Integration of n-c4/n-c4=/bd separation system for on-purpose butadiene synthesis
US-2015376091-A1 · Dec 31, 2015 · US
US9815755B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9815755-B2 |
| Application number | US-201514863714-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 24, 2015 |
| Priority date | Sep 26, 2014 |
| Publication date | Nov 14, 2017 |
| Grant date | Nov 14, 2017 |
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The present subject matter relates to methods and apparatuses for the continuous preparation of a cumene feed for a cumene oxidation process. More specifically, the subject matter relates to a process for passing a cumene alpha-methylstyrene stream through a caustic wash column having an integrated water wash section for the removal of organic acids.
Opening claim text (preview).
The invention claimed is: 1. An apparatus for treating an organic feed comprising: a line for introducing a feed stream from a feed tank containing organic feed into a caustic wash section of a caustic wash column, the feed stream comprising cumene, alpha-methylstyrene, and phenol; a line for introducing an aqueous caustic scrubbing solution into the caustic wash column; a line for introducing a water stream into a water wash section of the caustic wash column; jetting trays within the column for contacting of the feed through an aqueous caustic scrubbing solution to remove the phenol from the feed; a line for removing spent aqueous caustic and phenol from the caustic wash column; and a line for removing an organic product from the water wash section of the caustic wash column wherein the organic product has a reduced level of phenol relative to the feed stream. 2. The apparatus of claim 1 , wherein the apparatus removes 10-25 wt % of phenol. 3. The apparatus of claim 1 , wherein said aqueous caustic scrubbing solution contains sodium hydroxide. 4. The apparatus of claim 1 , wherein the aqueous scrubbing solution contains 40-50 wt % of sodium hydroxide. 5. The apparatus of claim 1 , wherein the organic product is a mixture comprising of 75-90 wt % cumene and alphamethylstyrene. 6. The apparatus of claim 1 , wherein the caustic wash column is operated at a pressure from about 0.1 to 3.0 kg/cm2(g) and a temperature from about 30 to 60° C. 7. The apparatus of claim 1 , further comprising a mesh blanket for coalescing of any water and aqueous caustic scrubbing solution. 8. The apparatus of claim 1 , wherein the caustic wash section comprises a plurality of trays. 9. The apparatus of claim 1 , wherein the water wash section comprises a plurality of trays. 10. An apparatus for treating an organic feed comprising: a line for introducing a feed stream from a feed tank into a caustic wash column having a caustic wash section and a water wash section, the feed stream comprising cumene, alpha-methylstyrene and phenol; a line for introducing a scrubbing solution comprising 45 wt % sodium hydroxide into the caustic wash column; a line for introducing a water stream into a water wash section of the caustic wash column; jetting trays within the column for contacting of the feed through an aqueous caustic scrubbing solution to remove the organic acid from the feed; a line for removing water, sodium hydroxide, and sodium phenate from the lower portion of the caustic wash column; and a line for removing 10-25 wt % phenol from the feed. 11. The apparatus of claim 10 , wherein the caustic wash column is operated at a pressure from about 0.1 to 3.0 kg/cm2(g) and a temperature from about 30 to 60° C. 12. The apparatus of claim 10 , further comprising a mesh blanket for coalescing of any water and aqueous caustic scrubbing solution. 13. The apparatus of claim 10 , wherein the caustic wash section comprises a plurality of trays. 14. The apparatus of claim 10 , wherein the water wash section comprises a plurality of trays.
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