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Others were still dominated by the solution gas drive.
As opposed to the oil, the viscosity of water is not considerably affected by the solution gas or by the pressure.
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Although the observed data do not have any recording for the produced gas rates, the model was able to give a trend of the produced gas during the history-matching process by using the solution gas oil ratio (Rs), as Fig. 7 shows.
It must be noted that for undersaturated reservoirs, only the solution gas reduction is affected by the BPR installation.
Moreover, some of the gas remains dissolved, governed by thermodynamics, as solution gas in the liquid.
The saturated oil was simulated by decreasing the cell pressure from the reservoir pressure to 4.0 MPa, and disengaging the released solution gas from oil by strong agitation in the PVT cell.
Primary recovery of heavy-oil is remarkably low due to high viscosity and low energy by solution gas exsolution to drive the oil.
The volume of solution gas produced by the pressure difference in the tubing is not taken into account.
Deoxygenation was achieved by switching superfusate to the same solution gassed ≥30 min prior to the experiment with 100% N2, and by flushing of the perfusion chamber with N2 during the deoxygenation period.
The reaction was stirred at room temperature in the dark for 4 h, after which residual bromine was removed by purging the solution with nitrogen gas for 1 h.
Solution gas.
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