α’-苯磺酰基-α，β-不饱和酮与开链二烯烃的不对称催化环加成反应

在手性金属钛催化剂存在下，研究了α’—苯磺酰基—α，β-不饱和酮与开 链二烯的不对称催化环加成反应，讨论了α’—苯磺酰基—α，β—不饱和酮与开 链二烯的反应活性和对映选择性，以高的收率和光学纯度合成了环己烯衍生物，并 对部分产物的构型进行了鉴定．     

Ru-[bmim]BF4 的制备及催化苯选择加氢反应性能

以离子液体1-丁基-3-甲基咪唑四氟硼酸盐([bmim]BF4)-水混合溶剂为介质,采用化学还原法制备了Ru-[bmim]BF4催化剂,并利用紫外-可见光谱、红外光谱、透射电镜、X射线衍射和X射线光电子能谱对催化剂进行了表征.结果表明,Ru在[bmim]BF4中分散较好,粒径~2nm,且离子液体中咪唑阳离子与部分Ru形成了金属卡宾配合物.利用苯选择加氢反应对该催化剂性能进行了评价,发现Ru-卡宾配合物存在时,催化剂活性较低,但环己烯选择性较高.在本文反应条件下,苯转化率为12.2%,环己烯选择性为40.5%.重复使用该催化剂时,由于Ru-卡宾配合物在反应中转变为Ru0,其催化活性增加,但环己烯选择性下降.继续多次使用该催化剂,其性能基本保持稳定.     

河南贫煤不同温度燃烧烟气中环烃类产物的分析研究

本文用色谱／质谱／红外联用系统研究了河南贫煤在不同温度下燃烧释放的烟气二氯甲烷富集液中的脂环烃，苯系物，多环芳烃及杂多环芳烃等环烃类物的组成和差异，尤其是对多环芳烃的种类，含量及分布特征进行了较详细的探讨。并与原煤常温二氯甲烷浸取中各化合物组成进行了对照。     

含吡啶、噻吩环大环化合物的合成及其与Cu(Ⅱ)的配合行为

以2，6－二溴甲基吡啶及2，5－二氯甲基噻吩分别与对甲基苯磺酰胺进行缩合反应得到新的大环化合物1，9，17，25－四对甲基苯磺酰基大环多胺｛[32]-Py4N4Ts4｝与1，8，15，22－四对甲基苯磺酰基大环化合物｛[28]-Th4N4Ts4｝。其中[32]－Py4N4Ts4在浓硫酸中脱去四个对甲基苯磺酰基后又得到新的大环多胺化合物[32]-Py4N4H4，并由紫外吸收光谱测定出其与Cu（Ⅱ）配合的配位比为1：2，证明形成了双核配合物。     

Y2O3掺杂ZrO2对苯选择加氢制环己烯催化剂Ru-La-B/ZrO2性能的影响

用水热合成法制备了纳米Zr O2和Y2O3掺杂的Zr O2(Zr O2-Y),并考察了它们作载体对苯选择加氢制环己烯催化剂Ru-La-B/Zr O2性能的影响。结果表明,2种Zr O2具有相同微晶尺寸、织构性质和粒度分布。但Zr O2仅含有单斜相Zr O2,而Zr O2-Y不但含有单斜相Zr O2,还含有一部分四方相Zr O2。Y2O3掺杂影响Zr O2的组成和物相,进而影响用其制备催化剂的组成和物相。掺杂的Y2O3可以占据一部分不适宜苯加氢生成环己烯的活性位。因此,Zr O2-Y负载Ru-La-B催化剂活性明显低于Zr O2负载的,在低苯转化率下环己烯选择性前者比后者高。由于四方相Zr O2表面羟基比单斜相少,Zr O2-Y负载Ru-La-B催化剂的亲水性比Zr O2负载的差。环己烯不易从Zr O2-Y负载的催化剂表面脱附。当苯转化率高于52%时,Zr O2-Y负载的催化剂的环己烯选择性低于单斜相Zr O2负载的。Zr O2负载的Ru-La-B催化剂上20 min的环己烯收率达到了52.1%,而Zr O2-Y负载的环己烯收率仅45.2%。纳米单斜相Zr O2较适宜作苯选择加氢制环己烯Ru催化剂的载体。     

二氧化硅负载磷钼酸铯催化苯液相硝化反应的研究

采用溶胶-凝胶法制备了二氧化硅负载磷钼酸铯催化剂,利用XRD、IR以及电位滴定等方法对催化剂进行了表征,并初步评价了催化剂的苯液相硝化反应催化性能。结果表明,溶胶-凝胶法制备的二氧化硅负载磷钼酸铯具有典型的Keggin结构,且在苯液相硝化反应中表现出优良的催化性能;催化剂用量、反应时间和温度等反应参数对催化苯液相硝化反应有明显的影响,在优化实验条件下,苯硝化转化率可达95%;催化剂可回收重复使用,多次反应后催化剂活性组分有所损失,但催化剂整体物相和结构没有发生明显变化。     

