共查询到20条相似文献,搜索用时 125 毫秒
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以2-羟基-1,3-丙二胺和2,6-二甲酰基-4-R-苯酚(R=CH3、Cl)通过Pb2+作模板进行缩合反应制备了四亚胺双酚双核Pb(II)配合物,再用硝酸Tb(III)置换Pb(II)离子,合成了单核Tb(III)配合物[Tb(III)(H4L)(NO3)2(H2O)](NO3).2(H2O),最后再弱碱性条件下用三联吡啶置换其中的一个NO3-和一个H2O,得到目标配合物[Tb(H3L)(NO3)(C5H3N(C5H4N)2)](NO3).H2O,获得了单晶结构,并进行了晶体结构分析和系统物理表征。 相似文献
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《化学试剂》2015,(8)
以2,6-二[N-(1'-甲基-2'-羟乙基)氨甲酰基]吡啶为配体与Cd(NO3)2·4H2O反应,合成了一个单核镉(Ⅱ)配合物,通过元素分析、红外光谱、紫外光谱及X-射线单晶衍射法对其结构进行了表征。结构分析表明,该配合物属三斜晶系,P-1空间群,晶胞参数a=0.938 22(18)nm,b=0.944 74(19)nm,c=1.299 9(2)nm,α=105.687(7)°,β=95.154(6)°,γ=101.755(7)°。V=1.073 1(4)nm3,Z=2,Dc=1.757 g/cm3,μ=1.089 mm-1,F(000)=576.0。配合物的中心镉(Ⅱ)离子配位数为8,处于扭曲的四方反棱柱构型。考察了配体对Cd(Ⅱ)离子的液膜传输性,结果表明2,6-二[N-(1'-甲基-2'-羟乙基)氨甲酰基]吡啶可作为良好的Cd2+离子载体。 相似文献
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以吡啶-2,6-二甲酸为起始原料合成了一种新型β-二酮配体4-(2-乙酰基-3-氧代丁基)吡啶-2,6-二甲酸甲酯(L),其结构通过红外光谱和核磁共振氢谱得以确定。同时制备了该配体与稀土离子Eu(Ⅲ)和Tb(Ⅲ)的配合物,通过元素分析、红外光谱确定了它们的组成结构,用荧光光谱研究分析了配合物Eu(L)3.2H2O和Tb(L)3.3H2O的光致发光性能。 相似文献
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依替米贝(Ezetimibe)是一种新型选择性胆固醇吸收抑制剂,在参考相关文献的基础上,以4-羟基苯甲醛、4-氟苯胺和氯化苄为原料一步合成得到N-(4-氟苯基)-4-苄氧基苯亚甲胺(化合物2),4-(4-氟苯甲酰基)丁酸与特戊酰氯反应成混酐后在氯化锂存在下直接和(S)-4-苯基-噁唑烷酮反应再经过CBS/BH3体系还原得到(4S)-3-[(5S)-5-(4-氟苯基)-5-羟基-1-氧代戊基]-4-苯基-2-噁唑烷酮(化合物4),经三甲基硅烷基保护羟基后直接和化合物2在TiCl2(OiPr)2催化下缩合后经三水合四丁基氟化铵催化环合和Pa/C催化氢化脱保护制得,总收率92.4%×91.6%×77.7%×85.3%=56%。最终产品和部分中间体经过熔点、MS和1H-NMR测定。该工艺路线不仅减少了关键原料的使用,提高了收率,同时也增强了有羟基保护基的中间体的稳定性,简化了反应操作,更加易于工业化。 相似文献
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Harold H. Kung 《Catalysis Reviews》2013,55(2):235-259
Abstract Methanol is a basic industrial chemical that is produced in the United States at an annual rate of over one billion gallons [1]. It is used as a solvent in many industrial processes, as a starting material for the production of other compounds, notably formaldehyde, and as a freezing point suppressing agent for gasoline lines and window washing liquids, as well as for many other purposes. Traditionally, methanol has been produced by catalytic hydrogenation of carbon monoxide. 相似文献
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GEORGE W. MOREY 《Journal of the American Ceramic Society》1953,36(9):279-285
The underlying theory of hydrothermal synthesis is presented and the apparatus used is described. By way of illustration the determination of the solubility of quartz in superheated steam at high pressures and the determination of the compositions of coexisting gas and liquid phases in the system H2 O–Na2 O–SiO2 at 400°C. are discussed. 相似文献
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Harold H. Kung 《Catalysis Reviews》1980,22(2):235-259
Methanol is a basic industrial chemical that is produced in the United States at an annual rate of over one billion gallons [1]. It is used as a solvent in many industrial processes, as a starting material for the production of other compounds, notably formaldehyde, and as a freezing point suppressing agent for gasoline lines and window washing liquids, as well as for many other purposes. Traditionally, methanol has been produced by catalytic hydrogenation of carbon monoxide. 相似文献
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(4R)-苯基恶唑烷酮乙酰氯,1,5-苯并硫氮杂zhuo、三乙胺在微波辐射下反应得标题化合物。实验表明微波辐射大大加快了反应速率和提高了反应产率。 相似文献
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K. C. Waugh 《Catalysis Letters》2012,142(10):1153-1166
Methanol, like ammonia, is one of the key industrial chemicals produced by heterogeneous catalysis. As with the original ammonia catalyst (Fe/K/Al2O3), so with methanol, the original methanol synthesis catalyst, ZnO, was discovered by Alwin Mittasch. This was translated into an industrial process in which methanol was produced from CO/H2 at 400?°C and 200 atm. Again, as with the ammonia catalyst where the final catalyst which is currently used was achieved only after exhaustive screening of putative “promoters”, so with methanol, exhaustive screening of additives was undertaken to promote the activity of the ZnO. Early successful promoters were Al2O3 and Cr2O3 which enhanced the stability of the ZnO but not its activity. The addition of CuO was found to increase the activity of the ZnO but the catalyst so produced was short lived. Current methanol synthesis catalysts are fundamentally Cu/ZnO/Al2O3, having high CuO contents of?~60?% with ZnO?~?30?% and Al2O3?~?10?%. Far from promoting the activity of the ZnO by incorporation of CuO, the active component of these Cu/ZnO/Al2O3 catalysts is Cu metal with the ZnO simply being involved as the preferred support. Other supports for the Cu metal, e.g. Al2O3, MgO, MnO, Cr2O3, ZrO2 and even SiO2 can also be used. In all of these catalysts the activity scales with the Cu metal area. The original feed has now changed from CO/H2 to CO/CO2/H2 (10:10:80), radiolabelling studies having provided the unlikely discovery that it is the CO2 molecule which is hydrogenated to methanol; the CO molecule acts as a reducing agent. The CO2 is transformed to methanol on the Cu through the intermediacy of an adsorbed formate species. These Cu/ZnO/Al2O3 catalysts now operate at?~230° and between 50 and 100 atm. This important step change in the activity of methanol synthesis has resulted in a significant reduction in the energy required to produce methanol. The “step change” however has been incremental. It has been obtained on the basis of fundamental knowledge provided by a combination of surface science techniques, e.g. LEED, scanning tunnelling microscope, TPD, temperature programmed reaction spectroscopy, combined with catalytic mechanistic studies, including radiolabelling studies and chemisorption studies including reactive chemisorption studies, e.g. N2O reactive frontal chromatography. 相似文献