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The ERT was used to measure the mixing time with and without solid particles (glass beads, 250 μm) in a stirred reactor.
It was found that for the range of superficial velocities examined (0.07 0.29 m/s) there was little change in mixing time with superficial velocity.
In contrast, it was found that the tracer injection point and measurement location had a large impact on the measured mixing time, with measured values ranging between 3 s and 25 s.
This paper investigates experimentally the effect of five parameters (demulsifying agent concentration, temperature, wash water dilution ratio, settling time and mixing time with wash water) on performance of the desalting/dehydration process.
For the SRE, the optimum values of demulsifying agent concentration, temperature, wash water dilution ratio, settling time and mixing time with wash water were fond to be 15 ppm, 77 °C, 10%, 3 min and 9 min respectively.
The variation of the continuous phase mixing time with impeller speed can be an effective method to determine the critical impeller speed for complete dispersion of oil phase.
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Particle Image Velocimetry (PIV) and Planar Laser Induced Fluorescence (PLIF) have been used to determine local velocity fields, shear rates, flow numbers and mixing times, with impeller power number Po obtained from torque measurements.
Mixing time increased with the increase in the sodium chloride level but peak height decreased with the increase in lactic acid level.
Thermal mixing time decreases with higher rotational speed and lower filling degree.
For perturbations with length scales larger than the reaction width, the conditionally filtered diffusion has the same form as non-reactive scalar mixing, with the mixing time scale determined by the flamelet.
Quantitative comparisons of the mixing time are conducted with mean value method, slope method and standard deviation method.
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