TY - JOUR
T1 - Oil Palm Empty Fruit Bunch (OPEFB) Pretreatment Simulation with Ammonia Soaking and Ammonia Expansion Method for Levulinic Acid and Furfural Production
AU - Muryanto,
AU - Karimah, Iffa
AU - Josua Sianipar, Andri
AU - Carisma Handita, Fabio
AU - Nisrina Sumayyah, Hasna
AU - Gabriella, Maria
AU - Alifa Hubeis, Nadhira
AU - Lizanoer Alviora, She
AU - Rahmanisa Fitri, Widya
AU - Abdurachim, Yahya
AU - Hermansyah, Heri
AU - Sudiyani, Yanni
AU - Gozan, Misri
N1 - Publisher Copyright:
© 2024 EDP Sciences. All rights reserved.
PY - 2024/3/20
Y1 - 2024/3/20
N2 - OPEFB is a waste product from oil palm mills and is abundant in quantity. OPEFB is a lignocellulosic compound containing cellulose, hemicellulose, and lignin. The cellulose in OPEFB can be converted into levulinic acid, while hemicellulose can be converted into furfural. The consumption of furfural and levulinic acid in Indonesia is increasing, and so far, the demand has been met through imports. Pretreatment is the first stage in converting OPEFB into valuable products. In this paper, we have simulated furfural and levulinic acid production from OPEFB using two pretreatment methods: ammonia soaking and ammonia expansion. Both process simulations were carried out using Superpro Designer v9.0, with 17,520 metric tons OPEFB/year capacity as input raw material. The simulation of furfural and levulinic acid production using the ammonia expansion pretreatment process resulted in feasibility indicators including a payback period of 2.56 years, an ROI (Return on Investment) of 34.07%, and an IRR (Internal Rate of Return) of 28.62%. On the other hand, using the ammonia-soaking process resulted in an IRR of 22.26%. These parameters indicate that furfural and levulinic acid production is more economically viable using the ammonia expansion pretreatment process than the ammonia soaking pretreatment process.
AB - OPEFB is a waste product from oil palm mills and is abundant in quantity. OPEFB is a lignocellulosic compound containing cellulose, hemicellulose, and lignin. The cellulose in OPEFB can be converted into levulinic acid, while hemicellulose can be converted into furfural. The consumption of furfural and levulinic acid in Indonesia is increasing, and so far, the demand has been met through imports. Pretreatment is the first stage in converting OPEFB into valuable products. In this paper, we have simulated furfural and levulinic acid production from OPEFB using two pretreatment methods: ammonia soaking and ammonia expansion. Both process simulations were carried out using Superpro Designer v9.0, with 17,520 metric tons OPEFB/year capacity as input raw material. The simulation of furfural and levulinic acid production using the ammonia expansion pretreatment process resulted in feasibility indicators including a payback period of 2.56 years, an ROI (Return on Investment) of 34.07%, and an IRR (Internal Rate of Return) of 28.62%. On the other hand, using the ammonia-soaking process resulted in an IRR of 22.26%. These parameters indicate that furfural and levulinic acid production is more economically viable using the ammonia expansion pretreatment process than the ammonia soaking pretreatment process.
UR - http://www.scopus.com/inward/record.url?scp=85190619673&partnerID=8YFLogxK
U2 - 10.1051/e3sconf/202450304007
DO - 10.1051/e3sconf/202450304007
M3 - Conference article
AN - SCOPUS:85190619673
SN - 2555-0403
VL - 503
JO - E3S Web of Conferences
JF - E3S Web of Conferences
M1 - 04007
T2 - 9th International Symposium on Applied Chemistry in conjuction with the 5th International Conference on Chemical and Material Engineering, ISAC-ICCME 2023
Y2 - 6 December 2023 through 8 December 2023
ER -