| Publisher |
Society of Petroleum Engineers
| Language | English |
| Document ID | 139552-MS | DOI
 | 10.2118/139552-MS |
| Content Type | Conference Paper |
| Title | Improving the Recovery of CO2 Injection in Sarkan Oil Field Reservoir in Iran by Selecting the Reasonable Dispersivity Coefficient for Injection Process |
| Authors |
M. Kamalipour, Iranian Central Oil Field; S.M. Farouq Ali, Heavy Oil Recover
Technology; A. Shahrabadi, Research Institute of Petroleum Industry; M.
Jamialahmadi, J. Nabimeybodiy, University of Louisiana; A. Jannat Rostami,
Iranian Central Oil Field
|
| Source |
SPE International Conference on CO2 Capture, Storage, and Utilization,
10-12 November 2010,
New Orleans, Louisiana, USA
|
| ISBN | 978-1-55563-317-2 |
| Copyright |
2010. Society of Petroleum Engineers
|
Discipline Categories | 6 Reservoir Description and Dynamics 6.4 Primary and Enhanced Recovery Processes 6.5 Reservoir Simulation
|
| Preview |
Abstract
Evaluation and improvement of sweep efficiency are important issues of miscible
displacement process. Miscibility is controlled by physical dispersion during
miscible processes. It comprises of two parameters: diffusion and mechanical
dispersion. Unfortunately this parameter is usually ignored during simulating
the miscible processes which would be considered as an enormous source of
error. Results show the existence of three regions at which each component of
physical dispersion controls the miscible CO2 injection. For dispersivities
between 0.123m to 0.175m the miscible process is controlled by physical
dispersion mechanism while dispersivities lower than 0.123m specifies a region
controlled by diffusion in the field case. The third region is the region for
dispersivities greater than 0.175m and the main parameter affecting the
miscible process in this region is mechanical dispersion. This study discusses
the the effect of this parameter on recovery, mixing zone length and
breakthrough time of injecting CO2 in a natural fracture reservoir in
Iran.
Introduction
Mixing of fluids in porous media during miscible injection process is due to
convection, diffusion and mechanical dispersion. Diffusion is the result of
concentration gradient while mechanical dispersion is due to velocity
variation. [1, 2]
The term physical dispersion which is usually used in miscible processes is the
summation of diffusion and mechanical dispersion. Physical dispersion in porous
media is a function of miscible fluids, structure of the medium, particle size
of the porous media and the velocity of displacement.
Although diffusion and physical dispersion are essential parameters to simulate
a miscible injection process, they are mostly neglected in simulations. This
study shows the effect of such simplification on performance of the process.
This simplification is mostly due to have scarce correlations at high pressure
and temperature. Knowing the appropriate methods to calculate diffusion and
mechanical dispersion, leaves no doubt in using these parameters in simulating
the miscible processes. [3]
The effect of neglecting physical dispersion on performance of the system has
been discussed in this Study. Effect of physical dispersion on breakthrough
time and recovery of the process has been considered.
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| File Size | 280 KB
| Number of Pages | 4 |