System for recovery of hydrocarbon-containing fluid from a hydrocarbon-bearing formation
US-2024117722-A1 · Apr 11, 2024 · US
US9527037B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9527037-B2 |
| Application number | US-201113883099-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 8, 2011 |
| Priority date | Nov 10, 2010 |
| Publication date | Dec 27, 2016 |
| Grant date | Dec 27, 2016 |
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A method for processing an amine-based solvent contaminated by the introduction of sulfur oxides is provided. A potassium compound is introduced into a contaminated solvent, and the contaminated solvent is cooled so that a solubility of a potassium sulfate becomes less than a specified concentration of potassium sulfate. Further, an oxidizing agent is introduced into the contaminated solvent so that a potassium sulfite is oxidized to potassium sulfate. The potassium sulfate is filtered out, wherein a prepared solvent is formed. Further, a device for processing an amine-based, sulfur oxide-contaminated solvent is provided.
Opening claim text (preview).
The invention claimed is: 1. A method for processing an amine-based solvent contaminated by the introduction of sulfur oxides, comprising: cooling the contaminated solvent so that potassium sulfate crystallizes out of the contaminated solvent; introducing a potassium compound into a contaminated solvent, wherein the step of introducing the potassium compound in the contaminated solvent compensates for the loss of potassium from the contaminated solvent caused by potassium sulfate crystallization; introducing an oxidizing agent into the contaminated solvent so that a potassium sulfite is oxidized to potassium sulfate, and filtering out the potassium sulfate, wherein a prepared solvent is formed. 2. The method as claimed in claim 1 , wherein the oxidizing agent and the potassium compound are mixed together before they are introduced into the contaminated solvent. 3. The method as claimed in claim 1 , wherein the oxidizing agent comprises hydrogen peroxide or ozone. 4. The method as claimed in claim 1 , wherein an amount of the potassium compound supplied is equimolar to an amount of crystallized potassium sulfate. 5. The method as claimed in claim 1 , wherein a temperature T of the contaminated solvent after cooling is between 5° C. and 45° C. 6. The method as claimed in claim 1 , wherein a heat exchange is provided between the prepared solvent and the contaminated solvent so that the contaminated solvent is cooled by the prepared solvent. 7. The method as claimed in claim 1 , wherein the contaminated solvent is obtained from a carbon dioxide-separating process of a fossil-fuel-fired power station process. 8. The method as claimed in claim 7 , wherein the contaminated solvent is processed batch-wise from the carbon dioxide-separating process. 9. The method as claimed in claim 1 , wherein the contaminated solvent is the amino based solvent, wherein the amino based solvent is a potassium-amino acid solution. 10. The method as claimed in claim 1 , wherein the contaminated solvent comprises one or more amines. 11. The method as claimed in claim 1 , wherein the potassium compound comprises potassium hydroxide KOH, potassium hydrogen carbonate or potassium carbonate.
Peroxides · CPC title
of potassium · CPC title
Ozone · CPC title
Cross-Sectional Technologies · mapped topic
Carbon dioxide · CPC title
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