Process for producing aqueous polyacrylamide solutions
US-2021179758-A1 · Jun 17, 2021 · US
US12264355B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12264355-B2 |
| Application number | US-201917286372-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 17, 2019 |
| Priority date | Oct 18, 2018 |
| Publication date | Apr 1, 2025 |
| Grant date | Apr 1, 2025 |
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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.
Opening claim text (preview).
The invention claimed is: 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.
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