Ru-catalyzed anode materials for direct hydrocarbon SOFCs

A solid oxide fuel cell using a thin ceria-based electrolyte film with a Ru-catalyzed anode was directly operated on hydrocarbons, including methane, ethane, and propane, at 600 °C. The role of the Ru catalyst in the anode reaction was to promote the reforming reaction of the unreacted hydrocarbons by the produced steam and CO₂, which avoided interference from steam and CO₂ in the gas-phase diffusion of the fuels. The resulting peak power density reached 750 mW cm⁻² with dry methane, which was comparable to the peak power density of 769 mW cm⁻² with wet (2.9 vol.% H₂O) hydrogen. More important was the fact that the cell performance was maintained at a high level regardless of the change in the methane utilization from 12 to 46% but was significantly reduced by increasing the hydrogen utilization from 13 to 42%. While the anodic reaction of hydrogen was controlled by the slow gas diffusion, the anodic reaction of methane was not subject to the onset of such a gas-diffusion process.     

Selective hydrogenation of oleic acid to 9-octadecen-1-ol: Catalyst preparation and optimum reaction conditions

A new catalyst, ruthenium-tin-alumina is found to selectively hydrogenate oleic acid to 9-octadecen-1-ol (oleyl + elaidyl alcohol) at low pressure with high yield. Catalyst preparation methods, catalyst raw materials and activation conditions have a significant effect on the activity of the catalyst. The optimum atomic ratio of ruthenium to tin is about 1:2. Catalyst prepared by an improved sol-gel method shows higher activity and selectivity than catalysts prepared by impregnation and coprecipitation methods. Chloride is found to have a negative effect on catalytic activity. The best catalyst is prepared from chloride-free ruthenium and tin raw materials. Under the optimum reaction conditions of 250°C and 5.6 MPa, the selectivities for 9-octadecen-1-ol and total alcohol (9-octadecen-1-ol + stearyl alcohol) formation are 80.9% and 97%, respectively, at a conversion of 81.3%.     

催化裂化干气回收乙烯用于制备环氧乙烷的研究

叙述了在YS型银催化剂作用下，利用催化裂化干气回收的乙烯制备环氧乙烷的实验研究。结果表明：在银催化剂上催化氧化生成环氧乙烷的过程中，使用回收的乙烯，催化剂的初选择性可达80％；在保持环氧乙烷时空产率不变，经过2000h催化剂稳定性试验后，选择性下降了3—4个百分点，反应温度上升约10℃，与用聚合级乙烯为原料进行比较，催化剂初选择性低2—3个百分点、稳定性略差。该结果为用回收乙烯生产环氧乙烷提供了试验依据。     

HPD-2型非临氢降凝催化剂工艺实验

利用HPD-2型非临氢降凝催化剂进行了中试实验。结果表明：HPD-2型非临氢降凝催化剂相对其他的同类催化剂产品液体收率较高，最高可达95％以上；在反应温度为380℃时，凝点降幅在50℃左右，降凝效果较好；产品性质稳定，具有很好的应用前景。     

酸性盐水及其配套装置的应用与运行

介绍了对进槽盐水由酸碱性改为微酸性的技术改造，减少了副反应的发生，从而提高了电解槽的电流效率。     

光催化氧化后四环素的分解率与COD去除率之间关系的探讨

以粉状无机半导体（ＺｎＯ）为催化剂，探讨了水溶液中四环素经光催化氧化分解率和ＣＯＤ去除率之间的关系。实验表明，在本实验中四环素的分解率和ＣＯＤ去除率之间有较好的正相关性。当反庆系统中有足量的活性催化剂和足够的光照时间时，绝大部分四环素将被较彻底地氧化分解成ＣＯ２，这不仅有助于光催化反应机理的研究，助于今后在环保中的实际应用。     

二(二甲苯基)丙烷合成工艺的研究

二氯丙烷(DCP)与二甲苯在混合金属氯化物催化剂(HD90)作用下合成二(二甲苯基)丙烷,生产过程简单,产品收率高。在60—80℃的温度下,二甲苯与二氯丙烷摩尔比为6∶1,HD用量50克/摩尔DCP的条件下反应5—6小时,二(二甲苯基)丙烷的收率可达88％以上。     

聚乙烯工艺及催化剂新进展

综述国内外聚乙烯生产工艺及其催化剂的最新进展，对国内如何开展这方面的工作提出了几点建议。     

CoFe2O4超细微粒催化剂的制备,性能与表征

用溶胶－凝胶法制备了钴铁复合氧化物超细微粒催化剂，用ＴＧ－ＤＴＡ、ＴＥＭ、ＸＲＤ等手段考察了加入聚乙二醇２００对其粉体特性及催化性能的影响，结果表明，添加金属量３％的聚乙二醇２００，可显著改善粒子团聚，得到平均粒径为３０ｎｍ、分散均匀的超细粒子，在３５０℃下焙烧２ｈ，可得到前驱体分解完全，非完整晶态的ＣｏＦｅ２Ｏ４，其对对甲酚催化氧化制取对羟基苯甲醛的性能较好。     

延长Pd/C催化剂使用寿命的途径

影响钯 炭催化剂使用寿命的因素主要有催化剂失活 ,运输、装填过程中的磨损 ,工艺操作条件等。延长催化剂的使用寿命的途径有正确的运输、装填方法 ,定期冲洗 ,定期碱洗和分阶段调整氢气加入量