TY - JOUR
T1 - Synergistic fermenter-electrolytic cell integration and phenomena-based process intensification for competitive bio-succinic acid production
AU - Malanca, Alina Anamaria
AU - Skiadas, Ioannis V.
AU - Gavala, Hariklia N.
AU - Pinelo, Manuel
AU - Mansouri, Seyed Soheil
PY - 2024
Y1 - 2024
N2 - The production of bio-succinic acid through fermentation presents a promising strategy for obtaining building-block chemicals from renewable sources. However, the limited yield of bio-succinic acid from fermentation and the complex purification procedures have hindered its competitiveness against petroleum-based succinic acid. One way to tackle this challenge is to develop a more efficient and sustainable production route, that is to integrate process synthesis with process intensification. In the present study, an existing flowsheet from our previous work based on process synthesis on bio-succinic acid batch fermentation was selected and subjected to heuristic and phenomena-based process intensification approaches. The heuristic approach involved integrating an electrolytic cell with the fermenter, employing an anionic exchange membrane for continuous extraction of organic acids. The resulting modified process flowsheet served as a base case for a systematic phenomena-based process intensification approach. Through this approach, intensified unit operations, such as an electro-membrane reactor and a membrane crystallizer, were generated. A total of 114 intensified process flowsheet alternatives were developed and ranked according to an enthalpy index. The top-ranked alternatives were evaluated in terms of economic performance and environmental impact. Notably, all analyzed process flowsheets exhibited improved indicators, with a minimum selling price below that of petroleum-based succinic acid (approximately $2kg-1).
AB - The production of bio-succinic acid through fermentation presents a promising strategy for obtaining building-block chemicals from renewable sources. However, the limited yield of bio-succinic acid from fermentation and the complex purification procedures have hindered its competitiveness against petroleum-based succinic acid. One way to tackle this challenge is to develop a more efficient and sustainable production route, that is to integrate process synthesis with process intensification. In the present study, an existing flowsheet from our previous work based on process synthesis on bio-succinic acid batch fermentation was selected and subjected to heuristic and phenomena-based process intensification approaches. The heuristic approach involved integrating an electrolytic cell with the fermenter, employing an anionic exchange membrane for continuous extraction of organic acids. The resulting modified process flowsheet served as a base case for a systematic phenomena-based process intensification approach. Through this approach, intensified unit operations, such as an electro-membrane reactor and a membrane crystallizer, were generated. A total of 114 intensified process flowsheet alternatives were developed and ranked according to an enthalpy index. The top-ranked alternatives were evaluated in terms of economic performance and environmental impact. Notably, all analyzed process flowsheets exhibited improved indicators, with a minimum selling price below that of petroleum-based succinic acid (approximately $2kg-1).
KW - Process intensification
KW - Bio-succinic acid
KW - Electrochemical extraction
KW - Anionic exchange membrane
KW - Techno-economic analysis
U2 - 10.1016/j.bej.2024.109258
DO - 10.1016/j.bej.2024.109258
M3 - Journal article
SN - 1369-703X
VL - 205
JO - Biochemical Engineering Journal
JF - Biochemical Engineering Journal
M1 - 109258
ER -