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tem boundaries for the various technological options had to be specified precisely. The project objectives to be achieved were: Overall process • Optimise the design and dimensioning of the components used in the overall process • Derive the dynamic load profiles that the electrolysis process will be subjected to • Compile LCAs and energy balance analyses • Compile a technical requirements document for the pilot plant Starting materials for the CO2 conversion process • Monitor the quality of the fossil-based CO2 to be used in the planned chemical conversion • Use the PEM electrolysis unit as a dynamic load-following unit to gener- ate renewable hydrogen • Scale-up of electrolysis process to a power rating of 100 kW • Test concept for incorporating waste heat from the electrolysis unit into the integrated chemical production facility to improve overall efficiency • Development of storage concepts CO2 conversion • Develop catalytic systems for the CO2 reforming and the RWGS reactions that will remain active over sustained periods • Innovative hybrid-heated reactor • Develop catalyst for the hydrogenation of CO2 to formic acid Interfacing with existing value chains • Quality assurance of CO and preparation of gas for conversion of CO to polymers Technology demonstration at lab and pilot plant scales • Construct an autonomous high-pressure electrolysis system (e.g. 50 bar) with a power rating of 100 kW; test under the simulated dynamic load requirements • Connect electrolysis unit and CO2 conversion unit (reforming and RWGS reactions) using a modular lab-scale set-up; include add-on hy- drogen storage system to determine the effect of fluctuating power gen- eration from renewable energy sources on the overall system. The overall concept represents an outstanding example of how a chemical process (CO2 conversion) and an electricity generating process (CO2 capture CO2RRECT FUNDED PROJECTS 145PDF Image | Chemical Processes and Use of CO2
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