Abstrak - MATTHEW JUSTIN LESMANA
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
BAB 1 Matthew Justin Lesmana
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
BAB 2 Matthew Justin Lesmana
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
BAB 3 Matthew Justin Lesmana
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
BAB 4 Matthew Justin Lesmana
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
BAB 5 Matthew Justin Lesmana
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
COVER Matthew Justin Lesmana
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
DAFTAR PUSTAKA Matthew Justin Lesmana
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
LAMPIRAN Matthew Justin Lesmana
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
Terbatas  Irwan Sofiyan
» Gedung UPT Perpustakaan
As global mean temperature increases, attention is now being paid to the
benefits of developing carbon capture, utilization, and storage (CCUS), which
can be critical for mitigating climate change. The mineral carbonation process
offers the possibility of storing CO2 permanently and safely. Fly ash is a
potential source of highly reactive feedstock for CO2 mineral carbonation. It
does not require pre-treatment processes and is produced in large volumes
annually from coal-fired power plants. Still, it has a low carbonation rate and
efficiency. To address these issues, the carbonation performance and
mechanism of fly ash, together with the CO2 capture process by KOH, was
studied in this research. The effects of temperature, ash concentration, and
reaction duration on the carbonation efficiency were systematically
investigated from the results of the semi-batch carbonation experiment. In
addition, a repeated carbonation reaction and solvent regeneration were studied
in the multi-cycle carbonation experiment. The result indicated that calciumbearing
phases in the fly ash (lime, anhydrite, and brownmillerite) reacted with
CO2, forming calcium carbonate with a maximum theoretical CO2 sequestration
capacity of 0.108 kg CO2/kg fly ash. Increasing the ash concentration and
reaction temperature during the carbonation process positively affects the
sequestration rate and carbonation efficiency. The multi-cycle experiment
showed that K2CO3 from the capture solvent facilitated the precipitation of
CaCO3 and was well regenerated in the process. The estimated cost for CO2
sequestration with this method is around US$140.4/tCO2. We conclude that fly
ash CO2 sequestration development is technically viable and economically
competitive compared to others. Still, more CCUS-specific policies are
recommended to ensure its development, especially in Indonesia.