Continuous through-flow settling vessel, and a method of adaptive separation of a mixture from gas and/or oil exploration
A continuous through-flow settling vessel for adaptive separation of a mixture from gas and/or oil exploration or production, said mixture comprising a varying mixture of liquid and gaseous phases, wherein the vessel is provided with: an inlet for a mixture, and a gas outlet, a water outlet and an oil outlet, the outlets being provided distant from the inlet, and the oil outlet being downstream of the water outlet, a weir downstream of the water outlet and upstream of the oil outlet, which weir functions as a barrier to a free through-flow in the vessel of the liquid phase which comprises a water phase and an oil phase, which phases are separated from each other by settling, the weir having a height lower than the gas outlet, and wherein the vessel is additionally provided with:—an oil draining means capable of controllably draining oil phase from the vessel upstream of the weir, said means being provided at a level below the weir height and above the water phase that is present during operation of the vessel. Method of adaptive separation of a mixture from gas and/or oil exploration or production, said mixture comprising a varying mixture of liquid and gaseous phases, wherein the mixture is introduced into a continuous through-flow settling vessel.
1. A method for separation of a mixture from gas and/or oil exploration or production, said mixture comprising a varying mixture of liquid and gaseous phases,
wherein the mixture is introduced into a continuous through-flow settling vessel, said vessel provided with:
an inlet for the mixture, a gas outlet, a water outlet and an oil outlet, the outlets being provided distant from the inlet, and the oil outlet being downstream of the water outlet,
a weir downstream of the water outlet and upstream of the oil outlet, which weir functions as a barrier to a free through-flow in the vessel of the liquid phase which comprises a water phase and an oil phase, which phases are separated from each other by settling, the weir having a height lower than the gas outlet,
and wherein the method of separation involves the continuous controlling of the velocity of flow through the inlet and outlets of the vessel, so that a liquid level of the liquid phase in the vessel is maintained during operation at or below a threshold value between the height of the weir and the height of the gas outlet,
and wherein the separation comprises the steps of:
determining the presence in a pipeline of a slug flow, said slug flow being an inhomogeneity in the mixture which is mainly liquid, before it enters the inlet of the vessel;
during a phase A which precedes the slug flow entering the vessel:
lowering the liquid level of the liquid phase in the vessel upstream of the weir to or below an adapted height lower than the threshold value; and
during a subsequent phase B which includes the slug flow entering the vessel:
allowing the liquid level to rise above the adapted height in the vessel upstream of the weir, and subsequently maintaining the liquid level at or below the threshold value; and
wherein the continuous through-flow settling vessel is additionally provided with: an oil draining means capable of controllably draining oil phase from the vessel upstream of the weir, said means being provided at a level below the weir height and above the water phase that is present during operation of the vessel,
wherein in phase A the oil draining means are in an active mode for draining, and in phase B these means are not in an active mode for draining.
2. The method according to claim 1 , wherein during phase A, the volume of oil phase in the vessel upstream of the weir is reduced.
3. The method according to claim 1 , wherein during phase A, the volume of water phase upstream of the weir is reduced.
4. The method according to claim 1 , wherein the method of separation additionally involves the water level of the water phase in the vessel upstream of the weir to be maintained during operation at or below a water threshold value.
5. The method according to claim 4 , wherein during phase A, the water level of the water phase in the vessel upstream of the weir is maintained at or below value which is lower than the water threshold value.
6. The method according to claim 1 , wherein the oil draining means of the continuous through-flow settling vessel comprises at least one duct with a controllable valve that is in fluid communication with the upstream side of the weir.
7. The method according to claim 6 , wherein the duct extends through the weir and is in fluid communication with the upstream and downstream side of the weir.
8. The method according to claim 6 , wherein the entry side of the duct is provided in the vessel at a height between 0.10 and 0.75 of the weir height.
9. The method according to claim 6 , wherein the duct merges with the oil outlet outside of the vessel, or alternatively, is in fluid communication with the vessel downstream of the weir.
10. The method according to claim 9 , wherein the controlling means are adaptable to allow the liquid level upstream of the weir to decline to or below an adaptive height which is lower than the threshold value.
11. The method according to claim 6 , which comprises controlling means for controlling the velocity of flow through the inlet and outlets of the vessel, so that a liquid level of the liquid phase in the vessel is maintained at or below a threshold value between the height of the weir and the height of the gas outlet.
12. The method according to claim 11 , wherein the controlling means allow temporarily the increase of outflow using the water outlet, the oil outlet, and/or the oil draining means in order to decline the liquid level to or below the adaptive height upstream of the weir.