Method of purification and purified products
US-2024075407-A1 · Mar 7, 2024 · US
US9487469B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9487469-B2 |
| Application number | US-201313963677-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 9, 2013 |
| Priority date | Aug 9, 2013 |
| Publication date | Nov 8, 2016 |
| Grant date | Nov 8, 2016 |
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.
A method for separating the components of a mixture containing methyl methacrylate, water, and methanol in which the mixture is dehydrated in a first stage membrane unit, producing a dehydrated mixture. Methanol in the dehydrated mixture is removed in a second stage membrane unit, producing a retentate stream containing methyl methacrylate and substantially no said methanol.
Opening claim text (preview).
We claim: 1. A method for separating methyl methacrylate from a mixture containing said methyl methacrylate, methanol, and water comprising the steps of: providing said mixture to a first stage membrane unit in which said mixture is dehydrated, producing a dehydrated mixture containing said methyl methacrylate and said methanol; and providing said dehydrated mixture to a second stage membrane unit in which said methanol is removed from said dehydrated mixture, producing a permeate stream containing said methanol and a retentate stream containing in a range of about 95% to about 100 wt % said methyl methacrylate; wherein the first stage membrane unit comprises a small-pore hydrophilic membrane having a thickness of greater than about 20 μm and pore sizes of about 0.35 to about 0.45 nanometers selected from the group consisting of the following, and combinations thereof: a) Na 12 Al 12 Si 12 O 48 •27H 2 O, b) Si x Al y P z O 2 , where x=0.01-0.98, y=0.01-0.60, z=0.01-0.52, c) microporous aluminophosphates; and the second stage membrane unit comprises a hydrophilic membrane having a faujasite structure. 2. The method of claim 1 , wherein said dehydrated mixture is provided to a polishing adsorption column in which any remaining trace amounts of water are removed. 3. The method of claim 1 , wherein said first stage membrane unit comprises a hydrophilic zeolite A membrane. 4. The method of claim 1 , wherein said second stage membrane unit comprises a zeolite FAU membrane. 5. The method of claim 2 , wherein said polishing adsorption column contains a column packing material comprising 3A zeolites. 6. The method of claim 1 , wherein said methanol is recycled to a methyl methacrylate production process. 7. A method for separating the components of a mixture containing methyl methacrylate, water, and methanol comprising the steps of: dehydrating said mixture in a first stage membrane unit, producing a dehydrated mixture; and removing said methanol from said dehydrated mixture in a second stage membrane unit, producing a retentate stream containing said methyl methacrylate and 5.0 wt % said methanol; wherein the first stage membrane unit comprises a small-pore hydrophilic membrane having pore sizes of about 0.35 to about 0.45 nanometers selected from the group consisting of the following, and combinations thereof: a) Na 12 Al 12 Si 12 O 48 •27H 2 O, b) Si x Al y P z O 2 , where x=0.01-0.98, y=0.01-0.60, z=0.01-0.52, c) microporous aluminophosphates; and the second stage membrane unit comprises a hydrophilic membrane having a faujasite structure. 8. The method of claim 7 , wherein said first stage membrane unit comprises a hydrophilic zeolite A membrane. 9. The method of claim 7 , wherein said second stage membrane unit comprises a zeolite FAU membrane. 10. The method of claim 7 , wherein said dehydrated mixture is provided to a polishing adsorption column in which any remaining trace amounts of said water are removed. 11. The method of claim 10 , wherein said polishing adsorption column contains a column packing material comprising 3A zeolites. 12. The method of claim 7 , wherein at least a portion of said methanol removed from said dehydrated mixture is recycled for use in the production of said methyl methacrylate. 13. The method of claim 7 , wherein the small-pore hydrophilic membrane has a thickness of greater than about 20 μm.
Related publications grouped by family.
Answers are generated from the same data shown on this page.