Method for determining a gas phase mass fraction and/or gas phase mass flow rate of a multi-phase medium with a liquid phase and a gas phase flowing in a measuring tube, and measuring sensor therefor
US-2024418552-A1 · Dec 19, 2024 · US
US10655997B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10655997-B2 |
| Application number | US-201916240246-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 4, 2019 |
| Priority date | Nov 21, 2013 |
| Publication date | May 19, 2020 |
| Grant date | May 19, 2020 |
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The invention relates to a flowmeter for liquid/gas two-phase cryogenic fluids, including: a separator of the liquid/gas phases, preferably made up of vessel, the cryogenic fluid being admitted into the top portion of said vessel; a liquid flow sensor, located on a liquid pipe in fluid communication with the bottom portion of the vessel, the vessel being placed in the top position in the space relative to the liquid flow sensor; a gas pipe, in fluid communication with the upper portion of the vessel, provided with a flow sensor of the gas phase circulating in said gas pipe; a three-way valve capable of recovering, in two of the channels thereof (A/B), the downstream end of said gas pipe and the downstream end of said liquid pipe; and a device for measuring the level of liquid in the vessel, preferably comprising two level sensors: a bottom level sensor and a top level sensor.
Opening claim text (preview).
What is claimed is: 1. A flowmeter for two-phase liquid/gas cryogenic fluids adapted and configured to operate in a storage phase and operate in a withdrawal phase, said flowmeter comprising: a liquid/gas phase separator, an upper portion of which receives the cryogenic fluid; a liquid line in fluid communication with a bottom portion of the separator; a liquid flow rate sensor located in the liquid line for measuring a flow rate of the liquid phase cryogenic fluid circulating therein, the separator being placed in an elevated position in space relative to the liquid flow rate sensor; a gas line in fluid communication with the upper portion of the tank provided with a flow rate sensor for measuring a flow rate of the gas phase cryogenic fluid circulating therein; a three-way valve having first, second, and third ports, the first port being in fluid communication with a downstream end of said gas line, the second port being in fluid communication with a downstream end of said liquid line, said three-way valve being configured and adapted to allow or disallow a flow of the gas phase cryogenic fluid via said first port and/or allow or disallow a flow of the liquid phase cryogenic fluid via said second port, the flow of the gas phase cryogenic fluid and/or liquid phase cryogenic fluid being directed by the third port to a downstream station that uses two-phase liquid/gas cryogenic fluid; a bottom level sensor and a top level sensor adapted and configured to measure a level of liquid in the tank; a controller adapted and configured: compare a level of liquid phase cryogenic fluid in the separator measured by the bottom and top level sensor to at least one setpoint value for a level of liquid phase cryogenic fluid in the separator; depending upon a result of said comparison, control operation of said three-way valve to allow or disallow the flow of gas phase cryogenic fluid into the first port and/or allow or disallow the flow of liquid phase cryogenic fluid into the second port, thus dictating a composition of the two-phase liquid/gas cryogenic fluid leaving the third port for the downstream station; determine a mass flow rate of the two-phase liquid/gas cryogenic fluid by summing the measured flow rates of the gas and liquid phase cryogenic fluids flowing in the gas and liquid lines, respectively; during a storage phase in which the flow rate of the liquid phase cryogenic fluid measured by the liquid flow rate sensor exceeds a flow rate of cryogenic fluid being directed by the third port to a downstream station, operate said three-way valve to allow a portion of the liquid phase cryogenic fluid flow in the liquid line to rise into the gas line and to allow a remaining portion of the liquid phase cryogenic fluid flow in the liquid line to exit the three-way valve through the third port; and during a withdrawal phase in which the flow rate of the liquid phase cryogenic fluid measured by the liquid flow rate sensor falls to a predetermined minimum flow rate specified by the liquid flow rate sensor, operate the three-way valve to disallow a flow of the liquid phase cryogenic fluid therethrough and to allow any of the liquid phase cryogenic fluid, that was previously allowed to rise into the gas line, to drop back down to the three-way valve to exit through the third port. 2. The flowmeter of claim 1 , wherein the liquid flow rate sensor has a head loss that is less than a pressure head of the liquid between the bottom portion of the tank and the liquid flow rate sensor. 3. The flowmeter of claim 2 , wherein the liquid flow rate sensor has a head loss equivalent to less than 2 meters of liquid height of the liquid phase cryogenic fluid. 4. The flowmeter of claim 1 , wherein the liquid/gas phase separator is a tank.
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