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The removal of toxic heavy metals by sorbents has been the focus of much recent research. In single metal/single sorbent systems, laboratory experiments have demonstrated capture of lead and cadmium by kaolinite and lime at high temperatures. However, practical systems (i.e., pulverized coal fired boilers) generally involve sodium as well as toxic metals and the amount of sodium usually exceeds that of the toxic metals. The purpose of this paper is to explore the effect of sodium on the capture of lead and cadmium by sorbents. Experiments were conducted in a 16 kW, 0.15 m ID, 6 m tall laboratory downflow furnace. Aqueous solutions of toxic metals and metal/sodium pairs were introduced into the furnace through a natural gas flame via atomization and subse quent vaporization. For all experiments, the total metal/sorbent equivalence ratio was maintained at 0.7. Approximately 0.5g/min of lime or kaolinite powder (mean particle diameter congruent 1.4 mu m) was injected along the furnace centerline in the post flame at a temperature of 1500 K. Further downstream, at 1200 K, particulate samples were isokinetically extracted and size segregated in a Berner low pressure impactor. Experimental results showed that cadmium and sodium were captured by lime. Furthermore, cadmium was captured by lime preferentially over sodium. Lead capture by lime occurred at a much slower rate than that for cadmium or sodium. Kaolinite, on the other hand, showed a preference for lead and sodium capture over cadmium. Consequently, for capture of multiple metals, a sorbent mixture of lime and kaolinite might be more effective than a single sorbent. 相似文献
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利用循环伏安法(CV)、现场红外光谱法、恒电位电解法开展了BQ在乙腈溶液中的电化学捕获CO2的研究.结果显示,CO2在BQ还原过程中被一价阴离子自由基BQ·-所捕获,表明BQ·-是可以当作亲核试剂来捕获CO2.采用恒电位电解的方法,得到了BQ电化学捕获CO2后的终产物.1H-NMR、IR、13C-NMR以及元素分析的结果表明,捕获CO2后的终产物为BQ与CO2进行化学反应的加合物,其化学计量比为1:2,且亲核进攻CO2的是BQ羰基上的氧,形成较为稳定的羧酸式结构.产物酸化处理生成对苯酚,进一步证明BQ电化学捕获CO2产物结构. 相似文献
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Model catalysts of Au clusters supported on TiO2 thin films were prepared under ultra-high vacuum (UHV) conditions with average metal cluster sizes that varied from ~2.5
to ~6.0 nm. The reactivities of these Au/TiO2 catalysts were measured for CO oxidation at a total pressure of 40 Torr in a reactor contiguous to the surface analysis chamber.
Catalyst structure and composition were monitored with Auger electron spectroscopy (AES) and scanning tunneling microscopy
and spectroscopy (STM/STS). The apparent activation energy for the reaction between 350 and 450 K varied from 1.7 to 5 kcal/mol
as the Au coverage was increased from 0.25 to 5 monolayers, corresponding to average cluster diameters of 2.5–6.0 nm. The
specific rates of reaction ((product molecules) × (surface site)-1 × s-1 were dependent on the Au cluster size with a maximum occurring at 3.2 nm suggesting that CO oxidation over Au/TiO2(001)/Mo(100) is structure sensitive.
