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US5741978A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for determination of flow rate in a fluid

Assignee: Individual
•
Filing: 1995-11-09
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Granted: 1998-04-21
•
Expires: 2015-11-09
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Abstract

Abstract A method for measuring the flow rate in a fluid flow, particularly a two-phase flow comprising oil, water and gas from an offshore well, in which a temporary transitory shut-off of the fluid flow by means of a valve is performed, and the fluid pressure at a location immediately upstream of the valve is recorded from a moment of time when the valve starts closing to a selected moment of time after the valve is fully closed. Subsequently, the valve is opened to reestablish the fluid flow, and the fluid mass flux G is determined as a function of fluid density, friction factor, pipe diameter, selected moment of time after closure of the valve, friction loss recorded at the selected moment after closure and a pressure surge pressure.

Inventors

  • 👤 Jon Steinar Gudmundsson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 23:51
CPC Classifications
G; G01; G01F; G01F1/00; G01F1/66; G01F1/05; G01F1/34; G01F1/36; G01F1/74; G01P; G01P5/00; G01P5/14; G01P5/24

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 147 words
Method for measuring the flow rate in a fluid flow (30), particularly a two-phase flow comprising oil, water and gas from a development well offshore, characterized in: performing a temporary transistory shut-off of the fluid flow by means of a valve (33), and recording the fluid pressure at a location (37) immediately upstream of the valve (33) from a moment of time when the valve starts closing to a selected moment of time after the valve is fully closed, and opening the valve to re-establish the fluid flow, and determining the fluid mass flux G according to the ratio ##EQU7## where ρ=fluid density, f=friction factor, d=pipe diameter, t'=a selected moment of time after closure of the valve, Δp f .sup.• is friction loss recorded at time t.sup.• and Δp a is pressure surge pressure represented by recorded pressure increase at the moment the valve is fully closed.
Claim 2
Dependent Claim 147 words
Method for measuring the flow rate in a fluid flow (30), particularly a two-phase flow comprising oil, water and gas from a development well offshore, characterized in: performing a temporary transistory shut-off of the fluid flow by means of a valve (33), and recording the fluid pressure at a location (37) immediately upstream of the valve (33) from a moment of time when the valve starts closing to a selected moment of time after the valve is fully closed, and opening the valve to re-establish the fluid flow, and determining the fluid mass flux G according to the ratio ##EQU7## where ρ=fluid density, f=friction factor, d=pipe diameter, t'=a selected moment of time after closure of the valve, Δp f .sup.• is friction loss recorded at time t.sup.• and Δp a is pressure surge pressure represented by recorded pressure increase at the moment the valve is fully closed.
Claim 3
Dependent Claim 65 words
The method of claim 1, characterized in determining the velocity of acoustic pulse propagation in the fluid by measuring pressure as a function of time during shut-off of the valve by a reference metering means (35) and a metering means (36) located at a known distance downstream of the reference metering means (35), and determining said acoustic pulse propagation velocity according to the equation a=L/t.
Claim 4
Dependent Claim 56 words
The method of claim 1, characterized in determining the flow rate and acoustic pulse propagation velocity in a flowing multi-phase medium from a development well by a reference metering means (57) located immediately upstream of the shut-off valve (51) and a metering means (58) located at a known distance upstream of the reference metering means (57).
Claim 5
Dependent Claim 227 words
Method for measuring the flow rate of a fluid flow (40) comprising at least two phases, by means of pressure sensors (45, 46) downstream and pressure sensors (47, 48) upstream of a pulse generating means (43), characterized in using a quick-closing valve as said pulse generating means (43), and changing the valve (43) position from substantially open to fully closed, recording the fluid pressure by the pressure sensors (47, 48) and (45, 46) from a time when the valve starts closing to a selected moments time after the valve is fully closed, and then opening the valve to re-establish the fluid flow, determining the fluid flow velocity and specific acoustic velocity according to the ratio ##EQU8## where u N is the pressure pulse propagation velocity downstream and u o is the pressure pulse propagation velocity upstream, and providing the fluid flow velocity u from the formula u=0.5·(u N -u o ) or by substracting the fluid specific acoustic velocity a from the measured pulse propagation velocity: u=u N -a, and determining the fluid density ρ according to the ratio Δp.sub.a =ρ·a·Δu (2) where Δu is the change of fluid velocity, a is the velocity of acoustic pulse propagation in the fluid, thus determining the fluid flow rate G according to the equation G-ρ·u (7) where u is the fluid flow rate immediately before the valve starts closing.
Claim 6
Dependent Claim 227 words
Method for measuring the flow rate of a fluid flow (40) comprising at least two phases, by means of pressure sensors (45, 46) downstream and pressure sensors (47, 48) upstream of a pulse generating means (43), characterized in using a quick-closing valve as said pulse generating means (43), and changing the valve (43) position from substantially open to fully closed, recording the fluid pressure by the pressure sensors (47, 48) and (45, 46) from a time when the valve starts closing to a selected moments time after the valve is fully closed, and then opening the valve to re-establish the fluid flow, determining the fluid flow velocity and specific acoustic velocity according to the ratio ##EQU8## where u N is the pressure pulse propagation velocity downstream and u o is the pressure pulse propagation velocity upstream, and providing the fluid flow velocity u from the formula u=0.5·(u N -u o ) or by substracting the fluid specific acoustic velocity a from the measured pulse propagation velocity: u=u N -a, and determining the fluid density ρ according to the ratio Δp.sub.a =ρ·a·Δu (2) where Δu is the change of fluid velocity, a is the velocity of acoustic pulse propagation in the fluid, thus determining the fluid flow rate G according to the equation G-ρ·u (7) where u is the fluid flow rate immediately before the valve starts closing.

References Cited (Backward Citations)

US3523454A Cited
US4312234A Cited
US4364413A Cited
US5099697A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 2001-04-20 2001-10-20 2002-04-21 $2000.00 Window Closed / Lapsed
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