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The assumptions about the entrapped air behaviour are defined from a bibliographic study, and linear elastic behaviour is used for both the liquid phase and the solid skeleton.
Specifically, the new development exploits the fact that NMR spectroscopy is able to study both the liquid phase and the solid phase in a heterogeneous solid/liquid system using the same instrument, simply by changing the pulse sequence used to record the data.
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With ozone, oxidation of oxalic acid may occur both in the liquid phase (homogeneous reaction) and on the catalyst surface, while wet air oxidation appears to proceed mainly on the carbon surface.
There are known methods of preparation of 2,6-dimethylphenol, both in the liquid phase [1]-[3] and in the gaseous phase [4]-[16].
Therefore, the (Kc a) value is dependent on both the liquid-phase velocity (external resistance) and the soil fraction in the column (internal resistance); making forced convection and diffusion to be the main transport mechanisms involved in the adsorption process.
Rigorous reactor and pellet-scale simulations carried out for both the liquid-phase and gas-phase reaction, as well as for intra-reactor wet dry transition (hysteresis and rate multiplicity), are presented and discussed.
A three-stage process was identified in the temperature profiles obtained from drop tests using Al2O3 coated fine-wire thermocouples placed in both the liquid-phase and gas-phase regions.
A mechanism for the catalytic reduction of 4-NP with NaBH4 by Ag/rGO nanocomposite via both the liquid-phase and solid-phase routes has been suggested.
Accordingly, a scheme for the catalytic reduction of 4-NP with NaBH4 by Ag/rGO nanocomposite via both the liquid-phase and solid-phase routes could be described by Figure 8. Figure 8 Catalytic reduction of 4-NP with NaBH 4 by Ag/rGO nanocomposite via both the liquid-phase and solid-phase routes.
In addition, a mechanism for the catalytic reduction of 4-NP with NaBH4 by Ag/rGO nanocomposite via both the liquid-phase and solid-phase routes was suggested to describe the synergistic effect of rGO.
The 3D unsteady diffusion-reaction equation both in the liquid phase and the solid catalyst particles is solved.
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