.

7. Process according to claim 1 , wherein the relocatable bioconversion unit comprises a frame, a double-walled reaction vessel mounted into the frame having a volume from 10 m 3 to 150 m 3 , and an external temperature control circuit comprising at least a pump and a temperature control unit, wherein the composition of step (a) is circulated by means of a pump from the reaction vessel into the temperature control unit and back into the reaction vessel, thereby simultaneously controlling the temperature and mixing the composition of step (a).

8. Process according to any of claim 1 , wherein the relocatable bioconversion unit comprises a frame, a single walled reaction vessel mounted into the frame having a volume from 10 m 3 to 150 m 3 , and an external temperature control circuit comprising at least a pump and a temperature control unit, wherein the composition of step (a) is circulated by means of a pump from the reaction vessel into the temperature control unit and back into the reaction vessel, thereby simultaneously controlling the temperature and mixing the composition of step (a).

9. Process according to claim 8 , wherein the amount of the composition of step (a) cycled per hour through the temperature control circuit is from 100% to 1000% of the total volume of the composition of step (a) in the bioconversion unit.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Apr 16, 2021
From: GHISLIERI, DIEGO; OEDMAN, PETER; ZIMMERMANN, TOBIAS JOACHIM; SCHMIDT, ANNA-CORINA
To: BASF SE
Reel/Frame 055947/0834 →
Priority Claims (1)
EP 18201231 · Oct 18, 2018 · regional
Continuity (1)
Related Publication 20210348200A1 · Nov 11, 2021
References Cited (38)
US 6162624A · Symes et al. · 2000 [cited by applicant]
US 6361981B1 · Symes et al. · 2002 [cited by applicant]
US 6670158B2 · Dicosimo et al. · 2003 [cited by applicant]
US 8409854B2 · Erhardt · 2013 [cited by examiner]
US 20040175809A1 · Peterson et al. · 2004 [cited by applicant]
US 20090311759A1 · Abe et al. · 2009 [cited by applicant]
US 20210179758A1 · Sprafke et al. · 2021 [cited by applicant]
EA 202091019A1 · 2020 [cited by applicant]
EA 202091021A1 · 2020 [cited by applicant]
JP 2007002033A · 2007 [cited by applicant]
JP 4476822B2 · 2010 [cited by applicant]
WO 9721817A1 · 1997 [cited by applicant]
WO 2005054456A1 · 2005 [cited by applicant]
WO 2005054489A1 · 2005 [cited by applicant]
WO 2010133527A2 · 2010 [cited by applicant]
WO 2012069478A1 · 2012 [cited by applicant]
WO 2015024865A1 · 2015 [cited by applicant]
WO 2015086468A1 · 2015 [cited by applicant]
WO 2015158517A1 · 2015 [cited by applicant]
WO 2016050817A1 · 2016 [cited by applicant]
WO 2016131940A1 · 2016 [cited by applicant]
WO 2016131941A1 · 2016 [cited by applicant]
WO 2019081003A1 · 2019 [cited by applicant]
WO 2019081004A1 · 2019 [cited by applicant]
WO 2019081008A1 · 2019 [cited by applicant]
WO 2019081318A1 · 2019 [cited by applicant]
WO 2019081319A1 · 2019 [cited by applicant]
WO 2019081320A1 · 2019 [cited by applicant]
WO 2019081321A1 · 2019 [cited by applicant]
WO 2019081323A1 · 2019 [cited by applicant]
WO 2019081327A1 · 2019 [cited by applicant]
WO 2019081330A1 · 2019 [cited by applicant]
WO 2019081331A1 · 2019 [cited by applicant]
European Search Report for EP Patent Application No. 18201231.0, Issued on Apr. 3, 2019, 3 pages. [cited by applicant]
International Preliminary Report on Patentability received for PCT Patent Application No. PCT/EP2019/078158, mailed on Apr. 29, 2021, 13 pages. [cited by applicant]
International Search Report and Written Opinion received for PCT Patent Application No. PCT/EP2019/078158, mailed on Feb. 4, 2020, 16 pages. [cited by applicant]
Tevatia et al: “Kinetic modeling of photoautotrophic growth and neutral lipid accumulation in terms of ammonium concentration in Chlamydomonas reinhardtii”, Bioresource Technology, vol. 119, 2012, pp. 419-424. [cited by applicant]
Meledina T.V. et al., Equipment-specific methodological base of experiments in the field of food biotechnology of products from vegetable raw materials, Tutorial, St. Petersburg,ITMO University, 2017, p. 27. [cited by applicant]