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We also show that the long time solution to sub-diffusive and sub-advective fluid flow through porous media is largely independent of the initial fluid profile.
As a result, that segment will see an increase in flow rate and in water/gas cut compared to other segments of the lateral, potentially creating a new non-conforming fluid profile later in well life.
Our data, reflecting real-life use and thus a broad range of fluid strategies for different clinical reasons, do not disprove the existence of this phenomenon, as we lacked a detailed fluid profile in our dataset.
Based on recent advances in dynamic optimization, the objective is then to find the optimal process design (e.g. cooling systems design) and operating strategy (e.g. cooling fluid profile over time, hydrogen charging profile, etc).
The objective is to find the optimal process design (e.g. cooling systems design) and online operating strategy (e.g. cooling fluid profile over time) so as to minimize the storing time, while satisfying, a number of operating constraints.
The comparison of axial velocity profiles for different models here with theoretical and experimental values of axial velocity profile for Herschel Bulkley fluid model [39] reflects on the possibility for the latter to coincide with thixotropic fluid profile for (0.6leq lambda leq 0.8).
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The results of numerical calculation in terms of three phase fluid profiles, separation performance and secondary particles behavior were analyzed.
In the present study, the results of numerical calculations in terms of fluid profiles, separation performance and DPM particle behavior are used to choose the optimum vessel configuration.
To choose the optimum vessel configuration, the results of numerical calculations in terms of separation performance, secondary-phase particle behavior and fluid profiles are presented in this section.
The results of numerical calculations in terms of fluid profiles, separation performance and DPM particle behavior were used to choose the optimum vessel configuration.
Then, the results of numerical calculations in terms of fluid profiles, separation performance and DPM particle behavior were used to choose the optimum vessel configuration.
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