Effect of calcination temperature on catalytic performance of Pt-FeOx/γ-Al2O3 catalysts for HCHO oxidation
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摘要: 采用胶体沉积法制备了Pt-FeOx/γ-Al2O3催化剂,通过XRD、TEM、BET、XPS、H2-TPR和FT-IR等技术对催化剂进行了表征,考察了焙烧温度对Pt-FeOx/γ-Al2O3催化剂表面结构及其催化甲醛氧化性能的影响。结果表明,焙烧温度对Pt-FeOx/γ-Al2O3催化剂的氧化还原性能、Pt物种的化学状态以及表面羟基的数量有较大的影响。在室温下,所有Pt-FeOx/γ-Al2O3催化剂均表现出催化氧化活性,其中,200℃焙烧的Pt-FeOx/γ-Al2O3催化剂表现出最好的催化性能,可以将甲醛100%转化为CO2和H2O。较低温度焙烧的Pt-FeOx/γ-Al2O3催化剂表面Pt物种具有较好的价态分布以及更多的界面活性位,如Pt-O-Fe物种,因而在温和条件下对甲醛的催化氧化活性较高。Abstract: A series of Pt-FeOx/γ-Al2O3 catalysts were prepared by colloid-deposition method and characterized by XRD, TEM, BET, XPS, H2-TPR and FT-IR to investigate the effects of calcination temperature on the surface structure of Pt-FeOx/γ-Al2O3 catalyst and its catalytic performance in catalytic HCHO oxidation. The characterization results showed that the applied calcination temperature greatly influenced the redox properties and chemical states of the Pt species, as well as the amount of surface hydroxyl groups. All resultant Pt-FeOx/γ-Al2O3 catalysts demonstrated activity in HCHO oxidation. The sample with calcination at 200 ℃ exhibited the best performance, which afforded 100% conversion of HCHO into CO2 and H2O at room temperature. The catalysts with lower calcination temperature should be beneficial to have a better valence distribution of Pt species and produce more accessible interface active sites like Pt-O-Fe species, thus endowing Pt-FeOx/γ-Al2O3 catalyst with relatively high activity for the oxidation of formaldehyde under mild conditions.
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Key words:
- formaldehyde /
- catalytic oxidation /
- reactivity /
- calcination temperature /
- Pt nanoparticles
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图 3 t/γ-Al2O3-200和Pt-FeOx/γ-Al2O3-t催化剂的HRTEM电镜照片((a)-(d), (f)),Pt-FeOx/γ-Al2O3-200催化剂的HAADF-STEM电镜照片(e)和EDX元素能量分布图(g)
Figure 3 HRTEM ((a)-(d), (f)) of the Pt/γ-Al2O3-200 and Pt-FeOx/γ-Al2O3 -t catalyst, HAADF-STEM(e) and EDX mapping images(g) of the Pt-FeOx/γ-Al2O3-200 catalyst
(a): Pt/γ-Al2O3-200; (b): Pt-FeOx/γ-Al2O3-200; (c): Pt-FeOx/γ-Al2O3-300; (d): Pt-FeOx/γ-Al2O3-400 (e): Pt-FeOx/γ-Al2O3-200; (f): Pt-FeOx/γ-Al2O3-200; (g): Pt-FeOx/γ-Al2O3-200
图 4 Pt/γ-Al2O3-200、Pt-FeOx/γ-Al2O3-t催化剂和γ-Al2O3载体的甲醛催化氧化活性
Figure 4 HCHO catalytic oxidation activities of the Pt/γ- Al2O3-200, Pt-FeOx/Al2O3-t catalysts and γ-Al2O3 support
a: γ-Al2O3; b: Pt/γ-Al2O3-200; c: Pt-FeOx/γ-Al2O3-200; d: Pt-FeOx/γ-Al2O3-300; e: Pt-FeOx/γ-Al2O3-400 (reaction conditions: HCHO 375 mg/m3, φO2=20%, N2 balance, RH = 30%, GHSV: 60000 cm3/(g·h))
表 1 Pt/γ-Al2O3-200、Pt-FeOx/γ-Al2O3-t催化剂和γ-Al2O3载体的物化性能
Table 1 Physical properties of the Pt/γ-Al2O3-200, Pt-FeOx/Al2O3-t catalysts and γ-Al2O3 support
Catalyst ABET/(m2·g-1) Pore volume v/(m3·g-1) Pore size d/nm γ-Al2O3 162 0.23 6.0 Pt/γ-Al2O3-200 119 0.17 6.5 Pt-FeOx/γ-Al2O3-200 113 0.17 6.6 Pt-FeOx/γ-Al2O3-300 104 0.16 6.7 Pt-FeOx/γ-Al2O3-400 98 0.14 6.9 表 2 Pt/γ-Al2O3-200、Pt-FeOx/γ-Al2O3-t催化剂以及γ-Al2O3载体的Pt 4d和O 1s XPS拟合
Table 2 Pt 4d and O 1s XPS curve fitting results of Pt/γ- Al2O3-200, Pt-FeOx/Al2O3-t catalysts and γ-Al2O3 support
Catalyst Pt2+/Pt 0 OII/(OI+ OII) γ-Al2O3 0.37 Pt/γ-Al2O3-200 0.36 0.31 Pt-FeOx/γ-Al2O3-200 0.39 0.31 Pt-FeOx/γ-Al2O3-300 0.58 0.23 Pt-FeOx/γ-Al2O3-400 1.33 0.18 -
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