Controlling the rheology of a metal ore residue
US-12122884-B2 · Oct 22, 2024 · US
US12018101B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12018101-B2 |
| Application number | US-201917309079-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 25, 2019 |
| Priority date | Jul 25, 2019 |
| Publication date | Jun 25, 2024 |
| Grant date | Jun 25, 2024 |
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The present disclosure relates to a process and/or method for producing a polymer dispersion by free-radically initiated emulsion polymerization of radically polymerizable ethylenically unsaturated monomers within a polymerization reactor. The polymer dispersion obtained is transferred to a post-treatment reactor and is post-treated therein. The polymer dispersion within the post-treatment reactor is conveyed, simultaneously to the post-treatment, to a circuit for filtration and analysis and is then subsequently fed back into the post-treatment reactor.
Opening claim text (preview).
The invention claimed is: 1. A method for preparing a polymer dispersion, the method comprising the steps of: providing a polymerization reactor; obtaining a polymer dispersion by free-radically initiated emulsion polymerization of radically polymerizable ethylenically unsaturated monomers within the polymerization reactor; transferring the polymer dispersion obtained to a post-treatment reactor; and post-treating the polymer dispersion within the post-treatment reactor by physical and/or chemical methods and wherein the polymer dispersion in the post-treatment reactor is conveyed simultaneously to the post-treatment and to a circuit for filtration and analysis and then is subsequently fed back into the post-treatment reactor. 2. The method of claim 1 , wherein the polymer dispersion is an aqueous polymer dispersion. 3. The method of claim 1 , wherein the filtration is effected by automatic cleaning filters having mesh sizes of approximately 50 μm to approximately 1000 μm. 4. The method of claim 1 , wherein the analysis comprises determining mean particle size, molar mass, solids content, viscosity, VOC content, residual monomer content, redox potential and/or pH. 5. The method of claim 4 , wherein the analysis is measured using one or more analytical devices. 6. The method of claim 1 , wherein the post-treatment comprises a first phase and a second phase; wherein in the first phase the polymerized polymer dispersion is depressurized to a pressure from approximately 0.1 bar to approximately 5.0 bar absolute; and wherein in the second phase a gaseous phase resulting from the depressurization during the first phase is withdrawn. 7. The method of claim 6 , wherein the post-treatment further comprises a third phase and wherein in the third phase a post-polymerization occurs. 8. The method of claim 6 , wherein the post-treatment further comprises a fourth phase and wherein in the fourth phase volatile components are removed by passing over or passing through inert entrainment gases. 9. The method of claim 6 , wherein the post-treatment further comprises allowing the polymer dispersion to be cooled. 10. The method of claim 1 , wherein the filtration and analysis is carried out in single phases of the post-treatment or in every phase of the post-treatment. 11. The method of claim 1 , wherein the circuit is an external circuit. 12. The method of claim 11 , wherein during the post-treatment of the polymer dispersion the polymer dispersion is conveyed continuously from the post-treatment reactor to the external circuit for filtration and analysis and is then subsequently fed back into the post-treatment reactor.
Purification · CPC title
characterised by special features of the polymerisation apparatus used · CPC title
from polymer solutions, suspensions, dispersions or emulsions without recovery of the polymer therefrom · CPC title
containing three or more polymers in a blend · CPC title
containing two or more polymers of the same hierarchy C08L, and differing only in parameters such as density, comonomer content, molecular weight, structure · CPC title
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