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The model treats multiple concurrent physical processes, i.e., rigid-body translation and rotation of powder particles, grain growth through boundary migration, and various diffusion mechanisms including surface diffusion, grain boundary diffusion, volume diffusion, and vapor transport through evaporation and condensation.
This is the reason why the cumulative diffusion volume of gas in dead oil is larger than that of gas in saturated oil and foamy oil.
For gas diffusion in foamy oil, the cumulative diffusion volume at 20 MPa was 4.8 times of that at 8.65 MPa when the diffusion time was 35.22 h.
On the one hand, high levels of PEEP could reduce the cold indicator diffusion volume by squeezing pulmonary microvessels, leading to an underestimation of EVLWI [62].
On the other hand, high levels of PEEP could increase the cold indicator diffusion volume by recruiting some atelectatic lung regions and reducing hypoxic vasoconstriction, leading to an overestimation of EVLWI [58].
Through controlling the inner-contact density of the conductive porous structure (as shown in Fig. 8), the diffusion volume and rate of air inflow can be adjusted to achieve the purpose of adjustable sensitivity.
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It is shown that for cathodes in MCFCs the agglomerates may be viewed as equivalent diffusion volumes instead of real geometric representations.
Subsequently, the cumulative diffusion volumes kept increasing, but increased slowly compared with the initial stage.
The cumulative diffusion volumes and gas contents of the three types of oil increased with an increase in pressure.
The cumulative diffusion volumes of natural gas in these three types of oils rose sharply at the initial stage.
The cumulative diffusion volumes of gas in dead oil were larger than that in saturated oil and foamy oil at the same pressure and time.
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