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A typical CO2 pipeline is designed to operate at high pressure in the dense phase.
For a given superficial gas velocity, the average local particle concentration, the dense phase fraction and the particle concentration in the dense phase decrease with increasing bed temperature.
Mass transfer from a freely moving single sphere to the dense phase of a gas fluidized bed of inert particles.
The expansion of the dense phase during bubbling is compared with maximum bed expansion before bubbling.
Each of them and the dense phase are considered with lumped parameters.
At moderate gas velocity, they incline to mix well in the dense phase.
In this case, the dense phase porosity and the interstitial gas velocity decrease with height.
The catalytic reaction occurs in the three grid zones and the dense phase.
The bubbles cause the solid movement between the three grid zones and the dense phase.
Particle particle and back pressure interactions dominated in the dense phase at high solids circulation rates.
There is heat transfer from the grid zones and the dense phase to the surroundings, especially through the cooling tubes.
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CEO of Professional Science Editing for Scientists @ prosciediting.com