System and methods for removing entrained liquids
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.
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.