协同高效的铁催化剂构建及其在CO_2加氢制高碳烃中的应用

采用物理掺杂法制备了生物质灰分作为助剂的融铁催化剂,通过X射线衍射、透射电镜、穆斯堡尔谱等方法对催化剂进行了表征,并在固定床反应器中对其CO_2加氢制高碳烃的催化性能进行了评价。结果表明,与不含生物质灰分助剂的催化剂相比,添加助剂的融铁催化剂粒径较小且尺寸分布较窄,Fe_3O_4、Fe_5C_2、Fe_3C和α-Fe四相协同共存,进而促使逆水气变换反应与C-C偶联的串联反应高效进行,在有效抑制甲烷生成的同时,可明显提升高碳烃选择性。高碳烃产物以C_(4-18)的烃类为主,在300℃、1. 0 MPa、4800 h~(-1)、H~2/CO_2=3. 0、助剂添加量为5%(质量分数)的条件下,其在烃类产物中选择性最高可达73. 9%。     

碳化铁催化剂的制备及其对CO加氢的催化活性

 以Fe2O3为原料,采用两种预处理方法制备了碳化铁催化剂. 结果表明,直接在CO气氛下进行碳化处理,或者以H2预还原后再用CO进行碳化处理均可以制备出碳化铁催化剂. 碳化温度是制备过程中的关键因素. 对于Fe2O3样品,较适宜的碳化温度是350 ℃,而对于添加了K助剂的样品,只有经H2预还原处理后再于350 ℃用CO碳化处理4 h才能将样品完全转化为Fe5C2. 在CO加氢的评价实验中,碳化铁催化剂表现出很高的催化活性,生成的烃类产物中主要是饱和烷 烃,未检测到乙烯的生成. 而在K改性的催化剂上反应产物中烯烃的含量明显提高.     

纳米HZSM-5催化剂催化烃类转化反应

制备了纳米(20~50 nm)HZSM-5催化剂, 用XRF, TEM和NH3-TPD等手段对催化剂进行了表征. 以正辛烷及苯和正辛烷混合物的转化为模型反应, 研究了单烃和混合烃在纳米HZSM-5催化剂上的转化行为, 考察了反应条件对产物分布的影响. 结果表明, 纳米HZSM-5沸石催化剂具有很强的烃类转化能力, 烃类通过芳构化、 异构化和烷基化等反应转化为高辛烷值的异构烷烃和芳烃, 产物中异构烷烃(C4~C6)和芳烃的质量分数超过90%. 直链烷烃转化为芳烃以生成苯环为主, 混合烃转化为芳烃以苯和小分子烃的烷基化为主. 控制反应条件可抑制苯和C+9芳烃的生成. 产物分析结果表明, 烃类在纳米HZSM-5催化剂上的裂解、芳构化和异构化等遵循正碳离子机理.     

饱和烃C-H键的活化及其配位催化反应

本文评述了饱和烃C—H键活化的最近进展,从配位催化和量子化学的观点,推断了饱和烃C—H键活化及其配位催化反应的机理:首先是它的非定域轨道里的电子对配位在催化剂中心金属的d_z~2/d_■~2-■~2混合轨道上,然后电子从催化剂的HOMO流向底物的LUMO,发生氧化加成反应,生成烷基金属氢化物过渡态,最后经插入反应、还原消除反应,完成整个催化循环。此外,还展望了未来的发展前景。     

2-（1,3,4-噻二唑胺甲基）苯酚的合成及其杀菌活性

以2-氨基-5-烃基-1,3,4-噻二唑和水杨醛为原料,分别用"分步法"和"一锅法"经还原中间产物Schiff碱的CN双键合成了一系列2-((1,3,4-噻二唑基)胺甲基)苯酚类新化合物,"一锅法"的产率较高,为56%～80%。产物的结构用IR、1H NMR、13C NMR和MS进行了表征。初步测试了目标化合物的杀菌活性,证明化合物对赤星病菌具有较好的抑菌活性,当浓度为25 mg/L时,化合物3i的抑制率为76%,化合物3f、3h、3k和3l的为70%。     

还原温度对Co-La-Zr／AC催化剂合成气制高碳混合醇性能的影响

采用共浸渍法制备了Co-La-Zr/AC催化剂并考察了不同温度还原的催化剂的CO加氢催化性能. 结果表明,在3.0 MPa, 495 K, H2/CO(V/V)=2和GHSV=500 h-1 条件下,经703 K还原的催化剂, CO的转化率和醇的选择性分别为59.1%和42.0%, 其中C6～C18 的高碳醇在总醇中占到50.4%. XRD结果显示,反应后催化剂的主要物相为金属态的钴和碳化钴(Co2C). 还原温度可影响催化剂中钴的晶粒分散度和碳化钴的生成. 碳化钴的形成可能在合成气生成醇类的反应中起重要作用.     