This revised version was published online in July 2006 with corrections to the Cover Date. 相似文献
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Polarization modulation infrared reflection absorption spectroscopy (PM-IRAS) was used to investigate the effects of water on CO oxidation catalyzed by TiO2 supported Au. The introduction of water into the reactant mixture caused two effects: (1) a decrease in the CO coverage; and (2) the appearance of a carbonate species. Since both effects inhibit CO oxidation, the promotional effects of water found by previous researchers can only be rationalized by its effects on molecular oxygen adsorption and activation. Although this argument is not confirmed by the PM-IRAS data alone, this conclusion is consistent with previous studies. It is further inferred from this study that carbonate species first form on TiO2 sites and then migrate to Au sites. Surface hydroxyl species may play the same promotional role as adsorbed water. 相似文献
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以聚苯胺为原料,采用NaOH活化法,在原料与活化剂质量比为1砄4的情况下,研究了不同的活化时间(0.5 h、1 h、2 h)对多孔炭孔隙结构和CO2吸附性能的影响。通过N2吸附脱附、扫描电子显微镜(SEM)、透射电子显微镜(TEM),对样品的孔隙结构和形貌进行了表征。采用变压吸附法在常温常压下测试了样品对CO2的吸附性能。结果表明:当活化时间为1 h时,比表面积达到最大值2024 m2/g,微孔孔容达到最大值0.926 cm3/g。然而,当活化时间为0.5 h时, CO2吸附量达到了最大值159 mg/g,表明了CO2吸附量与窄微孔孔径分布有直接关系。 相似文献
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随着社会经济的迅速发展,人类对于化石燃料的需求量越来越大,燃料燃烧后排放的有害物质也越来越多,全球环境污染问题严峻,温室效应尤为严重。CO2是主要温室气体,CO2总排放量的75%是由石化燃料燃烧产生的,我国CO2排放总量的一半来自电力工业[1]。中国作为负责任的国家,到2020年,中国要实现单位国内生产总值CO2排放量比2005年下降40%~45%这一目标。因此,火电厂CO2减排任务重大,采用CO2捕集与封存技术能减少电厂80%~95%排放量,理论上具有巨大的减排潜力,是当今世界公认的CO2减排的重要途径。目前电厂捕集技术大体上分作三种:燃烧前捕集、燃烧后捕集和富氧燃烧捕集。 相似文献
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在TiO2上CO的光催化氧化 总被引:3,自引:0,他引:3
最近在“氧化的”TiO2(即表面无氧空位和Ti^3+)上进行的CO光催化氧化研究发现:室温下,以黑光灯(峰值λ=365nm)光照时,“氧化的”TiO2无CO催化氧化的活性,但以杀菌灯(峰值λ=253.7nm)光照时,则对CO产生显著的催化活性。参照CO在过渡金属表面的催化氧化机理,对本现象进行了解释:黑光灯照时,O2在TiO2表面只生成O^-2(a),而O^-2(a)不能使CO氧化,只有以杀菌灯照 相似文献
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Nattaya Comsup Joongjai Panpranot Piyasan Praserthdam 《Journal of Industrial and Engineering Chemistry》2010,16(5):703-707
Nanocrystalline TiO2 and Si-modified TiO2 with Si/Ti ratios 0.01, 0.05, 0.1, and 0.3 were prepared by the solvothermal method and employed as the supports for Ag/TiO2 catalysts for CO oxidation reaction. The incorporation of Si into the TiO2 lattice in the form of Ti–O–Si as revealed by FT-IR results could inhibit the agglomeration of TiO2 crystallites, resulting in an increase of both surface area and metal dispersion. However, there existed an optimum content of Si/Ti at ca. 0.05–0.1 which resulted in an improved catalytic activity of Ag/TiO2 in CO oxidation. Based on the O2-temperature program desorption (O2-TPD) results, the catalysts with appropriate amounts of Si/Ti exhibited higher amount of O2 adsorption and much lower desorption temperature. It is suggested that the presence of Ti–O–Si promoted the formation of active oxygen species and increased the mobility of lattice oxygen so that the catalytic activity was enhanced. There was no improvement in CO oxidation activity of the Ag/TiO2 catalyst when the Si/Ti was further increased to 0.3 due probably to the formation of amorphous SiO2 instead of the Ti–O–Si bond. 相似文献
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Rajender R. Kondakindi Snezana Aleksic William Whittenberger Martin A. Abraham 《Topics in Catalysis》2013,56(18-20):1944-1951
Worldwide increase in energy demand coupled with a continued reliance on fossil fuel resources have contributed to a significant increase in atmospheric levels of carbon dioxide. According to the International Energy Agency’s (IEA’s) World Energy Outlook 2010 main scenario, the projected growth in energy demand will translate into a 21 % rise in energy related CO2 emissions between 2008 and 2035, mostly due to robust economic growth in developing countries. This quantity of greenhouse gas emissions would make it next to impossible to meet a 2 ºC goal thought to avoid the worst consequences of global climate change without additional actions. Scenarios for stabilizing climate-forcing emissions suggest atmospheric CO2 stabilization can only be accomplished through the development and deployment of a robust portfolio of solutions, of which carbon capture and sequestration represent one component. In previous work [1], Na2CO3/Al2O3 distributed on metal foil was shown to be effective for CO2 capture. In the current work, Na2CO3/Al2O3 prepared in the powder-form and foil-form were tested in a fixed-bed reactor and characterized by X-ray diffraction, BET surface area, Raman spectroscopy and scanning electron microscopy, before and after testing, to better understand the performance of the sorbents. The powder sorbents exhibited higher performance, in general, but one of the foil samples showed the highest performance out of all the power and foil sorbents. The same sorbent was also tested for 500 cycles to understand the long-term stability. 相似文献
