Method for separating gas and liquid and cyclone separators therefore
A cyclone separator for separating a fluid into a gas phase and a liquid phase. The cyclone separator includes a vertically oriented vessel with a gas phase outlet at an upper end of the vessel and a liquid phase outlet at a lower end of the vessel; at least one tangentially oriented fluid inlet at the upper end below the gas phase outlet of the vessel; a liquid extractor extracting liquid through the liquid phase outlet at a rate which forms a bulk liquid phase at the lower end of the vessel; and a gas extractor extracting gas through the gas phase outlet. The cyclone separator has at least one flow velocity deflector located at a level in proximity to the bulk liquid-gas interphase which changes the vertical velocity component of a liquid film travelling down the internal wall of the vessel to a horizontally oriented velocity component.
1. A method for separating a fluid into a gas phase and a liquid phase, the method comprising:
employing a vertically oriented cyclone separator vessel having a gas-phase outlet arranged in an upper end of the vessel and a liquid phase outlet arranged at a lower end of the vessel;
feeding the fluid, which is to be separated, into the vessel at a tangential flow direction at a height level below the gas phase outlet at a flow velocity sufficient to form a liquid film travelling down an internal wall of the cyclone separator vessel in a helical flow pattern;
extracting liquid through the liquid phase outlet at a rate which forms a bulk liquid phase at a lower part of the cyclone separator vessel with a relatively constant height level of a bulk liquid-gas interphase; and
extracting gas through the gas phase outlet,
wherein at least one flow velocity deflector arranged adjacent to the internal wall of the cyclone separator vessel is employed at a level in proximity of the bulk liquid-gas interphase which changes a vertical velocity component of the liquid film travelling down the internal wall of the cyclone separator vessel to a horizontally oriented velocity component,
wherein the at least one flow velocity deflector is arranged below the bulk liquid-gas interphase.
2. A method according to claim 1 , wherein the at least one flow velocity deflector is arranged in a range of 1 to 25 cm below the bulk liquid-gas interphase.
3. A method according to claim 1 , wherein the method further includes limiting a swirling motion of a bulk liquid at a level in proximity of the bulk liquid-gas interphase, by employing at least one baffle arranged in the bulk liquid.
4. A method according to claim 1 , wherein the at least one flow velocity deflector is arranged adjacent to the internal wall of the cyclone separator vessel with a smooth transition.
5. A method according to claim 1 , wherein the at least one flow velocity deflector has an optimized curved shape to minimize stirring and whirling of the liquid.
6. A method according to claim 1 , wherein the method comprises employing two or more radially-spaced flow velocity deflectors, positioned at different levels compared to the bulk liquid-gas interphase.
7. A cyclone separator for separating a fluid into a gas phase and a liquid phase, the cyclone separator comprising:
a vertically oriented vessel with cylindrical symmetry and which has a gas phase outlet at an upper end of the vessel and a liquid phase outlet at a lower end of the vessel;
at least one tangentially oriented fluid inlet at the upper end below the gas phase outlet of the vessel, able to form a helical liquid flow down along an internal wall of the vessel;
a liquid extractor for extracting liquid through the liquid phase outlet at a rate which forms a bulk liquid phase at the lower end of the vessel with a relatively constant height level of a bulk liquid-gas interphase;
a gas extractor extracting gas through the gas phase outlet; and
at least one flow velocity deflector arranged adjacent to the internal wall of the vessel, the flow velocity deflector being located at a level in proximity of the bulk liquid-gas interphase and configured to change a vertical velocity component of a liquid film travelling down the internal wall of the vessel to a horizontally oriented velocity component,
wherein the at least one flow velocity deflector is arranged below the bulk liquid-gas interphase, and
wherein the at least one flow velocity deflector is a curved flow velocity screen.
8. A cyclone separator according to claim 7 , wherein the at least one flow velocity deflector is arranged in a range of 1 to 25 cm below the bulk liquid-gas interphase.
9. A cyclone separator according to claim 7 , wherein the cyclone separator further includes at least one vortex breaking baffle arranged at a level in proximity to the bulk liquid-gas interphase.
10. A cyclone separator according to claim 9 , wherein the at least one vortex breaking baffle is arranged below the bulk liquid-gas interphase.
11. A cyclone separator according to claim 7 , wherein the cyclone separator further comprises a waterspout protection element located above the bulk liquid-gas interphase.
12. A cyclone separator according to claim 7 , wherein the cyclone separator comprises two or more radially-spaced flow velocity deflectors, positioned at different levels compared to the bulk liquid-gas interphase.