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The results reveal a strong correlation between the reactant composition and the catalytic activity, showing an optimum reaction rate for compositions close to the stoichiometric value for complete oxidation of propane.
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At temperatures below an optimum reaction temperature, the overall reaction rate is probably limited by the leaching rate of Ca. At higher temperatures, nucleation and growth of calcium carbonate are probably limiting the conversion, due to a reduced (bi carbonate activity.
Since the ammonia synthesis process is highly exothermic, higher per-pass conversions in industrial adiabatic reactors are often achieved by using various sequential catalyst beds, where a near-optimum profile of reaction rate vs temperature can be attained by regulating the inlet temperature of each bed.
The sulfur content of DBT in model oil can be decreased from 200 ppm to 3 ppm (S-removal rate up to 98.4%) under optimum reaction conditions (air flow rate, 90 ml/min; amplitude of applied voltage (U) on DBD, 30 kV; input frequency (f), 600 Hz; catalyst amount, 3 wt%; the reaction time (t), 30 min).
However, it was observed that above a certain optimum catalyst mass, the reaction rate even decreases and becomes independent of the catalyst concentration [29].
However, for every gas composition arising during the reaction process an optimum temperature exists at which the reaction rate is highest.
The reaction rate constant of the optimum active C0.50%/CN heterojunction for the photodegradation of RhB and TC-HCl were about 3.7-fold and 1.9-fold higher than that of bare g-C3N4, respectively.
The optimum pH for the system proved to be 8.0, whereas optimum temperature range was 50 65 °C, with the maximum reaction rate at 60 °C.
At the same time, the concentration of acid solution in the pickling step needs to be maintained at the optimum value in order to obtain the maximum reaction rate.
The results predicted by the developed correlation at the optimum determined conditions, 28.63 mol/l h for the reaction rate and 1.97 mol% CH4, were reasonably compared with the experimental data obtained for the reaction rate and methane formation of 27.10 mol/l h and 3.06 mol% CH4, respectively.
The influence of several reaction parameters, such as kind of carriers, reaction temperature, gas flow rate, was investigated to search for optimum reaction conditions.
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