Separating sweet gas from a sour gas stream
An oxidation-reduction desulfurization system includes a reactor vessel with sour gas inlet at the bottom and a gas outlet at the top. A primary stage phase separator includes a vertically-oriented pipe with an inlet located inside the reactor vessel. The ratio of the reactor vessel diameter to the pipe inlet diameter is in a range of 2:1 to 5:1. Surface foam and non-gaseous multi-phase mixture including emulsion flow into a partially gas-filled upper section of the vertically-oriented pipe and freefall to a lower level, thereby facilitating mechanical breaking of the foam and the emulsion. A secondary stage phase separator connected to the gas outlet separates non-gaseous surge from sweet gas. Valves and a controller automatically maintain target levels of the non-gaseous multi-phase mixture and non-gaseous surge.
1. A method comprising:
generating a non-gaseous multi-phase mixture and sweet gas from a sour gas stream in a reactor vessel, the non-gaseous multi-phase mixture comprising an emulsion and foam;
separating the sweet gas from the non-gaseous multi-phase mixture with a primary stage phase separator comprising an inlet disposed within the reactor vessel, the reactor vessel having a diameter that is between two-times and five-times, inclusive, a diameter of the inlet; and
at least partly mechanically breaking the emulsion and foam by causing the non-gaseous multi-phase mixture to freefall from an upper level of a partly gas-filled vertically-oriented section of the primary stage phase separator to a lower level of the vertically-oriented section of the primary stage phase separator at which an aqueous multi-phase mixture is maintained such that the emulsion and foam are mechanically broken at the lower level of the vertically-oriented section only by freefalling and force of contact with the aqueous multi-phase mixture.
2. The method of claim 1 , wherein the lower level is defined by a portion of the primary stage phase separator that is filled with the non-gaseous multi-phase mixture, comprising automatically adjusting flow of the non-gaseous multi-phase mixture out of the primary stage phase separator to maintain the lower level within a predefined range.
3. The method of claim 2 , comprising separating non-gaseous multi-phase mixture surge from the sweet gas in a secondary stage phase separator comprising a second pressure vessel, a third inlet connected to a first outlet of the primary stage phase separator, a third outlet for the sweet gas, and a fourth outlet for the non-gaseous multi-phase mixture surge.
4. The method of claim 3 , comprising controlling flow of the non-gaseous multi-phase mixture surge out of the second pressure vessel with a valve.
5. The method of claim 4 , comprising adjusting the valve to maintain the non-gaseous multi-phase mixture surge at a target level within the second pressure vessel.
6. The method of claim 1 , wherein the primary stage phase separator comprises a vertically-oriented upper section, a vertically-oriented lower section, and a horizontally-oriented section that traverses a wall of the reactor vessel and connects the upper section with the lower section, and wherein the lower level is defined by a portion of the vertically-oriented lower section that is filled with separated non-gaseous multi-phase mixture, and comprising controlling flow of the separated non-gaseous multi-phase mixture out of the primary stage phase separator with a valve.
7. The method of claim 6 , comprising adjusting the valve to maintain the separated non-gaseous multi-phase mixture at a target level within the vertically-oriented lower section.
8. The method of claim 1 wherein the vertically-oriented section of the non-gaseous multi-phase mixture and comprising controlling flow of the separated non-gaseous multi-phase mixture out of the primary stage phase separator with a valve.
9. The method of claim 8 , comprising adjusting the valve to maintain the separated non-gaseous multi-phase mixture at a target level within the vertically-oriented pipe.