金属富勒烯La@C2的合成,提取及其ESR和MS表征

采用对掺入Ｌａ２Ｏ３的石墨棒原位活化并结合交换电极回放方法制备了产率较高的金属富勒烯，并用甲苯温热提取的方法有效地提取的Ｌａ＠Ｃ２ｎ，其中Ｌａ＠Ｃ７１为可溶性金属富勒烯增加了新成员，同时，首次采用解吸电子轰击质谱对提取物进行了表征，讨论了提取物的ＥＳＲ谱。     

C40,Nb@C40^＋,La@C40^＋的从头算研究

用量子化学从头算方法研究了Ｃ４０、Ｎｂ＠Ｃ４０＾＋，Ｌａ＾＠Ｃ４０＾＋的几何构型和电子结构，Ｃ４０最稳定构型具有Ｄ２对称性。Ｌａ和Ｎ原子内含于Ｃ４０笼中，形成金属夹心碳笼Ｎｂ＠Ｃ４０＾＋、Ｌａ＠Ｃ４０＾＋。Ｃ４０结合能大于Ｍ＠Ｃ４０＾＋（Ｍ＝Ｎｂ，Ｌａ）。     

CaO／La2O3催化剂上的甲烷氧化偶联反应的研究

研究了不同配比的ＣａＯ／Ｌａ_２Ｏ_３催化剂对甲烷氧化偶联反应的催化性能。适当配比的ＣａＯ／Ｌａ_２Ｏ_３催化剂的性能明显优于纯Ｌａ_２Ｏ_３或ＣａＯ，在钙含量为２４％和８１％（Ｃａ／（ｃａ＋Ｌａ））处，Ｃ_２选择性和Ｃ_２收率分别出现两个峰值。同时还发现，１３％ＣａＯ／Ｌａ_２Ｏ_３样品显示出良好的低温催化性能，在５５０℃反应温度下获得了３１．５％的甲烷转化率和４５％的Ｃ_２选择性。并采用ＸＲＤ、ＸＰＳ和Ｃｏ_２ＴＰＤ等技术研究了催化剂的结构。结果表明，ＣａＯ／Ｌａ_２Ｏ_３体系催化剂上没有检测到新物相产生。但是，催化剂中ＣａＯ与Ｌａ_２Ｏ_３两组分之间存在着相互作用，有利于表面活性中心的形成。     

1－苯基－3－甲基－4－苯甲酰基－5－吡唑啉酮（HPMBP）与金属离子配合物的结构研究──（Ⅲ）La（pmbp）_3（H_2O）_2的合成与晶体结构

报道标题化合物Ｌａ（ＰＭＢＰ）_３（Ｈ_２Ｏ）_２，Ｈｐｍｂｐ＝Ｃ_（１７）Ｈ_（１４）Ｎ_２Ｏ_２的合成及晶体结构，晶体属于单斜晶系，空间群Ｃ２／ｃ，晶体学数据：ａ＝２４．７４４（５），ｂ＝１６．３２５（６），ｃ＝２５．８７１（５），β＝１０５．４４（３）°，Ｖ＝１００７３（２）３，Ｍ_ｒ＝１００６，Ｚ＝８，Ｄ_ｘ＝１．３２８ｇ／ｃｍ~（－３），μ＝９．０４２ｃｍ~（－１），Ｆ（０００）＝４０９４。最终偏离因子Ｒ＝０．０４９，Ｒ_ｗ＝０．０５９。分子中Ｌａ（Ⅲ）与８个氧原子配位形成三角十二面体构型，Ｌａ－Ｏ平均键长为２．４９６（２）。     

LaCl_3－SrCl_2－MgCl_2三元体系相图

本文借助于ＤＴＡ和Ｘ射线结构分析测定了ＬａＣｌ_３－ＳｒＣｌ_２－ＭｇＣｌ_２三元体系相图，发现它属简单低共熔型，体系内有对应于ＬａＣｌ_３、ＳｒＣｌ_２和ＭｇＣｌ_２的３个液相面、３条２次结晶线和１个三元低共熔点Ｅ（１５．０ｗｔ％ＬａＣｌ_３，４９．５ｗｔ％ＳｒＣｌ_２，３５．５ｗｔ％ＭｇＣｌ_２；５４５℃），并且在固相下有一个不稳定的化合物生成，在约５００℃时分解。     

