Year 1
WP1 - Pyrolysis
A survey was conducted on biomass resources and pyrolysis studies in the literature. Straw, hardwood, softwood, and nitrogen-rich coffee silverskin were selected as biomass feedstock. Since low pyrolysis temperature and heating rate are suitable for producing biochar for nitrogen adsorption, pyrolysis of biomass in N2 and CO2 has been investigated for temperatures of 360, 450, and 600 °C and a heating rate of 10 °C/min. Experimental studies have been made to verify conditions that suit the MINICOR process steps and to obtain data for the development and validation of numerical models. Data on the biochar product will further serve as input for project WP5.
The experimental studies have been carried out using various techniques to assess pyrolysis product yields and compositions. These include
- Thermogravimetric analysis to analyze biomass decomposition versus time and temperature by monitoring mass loss due to the release of volatiles.
- Techniques to analyze various aspects of chemical composition
- Calorimetry techniques to determine heating values.
WP2 -MILD combustion/dry reforming
Bio-oil oxidation and reforming studies were initiated in M6 with preparations of experimental work planned for the following period. Thermal conversion of bio-oil will be investigated by studying selected chemical components and the experimental facility has been adapted accordingly. Initial runs were made on gases, and a preliminary analysis was carried out. A reactor has also been adapted for further studies at higher temperatures.
A numerical study of dry reforming was carried out for different hydrocarbons, and the temperature corresponding to 10% of CO2 captured was evaluated using kinetic models. Methane requires the highest temperature to achieve 10% CO2 conversion, whereas heavier and more complex molecules, which could represent bio-oil, e.g. guaiacol and butanol, require lower temperatures.
The overall goal of the project is to demonstrate a combined pyrolysis/MILD system. As a first step to address this objective, process simulations were made using the Aspen Plus V.14 software to evaluate the impact of the MINICOR concept on the carbon and nitrogen cycles, analyze energy and carbon flows, and identify operational conditions to maximize syngas production. In addition, the study addressed integration strategies and valorization of waste heat. The results indicate that up to 65% of the carbon going into the process can be sequestered through the optimization of pyrolysis for bio-oil production and, subsequently, syngas yield in CO2 reforming.