Method and equipment for determining the interface between two or more fluid phases
View Patent ↗A method and equipment are provided for determining the level/height, of one or more interfaces between two or more fluid phases of different density that are contained in a vessel, tank or the like. The position of the different interfaces in a tank is determined by measuring the pressure thereby determining the density of the fluid over the height of the tank by using a pressure measuring rod, equipped with pressure sensors, positioned in the tank. A mathematical model or algorithm is used which calculates how the density and hence the pressure vary over the height of the tank as a function of the fluid properties of the respective fluids in the tank, the interface, on the basis of the density being the same within each layer of the respective fluid, as a respective point at which the density changes from one layer to the next in the tank.
1. A method for determining (measuring) the level/height of one or more interfaces, h 1 -h x , between two or more fluids/process media (fluid phases) of different density that are contained in a vessel or a tank ( 1 ) the method comprising:
determining the position (the level) of the different interfaces in a tank ( 1 ) by measuring the pressure and thus indirectly determining the density of the fluid over the height of the tank
positioning a pressure measuring rod ( 2 , 4 ), equipped with pressure sensors ( 3 , 5 ), in and extending over the height of the tank ( 1 ), to determine the position of the different interfaces wherein, there are more pressure sensors and pressure measurements than the number of variables that are to be determined, so that the system is overdefined and thus more robust,
determining the interfaces using a mathematical model or algorithm which calculates how the density and hence the pressure vary over the height of the tank as a function of the fluid properties of the respective fluids in the tank, the interface, on the basis of the density being relatively similar within each layer of the respective fluid, being defined as the respective point (level) at which the density changes from one layer to the next in the tank.
2. A method according to claim 1 , wherein the respective interfaces, h 1 -h x , are determined through the use of the following algorithm by minimising the difference between:
u
=
arg
min
u
P
-
P
^
(
u
,
·
)
where u in the algorithm is a vector of variables that are to be determined, P is a vector of measured pressure and {circumflex over (P)} is calculated pressure based on the variables in the vector u.
3. A method according to claim 2 , wherein the algorithm is based on the least squares method or a Kalman filter.
4. Equipment for determining the level/height of one or more interphase borders/interfaces, h 1 -h x , between two or more fluids/process media (fluid phases) of different density that are contained in a vessel or a tank ( 1 ), comprising
a unit for measuring/recording a state in the tank and a second unit for determining the position (level) of the interface(s), wherein the equipment is based on the position of the different interfaces, h 1 -h x , being determined by measuring the pressure and thus indirectly determining the density of the fluid in the tank over the height of the tank using
a pressure measuring rod ( 2 ) equipped with pressure sensors ( 3 ) distributed along the whole length of the rod, and which is adapted to be positioned vertically in and extend over the height of the vessel ( 1 ) where the position of the interfaces is to be measured, wherein there are more pressure sensors and pressure measurements than the number of variables that are to be determined, so that the system is overdefined and thus more robust.
5. Equipment according to claim 4 , wherein the pressure that is measured/recorded is a differential pressure between the process medium and a reference fluid, the differential pressure being measured/recorded by a differential pressure measuring rod ( 4 ) equipped with differential pressure sensors ( 5 ) arranged along the length of the rod.
6. Equipment according to claim 5 , wherein the measuring rod has a cavity ( 6 ) in its longitudinal direction that is filled with reference fluid, the differential pressure sensors being arranged in the wall of the measuring rod ( 4 ) and adapted to measure the differential pressure between the process medium outside and the reference fluid in the cavity ( 6 ), a pressure equalising membrane ( 7 ) being arranged in connection with the differential pressure measuring rod between the reference fluid and the process medium outside.
7. Equipment according to claim 5 , wherein the measuring rod ( 2 , 4 ) comprises an elongate body and is adapted to be arranged vertically or aslant in the tank ( 1 ).
8. Equipment according to claim 5 , wherein the measuring rod ( 2 , 4 ) is arranged in connection with a substantially circular body ( 8 ) which is adapted to be positioned along the periphery of the tank ( 1 ).
9. Equipment according to claim 5 , wherein the measuring rod ( 2 , 4 ) is arranged in connection with a substantially circular body ( 8 ) that is adapted to be positioned in a flange of the tank ( 1 ).
10. Equipment according to claim 6 , wherein the measuring rod ( 2 , 4 ) comprises an elongate body and is adapted to be arranged vertically or aslant in the tank ( 1 ).
11. Equipment according to claim 6 , wherein the measuring rod ( 2 , 4 ) is arranged in connection with a substantially circular body ( 8 ) which is adapted to be positioned along the periphery of the tank ( 1 ).
12. Equipment according to claim 6 , wherein the measuring rod ( 2 , 4 ) is arranged in connection with a substantially circular body ( 8 ) that is adapted to be positioned in a flange of the tank ( 1 ).