Post-functionalization of polymeric mesoporous C@Zn core-shell spheres used for methyl ester production

被引:16
作者
Soltani, Soroush [1 ]
Rashid, Umer [1 ,2 ]
Yunus, Robiah [3 ]
Taufiq-Yap, Yun Hin [4 ]
Al-Resayes, Saud Ibrahim [2 ]
机构
[1] Univ Putra Malaysia, Inst Adv Technol, Upm Serdang 43400, Selangor, Malaysia
[2] King Saud Univ, Coll Sci, Dept Chem, Riyadh 1145, Saudi Arabia
[3] Univ Putra Malaysia, Fac Engn, Dept Chem & Environm Engn, Upm Serdang 43300, Selangor, Malaysia
[4] Univ Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr, Upm Serdang 43400, Selangor, Malaysia
关键词
Mesoporous catalyst; Hydrothermal method; Surface modification; Post-sulfonation treatment; Esterification; Microwave-assisted technique; SOLID ACID CATALYST; ZINC ALUMINATE SPINEL; BIODIESEL PRODUCTION; POLYETHYLENE-GLYCOL; HOLLOW SPHERES; CARBON; OXIDE; ESTERIFICATION; INACTIVATION; ZNO/ZNAL2O4;
D O I
10.1016/j.renene.2016.08.025
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
In the present study, the mesoporous carbon@zinc (C@Zn) core-shell spheres were hydrothermally synthesized, using polyethylene glycol (PEG) as the surfactant and D-glucose as the pore forming agent. Then, the post-sulfonation treatment was carried out to prepare polymeric mesoporous SO3H-ZnO catalyst. The physicochemical, structural, textural and morphological properties of the synthesized catalysts were characterized by X-ray powder diffraction (XRPD), surface area analysis (Brunauer-Emmett-Teller equation), temperature programed desorption (TPD), field emission scanning electron microscopy (FE-SEM), and transmission electron microscopy (TEM). The polymeric mesoporous SO3H-ZnO catalyst owned a high surface area of 396.56 m(2)/g with the average pore size of 3.45 nm and acid strength of 1.92 +/- 0.05 mmol/g. The catalytic activity of the synthesized catalyst was further studied via esterification of the palm fatty acid distillate (PFAD), using a microwave-assisted technique. The biodiesel yield of 91.20% was achieved under the optimized esterification conditions as follows: the methanol to PFAD molar ratio of 9:1, catalyst concentration of 1.5 wt%, reaction temperature of 90 degrees C and reaction time of 15 min. The spent mesoporous catalyst was highly stable for reuse with nine continuous runs without further treatment. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1235 / 1243
页数:9
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