用于燃料电池的甲醇水蒸气重整反应制氢的研究

研究了甲醇水蒸气重整制氢反应过程中各种因素对Cu／ZnO／Al2O3催化剂的活性和选择性的影响。结果表明：Cu／Zn比为2．0的催化剂在250℃反应时，催化剂效果较好，最合适反应条件是：压力0．1MPa，温度250℃，n(H2O)：n(CH3OH)=1．0-1．2，液体流速0．1mL／min。在Cu／ZnO／Al2O3)，催化剂上，甲醇水蒸气重整、甲醇分解和水气转换反应随反应条件的不同而发生相互抑制或促进作用。     

浅谈热泵技术在兖矿集团的应用

通过对兖矿集团所属煤矿供暖小区的现状以及能耗进行调查、分析,本文就如何采用先进的热泵技术,对矿区燃煤小锅炉进行节能技术改造展开探讨,对类似节能改造有较高借鉴作用。     

Steam reforming of glycerol for syngas generation under cold plasma conditions: A DFT study

Density functional theory (DFT) has been used to investigate the reaction pathways with steam reforming of glycerol under cold plasma conditions. Total energies, energy barriers, and reaction enthalpies at 298.15 K have been calculated at the GGA/PW91/DNP level. The calculation shows that, with the presence of steam, the energy barrier of glycerol conversion is reduced and the conversion from glycerol to H₂ and CO is promoted under cold plasma conditions. The formation of syngas was through a multi-step pathway via the conversion of OHCH₂CHOH, CH₂OH, CH₂O, HCO,·and CH₃, while the recombination of H generated extra H₂. The synthesis of hydrocarbons are from the recombination of·CH₃,·CH₂, and·CH, which could be primarily generated through glycerol dissociation. The structure of glycerol anion was also studied in this work, and it was less stable than the neutral molecule. The route for the formation of OHCH₂CHOH·and CH₂OH·from glycerol anion is thermodynamically favorable.     

富含甲烷的可再生资源重整制氢的研究进展

将富含甲烷气体的可再生资源用于重整制氢不仅可以节省天然气等不可再生资源,同时可以减少CH4、CO2等温室气体的排放,因此具有节约能源和保护环境两方面的重大意义。文章分析了可再生资源的富含甲烷气体的种类及其特性,以及该种可再生资源作为重整制氢原材料的优势和可能转化途径,并综述了国内外在这一领域近几年的研究工作,最后对富含甲烷气体的可再生资源作为制氢原料的前景进行了展望。     

基于保护的瓷窑型遗址绿化改造研究——以长沙铜官窑遗址为例

瓷窑型遗址由于其埋藏浅、需要恒温恒湿等特点,对绿化的要求与其它遗址不尽相同。基于保护为主的绿化改造是瓷窑型遗址保护的重要内容。文章以长沙铜官窑遗址为例,在分析了长沙铜官窑遗址的植被组成、绿化现状以及现有植被对遗址保护的利弊基础上,提出了基于保护为主的绿化改造总体设想、主要对策措施和技术模式,希望为中国瓷窑型遗址的绿化改造提供借鉴。     

Influence of H2S and NH3 on biogas dry reforming using Ni catalyst: a study on single and synergetic effect

● NH₃ in biogas had a slight inhibitory effect on dry reforming. ● Coexistence of H₂S and NH₃ led to faster decline of biogas conversion. ● Regeneration was effective for catalysts deactivated under synergetic effect. Biogas is a renewable biomass energy source mainly composed of CH₄ and CO₂. Dry reforming is a promising technology for the high-value utilization of biogas. Some impurity gases in biogas can not be completely removed after pretreatment, which may affect the performance of dry reforming. In this study, the influence of typical impurities H₂S and NH₃ on dry reforming was studied using Ni/MgO catalyst. The results showed that low concentration of H₂S in biogas could cause serious deactivation of catalyst. Characterization results including EDS, XPS and TOF-SIMS confirmed the adsorption of sulfur on the catalyst surface, which was the cause of catalyst poisoning. We used air calcination method to regenerate the sulfur-poisoned catalysts and found that the regeneration temperature higher than 500 °C could help catalyst recover the original activity. NH₃ in the concentration range of 50–10000 ppm showed a slight inhibitory effect on biogas dry reforming. The decline rate of biogas conversion efficiency increased with the increase of NH₃ concentration. This was related to the reduction of oxygen activity on catalyst surface caused by NH₃. The synergetic effect of H₂S and NH₃ in biogas was investigated. The results showed that biogas conversion decreased faster under the coexistence of H₂S and NH₃ than under the effect of H₂S alone, so as the surface oxygen activity of catalyst. Air calcination regeneration could also recover the activity of the deactivated catalyst under the synergetic effect of H₂S and NH₃.     

Preparation and catalytic properties of ZrO2-Al2O3 composite oxide supported nickel catalysts for methane reforming with carbon dioxide

ZrO2-Al2O3 composite oxides and supported Ni catalysts were prepared, and characterized by N2 adsorption/desorption, X-ray diffraction (XRD) and X-ray photoelectron spectroscopy (XPS) techniques. The catalytic performance and carbon deposition was also investigated. This mesoporous composite oxide is shown to be a promising catalyst support. An increase in the catalytic activity and stability of methane and carbon dioxide reforming reaction was resulted from the zirconia addition, especially at 5wt% ZrO2 content. The Ni catalyst supported ZrO2-Al2O3 has a strong resistance to sintering and the carbon deposition in a relatively long-term reaction.     

厂矿企业大宗原、燃料卸车机械安全改造技术

厂矿企业卸车机械长期运行,存在设备老化、检修频繁的现象.通过对卸车机械存在安全隐患的分析,论述了机械系统的行走机构、挖掘机构、钢结构框架、皮带输送机构、操作室和电气系统的供电电源、大车行走电机回路、卷扬电机等部件的安全改造技术.     

Simulation Study of a PEM Fuel Cell System with Steam Reforming

Abstract

This article summarizes the results of a study for a 100 kWe DC electrical power PEM fuel cell system. The system consists of a pre-steam reformer, a steam reformer, high and low temperature shift reactors, a preferential oxidation reactor, a PEM fuel cell, a combustor, and an expander. Acceptable net electrical efficiency levels can be achieved via intensive heat integration within the PEM fuel cell system. The calculations take into account the auxiliary equipment such as pumps, com pressors, heaters, coolers, heat exchangers and pipes. The process simulation package “Aspen-HYSYS 3.1’’ has been used. The operation parameters of the reactors have been determined considering all the technical limitations involved. A gasoline type hydrocarbon fuel has been studied as hydrogen rich gas source. Thermal efficiencies have been calculated for all of the major system components for selected operation conditions. The fuel cell stack efficiency has been calculated as a function of cell numbers (500, 750, 1000, and 1250 cells). Efficiencies of all of the major system components along with auxiliary unit efficiencies determine the net electrical efficiency of the PEM fuel cell system. The obtained net electrical efficiency levels are between 34 (500 cells) to 41% (1250 cells).     

石化企业污水生化处理改造措施分析

随着各炼油厂加工深度和加工能力的日益提高,排放的污水水量不断增加,水质不断恶化,原有的“老三套”中的曝气装置已无法满足生产需要。为此,不少炼油厂都针对各自的具体情况,对生化系统进行了技术改造,主要措施有：淘汰现有表曝池,改造现有表曝池,向表曝池中投加多孔物质或硝化反应与反硝化菌,增建生化预处理设施及将一级生化处理改为二级生化处理等。