Combined degassing and flotation tank
A combined degassing and flotation tank for separation of a water influent containing considerable amounts of oil and gas. A rotational flow is created in the tank which forces the lighter components such as oil and gas droplets towards an inner concentric cylindrical wall where they coalesce and rise to the surface of the liquid and are removed via the outlet. The heavier parts are forced down where the heavy particles sink to the lower part where they can be removed as a sludge. The water is discharged via an outlet in the lower part of the tank. The combined degassing and flotation tank is particular suited for use in oil production at sea for removal of oil and gases from water streams before the water is returned to the sea.
1. A method of separating a water mixture that includes water, hydrocarbonaceous oil not miscible with and having a lower density than water, and gas, comprising the step of separating hydrocarbonaceous oil and gas from the water using a combined degassing and flotation tank having an essentially cylindrical vertical tank, a tangentially arranged inlet, at least one outlet for gas and oil in the upper part of the tank, an outlet for water placed in the lower part of the tank, and an inner concentric cylindrical wall forming a flotation and degassing zone between said inner concentric wall and the wall of the tank in the upper part of the tank, said combined tank being operated at a pressure below 10 bar.
2. The method according to claim 1 , further comprising injecting additional gas into the water mixture entering said tank before said mixture enters the tank.
3. The method according to claim 1 , further comprising injecting a flocculant into the water mixture entering said tank before said mixture enters the tank.
4. The method according to claim 1 , further comprising using said tank in oil production at sea level or at sea bed level.
5. The method according to claim 1 , further comprising using said tank in combination with a filtration unit connected to the water outlet of said tank.
6. The method according to claim 3 , further comprising using said tank for treating water from which a portion of oil and gas has been removed previously by conventional means.
7. A method of phase separation of a mixture of at least two phases comprising at least the steps of:
a) introducing the mixture to a tank through a tangentially arranged inlet;
b) separating phases of the mixture in a flotation and degassing zone formed in a space between a tank wall and an inner concentric cylindrical wall;
c) outputting at least one phase through at least one outlet in a lower part of the tank;
d) outputting at least one other phase through at least one outlet above the inlet to the tank;
said mixture introduced into the tank being guided in a mainly upwards spiralling movement in said space between the tank wall and the inner concentric cylindrical wall, said at least one phase being selected from the group consisting of water and solid materials, and said at least one other phase being selected from the group consisting of oil and gas, at least water being liquid under conditions of operation, and said tank being operated at a pressure below 10 bar.
8. The method according to claim 7 , wherein the phases are oil, water and gas.
9. The method according to claim 7 , wherein the at least one phase is water and the at least one other phase is oil and gas.
10. The method according to claim 7 , wherein the upward spiralling movement is controlled by an inlet guide vane.
11. The method according to claim 7 , wherein the mixture has a residence time in the tank between 5 to 300 seconds.
12. The method according to claim 7 , wherein the pressure is below 5 bar.
13. The method according to claim 7 , wherein additional gas is injected into the mixture.
14. A method of separating in a tank a mixture comprising water, hvdrocarbonaceous oil, and a gas into these constituents, wherein the method comprises the steps of:
conducting incoming mixture into a tangentially arranged, mainly upwards spiralling movement between a tank wall and an inner concentric cylindrical wall;
taking out gas and said oil in an upper part of the tank;
taking out water and possible solids in a lower part of the tank; and
said tank being operated at a pressure below 10 bar allowing the gas to escape the water phase and form gas bubbles, said gas bubbles enhancing the separation of said oil from the mixture.
15. The method according to claim 14 , wherein the upward spiralling movement is controlled by an inlet guide vane.
16. The method according to claim 14 , wherein the mixture has a residence time in the tank between 5 and 300 seconds.
17. The method according to claim 14 , wherein additional gas is injected into the mixture.
18. The method according to claim 7 , further comprising the step of using said method for purifying water.
19. The method according to claim 7 , further comprising the step of using said method for purifying water from oil.
20. The method according to claim 7 , further comprising the step of using said method for purifying water in an oil producing plant.
21. The method according to claim 14 , further comprising the step of using said method for purifying water.
22. The method according to claim 14 , further comprising the step of using said method for purifying water from oil.
23. The method according to claim 14 , further comprising the step of using said method for purifying water in an oil producing plant.
24. The method according to claim 1 , wherein said water mixture is coming from separation at a well-head at offshore oil production.
25. The method according to claim 24 , wherein said water mixture is coming from an aged oil field.
26. The method according to claim 1 , wherein said water mixture is coming from separation at separators subsequent to a well-head at offshore oil production.
27. The method according to claim 26 , wherein said water mixture is coming from an aged oil field.
28. The method according to claim 1 , wherein said water mixture is coming from an aged oil field.
29. The method according to claim 1 , wherein said water mixture is coming from an oil field in an arctic area.
30. The method according to claim 1 , wherein said water mixture is coming from an oil field in a fishing area.
31. The method according to claim 1 , wherein the mixture introduced into the tank is guided in a mainly upwards spiralling movement in said flotation and degassing zone.
32. The method according to claim 1 , wherein the incoming water is guided into an upward spiralling flow by an inlet guide vane.
33. The method according to claim 1 , wherein the oil content in the mixture is reduced to less than 20 mg/l.
34. The method according to claim 7 , wherein the oil content in the mixture is reduced to less than 20 mg/l.
35. The method according to claim 14 , wherein the oil content in the mixture is reduced to less than 20 mg/l.