Integration of n-c4/n-c4=/bd separation system for on-purpose butadiene synthesis
US-2015376091-A1 · Dec 31, 2015 · US
US9522861B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9522861-B2 |
| Application number | US-201314083116-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 18, 2013 |
| Priority date | Nov 18, 2013 |
| Publication date | Dec 20, 2016 |
| Grant date | Dec 20, 2016 |
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Methods and apparatuses are provided for producing low sulfur propane and butane. The method includes reacting a mercaptan in a washed feed stream with a caustic stream to produce a mercaptan salt in a rich caustic stream and a hydrocarbon treated stream. The mercaptan salt in the rich caustic stream is reacted with oxygen and water to produce a mixed caustic/disulfide stream, and the caustic and disulfides in the mixed caustic/disulfide stream are separated to produce a disulfide stream and the caustic stream. The hydrocarbon treated stream is fractionated to produce a propane stream, a butane stream, and a C5+ stream.
Opening claim text (preview).
The invention claimed is: 1. A method for producing low sulfur propane and butane, the method comprising the steps of: reacting, in the liquid phase, a mercaptan in a liquid phase washed feed stream containing hydrocarbon with a caustic stream to produce a mercaptan salt in a rich caustic stream and a hydrocarbon treated stream wherein the liquid phase washed feed stream is derived from hydraulic fracturing of shale; reacting the mercaptan salt in the rich caustic stream with oxygen and water to produce a mixed caustic/disulfide stream; separating caustic and disulfides in the mixed caustic/disulfide stream to produce a disulfide stream and the caustic stream; and fractionating the hydrocarbon treated stream by debutanizing the hydrocarbon treated stream to produce a C3-4 stream and the C5+ stream, and depropanizing the C3-4 stream to produce the propane stream and the butane stream. 2. The method of claim 1 further comprising: prewashing the liquid phase washed feed stream prior to reacting the mercaptan in the liquid phase washed feed stream with the caustic stream, wherein prewashing comprises contacting the washed feed stream with a prewash stream comprising sodium hydroxide wherein the prewashing is conducted in the liquid phase. 3. The method of claim 1 wherein reacting the mercaptan salt in the rich caustic stream with oxygen further comprises contacting the rich caustic stream with air. 4. The method of claim 1 wherein reacting the mercaptan salt in the rich caustic stream further comprises adding an oxidation catalyst to the rich caustic stream. 5. The method of claim 1 wherein reacting the mercaptan salt in the rich caustic stream further comprises adding an oxidation catalyst to the rich caustic stream wherein the oxidation catalyst is in liquid form, and wherein the oxidation catalyst comprises a metal chelate. 6. The method of claim 1 wherein reacting the mercaptan in the washed feed stream with the caustic stream further comprises reacting the mercaptan in the washed feed stream with the caustic stream wherein 90 mass percent or more of the washed feed stream comprises hydrocarbons with 3 to 5 carbon atoms. 7. The method of claim 1 further comprising: replenishing the caustic stream with fresh caustic.
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