TY - JOUR
T1 - Dual structure Brønsted sites activated carbon beads solid acid enhances the highly efficient synthesis of HMF
T2 - From batch to continuous
AU - Yang, Wei Yao
AU - Wen, Meng
AU - Zhang, Hong Da
AU - Tian, Ya Qiao
AU - Su, Shi Chao
AU - Lang, Yu
AU - Zhao, Zhi Ping
AU - Sang, Le
N1 - Publisher Copyright:
© 2025 Elsevier B.V.
PY - 2025/7/15
Y1 - 2025/7/15
N2 - In this work, ACB18-SO3H-Cl with dual structure Brønsted sites was prepared via chemical grafting method, and promoted the efficient production of HMF from batch to continuous reactors. The optimal catalyst was obtained by adjusting the acid etching time and the grafting amount of acidic functional groups. Through BET and NH3-TPD, it was found that the specific surface area of the 0.3 mm spherical activated carbon support reached 1179 m2/g, and the acid concentration of prepared ACB18-SO3H-Cl catalyst reached 7.86 mmol/g. The fructose conversion of 99.2 % and HMF yield of 96.2 % were achieved in stirred tank reactors (STRs) within 2 h, and 90.6 % HMF yield was obtained in micropacked bed reactors (μPBRs) within 86.4 s. Meanwhile, Py-IR and selective poisoning experiments confirmed that the Brønsted acid site is the catalytic active center, and there is a synergistic catalytic effect between the two structural Brønsted sites. The space–time yield (STY) of HMF in μPBRs can reach 2.96 kg/L/h/g, which is at least one order of magnitude larger than reported values in batch and continuous reactors. Moreover, based on the synergistic strengthening effect of μPBRs and ACB18-SO3H-Cl, the apparent activation energy for synthesizing HMF in μPBRs is lower than that of STRs.
AB - In this work, ACB18-SO3H-Cl with dual structure Brønsted sites was prepared via chemical grafting method, and promoted the efficient production of HMF from batch to continuous reactors. The optimal catalyst was obtained by adjusting the acid etching time and the grafting amount of acidic functional groups. Through BET and NH3-TPD, it was found that the specific surface area of the 0.3 mm spherical activated carbon support reached 1179 m2/g, and the acid concentration of prepared ACB18-SO3H-Cl catalyst reached 7.86 mmol/g. The fructose conversion of 99.2 % and HMF yield of 96.2 % were achieved in stirred tank reactors (STRs) within 2 h, and 90.6 % HMF yield was obtained in micropacked bed reactors (μPBRs) within 86.4 s. Meanwhile, Py-IR and selective poisoning experiments confirmed that the Brønsted acid site is the catalytic active center, and there is a synergistic catalytic effect between the two structural Brønsted sites. The space–time yield (STY) of HMF in μPBRs can reach 2.96 kg/L/h/g, which is at least one order of magnitude larger than reported values in batch and continuous reactors. Moreover, based on the synergistic strengthening effect of μPBRs and ACB18-SO3H-Cl, the apparent activation energy for synthesizing HMF in μPBRs is lower than that of STRs.
KW - 5-Hydroxymethylfurfural
KW - Activated carbon catalyst
KW - Fructose
KW - Kinetics study
KW - Micropacked bed reactor
UR - http://www.scopus.com/inward/record.url?scp=105005960487&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2025.164098
DO - 10.1016/j.cej.2025.164098
M3 - Article
AN - SCOPUS:105005960487
SN - 1385-8947
VL - 516
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
M1 - 164098
ER -