摘要
In this work, ACB 18 -SO 3 H-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 NH 3 -TPD, it was found that the specific surface area of the 0.3 mm spherical activated carbon support reached 1179 m 2 /g, and the acid concentration of prepared ACB 18 -SO 3 H-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 ACB 18 -SO 3 H-Cl, the apparent activation energy for synthesizing HMF in μPBRs is lower than that of STRs.
危险品化学品经营许可证(带存储)