Abstract: An apparatus and related method for measuring the properties and individual flow rates of a two-phase flow comprising a gas and a liquid is disclosed. This apparatus and related method also can determine whether the liquid is travelling in primarily a mist or stratified flow. More precisely, one embodiment of the disclosed invention uses measured parameters such as gain, standard deviation in upstream and downstream travel times for an ultrasonic signal, measured speed of sound, noise, signal quality, batch failure rate, and velocity profile to infer the amount of liquid in the gas flow, and in what form the liquid is travelling. For a horizontal two-phase flow, an internal measurement can be used as a dry gas reference, although the invention is also applicable to a vertical flow. For increased confidence, these determinations may be corroborated by the disclosed liquid level measurement device.

Abstract: A system monitors the composition of emulsions (e.g., oil/water mixtures) by measuring one or more electrical properties (e.g., dielectric constant) of the emulsion. A computer processor determines a plurality of possible solutions using a predetermined relationship between the measured electrical properties and the component fractions of the emulsion. One possible solution is determined for each component that might be the continuous phase in the emulsion. The computer processor then evaluates the component fractions resulting from each possible solution to choose which single solution is most reasonable based on known physical limits for a continuous phase emulsion involving the component associated with each possible solution. The component fractions associated with the selected solution are output by the processor.

Abstract: To study the properties of a multiphase fluid under pressure flowing along a duct, such as the petroleum stream produced by an oil well, a fraction of the fluid is taken from a substantially vertical first length of the duct within which the fluid is agitated and flows upwards, and this fraction is transferred into a separator receptacle with the top of said receptacle being connected to a second length of the duct located downstream from the first length and at a slightly lower pressure relative thereto. Thereafter, the volume ratio of the liquid phases can be determined, e.g. by pouring them into the separator receptacle and measuring the levels thereof, or by causing the liquid emulsion to flow through an appropriate sensor device and where the emulsion density can be determined by weighing the separator receptacle before and after such a liquid phase/emulsion pouring step.