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The temperature contours are presented in Fig. 20 for increasing sweep flow rates.
Open image in new window Fig. 14 Oxygen permeation with increasing sweep flow rates.
Figure 23 shows the volume average devolatilization of methanol with increasing sweep flow rate.
Open image in new window Fig. 23 Volume average devolatilization with increasing sweep flow rates.
Open image in new window Fig. 15 Maximum temperatures with increasing sweep flow rates Open image in new window Fig. 16 Maximum reaction rates with increasing sweep flow rates.
Open image in new window Fig. 20 Temperature contours with increasing sweep flow rates Open image in new window Fig. 21 CH3OH mass fraction contours with increasing sweep flow rates Open image in new window Fig. 22 Mass weighted average temperature with increasing sweep flow rates.
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Polymer flooding increases sweep efficiency due to higher water viscosity but may have lower injectivity.
Water-alternating-gas (WAG) floods are designed to lessen the mobility of CO2 and thereby increase sweep efficiency.
Previous research has testified that nitrogen foam can increase sweep area and control water and gas mobility.
These methods are utilized in order to reduce the interfacial tension, to increase brine viscosity for mobility control, and to increase sweep efficiency in tertiary recovery.
Polymers are used in enhanced oil recovery (EOR) to increase sweep efficiency, but recent experimental and field data suggest that viscoelastic polymers such as hydrolyzed polyacrylamide (HPAM) reduce residual oil saturation as well.
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