APPARATUS FOR PREPARING GLYCOL AND METHOD OF PREPARING THE SAME (As Amended)
US-2017349512-A1 · Dec 7, 2017 · US
US10358406B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10358406-B2 |
| Application number | US-201816023442-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jun 29, 2018 |
| Priority date | Jun 29, 2017 |
| Publication date | Jul 23, 2019 |
| Grant date | Jul 23, 2019 |
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The present invention relates to process and apparatus for removing aldehydes from acetone. More specifically, the present invention relates to a process and apparatus for removing aldehydes from acetone by reacting the aldehydes with caustic in an acetone column and washing the organic phase with a plurality of water streams.
Opening claim text (preview).
The invention claimed is: 1. A process for removing aldehydes from acetone, comprising: introducing a feed stream containing at least one organic compound in a column; introducing an aqueous caustic scrubbing solution into the column; introducing a first water stream into a lower portion of the column; introducing a second water stream into the lower portion of the column; removing spent aqueous caustic and aldehyde solution from the column; and removing an organic product from an upper portion of the column having a reduced level of aldehydes relative to the feed stream. 2. The process of claim 1 , wherein the feed stream comprises acetone, cumene, water, and aldehydes. 3. The process of claim 1 , wherein the organic compound is acetone. 4. The process of claim 1 , wherein the process removes about 99% of aldehydes. 5. The process of claim 1 , wherein the caustic scrubbing solution contains about 0.5 wt % caustic to about 20 wt % caustic. 6. The process of claim 1 , wherein the caustic scrubbing solution contains about 1% of caustic. 7. The process of claim 1 , wherein the column is a finished acetone column. 8. The process of claim 1 , wherein the column is operated at a pressure from about −0.50 kg/cm2(g) to about 2.0 kg/cm2(g) and a temperature from about 40° C. to about 100° C. 9. The process of claim 1 , wherein the first water stream comprises water and about 10% acetone. 10. The process of claim 1 , wherein the second water stream is 100% water and is introduced to the column at a rate of 0.1 kg water/kg acetone product to about 0.4 kg water/kg acetone product. 11. The process of claim 1 , wherein the aldehydes react with acetone, catalyzed by the caustic scrubbing solution inside the column to form an aldol or heavy, soluble in the cumene-rich organic phase, which is rejected to the bottom of the column.
by liquid-liquid treatment · CPC title
with stationary contacting elements, sieve plates or loose contacting elements · CPC title
of hydroperoxides · CPC title
Applications, solvents used · CPC title
by treatment giving rise to a chemical modification (by chemisorption C07C45/79) · CPC title
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