Even though the novel catalyst packing has a three times lower catalyst density compared to the currently used packings containing catalyst pockets, it is anticipated that this difference can be compensated for by the potential activity increase of the zeolitic coating, and the higher efficiency and selectivity of the coating.
A comparison is made with two commonly used packings, catalyst bales and open cross-flow structures.
Reactive distillation using catalytic packings was studied previously in detail (Parada, 2008; Schmitt et al., 2004, 2005) with the same test system.
In the beginning, major attempts were first made to develop highly efficient systems leading to a dramatic improvement in column technology using microparticulate packings and to an optimised design of column hardware resulting in extremely low extra-column peak dispersion through the column.
The subsection-controlling strategy was applied to the design of the adsorptive reactor to improve the sorption-enhanced steam methane reforming (SMR), by using subsection-packing ratio of adsorbent and catalyst, and subsection-controlling wall temperature.
On-line digestion experiments with micro-HPLC separations were conducted using LC-Packings instruments and columns (Amsterdam, The Netherlands).
Using Mellapak structured packings within the reactor, it was possible to increase in 35% the oxygen transfer to liquid phase.
In recent years, the pilot plant has been utilized to determine the mass transfer and hydraulic characteristics of various structured and random packings using amine-based solvents for CO2 absorption.
Comparison of the experimental results of towers using these three packings with the conventional spray tower show improvement in the performance of spray tower (∼30%) without mounting air side pressure drop burden.
Peptides were separated on a 15 cm C18 PepMap™ column (LC Packings) using a Bruker Easy-nLC platform with a flow rate of 300 nl/min.
