Calcium oxide or magnesium oxide production with alkali and sulfur dioxide intermediates
US-12017985-B2 · Jun 25, 2024 · US
US11279666B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11279666-B2 |
| Application number | US-202016942888-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 30, 2020 |
| Priority date | Jul 30, 2019 |
| Publication date | Mar 22, 2022 |
| Grant date | Mar 22, 2022 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Disclosed herein are methods for the recovery of target bio-base carboxylic acid products using a sorption-based technology with a mixed elution solvent optimized for minimized downstream distillation energy input. The sorption-based technology includes absorbing the targeted bio-base carboxylic acid products onto a non-ionic resin and eluting the targeted bio-base carboxylic acid products with a mixed elution solvent. The mixed elution solvent includes a first solvent and a second solvent. The first solvent has a boiling point that is lower than the targeted bio-base carboxylic acid products and the second solvent is selected from the group consisting of a phosphine oxide or tertiary amine.
Opening claim text (preview).
We claim: 1. A method for separating a bio-based carboxylic acid product from an aqueous solution comprising the step of selecting a first solvent and a second solvent wherein the first solvent has a boiling point that is lower than the bio-based carboxylic acid product and wherein the second solvent is selected from the group consisting of a phosphine oxide or tertiary amine and is miscible with the first solvent and has a boiling point above the bio-based carboxylic acid product; and further comprising the adsorption of the bio-based carboxylic acid product onto a non-ionic resin. 2. The method of claim 1 wherein the carboxylic acid is lactic acid or butyric acid. 3. The method of claim 1 wherein the first solvent is selected from the group consisting of acetone and methanol. 4. The method of claim 1 wherein the non-ionic resin is selected from the group consisting of Amberlite™, Dowex®, or Polybenzimidazole (PBI). 5. The method of claim 1 wherein the non-ionic resin is poly(4-vinylpyridine). 6. The method of claim 1 wherein the method further comprises desorbing the bio-based carboxylic acid product from the resin using a mixture of the first solvent and the second solvent. 7. The method of claim 6 further comprising distilling the first and second solvent from a mixture of the desorbed bio-based carboxylic acid product and the first and second solvent. 8. The method of claim 7 wherein the bio-based product is isolated. 9. A method for separating a carboxylic acid fermentation product from an aqueous solution comprising adsorption of the carboxylic acid fermentation product onto a non-ionic resin and further comprising the step of selecting a first solvent and a second solvent wherein the second solvent is selected from the group consisting of a phosphine oxide or tertiary amine and wherein the first solvent has a boiling point that is lower than the carboxylic acid fermentation product and wherein the second solvent is miscible with the first solvent and has a boiling point above the carboxylic acid fermentation product. 10. The method of claim 9 wherein the first solvent is selected from the group consisting of acetone and methanol. 11. The method of claim 9 wherein the non-ionic resin is poly(4-vinylpyridine). 12. The method of claim 9 wherein the method further comprises desorbing the fermentation product from the resin using a mixture of the first solvent and the second solvent. 13. The method of claim 12 further comprising distilling the first and second solvent from a mixture of the desorbed carboxylic acid fermentation product and the first and second solvent. 14. The method of claim 13 wherein the carboxylic acid fermentation product is isolated.
in the liquid phase · CPC title
Extractive distillation · CPC title
obtained by reactions only involving carbon to carbon unsaturated bonds (macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds per se C08F) · CPC title
by two or more of a fractionation, separation or rectification step · CPC title
by solid-liquid treatment; by chemisorption · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.