Title : Relevance of synergetic approaches in intensifying catalytic reactors
Abstract:
Intensifying chemical reactors by development of an efficient synergy between the reactor and catalyst is leading to non-negligible saving in capital and operating costs of chemical plants while meeting requirements over conversion, selectivity and energy consumption. Recent achievements in developments in the topic of multifunctional catalytic reactors by combination of the chemical reaction with momentum, heat and mass transports in a single chemical unit are presented through a number of examples, including among others, hybrid catalytic reaction and separation, local catalyst deactivation in real flow system and multiphase flow in engineered packing type of internals. In the first example, the etherification of tert-amyl alcohol with ethanol was carried out in a catalytic reactive distillation column inserted by a pervaporative zeolite NaA membrane tube. The design has shown alleviation of azeotropes of H2O-reaction components mixtures and a gain of 10% in tert-amyl ethyl ether yield. In the second example, local deactivation of the preferential oxidation of CO was investigated in real flow reactor by three-dimensional modelling of flow and experimental tomography where the profiles of deactivation were found sensitive to the rates of deactivation, heat transfer by dispersion and intra-particle mass transfer at both reactor and packing pore scales. For instance, elevated deactivation was seen close to the wall due to a preferential flow circulation and progressed at the exteriors of the catalytic particles, particularly over the regions in contact with the convective flow. This presentation brings attention to relevance of accessing to real-time data of concentration, temperature and flow velocity, as well as relevance of the space scales by in-situ sensing. It also emphasizes the multidisciplinary approach when dealing with the simultaneous design of catalyst and catalytic reactor.
Keywords: catalytic process intensification, multifunctional reactor, multiscale design, in-situ sensing, engineered catalytic packing
Audience take-away:
- Process intensification is innovative strategy to deisgn reactive processes while looking at multiple aspects associated with reducing heat conception, by-products, unit size and catalyst load while promoting sustainable practices. The audience will appreciate relevance of innovative techniques to access to data while reactors are in operation along with prediction by modelling and design of conditions, which are not affordable to reproduce experimentally.
- Since the theme of the conference is about CCET, the audience will appreciate in the daily laboratory operations the fact that designing a catalyst and reactor is regarded as multidisciplinary subject where sub-subjects should be investigated simultaneously. A number of worked examples will be presented which could be taken further depending on their research interests. These examples are not final solutions but would contribute to solutions that can simply design of multifunctional catalytic reactors. The design by process intensification is intended to promote conversion, selectivity under less raw material and energy uses