冠醚化双西佛碱钴(Ⅱ)配合物的合成、氧合和催化氧化性能 研究

合成和表征了三个新的冠醚化双西佛碱4',5'-双(2-羟基苯亚甲基亚氨基)苯并-12-冠-4(L^1H2),4',5'-双(5-氯-2-羟基苯亚甲基亚氨基)苯并-12-冠-4(L^1H2)和4',5'-双(5-溴-2-羟基苯亚甲基亚氨基)苯并-12-冠-4(L^3H2)以及它们的钴配合物。在吡啶溶液中和不同温度下,测定了配合物的饱和吸氧量,求出了它们的氧加合常数和热力学参数△H°,△S°,并以这些配合物为催化剂,活化分子氧氧化环已烯制备环已烯酮,通过与未冠醚化的类似物作比较,讨论了冠醚环的引入对配合物与氧分子加合性能以及催化氧化性能的影响。     

负载型非晶态催化剂Ru-B/TiO2的制备及应用

本工作用浸渍法和沉淀法制得了两种负载型非晶态催化剂Ｒｕ－Ｂ／ＴｉＯ２「ｗ（Ｒｕ）＝５％」。Ｘ射线衍射和差动热分析实验结果证实了Ｒｕ以非晶态形式存在,这两种非晶态催化剂在温和条件下对苯和环己烯均具有很高的催化加氢活性并对ＣＳ２也有良好的抗毒性能,在９０℃,０．２２ＭＰａ条件下,苯在这两种非晶态催化剂上加氢生成环己烷的转化率分别为９９．４％和９１．０％;当环己烯中ＣＳ２的含量为２．５％时环己烯在这两种催化剂上的加氢转化率分别为１００％和３１．３％。     

1,4-二乙氧基苯的相转移催化合成

采用大孔型交联聚苯乙烯为载体研究制得新型季Lin盐型相转移催化剂Y98B，并将其于1，4－二乙氧基苯的催化合成反应，进行了产品的红外光谱分析和熔点测定，探讨了催化剂用量、对苯二酚与溴乙烷物的质量比、反应温度和反应时间等动力学条件对产品收率的影响。确定了在反应温度为70℃,mol对苯二酚：mol溴乙烷＝1：3．5，反应时间4h，催化剂用量3．0g的条件下产品收率可达84.3%。     

一种新型Ru-Zn体系催化苯选择加氢制环己烯的研究

制备了一种新型苯选择加氢制环己烯Ru-Zn催化剂.研究表明,该催化剂不但具有较好的活性选择性,而且具有稳定的晶态结构,良好的沉降分离性能.Zn/Ru比为8/92时,15min环己烯的收率达48.3%.利用XRD和物理吸附仪等手段对催化剂进行了表征.XRD证实了Ru和Zn形成固溶体,并观察到金属锌物相的存在.     

Advanced Methodologies for Sampling and Analysis of Toxic Organic Chemicals in Ambient Outdoor,Indoor, and Personal Respiratory Air

Many different kinds of sampling devices and analytical techniques are required to assess the potential adverse effects of toxic air pollutants on human health and the ecosystem. The U.S. Environmental Protection Agency has an on-going research and development program designed to provide the necessary tools to monitor air quality both outdoors and indoors and to measure personal respiratory exposures. Particular emphasis in recent years has been placed on real-time and integrative methods for neutral and polar volatile organic chemicals (e.g., chlorinated hydrocarbons, single-ring aromatics, alcohols, aldehydes, ethers, thiols, nitriles) and semi-volatile organics (e.g., polynuclear aromatics, nitrated aromatics, pesticides, phenols). Samplers capable of obtaining sufficient quantities of chemicals for ultratrace analyses and sometimes bioassay, that are also quiet, unobtrusive and user-friendly, are being developed and evaluated for indoor, outdoor, and personal monitoring. New analytical techniques such as matrix-isolation GC/FTIR, and supercritical fluid extraction and chromatography are being adapted to characterize collected samples.     

Selective transalkylation of polynuclear aromatics over solid acid catalysts

A selective transalkylation technique in the linear position of polynuclear aromatics, including biphenyl and related polynuclear aromatics, naphthalene, and dibenzofuran, is reviewed in comparison with the shape-selective alkylation over zeolite catalysts. Steric hindrance and electron density at the substitution sites of polynuclear aromatics are two influential factors for the selectivity.     