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In this paper we present adsorption isotherms of carbon dioxide on five different activated carbons from CHEMVIRON CARBON Belgium (Centaur HSV, BPL 410, F30-470, WS 42, Reactivated) and on a carbon molecular sieve from BERGBAU FORSCHUNG Gmbh (CMS II). The temperature is 303 K and the pressure ranges from 100 kPa up to 4000 kPa. Such conditions correspond to relative pressures ranging from 0.01 to 0.5. We also provide, for the same six sorbents, the nitrogen isotherms at 77 K (pressure: 0.001 to 100 kPa, relative pressure: 10-5 to 1). A theoretical treatment based on the Dubinin-Radushkevich and Stoeckli concept is presented and applied to the experimental results in order to obtain the micropore size distribution function (considered as Gaussian) of each sorbent. Using the CO2 data, it is possible to point out important structural differences between the six carbons. The theoretical treatment provides micropore size distribution functions in agreement with what is physically expected. Using N2 data, the structural differences are not so well marked. As a consequence, the structural parameters provided by the theoretical treatment are not reliable: except for the total micropore volume, they fluctuate strongly when changing the relative pressure domain of the used data. 相似文献
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The adsorption of CO has been measured on a 2.5 wt% Pt/TiO2 catalyst using TPD. A somewhat surprising observation is that (i) CO2 is produced, even though oxygen is not dosed into the system, (ii) repeated experiments result in the same amount of CO2 desorption. The results appear to be due to a combination of factors–(i) is due to spillover of CO from the Pt to the TiO2 support, while (ii) is due to the diffusion of Ti3+ into the bulk of the TiO2 crystallite, which effectively removes the surface non-stoichiometry which might otherwise be expected. 相似文献
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Preoxidized Au/TiO2 showed no initial activity during a first heating stage up to 70°C, while prereduction yielded a high initial CO conversion
at room temperature. With FTIRS, two different CO absorption bands were detected. One band is usually attributed to CO on
an oxidic gold species (2151 cm-1), the other one is characteristic of CO on metallic gold (2112 cm-1). The presence of the first species appears to have a detrimental effect on the CO oxidation by O2. The present results do not support a model in which the activity of supported gold catalysts in CO oxidation is ascribed
to ionic Au particles.
This revised version was published online in July 2006 with corrections to the Cover Date. 相似文献
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N. M. Gupta V. S. Kamble R. M. Iyer K. Ravindranathan Thampi M. Gratzel 《Catalysis Letters》1993,21(3-4):245-255
FTIR spectra of a Ru-RuOx/TiO2 catalyst obtained on co-adsorption of CO, CO2 and H2 in the temperature range of 300–500 K were found to be the sum total of corresponding spectra observed during methanation of individual oxides. The two oxides compete for metal sites and at each temperature they reacted simultaneously to form distinct transient Ru(CO)n type species even though the nature, the stability and the reactivity of these species were different in the two cases. The monocarbonyl species formed during adsorption/reaction of CO alone or of CO + H2 were bonded more strongly than those formed during CO2 + H2 reaction. 相似文献
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The preferential oxidation of carbon monoxide in the presence of hydrogen (PROX reaction) was studied on Cu catalysts promoted with Fe, Nb, Ce, and Ni supported on TiO2 and on TiO2 nanotubes. The surface area of the untreated TiO2 anatase (150 m2/g) support was increase to 350 m2/g when transformed into TiO2 nanotubes (NT). XRD and SEM results confirm the formation of nanotubular structures responsible of the increase in BET surface area. The activity results indicate that a 10% Cu/5% Nb/TiO2-NT catalyst is highly active for this reaction compared to other transition metals and with a catalyst with the same composition supported on untreated TiO2. We found close to 80% CO conversion and 40% selectivity to CO2 formation at 170 °C. The higher activity is ascribed to a higher dispersion of Cu on the TiO2 NT structures. 相似文献
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相对于传统的脱碳方法,中空纤维膜脱除烟气中CO2是一种清洁、高效的技术方法。运用有限单元法建立了一个疏水性中空纤维膜脱除烟气中CO2的二维模型,考察了膜丝直径、壁厚、孔隙率、曲折因子、纤维膜根数、膜柱内径和长度等方面对CO2脱除率的影响,模型结果与实验值相符。结果表明四种吸收剂的脱除率从大到小依次为EDAMEADEAAMP。当液速为0.1 m·s–1、气速0.211 m·s–1、操作压力为0.1 MPa时,减小曲折因子、膜丝壁厚和膜柱内径,增大孔隙率、膜丝内径与膜柱长度都有利于膜吸收CO2。 相似文献