As an important secondary resource with abundant platinum group metals (PGMs), spent
catalysts demand recycling for both economic and environmental benefits. This article …

The term “three phase catalytic reactors” generally refers to gas-liquid-solid reaction
systems, in which the solid is typically a heterogeneous catalyst [1]. A fundamental division …

Here, different loading of palladium (Pd), ranged from 0.5 to 5 wt%, was incorporated into
the three dimensional siliceous mesoporous material; TUD-1. The synthesis procedure was …

Performance of trickle‐bed and up‐flow reactors was studied experimentally and
theoretically for an exothermic multistep hydrogenation of 1, 5, 9‐cyclododecatriene (CDT) …

Many of the chemical reactors employed in various sectors of the process and chemical
industries, such as petroleum refining, downstream processing and petrochemicals, bulk …

Palladium (Pd) was incorporated into TUD-1 mesoporous siliceous material by using one-
pot synthesis procedure. The catalytic activity of the prepared samples was evaluated in the …

The kinetics of hydrogenation of 2, 4-dinitrotoluene (2, 4-DNT) using a 10% Ni supported on
zeolite Y (10% Ni/HY) powdered catalyst (dp= 1× 10-5 m) was studied experimentally in a …

High initial conversions for the cyclododecatriene (CDT) hydrogenation in a slurry reactor at
433 K and 1.2 MPa were obtained from a supercritical (sc) CO2-cleaned 0.5% Pd/Al2O3 …

The performance of trickle-and flooded-bed reactors has been investigated and compared
for an exothermic multi-step catalytic reaction. Selective hydrogenation of cyclododecatriene …

Chemists are frequently interested in rate equations, which are first-order differential
equations. Numerical integration of these equations allows the researcher to accurately …