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| 1 | 城市垃圾焚烧过程中重金属释放行为的试验研究显示文摘以城市垃圾为研究对象,在流化床试验装置上进行焚烧试验,并采用电感耦合等离子体发射光谱仪在线测量烟气中的重金属浓度,研究不同气氛条件(空气、混合气和氮气)下Cd、Pb及Zn3种重金属的释放特性.试验发现,城市垃圾焚烧过程中,在还原气氛及HCl存在的情况下,Cd及Pb较易挥发释放,而Zn释放程度较低,且基本不受气氛条件的影响.研究结果对揭示城市垃圾流化床焚烧过程中重金属释放行为有一定的意义. | 孙路石 陆继东 张娟 Abanades S Flamant G Gauthier D | 2003 | 燃烧科学与技术2003，9，6： | 9 |
| 2 | Improving photoreduction of CO2 with water to CH4 in a novel concentrated solar reactor显示文摘CO_2 photoreduction is an attractive process which allows the storage of solar energy and synthesis of solar fuels. Many different photocatalytic systems have been developed, while the alternative photo-reactors are still insufficiently investigated. In this work, photoreduction of CO_2 with H_2O into CH_4 was investigated in a modified concentrating solar reactor, using TiO_2 and Pt/TiO_2 as the catalysts. The TiO_2 and Pt/TiO_2 samples were extensively characterized by different techniques including powder X-ray diffraction(XRD), N_2 adsorption/desorption and UV–vis absorption. The catalytic performance of the TiO_2 and Pt/TiO_2 samples in the gas phase was evaluated under unconcentrated and concentrated Xe-lamp light and nature solar light with different concentrating ratios. Various parameters of the reaction system and the catalysts were investigated and optimized to maximize the catalytic performance of CO_2 reduction system. Compared with the normal light irradiation, the TiO_2 and Pt/TiO_2 samples show higher photocatalytic activity(about 6–7 times) for reducing CO_2 into CH_4 under concentrated Xe-lamp light and nature solar light. In the range of experimental light intensity, it is found that the concentration of the light makes it suitable for the catalytic reaction, and increases the utilization efficiency of the TiO_2 and Pt/TiO_2 samples while does not decrease the quantum efficiency. | Sisi Han Yinfei Chen Stéphane Abanades Zekai Zhang | 2017 | Journal of Energy Chemistry2017，26，4： | 2 |
| 3 | Solar chemical looping reforming of methane combined with isothermal H2O/CO2 splitting using ceria oxygen carrier for syngas production显示文摘The chemical looping reforming of methane through the nonstoichiometric ceria redox cycle(CeO2/CeO2-δ) has been experimentally investigated in a directly irradiated solar reactor to convert both solar energy and methane to syngas in the temperature range 900–1050 °C. Experiments were carried out with different ceria shapes via two-step redox cycling composed of endothermic partial reduction of ceria with methane and complete exothermic re-oxidation of reduced ceria with H2 O/CO2 at the same operating temperature, thereby demonstrating the capability to operate the cycle isothermally. A parametric study considering different ceria macrostructure variants(ceria packed powder, ceria packed powder mixed with inert Al2 O3 particles, and ceria reticulated porous foam) and operating parameters(methane flow-rate, reduction temperature, or sintering temperature) was conducted in order to unravel their impact on the bed-averaged oxygen non-stoichiometry(δ), syngas yield, methane conversion, and solar reactor performance. The ceria cycling stability was also experimentally investigated to demonstrate repeatable syngas production by alternating the flow between CH4 and H2 O(or CO2). A decrease in sintering temperature of the ceria foam was beneficial for increasing syngas selectivity, methane conversion,and reactor performance. Increasing both CH4 concentration and reduction temperature enhanced δ with the maximum value up to 0.41 but concomitantly