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With the shear rate increasing, the reaction rate rises.
Increasing the reaction temperature to 75 °C increased the production rate to 21.0 μmol/g h.
Increasing the reaction temperatures resulted in a decrease of the final density of samples.
Additionally, it is found that with increasing the reaction stage number, the residence time and the reaction conversion increase.
Increasing the reaction temperature from 850 °C to 1050 °C resulted in similar surface morphologies, but increased grain size.
Moreover the deactivation could be reduced by increasing the reaction temperature.
Enhanced activities were observed on increasing the reaction temperature to 100 °C.
However, the conversions of C3H8 and NO showed oscillation with continuously increasing the reaction temperature.
CO2 conversion and CO selectivity increased on increasing the reaction temperature.
Further increasing the reaction temperature to above 400 °C reduced gasoline yield.
With an exact stoichiometric balance, increasing the reaction time can be used to obtain polymers of longer chain lengths as there is no termination of the polymer reactive end.
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