US4726219A
Expired / Lapsed
US
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Method and system for determining fluid pressures in wellbores and tubular conduits
Assignee: Atlantic Richfield Co
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Filing: 1986-02-13
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Granted: 1988-02-23
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Expires: 2006-02-13
Abstract
Abstract Friction pressure losses are obtained for non-Newtonian or generalized Newtonian fluids being pumped through conduits at high flow rates, such as in hydraulic fracturing of subterranean formations, by measuring friction pressure losses in a pipe viscometer under laminar flow conditions. The pipe viscometer includes a pump which supplies fluid to a continuous loop having three pipe sections of different diameter for measuring pressure drop at different flow velocities. Sets of data points of generalized shear stress and shear rate are measured for determining the consistency index (K') and the Power Law or flow behavior index (n'). The generalized Reynolds number of the fluid being pumped is determined using the values of consistency index and flow behavior index and this Reynolds number is maintained in a second pipe viscometer section arranged in parallel with the laminar flow loop by pumping the same fluid wherein the second pipe viscometer section has the same roughness as the conduit through which friction pressure loss is to be determined. The Fanning friction factor (f) is determined for the pipe viscometer section from known values of friction pressure drop over a predetermined length of the pipe viscometer section at a known flow velocity, known fluid density and known hydraulic radius of the pipe viscometer section. The actual pressure drop over a predetermined length of conduit is determined using the calculated value of friction factor (f) and measured values of fluid density, flow velocity and conduit dimensions.
Inventors
- 👤 C. Mark Pearson
- 👤 Fevzi Zeren
- 👤 Ahmed S. Abou-Sayed
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-29 22:29
CPC Classifications
G; G01; G01N; G01N11/00; G01N11/02; G01N11/04; G01N11/08; E; E21; E21B; E21B21/00; E21B21/01; E21B43/00; E21B43/25; E21B43/26; E21B43/2607
Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
252 words
A method for determining friction pressure losses in a flow conduit through which a non-Newtonian or generalized Newtonian fluid is being pumped, at a predetermined rate comprising the steps of: pumping said fluid through conduit means of known length and diameter and at plural known velocities and measuring the pressure differential due to friction over said known length at said plural velocities, respectively; calculating the generalized shear stress and shear rate for said plural velocities and respective pressure differentials due to friction losses; determining the consistency index (K') and the Power Law Index (n') for said fluid from the respective sets of values of shear stress and shear rate; selecting a scaling parameter of the fluid flowing through said flow conduit and determining a value of said scaling parameter for the flow conditions of said fluid flowing through said flow conduit; conducting said fluid through a pipe viscometer section at the same value of said scaling parameter; measuring the friction pressure loss, the fluid density, and the velocity of fluid flow through said viscometer section; calculating the value of the Fanning friction factor (f) based on the measured values of friction pressure loss, fluid density, fluid velocity and the effective diameter and length of said viscometer section; and determining the friction pressure loss through said flow conduit by measuring the effective diameter of said flow conduit, the effective length of said flow conduit, the density of said fluid, the velocity of fluid flow through said flow conduit and using said friction factor.
Claim 2
Independent Claim
252 words
A method for determining friction pressure losses in a flow conduit through which a non-Newtonian or generalized Newtonian fluid is being pumped, at a predetermined rate comprising the steps of: pumping said fluid through conduit means of known length and diameter and at plural known velocities and measuring the pressure differential due to friction over said known length at said plural velocities, respectively; calculating the generalized shear stress and shear rate for said plural velocities and respective pressure differentials due to friction losses; determining the consistency index (K') and the Power Law Index (n') for said fluid from the respective sets of values of shear stress and shear rate; selecting a scaling parameter of the fluid flowing through said flow conduit and determining a value of said scaling parameter for the flow conditions of said fluid flowing through said flow conduit; conducting said fluid through a pipe viscometer section at the same value of said scaling parameter; measuring the friction pressure loss, the fluid density, and the velocity of fluid flow through said viscometer section; calculating the value of the Fanning friction factor (f) based on the measured values of friction pressure loss, fluid density, fluid velocity and the effective diameter and length of said viscometer section; and determining the friction pressure loss through said flow conduit by measuring the effective diameter of said flow conduit, the effective length of said flow conduit, the density of said fluid, the velocity of fluid flow through said flow conduit and using said friction factor.
Claim 3
Dependent Claim
104 words
The method set forth in claim 1 wherein: the steps of selecting the scaling parameter and of conducting flow through said flow conduit and through said viscometer section at the same value of said scaling parameter comprises determining the generalized Reynolds number of flow through said flow conduit using the determined values of consistency index and Power Law Index, the density of said fluid, the velocity of fluid flow through said flow conduit, and the effective diameter of said flow conduit; and conducting fluid flow through said viscometer section at the same Reynolds number as calculated for the fluid flow through said flow conduit.
Claim 4
Dependent Claim
61 words
The method set forth in claim 1 wherein: the step of pumping said fluid through said conduit means comprises providing said conduit means as a continuous length of conduit having discrete portions of different diameter and measuring the pressure differential due to friction over separate predetermined lengths of said discrete portions, respectively, at a predetermined flow rate through said conduit means.
Claim 5
Dependent Claim
33 words
The method set forth in claim 3 wherein: said predetermined flow rate is conducted at a Reynolds number of said fluid which provides for substantially laminar flow of fluid through said discrete portions.
Claim 6
Dependent Claim
71 words
The method set forth in claim 1 wherein: said conduit means of known length and diameter and said viscometer section comprise a common length of pipe having means for measuring a pressure differential due to friction across said known length, and the step of pumping said fluid comprises pumping said fluid through said viscometer section at selected flow rates to provide said plural velocities and pressure differentials due to friction losses.
Claim 7
Dependent Claim
25 words
The method set forth in claim 5 wherein: said selected flow rates are selected to provide substantially laminar flow of fluid through said viscometer section.
Claim 8
Dependent Claim
21 words
The method set forth in claim 6 wherein: said step of selecting a scaling parameter comprises using the generalized Reynolds number.
Claim 9
Dependent Claim
33 words
The method set forth in claim 7 wherein: said step of selecting said scaling parameter includes providing said viscometer section with the same surface roughness as the surface roughness of said flow conduit.
Claim 10
Dependent Claim
34 words
The method set forth in claim 8 wherein: said step of selecting said scaling parameter includes providing said viscometer section with the same ratio of hydraulic radius to surface roughness as said flow conduit.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1991-02-22 | 1991-08-24 | 1992-02-23 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1995-02-22 | 1995-08-24 | 1996-02-23 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1999-02-22 | 1999-08-24 | 2000-02-23 | $7700.00 | Window Closed / Lapsed |