Systems and methods for measuring flow rates and densities of the components of oil, water and gas mixtures
AssigneeAtlantic Richfield Company
InventorMiroslav M. Kolpak
Life of this patent
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AssigneeAtlantic Richfield Company
InventorMiroslav M. Kolpak
Estimating the term…
Multiphase fluid flowstreams of gas, oil and water are measured by flowmeters which include an embodiment using a turbine flowmeter and a densitometer with total accuracy in the range of .+-.15%, and an embodiment using a gas-liquid separator and a Coriolis flowmeter for flowstreams of a relatively high gas-to-liquid ratio with accuracies of .+-.5% when the gas carry-over in the liquid flowstream is less than about 5%. A second alternate embodiment includes a water fraction meter, a turbine flowmeter and a densitometer for measuring flows with relatively low gas-to-liquid ratios but accurate measure of the water fraction. A meter capable of handling relatively high gas-to-liquid ratio but with residual gas in the liquid flowstream of less than 5% includes a separator, a Coriolis meter for measuring the liquid density and mass flow rate in the liquid flowstream and a densitometer and turbine flowmeter for measuring the fluid in the gas flowstream leaving the separator. A fourth alternate embodiment includes a turbine flowmeter and a densitometer in both flowstreams leaving the separator and a water fraction meter in the liquid flowstream wherein mixtures with high gas-to-liquid ratio and residual gas in the liquid flowstream of up to about 20% may be measured.
A method for determining the gas density, liquid density, and the volumetric flow rates of a multiphase fluid and each of the components of said multiphase fluid comprising a gas and a liquid mixture of oil and water without separating gas from said multiphase fluid, wherein the densities of the oil and water are known, the specific gravity of the gas is known, the pressure and temperature of said multiphase fluid flowstream are either assumed or measured, and the fraction of one liquid in the liquid mixture is known, comprising the steps of:
A method for determining the gas density, liquid density, and the flow rates of a multiphase fluid and each of the components of said multiphase fluid comprising gas and a liquid mixture of oil and water, wherein the densities of the oil and water are known, the pressure and temperature of said multiphase fluid flowstream are either assumed or measured, and the specific gravity of the gas is known, comprising the steps of:
The method set forth in claim 6 including the step of:
A flowmeter for determining the flow rate of each of the fluid components of gas, oil and water in a multiphase fluid comprising a mixture of said gas, oil and water, comprising:
A method for determining the volumetric flow rate of a multiphase fluid comprising gas and a liquid mixture of oil and water wherein the oil density, water density, gas specific gravity, gas compressibility factor, and water fraction in the liquid mixture of oil and water are known, and the pressure and temperature of said multiphase fluid flowstream are either assumed or measured, using a multiphase fluid flowmeter including a liquid-gas separator having a liquid mixture discharge conduit and a conduit for conducting a fluid which is primarily gas from said separator, a Coriolis meter for measuring the density of the liquid mixture and the liquid mixture mass flow rate flowing from said separator, a densitometer for measuring the density of said fluid flowing from the separator and a volumetric flowmeter for measuring the volumetric flow rate of said fluid flowing from said separator, said method including the steps of:
A flowmeter for determining the flow rate of each of fluid components of gas, oil and water in a multiphase fluid flowstream comprising a mixture of said gas, oil and water, comprising:
A method for determining the volumetric flow rates of oil, water and gas in a multiphase fluid flowstream wherein the oil density, water density, gas specific gravity, gas compressibility factor are known, and the pressure and temperature of the multiphase fluid flowstream are either assumed or measured, comprising the steps of:
Dependencies are inferred from the claim text.