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Column diameter (m).
No significant effect of column diameter was observed.
For the absorber, estimated column diameter was 13.78 m.
Results show that the gas phase density has the most significant effect on the column diameter.
In addition, the effects of column diameter and packed height on liquid distribution were studied.
The efficiency loss due to the distributor when increasing column diameter during scale-up is quantified.
Column diameter did not affect separation, implying linear scalability with constant flow distribution.
When D⩽15.2cm, gas holdup decreases with increasing column diameter for the transitional and heterogeneous flow regime, and column diameter effects are negligible in the homogeneous flow regime.
According to the strategy, the column spacing, draft, and column diameter should be increased in sequence.
This correlation can be used to estimate pressure drop for a given loading and column diameter.
Variables considered are yield stress of steel tube and column diameter.
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