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Table 1 lists the manufactured MEAs using a commercial catalyst and a synthesized Pt/CNF.
Hydrotreating of light gasoil (LGO) in two stages using a commercial catalyst of Co Mo supported in alumina was made.
The catalytic oxidation of phenol in aqueous-phase has been investigated using a commercial catalyst CuO 2(CuO)·Cr2O3 CrO4Ba Al2O3 at 400 K and an oxygen pressure of 8 atm, changing the pH and catalyst concentration.
One of the objectives of the present work is to expose the use of a trickle bed reactor model to predict the quality of products during the hydrotreatment of vacuum gas oil using a commercial catalyst and based on data obtained at pilot-plant scale, where catalytic experiments were carried out under typical industrial considerations, at different temperatures, pressures, and space-velocity (LSHV).
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These reactions were studied in a microreactor testing unit using a commercial Cu ZnO/Al2O3 catalyst for the first three reactions and Pt Fe/γ-alumina catalyst for the last reaction.
The use of the high-performance Cu/ZnO/Al2O3 catalyst allows for higher hydrogen production rates than possible using a commercial Cu/ZnO catalyst.
The process has been studied experimentally in a bench-scale device using a commercial monolithic catalyst.
A new fuel processor is developed using a commercial shift catalyst.
The kinetics of the Fisher Tropsch synthesis is studied in a laboratory CSTR slurry reactor using a commercial Cobalt catalyst.
In this work, an integrated experimental and CFD modelling technique was used to evaluate a microchannel reactor producing hydrogen from ammonia decomposition using a commercial Ru/Al2O3 catalyst.
We have compared steam reforming (SR), autothermal reforming (ATR), and ATR membrane reactor based fuel processors using a commercial CuO/ZnO/Al2O3 catalyst.
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