TY - JOUR
T1 - Isobutyric and n-butyric acid production from H2 and CO2 by Clostridium luticellarii in a hollow fiber membrane biofilm reactor: Reactor operation and process modelling
AU - Mariën, Quinten
AU - Flores-Alsina, Xavier
AU - Aslam, Umair
AU - Gernaey, Krist V.
AU - Regueira, Alberte
AU - Ganigué, Ramon
PY - 2024
Y1 - 2024
N2 - Clostridium luticellarii is an acetogen uniquely capable of producing acetic, n-butyric and isobutyric acid from H2 and CO2.
Since n-butyric and isobutyric acid are currently produced from
petrochemically derived propylene, establishing a direct production
route from CO2 and H2 could greatly improve their
sustainability as platform chemicals while simultaneously capturing
carbon. Here, we demonstrate for the first time the production of these
acids from H2 and CO2 by C. luticellarii
in a continuously operated hollow fiber membrane biofilm reactor
(HFMBR). The HFMBR was operated for 80 days while gradually increasing
the H2:CO2 ratio from 2.5 to 5.0. Concentrations of acetic, n-butyric and isobutyric acid of respectively 8.93 ± 0.22 g L−1, 1.56 ± 0.04 g L−1 and 1.51 ± 0.06 g L−1 were achieved at a dilution rate of 0.25 d−1.
Subsequently, a holistic process model was developed to gain deeper
insights into the performance of the system and how to optimize its
operation. The model described the autotrophic production of the acids,
as well as mass transfer of H2 and CO2 through the
membrane, biofilm diffusion and convective movement of particulates,
and biofilm growth and detachment. Calibration against experimental data
confirmed the model accuracy in reflecting the production dynamics
(NRMSE of products < 0.1). Scenario analyses highlighted the
importance of biofilm thickness control to minimize pH gradients and
revealed that increased membrane surface area and optimized dilution
rates are critical in enhancing volumetric production rates and steering
product selectivity. Overall, these combined experimental results and
model-generated insights can inform future optimization of HFMBRs for
the production of added-value products from H2 and CO2.
AB - Clostridium luticellarii is an acetogen uniquely capable of producing acetic, n-butyric and isobutyric acid from H2 and CO2.
Since n-butyric and isobutyric acid are currently produced from
petrochemically derived propylene, establishing a direct production
route from CO2 and H2 could greatly improve their
sustainability as platform chemicals while simultaneously capturing
carbon. Here, we demonstrate for the first time the production of these
acids from H2 and CO2 by C. luticellarii
in a continuously operated hollow fiber membrane biofilm reactor
(HFMBR). The HFMBR was operated for 80 days while gradually increasing
the H2:CO2 ratio from 2.5 to 5.0. Concentrations of acetic, n-butyric and isobutyric acid of respectively 8.93 ± 0.22 g L−1, 1.56 ± 0.04 g L−1 and 1.51 ± 0.06 g L−1 were achieved at a dilution rate of 0.25 d−1.
Subsequently, a holistic process model was developed to gain deeper
insights into the performance of the system and how to optimize its
operation. The model described the autotrophic production of the acids,
as well as mass transfer of H2 and CO2 through the
membrane, biofilm diffusion and convective movement of particulates,
and biofilm growth and detachment. Calibration against experimental data
confirmed the model accuracy in reflecting the production dynamics
(NRMSE of products < 0.1). Scenario analyses highlighted the
importance of biofilm thickness control to minimize pH gradients and
revealed that increased membrane surface area and optimized dilution
rates are critical in enhancing volumetric production rates and steering
product selectivity. Overall, these combined experimental results and
model-generated insights can inform future optimization of HFMBRs for
the production of added-value products from H2 and CO2.
KW - Carbon capture and utilization
KW - Carbon dioxide
KW - Gas fermentation
KW - Hydrogen
KW - Simulation
U2 - 10.1016/j.cej.2024.153216
DO - 10.1016/j.cej.2024.153216
M3 - Journal article
SN - 1369-703X
VL - 495
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 153216
ER -