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3 ENERGY-EFFICIENT PROCESSES HY-SILP 3.11.4 Exploitation, commercialisation and dissemination of results The HY-SILP project produced a deeper and lasting understanding of sup- ported ionic liquid phase (SILP) catalyst systems and identified the weak- nesses of this type of technology. The unexpectedly strong formation of high-boiling components through aldol condensation of the aldehyde products makes direct commercial application of the HY-SILP process un- economical. However, it was also found that the selective separation of the aldehyde product from the catalyst centre represented a very promising optimisation of this new technology. This approach has been studied since September 2015 within the EU-funded project ROMEO – Reactor Optimi- sation by Membrane Enhanced Operation, which is part of the Contractual Public-Private Partnership (cPPP) ‘Sustainable Process Industries and Re- source Efficiency’ (SPIRE). In addition to Evonik Industries AG, Linde AG, Friedrich-Alexander University Erlangen-Nuremberg (FAU) and RWTH Aachen University, the consortium also includes other experts in the fields of catalysis, membrane processes and reactor technology in Germany, Aus- tria, Denmark, Spain and Belgium. The results of the HY-SILP project are therefore being directly used as the foundation for the ongoing ROMEO project, in which the focus is not just on the large-scale hydroformylation process, but also on the industrially signi- ficant water-gas shift reaction. The goal is to develop an innovative reactor concept for homogeneously catalysed gas-phase reactions that combines both the reactive and material separation stages (see Figure 6). By combining two unit operations in this way, energy savings of up to 78% and emission reductions of 90% can be achieved in the case of hydroformylation. Fig. 105: The aim of the EU project ROMEO is to develop an innovative reactor model for homogeneously catalysed gas-phase reactions Separation Unit ROMEO Reactor CSTR homogeneous catalysis 260PDF Image | Chemical Processes and Use of CO2
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