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The total active surface area increases with increasing catalyst dosage.
Meanwhile, all single aromatic hydrocarbons went up gradually with the increasing catalyst with γ-alumina.
As expected, the activity decreased with increasing catalyst particle size.
The reaction rate and C5 + selectivity increased with increasing catalyst pore diameters.
A main focus of bio-oil upgrading research is increasing catalyst lifetimes to 1 year.
The amount and formation of QS2O8 (quaternary ammoniumperoxydisulphate complex) are increased with increasing catalyst (dual active-site) concentration.
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Notably, for catalyst 26, the activity as well as molecular weight of the polymer increased with increasing catalyst-to-MAO ratio [33].
It also increased catalyst deactivation.
Increasing hydrogen pressure from 0.03 to 0.10 MPa (Table 1, entry 2 4) did not increase catalyst activity obviously.
In this method, a minute level (~ 150 ppm) of water is inserted into the growth ambient to increase catalyst activity.
The same is observed when catalyst slip increases (catalyst residence time in reactor increases).
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