2013
DOI: 10.1016/j.cej.2013.08.005
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Enhanced catalytic oxidation of formaldehyde over dual-site supported catalysts at ambient temperature

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Cited by 25 publications
(6 citation statements)
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“…Besides, formaldehyde could condense with surface acetate and acetic acid to form carboxylic acids, a precursor for olefins via decarboxylation (Figure b) . Additionally, formaldehyde could promote aromatics selectivity, accelerating the deactivation via forming bulky coke species (Figure a). , Since the Lewis acid site (LAS) (e.g., CeO 2 , ZnO, TiO 2 ) could decompose formaldehyde, utilizing the bifunctional BAS-LAS zeolite system would be an appropriate way to improve the catalyst lifetime (Figure c; BAS, Brønsted acid site). , With this objective, Hwang et al evaluated the lifetime of bifunctional catalysts (H-SAPO-34 and Y 2 O 3 ) in different fixed-bed configurations: Y 2 O 3 packed upstream of H-SAPO-34, Y 2 O 3 packed downstream of H-SAPO-34, an interpellet physical mixture of H-SAPO-34 with Y 2 O 3 , and an intrapellet physical mixture of H-SAPO-34 with Y 2 O 3 , in addition to the standalone zeolite. The addition of Y 2 O 3 does not directly influence the MTH reaction, yet it facilitates HCHO decomposition into CO.…”
Section: Zeolite-catalyzed Methanol Conversionmentioning
confidence: 99%
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“…Besides, formaldehyde could condense with surface acetate and acetic acid to form carboxylic acids, a precursor for olefins via decarboxylation (Figure b) . Additionally, formaldehyde could promote aromatics selectivity, accelerating the deactivation via forming bulky coke species (Figure a). , Since the Lewis acid site (LAS) (e.g., CeO 2 , ZnO, TiO 2 ) could decompose formaldehyde, utilizing the bifunctional BAS-LAS zeolite system would be an appropriate way to improve the catalyst lifetime (Figure c; BAS, Brønsted acid site). , With this objective, Hwang et al evaluated the lifetime of bifunctional catalysts (H-SAPO-34 and Y 2 O 3 ) in different fixed-bed configurations: Y 2 O 3 packed upstream of H-SAPO-34, Y 2 O 3 packed downstream of H-SAPO-34, an interpellet physical mixture of H-SAPO-34 with Y 2 O 3 , and an intrapellet physical mixture of H-SAPO-34 with Y 2 O 3 , in addition to the standalone zeolite. The addition of Y 2 O 3 does not directly influence the MTH reaction, yet it facilitates HCHO decomposition into CO.…”
Section: Zeolite-catalyzed Methanol Conversionmentioning
confidence: 99%
“…104 Additionally, formaldehyde could promote aromatics selectivity, accelerating the deactivation via forming bulky coke species (Figure 6a). 105,106 Since the Lewis acid site (LAS) (e.g., CeO 2 , 107 ZnO, 108 TiO 2 109 ) could decompose formaldehyde, utilizing the bifunctional BAS-LAS zeolite system would be an appropriate way to improve the catalyst lifetime (Figure 6c; BAS, Brønsted acid site). 107,108 With this objective, Hwang et al 110 6d).…”
Section: Impact Of Kochmentioning
confidence: 99%
“…A long-term exposure to HCHO can cause serious health problems such as eye irritation, respiratory tract, headache, pneumonia, and even cancer. , Therefore, the elimination of gaseous HCHO from the indoor environment is an important issue. Usually physical adsorption and chemical oxidation are used for HCHO removal. Physical adsorption is a simple and effective approach to eliminate HCHO under ambient conditions; however, its wide application is largely restricted by the limited adsorption capacity and the need for adsorbent regeneration. Catalytic oxidation of HCHO is advantageous as compared to physical adsorption, because it can completely decompose HCHO into CO 2 and H 2 O. Catalysts like transition metal oxides and supported noble metals, such as Pt, Au, and Pd, have been extensively explored for oxidation of gaseous HCHO. , As compared to the transition-metal oxide catalysts, the supported noble metal catalysts are usually very efficient for complete oxidation of HCHO at lower temperatures, even at room (or ambient) temperature.…”
Section: Introductionmentioning
confidence: 99%
“…Transformation rate is 1:1, which means that one mol produces one mol of carbon dioxide [9][10][11][12][13][14][15][16][17]. Fig.…”
Section: Resultsmentioning
confidence: 99%
“…These parameters allowed calculating the photocatalytic activity of layers. The first derivate in x 0 point is: (2) This was used to calculate the maximum rate of chemical reaction [9][10][11][12][13][14].…”
Section: Resultsmentioning
confidence: 99%