氧糖剥夺条件下PC12细胞RAGE的表达及对其损伤的影响

目的探讨大鼠肾上腺嗜铬细胞瘤(PC12)细胞在氧糖剥夺(OGD)的条件下,晚期糖基化终产物受体(RAGE)的表达及其对PC12细胞损伤的影响。方法PC12细胞随机分为3组:OGD培养组(PC12细胞在无血清无糖的DMEM培养液中厌氧培养);封闭RAGE的OGD培养组(PC12细胞在加5μg/mlRAGE抗体的无血清无糖DMEM培养液中厌氧培养);对照组(PC12细胞在无血清无糖DMEM培养液中培养)。免疫组化法检测RAGE表达。收集细胞上清液,检测乳酸脱氢酶(LDH)活性和一氧化氮(NO)含量,并对细胞死亡率进行检测。结果在OGD条件下PC12细胞培养8、11、20h均有RAGE表达,与对照组相比表达均明显增加,OGD培养组与封闭RAGEOGD培养组相比,LDH活性差异显著。随着厌氧时间的延长,PC12细胞死亡率明显增高,封闭RAGEOGD培养组与OGD培养组相比,PC12细胞死亡率明显降低。NO含量差异无显著意义,但与对照组相比差异显著。结论在OGD条件下,PC12细胞RAGE表达增高。RAGE的表达对细胞的损伤起促进作用。     

Hydrolytic decomposition of dichlorodifluoromethane on modified zirconium oxide surfaces

The hydrolytic decomposition of dichlorodifluoromethane (CFC-12) on various modified zirconium oxide surfaces has been studied. The reaction was carried out under flow conditions at 500°C. Complete CFC-12 conversion and long-time stability of the catalysts were achieved accompanied by a limitation of the undesired CFC-13 formation. A maximum CFC-12 conversion was observed on catalysts of sulfated zirconia or zirconia obtained from temperature-controlled calcination of zirconium oxide hydrate. The reaction depends on the presence or in situ formation of Brønsted acid sites. FTIR-photoacoustic measurements were performed on pyridine complexes chemisorbed on the catalyst surface in order to analyze the changes in the catalyst's acidity. The effects of the temperature and water in the reaction gas on the catalyzed decomposition of CFC-12 are examined.     

H4SiW12O40-PAn催化剂催化合成苯甲醛乙二醇缩醛

报道了以自制的H4SiW12 O40 (硅钨酸 ) -PAn (聚苯胺 )为催化剂 ,通过苯甲醛和乙二醇为原料合成了苯甲醛乙二醇缩醛。实验表明 :合成苯甲醛乙二醇缩醛适宜反应条件为 :n(苯甲醛 ) /n(乙二醇 ) =1 /2 .0 ,催化剂用量为反应物料总质量的 1 .0 % ,环己烷为带水剂 ,反应时间 1 .0h。上述条件下 ,苯甲醛乙二醇缩醛的收率可达 86.7% .     

Minor components in the sex pheromone of legume podborer: Maruca vitrata development of an attractive blend

The legume podborer, Maruca vitrata (syn. M. testulalis) (F.) (Lepidoptera: Pyralidae) is a pantropical pest of legume crops. Sex pheromone was collected by gland extraction or trapping of volatiles from virgin female moths originating in India, West Africa, or Taiwan. Analysis by GC-EAG and GC-MS confirmed previously published findings that (E,E)-10,12- hexadecadienal is the most abundant EAG-active component with 2–5% of (E,E)-10,12-hexadecadienol also present. At least one other EAG response was detected at retention times typical of monounsaturated hexadecenals or tetradecenyl acetates, but neither could be detected by GC-MS. Laboratory wind-tunnel bioassays and a field bioassay of blends of (E,E)-10,12-hexadecadienal with (E,E)-10,12-hexadecadienol and a range of monounsaturated hexadecenal and tetradecenyl acetate isomers indicated greatest attraction of males was to those including (E,E)-10,12-hexadecadienol and (E)-10-hexadecenal as minor components. In subsequent trapping experiments in cowpea fields in Benin, traps baited with a three-component blend of (E,E)-10,12-hexadecadienal and these two minor components in a 100:5:5 ratio caught significantly more males than traps baited with the major component alone, either two-component blend, or virgin female moths. Further blend optimization experiments did not produce a more attractive blend. No significant differences in catches were found between traps baited with polyethylene vials or rubber septa, or between lures containing 0.01 and 0.1 mg of synthetic pheromone. Significant numbers of female M. vitrata moths, up to 50% of total catches, were trapped with synthetic blends but not with virgin females. At present there is no clear explanation for this almost unprecedented finding, but the phenomenon may improve the predictive power of traps for population monitoring.     

Study of the sorption and acidic properties of MTW-type zeolite

The acidity of H-MTW-type zeolite has been investigated using infrared spectroscopy of adsorbed pyridine. Pore volume has been measured by nitrogen andn-hexane adsorption. The zeolite exhibits infrared signals at 3612 and 3580 cm^–1 tentatively attributed to bridging hydroxyl groups vibrating in the main channel and in the six-membered rings of the structure, respectively. Both hydroxyl groups possess high acid strength and are readily accessible to pyridine. H-MTW shows an-hexane cracking activity at 350°C comparable to that obtained with MFI and BEA-type materials with a product selectivity between medium and large pore structural types.     

