The Activity and Stability of Promoted Cu/ZnO/Al2O3 Catalyst for CO2 Hydrogenation to Methanol

被引:1
|
作者
Berahim, Nor Hafizah [1 ,2 ]
Zabidi, Noor Asmawati Mohd [2 ]
Ramli, Raihan Mahirah [3 ]
Suhaimi, Nur Amirah [2 ]
机构
[1] PETRONAS Res Sdn Bhd, Grp Res & Technol, Carbon Capture Utilizat & Storage Dept, Kajang 43000, Selangor, Malaysia
[2] Univ Teknol PETRONAS, Inst Contaminant Management Oil & Gas, Ctr Contaminant Control & Utilizat CenCoU, Dept Fundamental & Appl Sci, Seri Iskandar 32610, Perak, Malaysia
[3] Univ Teknol PETRONAS, Ctr Innovat Nanostruct & Nanodevices COINN, Dept Chem Engn, Seri Iskandar 32610, Perak, Malaysia
关键词
Cu; ZnO; Al2O3; catalyst; methanol synthesis; stability; activity; SULFUR TOLERANCE; CARBON-DIOXIDE; DEACTIVATION; ADSORPTION; INTERFACE; SURFACE; SYNGAS; SITES; SIZE; XPS;
D O I
10.3390/pr11030719
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Cu/ZnO/Al2O3 catalyst with the addition of tri-promoters (Mn/Nb/Zr) was investigated with respect to their catalytic activity and stability in a prolonged reaction duration in methanol synthesis. Spent catalysts were characterized using N-2 adsorption-desorption, FESEM/EDX, TEM, N2O chemisorption, and XPS for their physicochemical properties. The catalyst longevity study was evaluated at two days, seven days, and 14 days at 300 degrees C, 31.25 bar, 2160 mL/g.hr GHSV, and H-2:CO2 at 10:1. The CO2 conversion and methanol yield decreased by about 5.7% and 7.7%, respectively, when the reaction duration was prolonged to 14 days. A slight reduction in catalytic activity under prolonged reaction duration was found due to thermal degradation.
引用
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页数:14
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