Formation of isocyanic acid during the reaction of mixtures of NO, CO and H2 over supported platinum catalysts

On-line infrared spectroscopy has been used to show that isocyanic acid, HNCO, is a substantial primary product of the reaction between NO, CO and H₂ over a Pt/SiO₂ catalyst. At 230°C it accounts for more than 40% of the CO converted. No isocyanic acid is seen when Al₂O₃ is placed downstream of Pt/SiO₂, or when using a Pt/Al₂O₃ catalyst under the same conditions, due to rapid hydrolysis of HNCO on the alumina. Isocyanic acid may exist as a trace intermediate in automobile catalytic converters during their warm-up phase but it is unlikely to emerge from the pore system of aluminabased catalysts.     

Infrared studies of the interaction of carbon monoxide and dinitrogen with ferrisilicate MFI-type zeolites

Fourier transform IR spectroscopy of CO and N₂, adsorbed at liquid nitrogen temperature, was used to characterize an MFI-type H-FeZSM-5 ferrisilicate which was synthesized with a Si/Fe ratio of 50. Thermal treatment of this material at 773 and 973 K was performed in order to follow formation of extraframework species. On samples fired at 773 K Brønsted acid sites were present which gave an O-H stretching band at 3630 cm^–1. These hydroxyl groups formed adducts with both probe molecules, which were monitored by the corresponding bathochromic shift, . Corresponding values for adsorbed CO and N₂ were = –270 and = – 100, respectively. Increasing the firing temperature up to 973 K led to complete removal of iron from the zeolite framework, and consequent disappearance of Brønsted acidity. In this process, extraframework iron oxide species were formed which were also characterized by IR spectroscopy of the adsorbed probe molecules. Both CO and N₂ gave Lewis-type adducts with coordinatively unsaturated Fe³⁺ ions present in the extraframework material. A comparison is made with results of a previous study on the H-GaZSM-5 isomorph.     

非晶有机锆聚合物的制备及光催化CO2合成甲醇

采用溶剂热法在增透的多孔玻璃表面制备负载非晶态有机锆聚合物。通过SEM，XRD，BET，FTIR，UV-Vis，ICP，有机元素分析，荧光光谱（PL）及紫外光电子能谱（UPS ）等手段对催化剂进行了测试分析。非晶态有机锆聚合物（2.64 eV）具有比NH2-UiO-66(Zr)（2.74 eV）更窄的禁带宽度，更稳定的光生电子。在光催化反应器中放入2片负载非晶态有机锆的玻璃（总面积50.4 cm2），在300 W的氙灯照射下催化还原CO2合成甲醇，反应4 h后甲醇的产量为443.0 μmol，转换频率（TOF）为8.9 h-1。当0.1 g NH2-UiO-66(Zr)为催化剂时，甲醇的产量为244.3 μmol，TOF仅为0.17 h-1。非晶有机锆聚合物的光催化性能明显优于NH2-UiO-66(Zr)粉末，且循环稳定性良好。     

Low-pressure CO2 sorption in ammonium-based poly(ionic liquid)s

Ammonium-based ionic liquid monomers and their corresponding polymers [poly(ionic liquid)s] are synthesized and characterized for CO₂ sorption. The polymers have much higher CO₂ sorption capacities than the room-temperature ionic liquids and imidazolium-based poly(ionic liquid)s. For example, P[VBTMA][PF₆] with polystyrene backbone has a CO₂ sorption capacity of 10.67 mol%. The CO₂ sorption is selective over N₂ and O₂. The effects of cation, backbone, substituent, anion and crosslinking on CO₂ sorption are discussed. The sorption mechanism study indicates that CO₂ sorption by the poly(ionic liquid)s is a bulk and surface phenomenon.     

多组分氯盐体系镁锂分离规律初探

以Na₂CO₃为沉淀剂,初步研究了多组分氯盐混合体系（0.6 mol MgCl₂+1.1 mol LiCl+3.2 mol NaCl）中选择性沉镁的工艺规律。结果表明：在25~80 ℃,总C与总Mg物质的量比[n（C_T）/n（Mg_T）]为 0.8~1.1时,25 ℃形成针状MgCO₃·3H₂O,40 ℃以上形成Mg₅（CO₃）₄（OH）₂·4H₂O不规则片状团聚微球,其中40~50 ℃形成的片状物较为分散且粒径较小,导致固液分离困难。40 ℃时沉镁率最低。温度越高,Li₂CO₃越易形成,沉锂率越大。n（C_T）/n（Mg_T）越大沉镁率和沉锂率越高。室温（25 ℃）、n（C_T）/n（Mg_T）=1.0时,沉镁率达98%以上,且沉锂率<0.1%,镁锂分离效果最好。     