磷钨杂多酸催化剂制备工艺的放大研究

采用经典酸化-乙醚萃取法制备Keggin结构的磷钨杂多酸,在前期优化实验基础上,制备规模放大20倍进行工艺研究,以考察放大效应.实验得到最佳的制备工艺条件为:钨酸钠250 g,磷酸氢二钠40 g,加酸量为160 mL,在85 ℃的温度下反应2.5 h,磷钨酸的收率达到89.3%.并运用红外光谱(IR)、X射线衍射(XRD)、热重分析(TG-DSC)和Hammett指示剂法对最佳工艺制得的磷钨杂多酸进行了结构表征和酸性表征,结果表明制得的产品是Keggin结构且具有很强的酸性;以混合二元酸(丁二酸、戊二酸、己二酸)与正丁醇的酯化反应为探针反应,酯化率为衡量标准对催化剂进行性能表征,结果表明其对酯化反应具有很好的催化活性,放大后无明显的放大效应.     

Selective catalytic reduction of NO by ammonia using mesoporous Fe-containing HZSM-5 and HZSM-12 zeolite catalysts: An option for automotive applications

Mesoporous and conventional Fe-containing ZSM-5 and ZSM-12 catalysts (0.5–8 wt% Fe) were prepared using a simple impregnation method and tested in the selective catalytic reduction (SCR) of NO with NH₃. It was found that for both Fe/HZSM-5 and Fe/HZSM-12 catalysts with similar Fe contents, the activity of the mesoporous samples in NO SCR with NH₃ is significantly higher than for conventional samples. Such a difference in the activity is probably related with the better diffusion of reactants and products in the mesopores and better dispersion of the iron particles in the mesoporous zeolite as was confirmed by SEM analysis. Moreover, the maximum activity for the mesoporous zeolites is found at higher Fe concentrations than for the conventional zeolites. This also illustrates that the mesoporous zeolites allow a better dispersion of the metal component than the conventional zeolites. Finally, the influence of different pretreatment conditions on the catalytic activity was studied and interestingly, it was found that it is possible to increase the SCR performance significantly by preactivation of the catalysts in a 1% NH₃/N₂ mixture at 500 °C for 5 h. After preactivation, the activity of mesoporous 6 wt% Fe/HZSM-5 and 6 wt% Fe/HZSM-12 catalyst is comparable with that of traditional 3 wt% V₂O₅/TiO₂ catalyst used as a reference at temperatures below 400 °C and even more active at higher temperatures.     

用KF／Al2O3催化合成肉桂酸的研究

采用KF/Al2O3催化剂催化合成肉桂酸，用新催化剂催化反应可以降低反应温度。缩短反应时间。提高肉桂酸的产率，探索出了最佳反应条件；当反应温度控制在16℃，苯甲醛和乙酸酐的摩尔比1：3，用6.0gKF/Al2O3催化反应1.0h，得到肉桂酸的产率为85.4%。     

F-12纤维表面处理对复合材料壳体纤维强度转化率的影响

对F-12纤维表面进行聚合物涂层改性，通过NOL环复合材料剪切强度测试，研究不同浓度的聚合物表面处理液对复合材料层间剪切强度的影响．结果表明：F-12纤维表面经TDE-85／DDM体系处理后，复合材料层间剪切强度均高于未表面处理的纤维；当刚性涂层液质量分数为5％时，层间剪切强度最高，比未表面处理的纤维高50％左右．φ150mm容器爆破试验结果表明，F-12纤维表面经涂层液处理后，复合材料壳体纤维强度转化率平均提高2．3％，容器特性系数平均提高12．5％．     

Heterogeneous asymmetric reactions. 23. Enantioselective hydrogenation of ethyl pyruvate over cinchonine- and α-isocinchonine-modified platinum catalysts

The enantioselective hydrogenation of ethyl pyruvate to (S)-ethyl lactate over cinchonine- and 12vn2x82w47805w/xxlarge945.gif" alt="agr" align="BASELINE" BORDER="0">-isocinchonine-modified Pt/Al₂O₃ catalysts was studied as a function of modifier concentration and reaction temperature. The maximum enantioselectivities obtained under the applied mild conditions were 89% ee using cinchonine (0.014 mmol12vn2x82w47805w/xxlarge8201.gif" alt="thinsp" align="MIDDLE" BORDER="0">dm^–3, 1 bar H₂, 2312vn2x82w47805w/xxlarge8201.gif" alt="thinsp" align="MIDDLE" BORDER="0">°C, 6% AcOH in toluene), and 76% ee in the case of 12vn2x82w47805w/xxlarge945.gif" alt="agr" align="BASELINE" BORDER="0">-isocinchonine (0.14 mmol12vn2x82w47805w/xxlarge8201.gif" alt="thinsp" align="MIDDLE" BORDER="0">dm^–3, 1 bar H₂, –1012vn2x82w47805w/xxlarge8201.gif" alt="thinsp" align="MIDDLE" BORDER="0">°C, 6% AcOH in toluene). Since 12vn2x82w47805w/xxlarge945.gif" alt="agr" align="BASELINE" BORDER="0">-isocinchonine of rigid structure exists only in 12vn2x82w47805w/xxlarge8220.gif" alt="ldquo" align="MIDDLE" BORDER="0">anti-open12vn2x82w47805w/xxlarge8221.gif" alt="rdquo" align="MIDDLE" BORDER="0"> conformation these data provide additional experimental evidence to support the former suggestion concerning the dominating role of 12vn2x82w47805w/xxlarge8220.gif" alt="ldquo" align="MIDDLE" BORDER="0">anti-open12vn2x82w47805w/xxlarge8221.gif" alt="rdquo" align="MIDDLE" BORDER="0"> conformation in these cinchona-modified enantioselective hydrogenations.