System and method for real-time monitoring and estimation of intelligent well system production performance
US-10280722-B2 · May 7, 2019 · US
US11543276B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11543276-B2 |
| Application number | US-202017641017-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 2, 2020 |
| Priority date | Sep 5, 2019 |
| Publication date | Jan 3, 2023 |
| Grant date | Jan 3, 2023 |
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Embodiments include a multiphase flowmeter system (300). The multiphase flowmeter system (300) may include a first inline flow conditioner (310) for reducing a slip velocity between a liquid phase and a gas phase of a multiphase fluid, a flowmeter for measuring a flow rate of the multiphase fluid, a second inline flow conditioner (350) for separating the liquid phase and the gas phase of the multiphase fluid, a non-radioactive sensor system for measuring one or more of a gas void fraction of the multiphase fluid and a water-cut of the multiphase fluid, and a processor (480) for computing one or more flow rates of the multiphase fluid. Embodiments further include methods of measuring one or more flow rates of a multiphase fluid and other related methods, apparatuses, devices, and systems.
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What is claimed is: 1. A multiphase flow meter system comprising: a first inline flow conditioner for reducing a slip velocity between a liquid phase and a gas phase of the multiphase fluid, wherein the first inline flow conditioner receives the multiphase fluid from a flow inlet; a flow meter including one or more flow sensors for communicating data representing a total flow rate of the multiphase fluid, wherein the flow meter is downstream from and fluidly connected to the first inline flow conditioner; a second inline flow conditioner for separating the liquid phase and the gas phase of the multiphase fluid, wherein the second inline flow conditioner is downstream from and fluidly connected to the flow meter; a non-radioactive sensor subsystem for communicating data representing a gas void fraction of the multiphase fluid and a water-cut of the multiphase fluid, wherein the non-radioactive sensor subsystem is downstream from the second inline flow conditioner; and a processor for receiving data from the flow meter and the non-radioactive sensor subsystem and computing a flow rate of the liquid phase and a flow rate of the gas phase of the multiphase fluid. 2. The multiphase flow meter system according to claim 1 , wherein the first inline flow conditioner includes a flow homogenizer, the flow homogenizer including a horizontal pipe segment fluidly connected to a vertical pipe segment via a 90° pipe elbow. 3. The multiphase flow meter system of claim 1 , wherein the total flow rate includes one of a total volumetric flow rate and a total mass flow rate. 4. The multiphase flow meter system of claim 1 , wherein the one or more flow sensors of the flow meter include a first pressure sensor and a second pressure sensor, wherein the first pressure sensor and the second pressure sensor communicate data representing a differential pressure between the first pressure sensor and the second pressure sensor. 5. The multiphase flow meter system of claim 1 , wherein the second inline flow conditioner is configured to generate an annular flow in which the liquid phase is an outer phase and the gas phase in an inner phase. 6. The multiphase flow meter system of claim 1 , wherein the second inline flow conditioner is configured to generate a stratified flow. 7. The multiphase flow meter system of claim 1 , wherein the non-radioactive sensor subsystem includes a liquid-gas fraction measurement sensor for communicating data representing a gas void fraction of the multiphase fluid. 8. The multiphase flow meter system according to claim 7 , wherein the non-radioactive sensor subsystem further includes a water-cut sensor downstream from the liquid-gas fraction measurement sensor, wherein the water-cut sensor communicates data representing a water-cut of the multiphase fluid. 9. The multiphase flow meter system of claim 1 , wherein the non-radioactive sensor subsystem includes an ultrasonic probe for communicating data representing a gas void fraction of the multiphase fluid and a water-cut of the multiphase fluid. 10. The multiphase flow meter system according to claim 9 , wherein the ultrasonic probe includes one or more ultrasonic elements for emitting an ultrasonic wave. 11. The multiphase flow meter system of claim 1 , wherein the liquid phase includes a first liquid and a second liquid. 12. The multiphase flow meter system of claim 1 , wherein the flow rate of the liquid phase includes a first flow rate of a first liquid and a second flow rate of a second liquid. 13. The multiphase flow meter system of claim 1 , wherein the processor further computes a density of at least one of the liquid phase and the gas phase of the multiphase fluid. 14. An oil and/or gas production facility comprising one or more multiphase fluid meter systems; wherein the multiphase fluid meter system includes a first inline flow conditioner for reducing a slip velocity between a liquid phase and a gas phase of the multiphase fluid, wherein the first inline flow conditioner receives the multiphase fluid from a flow inlet; a flow meter including one or more flow sensors for communicating data representing a total flow rate of the multiphase fluid, wherein the flow meter is downstream from and fluidly connected to the first inline flow conditioner; a second inline flow conditioner for separating the liquid phase and the gas phase of the multiphase fluid, wherein the second inline flow conditioner is downstream from and fluidly connected to the flow meter; a non-radioactive sensor subsystem for communicating data representing a gas void fraction of the multiphase fluid and a water-cut of the multiphase fluid, wherein the non-radioactive sensor subsystem is downstream from the second inline flow conditioner; and a processor for receiving data from the flow meter and the non-radioactive sensor subsystem and computing a flow rate of the liquid phase and a flow rate of the gas phase of the multiphase fluid. 15. A method of measuring one or more flow rates of a multiphase fluid, the method comprising: flowing a multiphase fluid including a gas phase and a liquid phase through a first inline flow conditioner to reduce a slip velocity between the gas phase and the liquid phase; flowing the multiphase fluid through a flow meter including one or more sensors for communicating data representing a total flow rate of the multiphase fluid to a processor; flowing the multiphase fluid through a second inline flow conditioner for separating the liquid phase and the gas phase of the multiphase fluid; and flowing the multiphase fluid through a non-radioactive sensor subsystem which communicates data representing a gas void fraction of the multiphase fluid and a water-cut of the multiphase fluid to the processor; wherein the processor computers a flow rate of the liquid phase and the gas phase of the multiphase fluid using the data communicated by the flow meter and the non-radioactive sensor subsystem. 16. The method according to claim 15 , wherein the second inline flow conditioner generates an annular flow in which the liquid phase is an outer phase and the gas phase is an inner phase, or a stratified flow. 17. The method of claim 15 , wherein the non-radioactive sensor subsystem includes an ultrasonic probe and wherein the ultrasonic probe communicates data representing the gas void fraction of the multiphase fluid and the water-cut of the multiphase fluid. 18. The method according to claim 17 , wherein the ultrasonic probe includes one or more ultrasonic elements for emitting an ultrasonic wave. 19. The method of claim 15 , wherein the flow rate of the liquid phase includes a first flow rate of a first liquid and a second flow rate of a second liquid. 20. The method of claim 15 , wherein the processor further computes a density of at least one of the liquid phase and the gas phase of the multiphase fluid.
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Devices for measuring flow of a fluid or flow of a fluent solid material in suspension in another fluid · CPC title
using acoustic means · CPC title
with electrical or electro-mechanical indication (G01F1/37 and G01F1/38 take precedence) · CPC title
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