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China Surfactant Detergent & Cosmetics ›› 2022, Vol. 52 ›› Issue (4): 396-403.doi: 10.3969/j.issn.1001-1803.2022.04.008

• Development and application • Previous Articles     Next Articles

Preparation and characterization of magnetic solid acid catalyst Fe3O4/C-SO3H

Yu Hongmei,Hua Ping*(),Li Jianhua,Qian Feng   

  1. College of Chemistry and Chemical Engineering, Nantong University, Nantong, Jiangsu 226000, China
  • Received:2021-06-25 Revised:2021-03-25 Online:2022-04-22 Published:2022-04-25
  • Contact: Ping Hua E-mail:hua.p@ntu.edu.cn.

Abstract:

Fe3O4/C-SO3H was a magnetic carbon-based solid acid catalyst. It was prepared with Fe3O4, biomass carbon and sulfonic acid source, in which Fe3O4 was the magnetic core and biomass carbon (glucose, starch, sucrose) was the raw material. Firstly, Fe3O4/C was prepared by the carbonization reaction taken place between Fe3O4 and biomass. Then, sulfonation of Fe3O4/C with p-toluenesulfonic acid was carried out, and thus Fe3O4/C-SO3H was prepared. The synthesis of octyl glucoside was used as a probe reaction. The activity of the catalyst was measured by the conversion of glucose and the catalyst acid content. The influencing factors such as biomass carbon type, carbonization temperature, carbonization time, acid type, sulfonation temperature and sulfonation time were investigated. The catalyst was characterized by FT-IR, XRD, TG, SEM and Vibrating Sample Magnetometer (VSM). The results show that, the optimum preparation conditions of Fe3O4/C-SO3H are as follows: Starch is the best biomass carbon source among glucose, starch and sucrose; the mass ratio of Fe3O4 to starch is 1:10; carbonization temperature is 190 ℃; carbonization time is 8 h; among the three sulfonic acid sources (p-toluenesulfonic acid, dodecylbenzene sulfonic acid and concentrated sulfuric acid), p-toluenesulfonic acid is the best; the mass ratio of Fe3O4/C to p-toluenesulfonic acid is 1:0.6; the sulfonation temperature is 250 ℃; the sulfonation time is 4 h. Under the optimized conditions, the acid content of the catalyst is 1.17 mmol/g, and the glucose conversion is 97.9%. XRD results show that the crystal structure of magnetic Fe3O4 particles does not significantly change after carbonization and sulfonation, and the catalyst still retains good magnetic properties. FT-IR analysis shows that sulfonic groups are successfully loaded on the carrier Fe3O4/C. Thermogravimetric analysis shows that Fe3O4/C-SO3H has good thermal stability below 300 ℃. SEM shows that magnetic Fe3O4 particles are irregular spherical particles with uniform size distribution and agglomeration. After carbonization, Fe3O4 are encapsulated by starch, and the particle size becomes larger, and there is a certain pore structure. The Fe3O4/C-SO3H catalyst also has a certain core-shell structure, and the particle size is approximately 30 nm. The VSM curves show that the magnetic strength of Fe3O4/C and Fe3O4/C-SO3H is much smaller than that of Fe3O4, but Fe3O4/C-SO3H can be separated from the system rapidly by simple magnetic attraction. It shows that the final magnetic properties of Fe3O4/C-SO3H meet the requirements of magnetic separation and recovery.

Key words: magnetic catalyst, solid acid catalyst, octyl glucoside

CLC Number: 

  • TQ423