焦化干气一步法预处理多功能催化剂的工业侧线试验

对焦化干气一步法预处理工艺催化剂进行了工业侧线试验。考察了温度和体积空速对催化剂的活性及催化剂稳定性和加氢选择性的影响。催化剂为以复合型ZnO和过渡金属氧化物为活性组分的多功能催化剂,用于低温下焦化干气中烯烃加氢和硫化物脱除。试验结果表明,在压力1.6MPa、温度285～350℃、空速100～500h-1的条件下,多功能催化剂能将焦化干气中烯烃的体积分数由8%～14%降至0,总硫含量从10～70μg/g脱除至5μg/g以下;经28d考核,多功能催化剂仍保持良好的烯烃加氢和硫化物脱除性能,可用于精制焦化干气。     

Hydrogen production in solar reactors

The present work summarizes the recent activities of our laboratory in the field of solar-aided hydrogen production with structured monolithic solar reactors. This reactor concept, “transferred” from the well-known automobile exhaust catalytic after-treatment systems, employs ceramic supports optimized to absorb effectively solar radiation and develop sufficiently high temperatures, that are coated with active materials capable to perform/catalyze a variety of “solar-aided” reactions for the production of hydrogen such as water splitting or natural gas reforming. Our work evolves in an integrated approach starting from the synthesis of active powders tailored to particular hydrogen production reactions, their deposition upon porous absorbers, testing of relevant properties of merit such as thermomechanical stability and hydrogen yield and finally to the design, operation simulation and performance optimization of structured monolithic solar hydrogen production reactors. This approach, among other things, has culminated to the world's first closed, solar-thermochemical cycle in operation that is capable of continuous hydrogen production employing entirely renewable and abundant energy sources and raw materials – solar energy and water, respectively – without any CO₂ emissions and holds, thus, a significant potential for large-scale, emissions-free hydrogen production, particularly for regions of the world that lack indigenous resources but are endowed with ample solar energy.     

沼气脱硫技术研究

本文综述了近年研究人员在开发沼气脱硫工艺方面所做的工作,包括现代与传统的脱硫技术工艺.探讨了物理、化学和生物脱硫技术对沼气脱硫工艺的影响因素.     

Hydriding and Dehydriding Characteristics of Mechanically Alloyed LaMg_(17) Ni Composite Material

Magnesiumandmagnesiumalloyshavebeenin vestigatedashydrogenstoragematerialsforseveralde cadesbecausefarmorehydrogenbyweightcanbestoredinthemthaninmostoftheothercurrentlyknownhydrogenstoragealloys .Moreover ,thehighnaturalabundanceofMg ,itslightmassandenviron mentalcompatibilitypotentiallymakemagnesiumoneofthemostprospectivecandidatesforfuturehydrogenstoragematerials .Unfortunately ,thepracticalappli cationofMganditsalloyshasbeenlimitedonlytocertainstoragedevicebecauseoftheirpoorhydriding dehydr…     

小型加氢站网络的成本分析

在2008年之前,上海的燃料电池汽车数量将达到百辆级规模,为了示范运行这些车辆,迫切需要建立一个有若干个加氢站组成的小型网络来提供加氢服务,为此需要确定投资运营成本。本文通过建立氢气运输成本模型(HTCM)和加氢站成本模型(HSCM),以90辆燃料电池轿车和10辆燃料电池公交车为服务对象,对由4种不同类型共5个加氢站组成的小型网络为案例,计算了每个加氢站的投资运行成本、氢气使用成本。结果表明,整个加氢站网络的年均总成本大约为769万元,而氢气的最终使用成本依据不同的供氢方式在30~77元/kg之间。     

室温离子注氢CeO2的微结构及价态研究

利用高分辨透射电子显微镜(HRTEM)及电子能量损失谱(EELS)对室温下注入氢离子的CeO2烧结体的显微组织结构和价态进行了原位观察和分析。结果表明：室温注氢，虽可以使严重损伤区内氧的状态发生明显改变，却不能引起CeO2的相转变及Ce的价态改变；这一结果可能与氢离子因尺寸太小不能占据CeO2的正常格点位置从而无法有效形成氧空位以及室温下CeO2中Ce和O的扩散比较困难等因素有关。     

纳米Fe粉的制备研究

总结了纳米Fe粉的制备方法,重点介绍了一种新的制备方法——封闭循环氢还原法。该方法以FeSO·47H2O和NaOH为原料,采用沉淀方法制备粒径为30～70nm的Fe2O3粉末,其反应条件为:反应温度50℃,反应终点pH值大于12,陈化时间1h。用封闭循环氢还原法,在400℃下还原Fe2O3得到了Fe粉。其粒径在20～50nm之间,含量为99.16%。     

膜分离法回收合成氨弛放气中氢气

介绍了膜分离的原理和应用。实践表明该方法具有效率高、流程简单、操作灵活容易、纯度高和收率高等优点。     

Hydrogen Absorption and Release Behavior in Hydrogen Decrepitation Process of Nd-Fe-B Alloys

The behavior of hydrogen absorption and release in hydrogen decrepitation (HD) process of Nd-Fe-B alloys were investigated. The results reveal that the reactivity and the amount of hydrogen absorption in HD process are related to the surface activity of the alloy so that the fresh and active surface has a higher efficiency. The presence of Nd-rich phase at the grain boundary is an essential factor of the HD activity of the alloy at room temperature. On degassing, hydrogen is released from the HD powder continuously with increasing temperature. And the residual hydrogen is as low as 0.0015% at 1073K, which shows that the hydrogen is almost exhaused. It is feasible to remove the hydrogen from the HD powder by heating treatment at the temperature of 523-723K for 1h prior to the magnetic field forming in order to decrease the harmful effect of hydrogen on the easy axis alignment of HD magnet.