LaCl_3·3H_2O－18C6－C_2H_5OH体系（25℃）的相平衡研究及

采用半微量相平衡方法研究了ＬａＣｌ_３·３Ｈ_２Ｏ－１８Ｃ６－Ｃ_２Ｈ_５ＯＨ三元体系在２５℃时的溶解度，测定了各饱和溶液的折光率。结果表明：该体系在２５℃时形成了３种化学计量的配合物，组成分别为ＬａＣｌ_３·１８Ｃ６·３Ｈ_２Ｏ·２ＬａＣｌ－３·１８Ｃ６·６Ｈ_２Ｏ·Ｃ_２Ｈ_５ＯＨ及３ＬａＣｌ_３·１８Ｃ６·９Ｈ_２Ｏ·Ｃ_２Ｈ_５ＯＨ．考察了相平衡过程中水的行为，结果表明：无论在液相还是在固相中，Ｈ_２Ｏ／ＬａＣｌ_３的摩尔比总是３：１．制备了固态配合物，用ＩＲ、ＤＴＧ、ＴＧ与ＤＳＣ研究了配合物的组成与性质。由ＤＳＣ得到配合物不同分解步骤的焓变．     

［La（EO_3）_3（H_2O）］（ClO_4）_3·H_2O的晶体结构

稀土高氯酸盐开环冠醚三缩乙二醇（ＥＯ_３）［Ｌａ（Ｃ_６Ｈ_（１４）Ｏ_４）_３（Ｈ_２Ｏ）］（ＣｌＯ_４）_３·Ｈ_２Ｏ，单斜晶系，Ｐ２_１／ｃ空间群。晶胞参数为：ａ＝１５．４７４（２），ｂ＝１１．３８６（１），ｃ＝２０．８４１（４），β＝９９．８２（１）°，Ｖ＝３６１８（１），ＭｏＫα，Ｚ＝４，Ｄ_ｃ＝１．７１８ｇ／ｃｍ３，μ＝１．４９９ｍｍ￣（－１）。全矩阵最小二乘精细修正，结构因子Ｒ＝０．０５６，Ｒ_ｗ＝０．０８３。中心原子Ｌａ与开环冠醚醚链上的Ｏ（１）～Ｏ（９）及一个水分子形成１０配位双帽四方反棱柱结构。弱配体高氯酸根不参加配位。     

含铥金属富勒烯的生成及其特殊的溶解行为

金属富勒烯的合成及结构研究是当前富勒烯化学研究的重要内容[1]．一些稀土金属元素，如Sc[2]、Y[3]及大部分斓系元素（La、Ce、Nd、Sin、Eu、Gd、Tb、Ho）[4]形成的金属富勒烯已被合成出来．但仍有一些稀土富勒烯的合成尚未见报道，使人们难以对金属富勒烯的形成机制及物化性能作出全面的判断．本文采用原位活化、交换电极回放电弧放电及两步提取法首次得到含锡金属富勒烯．通过空白对比实验确定了Tin＠C。怕9生成．对甲苯及毗院提取液的质谱研究表明含镀金属富勒烯具有区别于其它金属富勒烯的特殊的溶解性能，显示出其可能具有独特的…     

CO2选择性氧化甲烷制C2烃催化剂La2O3/ZnO的氧化还原和CO2吸附性能

Ｌａ２Ｏ３／ＺｎＯ催化剂体系在以二氧化碳作为氧化剂的甲烷氧化偶联反应中具有很高的Ｃ２烃选择性和稳定性．采用ＣＯ２－ＴＰＤ－ＭＳ和ＴＰＲ技术考察了Ｌａ２Ｏ３／ＺｎＯ对ＣＯ２的吸附性质及其氧化还原行为．结果表明：（１）Ｌａ２Ｏ３／ＺｎＯ催化剂体系存在着强、弱两种碱中心，其中弱碱中心数量随样品中Ｌａ２Ｏ３含量增加而减少，强碱中心强度随样品中Ｌａ２Ｏ３含量增加而增强．（２）由于组分相互作用，高温下，Ｌａ２Ｏ３／ＺｎＯ易产生晶格氧空位，使之对ＣＯ２的吸附增强，吸附后的ＣＯ２与晶格氧作用形成立方晶型Ｌａ２Ｏ２ＣＯ３．（３）Ｌａ２Ｏ３／ＺｎＯ表面的Ｌａ３＋和Ｚｎ２＋可以部分被还原，由于组分间的相互作用，使得二者的还原都较单一组分存在时更难．（４）Ｈ２－ＣＯ２－Ｈ２氧化还原循环实验表明，Ｌａ２Ｏ３／ＺｎＯ表面被部分还原后，ＣＯ２可以将部分被还原的表面再氧化．在此基础上对Ｌａ２Ｏ３／ＺｎＯ催化剂上甲烷与ＣＯ２转化为Ｃ２烃的机制也进行了讨论．     

