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CO hydrogenation experiments were carried out in a high pressure continuous fixed bed reactor.
Catalytic dehydrogenation of cyclohexanol was carried out in the gas phase in a continuous fixed bed reactor under atmospheric pressure.
A continuous fixed bed study was carried out by using rice husk as a biosorbent for the removal of congo red (CR) from aqueous solution.
A continuous fixed bed study was carried out by using Mowital®B30H resin immobilized dried activated sludge as a biosorbent for the removal of phenol from aqueous solution.
The aqueous phase reforming (APR) of xylitol was studied in a continuous fixed bed reactor over three catalysts: Pt/Al2O3, Pt/TiO2 and Pt-Re/TiO2.
All the catalysts showed a significant catalytic activity for the F T reaction from synthesis gas (CO + 2H2), in a continuous fixed bed reactor system.
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This paper presents a novel continuous fixed-time convergent control law for dynamic systems in the presence of unbounded disturbances.
A continuous fixed-time convergent control is designed to drive all states of a multi-dimensional integrator chain at the origin for a finite pre-established (fixed) time, using a scalar input.
The effects of different operating parameters such as bed height, initial phosphate concentration, and flow rate were investigated in a continuous fixed-bed column, and the experimental data were fitted to three different breakthrough models, the Adams-Bohart, Thomas, and Yoon-Nelson models.
A continuous fixed-bed column study on WMIP was carried out at bed depths of 0.9 4.9 cm, flow rates of 1 3 mL min−1 with initial SA concentrations of 10 60 mg L−1 at temperatures of 298 318 K.
Let be a sequence of distinct points on the unit circle, and let We now define a continuous fixed-point free map for which.
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