dc.contributor.advisor | Torabi, Farshid | |
dc.contributor.author | Abedini, Ali | |
dc.date.accessioned | 2014-11-06T15:30:13Z | |
dc.date.available | 2014-11-06T15:30:13Z | |
dc.date.issued | 2014-07 | |
dc.identifier.uri | http://hdl.handle.net/10294/5503 | |
dc.description | A Thesis Submitted to the Faculty of Graduate Studies and Research
In Partial Fulfillment of the Requirements For the Degree of Doctor of Philosophy
in Petroleum Systems Engineering, University of Regina. xxvi, 228 p. | en_US |
dc.description.abstract | Carbon dioxide (CO2) injection processes are among the most promising
enhanced oil recovery techniques based on their great potential to improve oil production
while utilizing geological storage of carbon dioxide to reduce greenhouse gas emissions.
Among various CO2 injection modes, cyclic CO2 injection (CO2 huff-and-puff) scenarios
have seen significant increase in interest for the purpose of enhanced oil recovery (EOR)
in both non-fractured and fractured reservoirs. Several operating parameters, including
operating pressure, solvent (CO2) injection time, soaking period, water saturation, etc.,
affect the performance of this process. However, the number of studies that consider
these parameters is relatively limited. In this study, the performance of cyclic CO2
injection under various operating conditions for a light crude oil system is experimentally
investigated. First, a comprehensive experimental study on the phase behaviour of the
crude oil–CO2 system was conducted. Thereafter, a series of cyclic CO2 injection tests
was designed and carried out in non-fractured and fractured porous media to determine
the impact of various parameters on the recovery efficiency of this process.
For the cyclic CO2 injection tests conducted at operating pressures ranging from
immiscible to near-miscible conditions, it was found that the oil recovery increases
considerably with operating pressures and reaches near maximum value at miscible
condition. However, beyond this range, where the operating pressure exceeds the
minimum miscibility pressure, the oil recovery factor was almost constant and further
increase in operating pressure did not improve the oil recovery effectively. In addition,
although it was seen that a longer soaking period and the presence of connate water
saturation are positive parameters that enhance the recovery performance of immiscible cyclic CO2 injections, these parameters do not have noticeable influence in miscible
injection scenarios. Furthermore, the results showed that longer CO2 injection time does
not enhance the oil recovery. Additionally, it was observed that the cyclic CO2 injection
process has a great capacity for CO2 storage, and it was found that the CO2 storage
potential is more efficient if the cyclic injection process is implemented at pressures near
the minimum miscibility pressure.
The asphaltene precipitation inside the rock sample and its subsequent
permeability reduction due to the CO2 injection were examined. The amount of the
precipitated asphaltene in the porous media is considerably higher during miscible
injection scenarios resulting in drastic reduction of the oil effective permeability. The
compositional analysis of the remaining crude oil in the core also demonstrated that the
mechanism of light component extraction by CO2 is much stronger during miscible cyclic
CO2 injection compared to immiscible injection.
The effect of fractures in the porous media on the oil recovery of cyclic CO2
injection was investigated, and the results showed that the presence of fracture
significantly improves the oil recovery during the process. The impact of fracture was
found to be more effective during immiscible cyclic CO2 injection. In addition, the
examination of fracture orientation showed that horizontal fracturing remarkably
enhances the oil production, while no noticeable increase in oil production was observed
when the orientation of fracture was vertical. The numerical simulation of the process
also revealed that the oil recovery of cyclic CO2 injection gives larger benefits from
greater fracture width together with the presence of more fractures inside the system
through enlarging the contact area between the CO2 and oil in-place. | en_US |
dc.description.uri | A Thesis Submitted to the Faculty of Graduate Studies and Research In Partial Fulfillment of the Requirements for the Degree of Doctor of Philosophy *, University of Regina. *, * p. | en |
dc.language.iso | en | en_US |
dc.publisher | Faculty of Graduate Studies and Research, University of Regina | en_US |
dc.title | Mechanisms of Oil Recovery During Cyclic CO2 Injection process: Impact of Fluid Interactions, operating parameters, and Porous Medium | en_US |
dc.type | Thesis | en |
dc.description.authorstatus | Student | en |
dc.description.peerreview | yes | en |
thesis.degree.name | Doctor of Philosophy (PhD) | en_US |
thesis.degree.level | Doctoral | en |
thesis.degree.discipline | Engineering - Petroleum Systems | en_US |
thesis.degree.grantor | University of Regina | en |
thesis.degree.department | Faculty of Engineering and Applied Science | en_US |
dc.contributor.committeemember | Zeng, Fanhua | |
dc.contributor.committeemember | Shiriff, Ezeddin | |
dc.contributor.committeemember | Ibrahim, Hussameldin | |
dc.contributor.committeemember | Fallat, Shaun | |
dc.identifier.tcnumber | TC-SRU-5503 | |
dc.identifier.thesisurl | http://ourspace.uregina.ca/bitstream/handle/10294/5503/Abedini_Ali_200299172_PhD_PSE_Fall2014.pdf | |