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The parent and treated activated carbons were then checked for CWAO using a trickle bed at 140 °C and 2 bar of oxygen partial pressure.
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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).
The developed method can be used when modelling a trickle bed reactor operated with catalyst diluted by its support.
Hydrodesulphurization (HDS) kinetics of a straight run heavy gas oil has been studied using data collected from a trickle bed microreactor loaded with a diluted bed of a commercial catalyst.
Recent experiments using pulsed liquid flow in a trickle bed reactor have demonstrated increased average reaction rates and higher acid concentrations than can be achieved in steady-state processes.
The distribution of reactants and inert liquid between the vapor and liquid phase in a trickle bed reactor used for hydrotreating is affected by H2/feed ratio, relative volatilities and temperature.
Experimental results of the air water pulsating flows in a trickle bed column were obtained using the electrical capacitance volume tomography (ECVT) system.
A trickle bed reactor (TBR) is used in this work for hydrotreating (HDT) crude oil.
Gamma-ray tomography and a liquid collecting device have been used to detect liquid spreading from a single point source in a trickle bed.
A trickle bed reactor (TBR) with recycle was designed and tested using Aspergillus nidulans with a pyridoxine marker and over-expressing/secreting recombinant client xylanase B (XynB).
This phenomenon was more pronounced when the strain was cultured in a trickle bed reactor (TBR).
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