超临界相由合成气合成低碳醇的研究

选择有代表性的Ｃｕ－Ｃｏ,Ｚｎ－Ｃｒ和ＺＲ－Ｍｎ体系为催化剂,研究了超临界条件下由合成气 民低碳醇的规律及提高产物中Ｃ２＋ＯＨ含量的可能性。结果表明,三种催化剂上超临界相合成醇反应的ＣＯ转化率都比气相合成醇反应的高。Ｃｕ－Ｃｏ催化剂上超临界相合成反应的醇选择性低于气相合成者,但合成醇的产物与气相合成的相同,且均符合Ｓｃｈｕｌｚ－Ｆｌｏｒｙ分布。Ｚｎ－Ｃｒ和Ｚｒ－Ｍｎ催化剂上的产物分布不符合Ｓｃｈｕ     

Hydroformylation of propylene in supercritical CO2 + H2O and supercritical propylene + H2O

Hydroformylation of propylene has been carried out in supercritical CO₂ + H₂O and in supercritical propylene + H₂O mixtures using Rh(acac)(CO)₂ and triphenylphosphine trisulfonate trisodium salt (TPPTS), P(m-C₆H₄SO₃Na)₃, as catalyst. Visual observation of the reaction mixtures indicates that in both systems a single phase is present at supercritical temperatures and pressures so that the reaction occurs under homogeneous conditions. After reaction is complete, a biphasic system is formed when the pressure and temperature are reduced to ambient. This facilitates separation of the products in the organic phase and the rhodium catalyst in the aqueous phase. The rhodium concentration in the organic phase was found to be negligible (1.0 × 10⁻⁶ mg/ml). Furthermore, compared with traditional hydroformylation technology, the supercritical reactions also show better activity and selectivity.     

不同结构的芳烃对加氢裂化催化剂积炭的影响

在高压连续流动微型反应器上采用催速老化技术考察了不同结构的芳烃在加氢裂化催化剂上积炭行为，并用热分析、傅立叶变换红外和物理吸附仪等手段对积炭催化剂的积炭类型、酸强度分布和孔结构的变化进行了研究。结果发现：单环芳烃中，随着取代基的碳链长度、数目及不饱和度的增加，催化剂更容易积炭。稠环芳烃的环数越多，反应生成的总积炭和假石墨型积炭越多。积炭越多的催化剂，比表面积降低越多。积炭主要沉积在催化剂的小孔内或堵塞小孔孔口，有些积炭在催化剂表面形成机械孔。积炭后，催化剂上不同强度的酸数目均较新鲜催化剂降低，尤其是萘和菲，使强酸严重削弱。     

空气中苯系物的TiO2光催化降解研究进展

本文对近年来空气中挥发性苯系物的TiO2光催化降解机理、TiO2光催化降解苯系物的主要影响因素以及TiO2的失活与再生方法等的研究进展进行了较详尽的评述,并对今后的研究工作进行了展望。     

The effects of modifiers in supercritical fluid chromatography

Investigations have been initiated to examine the basic elements of resolution and how they vary individually and collectively in terms of modifiers used in supercritical fluid chromatography (SFC). Capacity factors (k′) have been determined for a mixture of polynuclear aromatic hydrocarbons from SFC experiments as function of modifier identity and concentration using different stationary phases. Using carbon dioxide as the primary mobile phase, the modifiers investigated included methanol, 2-methoxy ethanol, 1-propanol, tetrahydrofuran, dimethyl sulfoxide, acetonitrile, sulfur hexafluoride, and freon 11.     

On-Line coupling of supercritical fluid extraction with high performance liquid chromatography

Supercritical fluid extraction was coupled directly with high performance liquid chromatograph. The system was evaluated for direct injection of supercritical CO₂ and modified supercritical CO₂ at high pressure and temperature onto a HPLC system with varying mobile phase compositions and flow rates. Injection of 9 μL supercritical CO₂ onto the HPLC using methanol/water mobile phases from 100% methanol to 80% with a flow of 1.0 mL/min did not adversely affect the baseline of UV detector. However at higher percentages of water, CO₂ solubility in the mobile phase decreased and caused baseline interferences on the UV detector. At higher HPLC mobile phase flow rates, supercritical CO₂ was injected to higher percentages of water without any effect on the UV baseline. Also, increasing the extraction pressure or modifier concentration did not change the results. Separations of polynuclear aromatic hydrocarbons and linear alkenebenzene sulfonate test mixtures were obtained using on-line SFE/HPLC interfaced system.     

Photoelectron spectroscopy and substituent effects in halonaphthalenes

The electronic structure of two isomeric dibromonaphthalenes (C(10)H(6)Br(2)) has been investigated by HeI/HeII photoelectron spectroscopy. The spectra were assigned by Green's functions calculations and comparison with the spectra of related dibromobenzenes (C(6)H(4)Br(2)). The analysis of pi-orbital and halogen lone pair ionization energies, enabled us to determine the magnitude of bromine-bromine intramolecular interactions and distinguish between through-bond and through-space type interactions. We also discuss the halogen-halogen interactions in other polynuclear aromatics.     

Effect of CO2/CO Addition in Dehydroaromatization of Methane on Zeolite-Supported Mo and Re Catalysts Towards Hydrogen, Benzene and Naphthalene

High activity and high formation selectivity for aromatics in the dehydrocondensation reaction of methane were realized only on selected catalysts. The requisites of a metal and a zeolite support as the selected catalyst were described. However, the catalytic activity steadily declined even on the selected catalysts with time on stream because of coke accumulation. A stable catalytic activity was obtained when CO₂ or CO was added into methane feed due to effective removal of coke from the catalyst surface by CO or CO₂. The route from methane to aromatics and the formation process of active phase of catalyst were discussed.