Confidential CLEANKER deliverables

D2.1 Engineering and detailed design of the demons…

This document describes the layout and basic engineering of the Calcium Looping (CaL) demonstration plant to be built in Vernasca performed on base of the heat and mass balances calculated with a process model as given in the deliverable D2.3. The

D2.2 Project execution plan including detailed equ…

This document describes the design and detailed engineering of the demonstrator system. The output is the detailed equipment list of items to be purchased together with the technical specifications and drawings for items to be fabricated, including

D2.3: Heat and mass balances of the demonstration …

In this deliverable, pilot plant configuration and heat and mass balances of the CaL pilot plant to be built in the Vernasca plant are presented. Nine different cases have been calculated to support the design of the demonstration plant.

D2.4: Definition of measuring points and instrumen…

In this deliverable, the most suitable gas measurement and solid sampling points and port configurations will be defined. Technical drawings and instrumentation specifications will be given with short explanation/notes of the reasons of the main c

D4.2 Experimental test matrix for characterization…

In this report, an updated experimental text matrix for tests in the 120 kW USTUTT mini-pilot based on outcomes of the first experimental campaign and experimental test matrix for tests in the drop tube reactors at CSIC and TSIU is defined.

D4.3 Characterization of BUZZI demo-plant raw meal…

In this deliverable first results of the characterization of the raw meal used in the demonstration trials at BUZZI cement plant in Vernasca under relevant entrained flow conditions are presented: The focus of this report is on the achieved calcinati

D4.4: Comparative characterization of cement raw m…

This report will summarize the findings of the comparative characterization test with various raw meal qualities obtained in the 120 kW test rig at USTUTT. This will also include a comparison to the demonstration tests in WP3.

D4.6 Experimental determination of intrinsic calci…

This Deliverable includes the experimental results obtained in a drop tube furnace (L=6.5 m, ID=0.08 m) and in a thermogravimetric set-up available at INCAR-CSIC to determine the intrinsic calcination and carbonation kinetics for various raw meals

D5.2 Screening of kinetic parameters and performan…

The work of 5.1.1 will be extended to several other promising raw meals to be used for the tests at the demonstration plant Mechanistic description of bellite formation, depending on aggregation levels of Ca and Si in the raw meals,will be included

D5.3 First stage demo system simulations using the…

In this deliverable, new models for the global pilot plant and for the coupled calciner and carbonator reactors are presented and validated against previous simulations. CFD simulations of the splash boxes for calciner and carbonator indicate that

D5.4 Report on 1D and 3D model frames

The report describes the final 1D and 3D model frames for interconnected calciner and carbonator reactors. This includes decription of submodels and underlying model theories as well as sensitivity analyses of the reactor system operation.

D5.7: Modelling of full scale units

The fully developed and validated model frame is applied to simulate the full scale units. The deliverable reports the model results in selected process configurations and process conditions.

D5.8 Performance of CaL processes in full scale ce…

The purpose of this deliverable is to evaluate the energy – environmental performances of a full-scale cement plant integrated with the CaL Entrained Flow Reactors (EFR) system. The integrated CaL configuration is analyzed in details through a sens

D7.4 Lab-scale experiments on waste oil shale ash …

Lab tests were performed in order to: (a) specify the recommendations for a pilot design and (b) identify the most promising materials for CO2 capture. The respective mathematical models were implemented, developed and used for clarification and gene

D7.6: Final report with results of the mineralizat…

The Task aimed at demonstrating the feasibility of CO2 capture in Estonian burnt oil shale through the mineralization system developed in the framework of WP7 based on recommendation supplied in the Deliverable 7.5.

D7.7: Results from casting concrete containing CaL…

In this task the burnt oil shale (BOS) ashes carbonated via the pilot mineralization system installed in Vernasca and operated using the CO2 enriched gas stream coming from the oxyfuel calciner have been used in concrete, demonstrating the possible u

D9.2 First year technical report for ECRA

This deliverable is the first annual report to ECRA. The first part is dedicated to the project description in terms of goals, scope of works, consortium etc. The second part is dedicated to the work carried out during the first year.

D9.3 Second year technical report for ECRA

This deliverable is the second annual report to ECRA. It focuses on the activities carried out during the second year of CLEANKER project and in particular on the design and engineering of the demonstrator.

D9.4 Third year technical report for ECRA

This deliverable is the third annual report to ECRA. It focuses on the activities carried out during the second year of CLEANKER project and in particular on the design and engineering of the demonstrator.