Reactor design for CO2 photo-hydrogenation toward solar fuels under ambient temperature and pressure
dc.contributor.author | Chen, Chun-Ying | |
dc.contributor.author | Yu, Joseph Che-Chin | |
dc.contributor.author | Nguyen, Van-Huy | |
dc.contributor.author | Wu, Jeffrey Chi-Sheng | |
dc.contributor.author | Wang, Wei-Hon | |
dc.contributor.author | Kočí, Kamila | |
dc.date.accessioned | 2017-04-21T07:17:22Z | |
dc.date.available | 2017-04-21T07:17:22Z | |
dc.date.issued | 2017 | |
dc.identifier.citation | Catalysts. 2017, vol. 7, issue 2, art. no. 63. | cs |
dc.identifier.issn | 2073-4344 | |
dc.identifier.uri | http://hdl.handle.net/10084/117013 | |
dc.description.abstract | Photo-hydrogenation of carbon dioxide (CO2) is a green and promising technology and has received much attention recently. This technique could convert solar energy under ambient temperature and pressure into desirable and sustainable solar fuels, such as methanol (CH3OH), methane (CH4), and formic acid (HCOOH). It is worthwhile to mention that this direction can not only potentially depress atmospheric CO2, but also weaken dependence on fossil fuel. Herein, 1 wt % Pt/CuAlGaO4 photocatalyst was successfully synthesized and fully characterized by ultraviolet-visible light (UV-vis) spectroscopy, X-ray diffraction (XRD), Field emission scanning electron microscopy using energy dispersive spectroscopy analysis (FE-SEM/EDS), transmission electron microscopy (TEM), X-ray photoelectron spectroscopy (XPS), and Brunauer-Emmett-Teller (BET), respectively. Three kinds of experimental photo-hydrogenation of CO2 in the gas phase, liquid phase, and gas-liquid phase, correspondingly, were conducted under different H-2 partial pressures. The remarkable result has been observed in the gas-liquid phase. Additionally, increasing the partial pressure of H-2 would enhance the yield of product. However, when an extra amount of H-2 is supplied, it might compete with CO2 for occupying the active sites, resulting in a negative effect on CO2 photo-hydrogenation. For liquid and gas-liquid phases, CH3OH is the major product. Maximum total hydrocarbons 8.302 mu molg(-1) is achieved in the gas-liquid phase. | cs |
dc.format.extent | 5419047 bytes | |
dc.format.mimetype | application/pdf | |
dc.language.iso | en | cs |
dc.publisher | MDPI | cs |
dc.relation.ispartofseries | Catalysts | cs |
dc.relation.uri | http://dx.doi.org/10.3390/catal7020063 | cs |
dc.rights | © 2017 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license. | cs |
dc.rights.uri | http://creativecommons.org/licenses/by/4.0/ | cs |
dc.subject | CO2 reduction | cs |
dc.subject | Pt/CuAlGaO4 | cs |
dc.subject | photo-hydrogenation | cs |
dc.subject | photocatalysis | cs |
dc.subject | solar fuels | cs |
dc.title | Reactor design for CO2 photo-hydrogenation toward solar fuels under ambient temperature and pressure | cs |
dc.type | article | cs |
dc.identifier.doi | 10.3390/catal7020063 | |
dc.rights.access | openAccess | |
dc.type.version | publishedVersion | cs |
dc.type.status | Peer-reviewed | cs |
dc.description.source | Web of Science | cs |
dc.description.volume | 7 | cs |
dc.description.issue | 2 | cs |
dc.description.firstpage | art. no. 63 | cs |
dc.identifier.wos | 000395436800028 |
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