氯化铯和氯化镧溶剂体系及四类新化合物的合成

研究了四元体系ＣｓＣｌ－ＬａＣｌ３－ＨＣｌ－Ｈ２Ｏ（２５℃、「ＨＣｌ」＝１３％（ｗｔ），２３％（ｗｔ）和ＣｓＣｌ－ＬａＣｌ３－ＨＡｃ－Ｈ２Ｏ（３０℃，「ＨＡｃ」＝４２％（ｗｔ））的平衡态的溶度数据，并给出制了相应的溶度图，共得到了ＣｓＣｌ．ＬａＣｌ３．４Ｈ２Ｏ、２ＣｓＣｌ．ＬａＣｌ３．２Ｈ２Ｏ和３ＣｓＣｌ．ＬａＣｌ３．３Ｈ２Ｏ３种化合物。对得到的新相进行了热分析，Ｘ射线粉末衍射及偏光性质的测定，依     

含镧金属富勒烯不同溶剂的高温高压提取

将金属原子或离子置于以Ｃ６０、Ｃ８２为代表的富勒烯笼内形成金属富勒烯包合物是目前富勒烯研究的热点课题［１～３］．合成的金属富勒烯常伴随生成较难分离的空心富勒烯,传统的索氏提取法效率又较低,使得金属富勒烯的深入研究受到限制［１,２］．本文采用改进的高温...     

Supercritical fluid extraction of vapor-deposited pyrene from carbonaceous coal stack ash

The efficiencies of extraction of vapor-deposited pyrene from a high-carbon coal stack ash by Soxhlet extraction with methanol, ultrasonic extraction with toluene, acid pretreatment and subsequent ultrasonic extraction with toluene, batch extraction with toluene, and supercritical fluid extraction (SFE) are compared. SFE using CO(2) or isobutane yielded extraction recoveries virtually identical with those obtained using ultrasonic or Soxhlet extraction processes. Collection of the SFE extract was performed by expansion into a solvent or onto the head of a gas chromatography (GC) column. No loss of extracted pyrene was observed upon collection of methanol-modified CO(2) SFE by expansion into methanol. Also, no loss of pure CO(2) SFE extract was observed upon collection on the head of a GC column. However, use of a methanol or toluene modifier for CO(2) SFE directly coupled to GC effected complete loss of extracted pyrene.     

神华煤直接液化残渣超临界溶剂萃取研究

利用甲苯、苯和乙醇三种溶剂在反应釜中对神华煤直接液化残渣进行了超临界溶剂萃取,考察了压力、温度、萃取时间、溶剂/残渣比等对萃取产物收率和重质液体萃取组成的影响。结果表明,以甲苯为溶剂进行萃取时,萃取时间对重质液体产率及HS和A收率的影响不大,而温度、压力以及溶剂/残渣质量比都会影响萃取产物的产率及组成。溶剂超临界萃取过程中,有其他组分向HS组分转化,提高了HS的收率。三种溶剂中,苯显示了和甲苯相似的萃取性能,而乙醇的萃取性能相比苯和甲苯则较差,但乙醇萃取得到的重质液体中轻质组分含量高于苯和甲苯。萃取过程中,残渣中的灰分和硫分主要富集至萃取残渣中。     

Solvent extraction of copper(II) from sulfate medium with N -(2-hydroxybenzylidene)aniline

Solvent extraction of copper(II) from sulfate medium with N-(2-hydroxybenzylidene)aniline is studied with the following parameters: pH, concentration of the extractant, nature of diluent, and temperature. The extraction of copper(II) proceeds by a cation exchange mechanism and the extracted species are CuL₂ in cyclohexane and toluene and CuL₂ with some CuL₂HL in chloroform. The equilibrium constants have been calculated as well as thermodynamic parameters ΔH°, ΔS°, and ΔG°. The temperature effect on the solvent extraction of copper(II) with N-(2-hydroxybenzylidene)aniline in cyclohexane is discussed.     

N,N,N',N'-Tetrabutyladipicamide as a new extractant in toluene of nitric acid and uranium (VI)

N,N,N',N'-Tetrabutyladipicamide (TBAA) was used for the extraction of nitric acid and uranyl(II) ion from nitric acid media into toluene. The effects of nitric acid, uranyl(II) ion, and extractant concentration, temperature and back extraction on the distribution coefficient of uranyl(II) ion have been studied. The main adduct of TBAA and HNO₃ is TBAA·HNO₃ in 1.0 mol/l nitric acid solution. The 1:2:2 complex of uranyl(II) ion, nitrate ion and TBAA as extracted species is further confirmed by IR spectra of the extraction of uranyl(II) ion with TBAA. The values of the thermodynamic parameters have also been calculated.     