High catalytic activity of PdOx/MnO2 for CO oxidation and importance of oxidation state of Mn

PdO_x/MnO₂ has been examined as a catalyst for CO oxidation using a conventional flow reactor at reaction temperatures between 50 and 150°C. In the reaction conditions of GHSV (gashourlyspacevelocity) of 1.22 × 10⁵/h and CO concentration of 2000 ppm, PdO_x/MnO₂ showed higher catalytic activity compared with PdO_x/Mn₂O₃, which had been previously reported as an effective catalyst due to the cooperative action of Pd and Mn₂O₃ for this reaction. The reason for higher activity of PdO_x/MnO₂ than PdO_x/Mn₂O₃ has been investigated using TPR (temperatureprogrammed reduction) and XPS studies. TPR showed that PdO_x/MnO₂ could be reduced by CO at much lower temperature than PdO_x/Mn₂O₃. During the experiment of reduction and oxidation, XPS showed that the valence of Mn in the PdO_x/MnO₂ was between 4+ and 3+, which is higher than that of Mn in the PdO_x/Mn₂O₃ catalyst of which the valence has been reported to be between 3+ and 2+. It is known that in this catalyst system the support supplies oxygen onto Pd, where the oxidation occurs with adsorbed CO, and the ability of the support to provide oxygen improves the performance of the catalyst. Therefore, it was concluded that the readiness of MnO₂ to be reduced with maintaining a higher oxidation state showed higher CO oxidation activity than Mn₂O₃ as support for PdO_x.     

低CO2选择性的合成气制轻烯烃双功能催化剂

为开发高活性、高收率的合成气制低碳烯烃（STO）双功能催化剂，通过共沉淀法制备非化学计量尖晶石Zn-Cr-Al氧化物，对其织构性质、晶体结构、形貌特征以及表面电荷性质等进行研究。结果表明添加过量锌能够促进晶体粒径减小，表面氧空位增多。其中Zn/(Cr+Al)摩尔比为1.25时锌含量较为适宜，将其与SAPO-34沸石分子筛结合为双功能催化剂用于STO性能研究。在进气n(H2):n(CO)=2:1，3000 mL/(gcat·h)，3.2 MPa，400 ℃反应条件下，实现46.9% CO转化率，C2-4烯烃收率高达15.9%，高于大部分已有文献报道（8~14%），特别是副产物CO2选择性仅29.2%，低于普遍报道的40~50% CO2选择性。并且催化剂运行100 h后活性良好，稳定的催化性能使其具有工业应用价值。     

超支化含苯基聚硅氧烷亲二氧化碳特性及其分子模拟

通过水解缩聚法制备含有不同苯基含量的超支化聚硅氧烷，探究苯基的引入对超支化聚合物在CO2中溶解性能的影响。浊点压力测试得出苯基的引入在超支化结构中对聚合物在CO2中的溶解度影响不大，超支化聚合物中苯基含量的增加没有导致浊点压力的明显升高，有望实现作为CO2增稠剂兼具较好的溶解度和增稠性能。分子模拟计算分析了超支化聚硅氧烷和直链聚硅氧烷与CO2分子间的相互作用以及超支化聚硅氧烷分子间的相互作用，发现含苯基的超支化聚硅氧烷具有更低的内聚能密度（CED）和溶解度参数（δ），表现出更弱的聚合物分子间相互作用，有利于超支化有机硅氧烷在CO2体系中的溶解。     

Modification of catalytic performances due to the co-feeding of hydrogen or carbon dioxide in the partial oxidation of methane over a NiO/γ-Al2O3 catalyst

The influence of the addition of 1–10 vol.% of hydrogen or carbon dioxide to the feed during the partial oxidation of methane was studied over a NiO/γ-Al₂O₃ catalyst. The addition of H₂ decreases the conversion and syngas selectivity. This decrease of performance seems to be related to a higher reduction of the catalyst due to the H₂ co-feeding. The addition of CO₂ also appears unfavorable to the production of hydrogen but increases the CO yield. A combination of the dry reforming and the reverse water gas shift reactions is suggested to explain the observed modifications in the product yields.