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Open image in new window Fig. 6 Time-series of waterflood advance and oil withdrawal in an overbalanced doublet (wells separated by d* = 4).
However, increasing the oil withdrawal rate caused the viscous forces to become dominant compared to capillary forces, which led to instability in gas diffusion into the matrix part.
As it is obvious, among those experiments in which all properties except oil withdrawal rate were maintained constant, raising the production rate reduces the recovery factor at gas breakthrough.
Open image in new window Fig. 8 Time-series of waterflood advance and oil withdrawal in a balanced doublet (wells separated by d* = 20) affected by an impermeable fault.
However, when the FCC unit is blended with a certain amount (generally less than 20 wt%) of CGO, the activity and selectivity of catalyst decrease, the feedstock conversion drops, recycle oil and slurry oil withdrawal increase, the yield of coke increases, product distribution deteriorates, and CGO bending ratio becomes strictly limited [1, 2, 3].
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Oil-withdrawal contours in red, stream lines in yellow.
b Oil-withdrawal contours (red) and stream lines (yellow).
Time-of-flight contours, oil-withdrawal contours and streamlines corresponding to fluid withdrawal paths are visualized.
c Further expansion of the TOFCs for oil-withdrawal is halted by the water injection.
Oil-withdrawal contours spacing t* = 1 and total run time t* = 10.
This section presents oil-withdrawal patterns for field development with arbitrary well patterns.
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