A two-step supercritical fluid extraction of polycyclic aromatic hydrocarbons from roadside soil samples

A two-step procedure for the supercritical fluid extraction (SFE) of polycyclic aromatic hydrocarbons from soil samples was developed. The procedure consists of a static supercritical fluid treatment in a closed extraction cell at a high temperature (T=250 or 340degreesC for 20 min) and an SFE with a solvent trapping. During the static phase, the sample is exposed to a supercritical organic solvent (methanol, toluene, dichloromethane, ACN, acetone, and hexane). The solvent penetrates particles of the matrix to substitute strongly bonded molecules and dissolves the analytes in the supercritical phase. At ambient temperature, supercritical fluids became liquid and lost their solvation abilities. Most of the analytes condense on the surface of the particles or on the extraction cell walls without forming strong bonds or penetrating deep into the matrix. Thus, the pretreatment liberates the analytes and they behave similar to those in freshly spiked samples. The common SFE with toluene-modified CO2 as an extraction fluid follows the static phase. With the use of the most suitable extraction phases (toluene, ACN), the extraction efficiency of the combined procedure is much higher (approximately100%). The results of the combined procedure are compared to the SFE procedure of the same untreated sample (difference less than 5%) and to the Soxhlet extraction. The extracts were analyzed using a GC with the flame ionization detection.     

Influence of the characteristics of soil and fly ash on the supercritical carbon dioxide extraction of dioxins.

Several investigations on the extraction of dioxins from soil and fly ash with supercritical fluid have been reported; however, few of them describe the influence of components on the extraction. We extracted dioxins from eight samples with different values of organic carbon content and surface area with supercritical CO(2) at a temperature of 463 K, a pressure of 40 MPa, and using 10% toluene as an entrainer. We researched the influence of the characteristics of soil and fly ash on supercritical CO(2) extraction of dioxins. The results revealed that the extraction efficiencies of PCDD/DFs and PCBs were high for all soil samples, while that of fly ash samples decreased with the increase in organic carbon content and surface area. The extraction efficiencies of dioxins from four standard samples, activated carbon, humic acid, alumina, and florisil, were also examined. The results revealed that the extraction efficiencies were strongly influenced by activated carbon like components present in the samples.     

The Extraction of Uranium(VI) with n-Octyldecylsulfoxides (ODSO)-Toluene

The liquid-liquid extraction of uranium(VI) from aqueous nitric acid with n-octyldecylsulfoxide (ODSO) in toluene has been studied over a wide range of conditions. The extracted species appears to be UO₂(NO₃)₂·2ODSO. The extraction increased with increasing nitric acid concentration up to 2.0 mol/l and then decreased. Extraction also increased with increasing extractant concentration. The influence of temperature, salting-out agent concentration and complex anion concentration on the extraction equilibrium were also investigated, and the enthalpy of the extraction reaction was calculated.     

Extraction and separation of Th(IV) and U(VI) from nitric acid media using PIA-8 and HDEHP

Extraction behavior of Th(IV) and U(VI) has been investigated with bis(2-ethylhexyl) phosphinic acid (PIA-8) and bis(2-ethylhexyl) phosphoric acid (HDEHP) from nitric acid media in toluene. The optimum conditions for extraction of these metals have been established by studying various parameters like acid concentration, pH, reagent concentration, diluents and shaking time. The extraction of Th(IV) was found to be quantitative with 0.3-2.5M HNO₃ by 2.5^.10^-2M HDEHP and in the pH range 0.1-2.5 with 2.3^.10^-2M PIA-8 in toluene. U(VI) was completely extracted in the acidic range of 0.1-2.0M HNO₃ with 2.2^.10^-2M HDEHP and in the pH range of 1.0-3.0 with 2.0^.10^-2M PIA-8 in toluene. The probable extracted species have been ascertained by log D-log c plot as UO₂ R₂ ^.2HR with both the reagents and Th (NO₃)₂R₂ ^.2HR with PIA-8 and Th (NO₃)₃R^.3HR with HDEHP, respectively. Temperature dependence of the extraction equilibrium is examined by the temperature variation method. Separation of U(VI) and Th(IV) was also carried out from commonly associated metals.     

PDMS extraction bars for the determination of volatile aromatic hydrocarbons in water and wastewater

In this study, the preparation and application of extraction bars of PDMS were investigated to preconcentrate and determine benzene, toluene, ethylbenzene, and xylene in water and wastewater by means of HPLC with fluorescence detection. Aliquot samples from hospital wastewater were used as the model effluent. The independent variables for the sorptive extraction were as follows: ionic strength (added amounts of NaCl); pH; temperature and time of absorption; temperature and time of desorption. Under optimized conditions, by using a factorial design, the suspended extraction bars could allow the determination of benzene, toluene, ethylbenzene, and xylene (1.20 ± 0.05 μg/L; 10.40 ± 0.02 μg/L; 1.80 ± 0.04 μg/L; 15.9 ± 0.04 μg/L, respectively) in hospital effluent (fortified samples), by recoveries of 71.9 ± 4.9 to 74.8 ± 5.6%. This procedure represents an innovation that eliminates the time‐consuming stage of vacuum microfiltration, and allows the determination of volatile organic compounds by HPLC. As far as we know, this procedure is original and represents an important contribution to the field.