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The effect of distributor design and column height were investigated.
This parameter mainly depends on the liquid distributor design.
The effects of bed diameter, distributor design, baffles and mean bed particle size, respectively, are considered.
The model predicts that conversion is unlikely to be changed by alterations to the distributor design.
An improved distributor design, with a complementary fluid cavity was built and tested in this work.
Near the inlet, the particle distribution is dominated by the distributor design.
Similar(26)
Radial and fractal flow distributor designs were also tested.
with three distributor designs was used to test the gas solids flow conditions in the entrance region.
The two different distributor designs had no measurable effect on the streaming flow.
Moreover, Geldart group B bed materials with different bed aspect ratios and distributor designs viz., perforated plate, circular edged slots (90°) and novel swirling (45°) distributors are used.
Methanol conversion, product selectivities, and temperatures were measured at discrete axial positions as a function of H2O C ratios, feed temperatures, pressures, and two different air distributor designs.
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