Deliverables - Public
D6.3 - Systematic literature review of empirical analyses on the social acceptability of CaL-based CCUS technologies
D6.3 provides a systematic review of the literature on the level of knowledge/awareness of CCUS technologies, their social acceptability and the drivers and barriers of such social acceptability
D4.3 - Base-cases definitions and KPI calculation for cement, steel, Bio-CHP and WtE plants with and without capture
The first part of deliverable D4.3 provides a description of the reference facilities considered in the CaLby2030 project, the methodology and the definition of the various key performance indicators (KPIs) considered for energy, technical and economic comparisons. The integration of the various reference plants with a MEA solvent-based CO2 capture system is then described and analyzed. These plants are considered as benchmarks for comparing the performance of Calcium Looping (CaL) systems, which are analyzed in detail from an energy, technical and economic point of view for the different sectors in the last part of the deliverable.
D7.2 - Dissemination and communication package –From M1 to M30
D7.2 details the dissemination and communication activities carried out throughout the first reporting period of the CaLby2030 project, as described in Tasks 7.3 and 7.4. This deliverable will be updated in months 30 and 42
D4.6 - Methodology for multi-criteria optimisation of CO2 transport for various modes of CO2 transport
D4.6 describes the methodology developed for the multi-criteria optimisation of multi-modal CO2 transport, incorporating economical, environmental and safety impact.
D4.4 - Improvements of the CFB-CaL system integrated with CPU: sensitivity analysis of main CaL parameters
Deliverable D4.4 focuses on analysing different configurations of the CFB-CaL system integrated with CPU. Process modelling activities were conducted, exploring several process improvement options and varying key operating parameters, with the aim of increasing CO2 capture rates, enhancing energy efficiency, and reducing cost of CO2 avoided. Heat and mass balances, as well as economic KPIs, were calculated and compared to assess the performance of the various configurations
D6.1 - Initial LCA report for the BIO-CHP case study for socio-economic assessment
The first section of D6.1 provides a summary of climate change and global warming, including its causes, effects, main industrial contributors and potential mitigation strategies. The second part describes the LCA methodology considered when performing the environmental evaluation, while offering the main material and energy balance data. The third chapter focuses on the environmental performance of the MEA- and CaLby2030 CO2 capture technologies integrated within a Bio-CHP plant, emphasizing the main LCA results. The overall conclusions are provided in the final section.
D6.5 - Interim report semi-structured interviews
Deliverable 25 (D6.5) reports the results obtained during individual interviews to identify the necessary conditions that need to be in place for stakeholders to lend their support to the implementation of CaL-based CCUS, as mentioned in Task 6.3
D3.2 - Results of the experimental campaigns in the 1.7 MWth pilot plant, I
This deliverable presents the experimental results obtained to date in experimental campaigns carried out in la Pereda CFB-CaL pilot, under Task 3.2 of the CaLby2030 project. Progress in all sub-tasks has been achieved thanks to these results, including some key objectives of WP3. About 720 hours of additional operations on the pilot have been executed, accumulating more than 1320 hours since the beginning of CaLby2030. Successful initial tests achieved calcination efficiencies of between 96-98% when operating the calciner under oxy-combustion conditions burning biomass pellets. After solving issues linked to the solid circulation between reactors, tests with CO2 capture in the carbonator demonstrated the stability and controllability of the pilot when using biomass as a fuel in the calciner, reaching in some dedicated tests CO2 capture efficiencies over 99%. Interpretation of the results is consistent with basic models of the reactors and will supply information for the tuning of more advanced, dynamic and scalable models under development in WP4, supporting also design decisions for WP1-WP2. Preliminary tests on the la Pereda pilot, feeding plastics containing F and Cl as a proxy of WtE plants, indicate an extreme efficiency of the CFB-CaL system to capture in the solid phase Cl and F acid gases. These results are to be confirmed in future tests involving more realistic conditions (i.e. Ca(OH)2 powder injection to the carbonator, gas recycle in the calciner, full operation with flue gases in the carbonator) and in independent analysis of solid samples (Task 3.3 ongoing), to be reported in D3.3
TOP NEWS
17 March 2026 Lulea, Sweden