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Chemical Processes and Use of CO2

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Chemical Processes and Use of CO2 ( chemical-processes-and-use-co2 )

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FFPAG FUNDED PROJECTS properties under technically relevant conditions – information that will be critical in designing and constructing a pilot plant. In terms of its physical dimensions and the proposed quantities of carbon that it will produce, the trial batch production facility is the largest know non-plasma methane py- rolysis plant. The quantities of the carbon product samples that can be pro- duced are large enough for reliable tests to be carried out in the metallurgi- cal industry. To facilitate integration into the overall pyrolysis process, the work on de- veloping a catalyst for the CO2 activation stage and on the associated reactor design issues focused on achieving a catalyst formulation that exhibits good overall performance, both in terms of chemical conversion and selectivity, and that is stable over the long-term. The test facilities for developing the catalytic CO2 activation stage are shown in Figure 31. By the end of 2016, the catalyst development and reactor design work should be at a stage that will allow a pilot plant to be built once a final risk assessment has been con- ducted. The pilot plant will enable the usual questions regarding scale-up to industrial production levels to be addressed. The main result of the FfPaG project was the overall process design con- cept that covers the pyrolysis stage and the workup of the gaseous pyrolysis products. Potential sites will be selected on the basis of both economic and environmental factors. All of the key specifications and requirements for di- mensioning and building the pilot plant will be set out in a comprehensive design basis. In addition to the core component, the pyrolysis reactor, the design basis will include all the process steps needed in order to physically implement the material flow paths within the overall process. The suitability of candidate sites was also assessed in terms of their industrial integration potential by taking into account their proximity to existing production fa- cilities in the chemical, petrochemical and steel industries. Fig. 32: Test facilities for developing catalysts for use in the reverse water-gas shift reaction for CO2 activation; (2014 and 2015) 85

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