Fluid density from downhole optical measurements

• US 9,243,493 B2
• Filed: 05/03/2013
• Issued: 01/26/2016
• Est. Priority Date: 06/11/2008
• Status: Active Grant

• Current Assignee: Alcon Incorporated
• Original Assignee: Schlumberger Technology Corporation (SLB)
• Inventors: Hsu, Kai, Indo, Kentaro, Mullins, Oliver C., Hegeman, Peter S.
• Primary Examiner(s): Williams, Hezron E
• Assistant Examiner(s): NGUYEN, HOANG T
• Application Number:
  US13/886,605
• Publication Number:
  US 20130239664A1
• Time in Patent Office: 998 Days
• Field of Search: 731/521.8, 731/522.2, 731/522.4, 731/522.7, 731/522.8, 731/525.2, 73/15.7, 73/16.6, 73/16.7, 73/16.9, 73/17.1, 166/250.01, 166/250.07, 166/254.2, 175/40, 175/41, 175/48, 175/50
• US Class Current: 1/1
• CPC Class Codes: E21B 47/113 using electrical indications; using light radiations
• CPC Class Codes: E21B 49/08 Obtaining fluid samples or testing fluids, in boreholes or wells
• CPC Class Codes: E21B 49/0875 determining specific fluid parameters
• CPC Class Codes: E21B 49/088 combined with sampling

Abstract

A system and method for determining at least one fluid characteristic of a downhole fluid sample using a downhole tool are provided. In one example, the method includes performing a calibration process that correlates optical and density sensor measurements of a fluid sample in a downhole tool at a plurality of pressures. The calibration process is performed while the fluid sample is not being agitated. At least one unknown value of a density calculation is determined based on the correlated optical sensor measurements and density sensor measurements. A second optical sensor measurement of the fluid sample is obtained while the fluid sample is being agitated. A density of the fluid sample is calculated based on the second optical sensor measurement and the at least one unknown value.

Claims

1. An apparatus, comprising:

a main fluid flowline positioned within a housing;

a circulating fluid flowline positioned within the housing;

a multi-port valve positioned within the housing and coupling the main fluid flowline and the circulating fluid flowline, wherein the multi-port valve is configured to move between a first position that places the main fluid flowline and the circulating fluid flowline in fluid communication, and a second position that isolates the circulating fluid flowline from the main fluid flowline;

a downhole analysis module positioned within the housing and having a pressure and volume control unit (PVCU) controlled by a motive force producer, a density-viscosity sensor, a circulating pump, an optical sensor, and a pressure/temperature sensor, wherein each of the PVCU, density-viscosity sensor, circulating pump, optical sensor, and pressure/temperature sensor are coupled to the circulating fluid flowline; and

a control module positioned within the housing and having a communications interface coupled to the multi-port valve and the analysis module, a processor coupled to the communications interface, and a memory coupled to the processor, wherein the memory comprises a plurality of instructions executable by the processor, the instructions including instructions for;

manipulating the multi-port valve to the first position to allow a fluid sample to move from the main fluid flowline to the circulating fluid flowline and then manipulating the valve to the second position to isolate the circulating fluid flowline from the main fluid flowline;

setting a pressure of a fluid sample in the isolated fluid circulation loop to a starting pressure using the PVCU;

altering the pressure of the fluid sample in the fluid circulation loop for a first time period until a first stopping threshold is reached using the PVCU;

measuring a plurality of density-viscosity values and a plurality of optical values of the fluid sample using the density-viscosity sensor and the optical sensor, respectively, while the pressure of the fluid sample is being altered and while the circulating pump is not activated; and

correlating the plurality of density-viscosity values and the optical values.

2. The apparatus of claim 1 further comprising instructions for:

altering the pressure of the fluid sample in the fluid circulation loop for a second time period until a second stopping threshold is reached using the PVCU;

activating the circulating pump to agitate the fluid sample during the second time period; and

measuring a second plurality of optical values of the fluid sample using the optical sensor while the circulating pump is activated.

3. The apparatus of claim 2 further comprising instructions for calculating a fluid density of the fluid sample based on the correlation of the plurality of density-viscosity values and the optical values and based on the second plurality of optical values.

4. The apparatus of claim 1 further comprising instructions for assigning one or more wavelength channels to the optical sensor.