favored CH4 cracking reaction. The ceria reticulated porous foam showed better performance in terms of effective heat transfer, due to volumetric absorption of concentrated solar radiation and uniform heating with lower solar power consumption, thereby promoting the solar-to-fuel energy conversion efficiency that reached up to 5.60%. The energy upgrade factor achieved during cycle was up to 1.19. Stable patterns in the δ and syngas yield for consecutive cycles with the ceria foam validated material performance stability. | Srirat Chuayboon Stéphane Abanades Sylvain Rodat | 2020 | Journal of Energy Chemistry2020，29，2： | 2 |
| 4 | 流化床内重金属蒸发特性的动力学模型显示文摘在流化床内煤燃烧烟气中重金属浓度的实时监测基础上,发展动力学模型来研究重金属蒸发释放的动力学特性。该方法包括出口烟气中的重金属浓度变化的实验数据和一个反应器尺度的模型。在反应器的气体出口安装了在线分析系统,该在线分析系统可连续测量烟气中的重金属浓度变化规律。将烟气重金属在线分析的实验结果作为模型的输入参数,根据重金属的蒸发率和固体颗粒中重金属浓度的关系得到其蒸发的动力学规律,对于煤得到2级反应动力学规律。 | 刘晶 D Gauthier S Abanades G Flamant 郑楚光 | 2009 | 工程热物理学报2009，30，2： | 2 |
| 5 | Kinetic model- ling of methane decomposition in a tubular solar reac- tor显示文摘 | Rodat S Abanades S Couli6 J | 2009 | Chemical Engineering Journal2009，146，1： | 1 |
| 6 | Sorbent cost and performance in CO2 capture systems显示文摘 | Abanades J C Rubin E S Anthony E J | 2004 | Industrial & Engineering ChemistryResearch2004，43，13： | 1 |
| 7 | Reversible Coma Secondary to Cefepime Neurotoxicity显示文摘 | Abanades S Nolla J Rodrtguez-Campello A | 2004 | Ann Pharma- tother2004，38，4： | 1 |
| 8 | The maximum capture efficiency of CO2 using a carbonation/calcination cycle of CaO/Ca- CO3 显示文摘 | ABANADES J C | 2002 | Chemical Engineering Journal2002，90，3： | 1 |
| 9 | Conversion limits in the reaction of CO2 with lime显示文摘 | Abanades J C Alvarez D | 2003 | Energy & Fuels2003，17，2： | 1 |
| 10 | Conversion limits in the reaction of CO2 with lime显示文摘 | Abanades J C Alvarez D | 2003 | Energy Fuels2003，17，2： | 1 |
| 11 | Conversion limits in the reaction of CO2 with lime显示文摘 | ABANADES J C ALVEREZ D | 2003 | Energy & Fuels2003，17，2： | 1 |
| 12 | Carbon capture and storage update 显示文摘 | Boot-Handford M E Abanades J C Anthony E J | 2014 | Energy &Environ- mental Science2014，7，1： | 1 |
| 13 | Reactivity of highly cycled particles of CaO in a carbonation/calcination loop显示文摘 | Grasa G S Abanades J C Alonso M | 2008 | Chemical Engineering Journal2008，137，3： | 1 |
| 14 | Fate of heavy metals during municipal solid waste incineration显示文摘 | ABANADES S FLAMANT G GAGNEPAIN B GAUTHIER D | 2002 | Waste Manage Res2002，20，1： | 1 |
| 15 | The maximum capture efficiency of CO2 using a car- bonaton/calcinations cycle of CaO/CaCO3 显示文摘 | Abanades J C | 2002 | Chemical Engineer- ing Journal2002，90，3： | 1 |
| 16 | Cost structure of a postcombustion CO2 capture system using CaO 显示文摘 | ABANADES J C GRASA G ROMEO L M | 2007 | Environmental Science & Technology2007，41，15： | 1 |
| 17 | Average activity of CaO par- ticles in a calcium looping system 显示文摘 | Rodriguez N Alonso M Abanades J C | 2010 | Chemical Engineering Jour- nal2010，156，2： | 1 |
| 18 | CO2 capture capacity of CaO in long series of carbonation/calcination cycles 显示文摘 | GRASA G S ABANADES J C | 2006 | Ind Eng Chem Res2006，45，26： | 1 |
| 19 | Economics of CO2 capture using the calcium cycle with a pressurized fluidized bed combustor 显示文摘 | MACKENZIE A GRANATSTEIN D L ABANADES J C | 2007 | Energy & Fuels2007，21，2： | 1 |
| 20 | Pore-size and shape effects on the recarbonation performance of calcium oxide submitted to repeated calcination/recarbonation cycles 显示文摘 | Alvarez D Abanades J C | 2005 | Energy & Fuels2005，19，1： | 1 |
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