Wet Gas Measurement

Manus Henry; Michael S Tombs

Wet Gas Measurement

Manus Henry (Inventor), Michael S Tombs (Inventor)

University of Oxford

Research output: Patent

Abstract

A multi-phase process fluid is passed through a vibratable flowtube. Motion is induced in the vibratable flowtube. A first apparent property of the multi-phase process fluid based on the motion of the vibratable flowtube is determined, and an apparent intermediate value associated with the multi-phase process fluid based on the first apparent property is determined. A corrected intermediate value is determined based on a mapping between the intermediate value and the corrected intermediate value. A phase-specific property of a phase of the multi-phase process fluid is determined based on the corrected intermediate value.

Original language	English
Patent number	US2014373639A1
IPC	G01F 1/84
Priority date	28/08/06
Filing date	9/09/14
Publication status	Published - 25 Dec 2014
Externally published	Yes

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24 Patent

Wet Gas Measurement
Henry, M. (Inventor) & Tombs, M. (Inventor), 12 Jan 2016, IPC No. G01F 1/84, G01F 1/00, G01F 1/74, Patent No. US9234780B2, 9 Sept 2014, Priority date 28 Aug 2006, Priority No. US82375306P
Research output: Patent

File
Wet Gas Measurement
Henry, M. (Inventor) & Tombs, M. (Inventor), 9 Feb 2016, IPC No. GO1F 1/74, GO1F 1/84, Patent No. CA2658810C, 28 Aug 2007, Priority date 28 Aug 2006, Priority No. US82375306P
Research output: Patent

File
Wet gas measurement
Henry, M. (Inventor) & Tombs, M. (Inventor), 24 Nov 2015, IPC No. GO1F 1/74, Patent No. CA2683385C, 18 Apr 2008, Priority date 20 Apr 2007, Priority No. US91314807P
Research output: Patent

File

Cite this

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AB - A multi-phase process fluid is passed through a vibratable flowtube. Motion is induced in the vibratable flowtube. A first apparent property of the multi-phase process fluid based on the motion of the vibratable flowtube is determined, and an apparent intermediate value associated with the multi-phase process fluid based on the first apparent property is determined. A corrected intermediate value is determined based on a mapping between the intermediate value and the corrected intermediate value. A phase-specific property of a phase of the multi-phase process fluid is determined based on the corrected intermediate value.

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Wet Gas Measurement

Abstract

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