Gas-liquid separator
US-2024293767-A1 · Sep 5, 2024 · US
US9597622B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9597622-B2 |
| Application number | US-201414565018-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 9, 2014 |
| Priority date | Jan 8, 2014 |
| Publication date | Mar 21, 2017 |
| Grant date | Mar 21, 2017 |
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The present techniques are directed to a method for removing entrained liquid hydrocarbons in a countercurrent contact separator to produce a lean hydrocarbons gas. The method includes introducing a gas stream into an inlet of the countercurrent contact separator and flowing the gas stream through a bulk separator to capture a portion of the entrained liquid hydrocarbons. The method includes flowing the gas stream through a plurality of cyclone bundles, where the plurality of cyclone bundles are located in risers to capture a remaining fraction of the entrained liquid hydrocarbons. The method includes flowing the captured entrained liquids downward into a drain line countercurrent to the gas stream. The method includes removing the captured entrained liquids through a bottom outlet of the countercurrent contact separator. The method includes removing the lean hydrocarbons gas through a top outlet of the countercurrent contact separator.
Opening claim text (preview).
What is claimed is: 1. A method for removing entrained liquids, comprising: introducing a gas stream into an inlet of a column comprising a plurality of cyclones incorporated into risers, wherein the gas stream comprises entrained liquids; separating at least a portion of the entrained liquids from the gas stream using the plurality of cyclones; flowing the separated entrained liquids countercurrent to the flow of the gas stream; introducing a contact liquid into an inlet of the column; removing the separated entrained liquids through a bottom outlet of the column; and removing the gas stream through a top outlet of the column. 2. The method of claim 1 , wherein at least about 70% to 99.9% of the entrained liquids are separated from the gas stream. 3. The method of claim 1 , comprising flowing the gas stream through a bulk separator to remove at least a portion of the entrained liquids before flowing the gas stream through the plurality of cyclones. 4. The method of claim 1 , wherein separating at least a portion of the entrained liquids from the gas stream comprises implementing swirl tubes or a demisting cyclonic mechanism within the plurality of cyclones. 5. The method of claim 1 , comprising placing wire meshing or other elements for de-entrainment above the plurality of cyclones, inside of the risers, in an open window of the risers, or any combination thereof. 6. The method of claim 1 , wherein the gas stream contains about 0.1% to 30% of entrained liquids. 7. A method for removing entrained liquid hydrocarbons in a countercurrent contact separator to produce a lean hydrocarbons gas, comprising: introducing a gas stream into an inlet of the countercurrent contact separator; flowing the gas stream through a bulk separator to capture a portion of the entrained liquid hydrocarbons; flowing the gas stream through a plurality of cyclone bundles, wherein the plurality of cyclone bundles are located in risers to capture a remaining fraction of the entrained liquid hydrocarbons; flowing the captured entrained liquids downward into a drain line countercurrent to the gas stream; introducing a contact liquid into an inlet of the column; removing the captured entrained liquids through a bottom outlet of the countercurrent contact separator; and removing the lean hydrocarbons gas through a top outlet of the countercurrent contact separator. 8. The method of claim 7 , wherein capturing the remaining fraction of the entrained liquid hydrocarbons comprises implementing swirl tubes or a demisting cyclonic mechanism within the plurality of cyclone bundles. 9. The method of claim 7 , comprising flushing a bottom of each riser with a collector tray in an area excluding the cross-sectional area where the plurality of cyclone bundles are located. 10. The method of claim 7 , comprising placing wire meshing above the plurality of cyclone bundles, inside of the risers, in an open window of the risers, or any combination thereof. 11. The method of claim 7 , wherein the lean hydrocarbons gas contains about 0.1% to 30% of entrained liquids.
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