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Minimum particle diameter (m).
The minimum particle diameter to be completely collected is 1 μm at solid loading 20 g/m3.
Results showed that, in both cases, at least 50% of the energy density should be delivered by HPH to obtain the minimum particle diameter.
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The reactor temperature where the minimum primary particle diameter was produced was different for the two precursors due to differences in chemical reaction rates.
At least 20 particles of each material were analyzed during this procedure to determine the maximum, minimum, and mean particle diameter in micrometers (μm).
The results show that the minimum fluidization velocity depends on particle diameter, solids loading and the properties of the liquid phase.
To adequately represent the electrode microstructure, the characterized volume of the electrode should be equivalent to a cube having a minimum length of 7.5 times the particle diameter.
In the previous section, it has been found that the optimal concentration for the Al2O3 + water nanofluid at 324 K wall temperature is 0.04, and for maximum heat transfer rate, the particle diameter should be minimum.
Based on the set of measurements obtained here we postulate that the jet height is independent of the bed dimensions at flow rates of Q<0.7Qmf and bed dimensions of L/dp>55, where Q is the volumetric flow rate of the gas, Qmf is the volumetric flow rate of the gas at minimum fluidization and dp is the particle diameter.
The results show that the minimum spouting velocity increases with cone angle, particle diameter and static bed height.
Consequently, we can neglect the interparticle coupling because the expected minimum gap between the particles is still about 3.2 times the particle diameter when the system reaches its maximum particle size of 56.6 nm.
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