IP Library Granted Patent US 8,874,382
Granted Patent B2
US 8,874,382 · App. 12/771,751 · Granted Oct 28, 2014

Methods and systems for optimizing carbon dioxide sequestration operations

Inventors: Sandeep Verma (Acton, MA); Charles S. Oakes (Cambridge, MA); Terizhandur S. Ramakrishnan (Boxborough, MA)
Assignee: Schlumberger Technology Corporation
F17D1/04F17D1/005B01D2257/504F17D3/01G06Q99/00
View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 8,874,382
App. No.
12/771,751
Granted
Oct 28, 2014
Kind
B2
Abstract

Methods and systems are provided for controlling operational parameters of a CO 2 compression surface facility or pipeline in order to maintain a CO 2 stream having impurities flowing in the pipeline in a liquid or supercritical phase. Sensors may be provided to sense whether the flow is single-phase or two-phase flow, and feedback provided to adjust the pressure and/or temperature at the pipeline inlet. The system is preferably optimized to limit power consumption and/or cost.

Claims (31)

1. A method of controlling a mostly-CO2 effluent stream in a pipeline, comprising:

using at least at sensor to sense a state of said mostly-CO2 effluent stream along or at an outlet of said pipeline, and feeding an indication of said state back to a controller; and

using the controller to control at least one of operating pressure and temperature of the mostly-CO2 effluent stream in order to (i) maintain said effluent stream as a single-phase liquid or a supercritical fluid stream in the pipeline using said indication of said state of said mostly-CO2 effluent stream and (ii) cause said mostly-CO2 effluent stream to move closer to a bubble-point line, while maintaining said mostly-CO2 effluent stream as the single-phase liquid or the supercritical fluid stream, when said indication of said state of said mostly-CO2 effluent stream indicates single-phase flow.

2. A method according to claim 1 , wherein:

said controlling comprises generating a phase analysis of the mostly-CO2 effluent stream, and running a simulation of the pipeline using known characteristics of the pipeline and the phase analysis in order to set operating inlet pressure and temperature criteria for said mostly-CO2 effluent stream.

3. A method according to claim 2 , wherein.

said phase analysis is a pressure-temperature phase diagram computation.

4. A method according to claim 2 , wherein:

said generating a phase analysis comprises obtaining a sample of said mostly-CO2 effluent stream and analyzing said sample in a laboratory.

5. A method according to claim 2 , wherein:

said generating, a phase analysis comprises conducting a compositional analysis of said mostly-CO2 effluent stream utilizing at least one gas analyzer and generating said phase analysis based on aid compositional analysis.

6. A method according to claim 5 , wherein:

said generating a phase analysis comprises generating a phase diagram based on said compositional analysis by utilizing equations of state.

7. A method according to claim 6 , wherein

said equations of state are based on one of Helmholtz free energy, cubic equations of state, and virial equations of state.

8. A method according to claim 2 , wherein:

said known characteristics of said pipeline comprise at least a diameter of said pipeline, a roughness rating for said pipeline, a length of said pipeline, and ambient conditions associated with said pipeline.

9. A method according to claim 1 , wherein:

if said indication of said state of said mostly-CO2 effluent stream indicates two-phase flow, adjusting at least one of said operating press and temperature to cause said mostly-CO2 effluent stream to return o single-phase flow.

10. A method according to claim 9 , wherein:

said adjusting comprises increasing said operating pressure at an inlet to said pipeline.

11. A method according to claim 9 , wherein:

said adjusting comprises decreasing said operating temperature at an inlet to said pipeline.

12. A method according to claim 9 , wherein:

said adjusting comprises at least one of increasing said operating pressure and decreasing said operating temperature at a location along the pipeline other than at an inlet of said pipeline.

13. A method according to claim 1 , wherein:

said at least one sensor comprises at least one sensor at said pipeline outlet.

14. A method according, to claim 1 , wherein:

said at least one sensor comprises a plurality of sensors at a plurality of ocations along said pipeline.

15. A method according to claim 1 , wherein:

depending upon said indication of said state of said mostly-CO2 effluent stream, adjusting a compositional make-up of said mostly-CO2 effluent stream.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 16, 2010
From: VERMA, SANDEEP; OAKES, CHARLES S.; RAMAKRISHNAN, TERIZHANDUR S.
To: SCHLUMBERGER TECHNOLOGY CORPORATION
Reel/Frame 024700/0393 →
Continuity (2)
Provisional Application 61174821 · May 1, 2009
Related Publication 20100287123A1 · Nov 11, 2010