Method and device for neutralizing, by controlled gas injection, the formation of liquid slugs at the foot of a riser connected to a multiphase fluid transport pipe
Method and device for neutralizing, by controlled gas injection, the formation of liquid slugs at the foot of a pipe portion greatly inclined to the horizontal or riser connected to a pipe carrying circulating multiphase fluids such as hydrocarbons. Flow rate control is essentially obtained by injecting, at the base of the riser, a volume of gas proportional to the flow rate variation with time of the gas phase of the circulating fluids, and preferably substantially equal thereto, when this variation is positive. This action can be completed by modulating the injected gas flow by a quantity proportional to the flow rate variation of the liquid phase of the circulating fluids. Applications: offshore hydrocarbon production control for example.
1. A method for neutralizing, by controlled gas injection, liquid slug formation or accumulation at the foot of a pipe portion greatly inclined to the horizontal or riser connected to a pipe carrying circulating multiphase fluids, comprising:
measuring, at the bottom of the riser, the flow rate variation with time of the gas phase of the circulating fluids; and
injecting, at the base of the riser, a volume of gas substantially proportional to the flow rate variation with time of the gas phase of the circulating fluids, when this variation is positive.
2. A method as claimed in claim 1 , characterized in that the injected volume of gas is substantially equal to the flow rate variation with time of the gas phase of the circulating fluids.
3. A method as claimed in claim 2 , characterized in that said injected volume of gas is modulated by a quantity proportional to the flow rate variation of the liquid phase of the circulating fluids.
4. A method as claimed in claim 2 , characterized in that the flow rate variation with time of the gas phase of the circulating fluids, measured at a previous time interval, is injected at a time t.
5. A method as claimed in claim 1 , characterized in that said injected volume of gas is modulated by a quantity proportional to the flow rate variation of the liquid phase of the circulating fluids.
6. A method as claimed in claim 1 , characterized in that the flow rate variation with time of the gas phase of the circulating fluids, measured at a previous time interval, is injected at a time t.
7. A device for neutralizing, by controlled gas injection, liquid slug formation or accumulation at the foot of a pipe portion greatly inclined to the horizontal or riser connected to a pipe carrying circulating multiphase fluids, comprising gas injection means connected to the base of the riser, means for measuring the flow rate of the gas phase of the circulating fluids and a computer intended to control injection, by the injection means, of a volume of gas substantially proportional to the flow rate variation with time of the gas phase of the circulating fluids, when this variation is positive.
8. A device as claimed in claim 7 , characterized in that the computer is suited to control injection, by the injection means, of a volume of gas substantially equal to the flow rate variation with time of the gas phase of the circulating fluids.
9. A device as claimed in claim 8 , comprising means for measuring the flow rate of the liquid phase circulating in the pipe, the computer being suited to modulate the injected volume of gas by a quantity proportional to the measured flow rate variation of the liquid phase.
10. A device as claimed in claim 7 , comprising means for measuring the flow rate of the liquid phase circulating in the pipe, the computer being suited to modulate the injected volume of gas by a quantity proportional to the measured flow rate variation of the liquid phase.