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

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Investigation <strong>of</strong> Hybrid Steam-Solvent Processes to Increase Efficiency <strong>of</strong> Thermal<br />

Oil Recovery Methods<br />

Objectives<br />

Steam assisted gravity drainage (SAGD) has received<br />

considerable attention as a proven technique to<br />

recover heavy oil and bitumen which are immobile<br />

at reservoir conditions. The main drawbacks <strong>of</strong> this<br />

process are high energy intensity (steam generation<br />

requirements) and environmental issues.<br />

The addition <strong>of</strong> light hydrocarbon solvents to steam is<br />

the simplest and most important approach to improve<br />

SAGD process and reduce potential problems. Main<br />

benefits possibly obtained by a hybrid steam solvent<br />

process include: reduced Steam Oil Ratio, reduced<br />

environmental impact, increased recovery via<br />

reduced S or<br />

, reduced capital to startup and enhanced<br />

well productivity. Principal challenges are the choice<br />

<strong>of</strong> solvent and concentration and operating strategy.<br />

Our main research objective is to reduce energy<br />

intensity <strong>of</strong> SAGD process by using solvents<br />

and investigate the effect <strong>of</strong> different operating<br />

strategies. Key tasks are to evaluate the effect on<br />

oil recovery <strong>of</strong> the following:<br />

» Solvents, (e.g., butane, hexane and condensates)<br />

» Solvent concentration<br />

» Injection types (e.g., cyclic steam solvent injection)<br />

Fig. 1. Simulation results <strong>of</strong> oil recovery.<br />

with increasing concentration. The aluminum 2D<br />

cylindrical model is under construction. The sandmix<br />

space has an inner radius <strong>of</strong> 4 in, 1-in thickness, and<br />

10-in height, and will be lined with insulating Teflon<br />

layers (Fig. 2). The experimental set up is shown<br />

in Fig. 3.<br />

Approach<br />

Experiments will be carried out in a scaled 2D<br />

cylindrical cell to evaluate the effect <strong>of</strong> steam-solvent<br />

processes. Pujol and Boberg’s scaling method has<br />

been used to design the model. Advantages <strong>of</strong> the<br />

cylindrical model are the relatively high pressure<br />

capability without a pressure jacket, the use <strong>of</strong> inner<br />

thermal insulation, and the ability to conduct gravity<br />

drainage experiments (e.g., VAPEX, SAGD). Oil and<br />

water production, gas composition, and temperature<br />

would be measured and analyzed. Numerical<br />

simulation will be used for parametric studies.<br />

Accomplishments<br />

Compositional reservoir simulation studies <strong>of</strong> Cold<br />

Lake bitumen were performed to investigate the<br />

effect <strong>of</strong> solvent type and concentration on recovery<br />

under SAGD at 220°C and 3100 kpa (450 psia)<br />

(Fig. 1). With C5-C7 as solvents, bitumen recovery<br />

increases to about 80% at 20 wt%. C2 and C3<br />

however exist as vapor and act as thermal insulators<br />

at the steam-bitumen interface, reducing recovery<br />

Project Information<br />

1.3.22 Investigation <strong>of</strong> Hybrid Steam-Solvent Injection to<br />

Increase Efficiency <strong>of</strong> Thermal Oil Recovery Processes<br />

Related Publications<br />

Nasr T.N., and Ayodele O.R. New Hybrid Steam-Solvent<br />

Processes for the Recovery <strong>of</strong> Heavy Oil and Bitumen.<br />

Paper SPE 101717, presented at the 2006 International<br />

Petroleum Exhibition and Conference, Abu Dubai, UAE, 5-8<br />

November.<br />

Ayodele, O.R., et al. Laboratory Experimental Testing<br />

and Development <strong>of</strong> an Efficient Low Pressure ES-SAGD<br />

Process. <strong>2009</strong>. J. Cdn Pet. Tech. 48 (9).<br />

Contacts<br />

Daulat Mamora<br />

979.845.2962<br />

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

Mojtaba Ardali<br />

CRISMAN INSTITUTE<br />

36<br />

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

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