Methods and apparatus for removing dissolved gases from fermentation streams
US-9221734-B2 · Dec 29, 2015 · US
US2017174594A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017174594-A1 |
| Application number | US-201615349942-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 11, 2016 |
| Priority date | Dec 16, 2015 |
| Publication date | Jun 22, 2017 |
| Grant date | — |
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A process is presented for the removal of acetaldehyde from mixture of oxygenates. Acetaldehyde is selectively removed in the presence of other oxygenates like ketones, alcohols and nitriles using an amorphous sodium doped alumina derived from thermally decomposed Dawsonite. The process successfully removes acetaldehyde which can adversely impact catalyst operation.
Opening claim text (preview).
1 . A process for removal of acetaldehyde from a mixture of oxygenates comprising passing said mixture of oxygenates through an adsorbent bed; removing acetaldehyde preferentially as compared to other oxygenates from the said mixture; and wherein the adsorbent bed comprises an adsorbent comprising an active amorphous sodium doped alumina. 2 . The process of claim 1 wherein said active amorphous sodium doped alumina is a thermal decomposition product of a sodium aluminum carbonate hydroxide. 3 . The process of claim 1 wherein said active amorphous sodium doped alumina comprises from about 1 to about 30% Na on a Na 2 O basis on alumina. 4 . The process of claim 1 wherein said active amorphous sodium doped alumina comprises from about 4 to about 15% Na on a Na 2 O basis on alumina. 5 . The process of claim 1 wherein said active amorphous sodium doped alumina comprises about 12% Na on a Na 2 O basis on alumina. 6 . The process of claim 1 wherein said other oxygenates are selected from the group consisting of alcohols, ethers, and ketones. 7 . A process for removal of acetaldehyde from a hydrocarbon stream comprising passing said hydrocarbon stream through an adsorbent bed; and wherein an adsorbent in the adsorbent bed contains a thermally activated sodium aluminum carbonate hydroxide. 8 . The process of claim 7 wherein a greater proportion of acetaldehyde from said hydrocarbon stream is adsorbed than other oxygenates or nitriles from said hydrocarbon stream. 9 . The process of claim 7 wherein said thermally activated sodium aluminum carbonate hydroxide is an active amorphous sodium doped alumina. 10 . The process of claim 7 wherein at least 80% of said acetaldehyde is removed from said hydrocarbon stream. 11 . The process of claim 7 wherein said thermally activated sodium aluminum carbonate hydroxide is regenerated in a thermal swing adsorption process. 12 . The process of claim 7 wherein said thermal swing process uses a heated gas at a temperature between about 100° and 350° C. for regeneration. 13 . The process of claim 12 wherein said heated gas is at a temperature between 150° and 250° C. for regeneration. 14 . The process of claim 12 wherein said heated gas is at a temperature of about 230° C. regeneration.
Temperature swing adsorption · CPC title
Alumina · CPC title
Metals · CPC title
using hot gas · CPC title
by physical treatment · CPC title
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