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Crisman Annual Report 2009 - Harold Vance Department of ...

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Experimental and Simulation Modeling Studies <strong>of</strong> Steam Assisted Gravity<br />

Objectives<br />

Our main research objectives are to conduct<br />

experimental and simulation modeling studies to<br />

investigate oil recovery mechanisms and steam<br />

injection efficiency during production <strong>of</strong> heavy oil<br />

under Steam Assisted Gravity Drainage (SAGD).<br />

Additionally, the research will also investigate the<br />

feasibility <strong>of</strong> petroleum distillates as steam additives<br />

to improve SAGD efficiency.<br />

Approach<br />

A 2-D scaled physical model made <strong>of</strong> Teflon has been<br />

fabricated and successfully pressure tested. The<br />

physical model will contain the sand mix, consisting<br />

<strong>of</strong> sand and heavy oil (Athabasca oil). Expansion<br />

<strong>of</strong> the steam chamber, its shape and area, and<br />

temperature distribution (Fig.1) will be visualized<br />

using a thermal (infra-red) video camera. Isotherms<br />

and steam chamber interface will be analyzed to<br />

study oil recovery and drainage mechanisms. Other<br />

data including model pressure, steam injection rate,<br />

oil and water production volumes will be recorded<br />

using a data logger and a personal computer.<br />

Simulation will be conducted to investigate the effect<br />

<strong>of</strong> different solvent types and ratios on production<br />

performance.<br />

efficiency and steam injections. Co-injecting low<br />

concentration ratios <strong>of</strong> multi-component solvents can<br />

deliver higher production rates and recovery factors<br />

along with taking advantage <strong>of</strong> both vaporized and<br />

liquid solvents.<br />

Experimental work will be continued to investigate<br />

SAGD performance and steam injection efficiency<br />

using Athabasca oil. Pure steam injection, coinjecting<br />

different solvent, including pure solvent<br />

and solvent mixture, and different solvent ratio<br />

conditions will be studied.<br />

Fig. 2. SAGD simulation shows the effect <strong>of</strong> different solvent types and<br />

ratios on oil displacement.<br />

CRISMAN INSTITUTE<br />

Fig. 1. Typical photo captured by thermal (infra-red) video camera to<br />

show steam chamber temperature distribution.<br />

Accomplishments<br />

Simulation <strong>of</strong> SAGD using CMG has been performed.<br />

Results show solvent types and ratios affect<br />

production performance (Fig.2). Meanwhile,<br />

vaporized solvent can be delivered by steam to<br />

the entire steam chamber to reduce the bitumen<br />

viscosity. Liquid solvent accelerates near-well bore<br />

flow, and so improves the mobility oil drainage<br />

Project Information<br />

1.3.13 Experimental and Analytical Modeling Studies <strong>of</strong><br />

Steam Assisted Gravity Drainage (SAGD) with NaOH and<br />

Petroleum Distillate as Steam Additives<br />

Related Publications<br />

Butler, R.M. 1991 Thermal Recovery <strong>of</strong> Oil & Bitumen, 285-<br />

359. Prentice Hall Inc., New Jersey.<br />

Nasr, T.N., Beaulieu, G., Golbeck, H. and Heck, G. Novel<br />

expanding solvent-SAGD process “ES-SAGD”. January<br />

2003. J. Cdn. Pet. Tech. 42 (1): 13-16<br />

Contacts<br />

Daulat Mamora<br />

979.845.2962<br />

daulat.mamora@pe.tamu.edu<br />

Weiqiang Li<br />

30<br />

<strong>Crisman</strong> <strong>Annual</strong> <strong>Report</strong> <strong>2009</strong>

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