Ni/HZSM-5催化剂的结构及其催化山梨醇水相加氢合成烷烃性能

采用浸渍法制备了Ni/HZSM-5双功能催化剂,考察了焙烧温度对催化剂结构及其催化山梨醇水相加氢合成C5～C6烷烃性能的影响.结果表明,在金属中心和酸性载体的协同作用下,通过山梨醇中C-O键加氢和异构化高选择性合成了C5～C6烷烃.经500°C焙烧的Ni/HZSM-5催化剂上山梨醇水相加氢的活性最高,山梨醇转化率为62.0%,戊烷和己烷的总选择性为76.4%,其中异己烷选择性达45.4%.对催化剂进行N2物理吸附、X射线衍射、NH3程序升温脱附和H2程序升温还原等表征后发现,经500°C焙烧催化剂的有效比表面积和孔体积均明显增大,HZSM-5负载的硝酸镍分解成较小晶粒的NiO,表面酸量适中,且Ni物种与载体相互作用较强,较易被H2还原,Ni还原度达100%.这是其催化活性最高的原因.     

复合催化剂上CO_2加氢合成C_2~ 烃类

介绍了由 CO2 H2 合成 C2 烃的几种复合催化剂体系的研究进展 ,比较和评价了复合催化剂体系的活性和选择性及其对 C2 烃类生成的影响。着重于复合催化剂体系对 C4 烃的生成及产物分布的影响并简述反应机理     

Ni基催化剂上木质素模型化合物苯基苯乙醚C-O键的加氢裂解

研究了Ni基催化剂上木质素模型化合物苯基苯乙醚中C-O-C键加氢裂解性能.结果表明,Ni/C催化剂显示出优异的加氢裂解能力,苯基苯乙醚的转化率达到99%以上.Ni/C催化剂的还原方法对裂解选择性有重要影响;氢气还原制备的Ni/C-H催化剂上,C-O-C键裂解选择性为85%.Ru/C和Pd/C催化剂上裂解选择性分别为40%和69%.采用碳热还原方法制备的Ni/C-C催化剂,可以实现高选择性加氢和裂解,C-O-C键裂解选择性达到99%以上,其中芳烃化合物收率为44%.这可能与镍组分和载体碳之间的相互作用有关.     

原位产生二氧化锰催化构建S—S键

利用0.1～0.2 equiv.高锰酸钾在无水乙醇体系中原位生成高活性二氧化锰,并以此为催化剂,促使硫酚、硫醇类化合物在室温下发生自由基自身偶联反应构建S—S键,获得了14种对称双硫化物,产率介于70%～99%;同时发现该催化体系还可催化对称双硫化物与不同取代基的硫酚、硫醇或两个不同的对称双硫化物,发生自由基交叉偶联反应合成了13个不对称双硫化合物,产率19%～72%.该法具有简单高效、后处理简单、绿色溶剂、底物适用范围广、条件温和等优点,所有产物均经~1H NMR、~(13)C NMR结构确证.     

Influence of residence time and catalyst regeneration on the pyrolysis–zeolite catalysis of oil shale

Oil shale from the Kark region of Pakistan has been pyrolysed in a fixed bed batch reactor and the properties of the derived shale oil determined. The reactor system was then modified to incorporate a second reactor where the derived vapours from oil shale pyrolysis were passed directly to the second reactor containing zeolite ZSM-5 catalyst. The influence of the process parameters of vapour residence time (VRT) over the catalyst and the regeneration of the catalyst were examined. The yield and composition of the derived gases before and after catalysis were determined. In addition, the yield and composition of the derived oil in terms of total nitrogen and sulphur content and the content of aromatic hydrocarbons in the oils was investigated. The results showed that the yield of oil after catalysis was reduced with a consequent higher yield of gases and formation of coke on the catalyst. The main gases from the pyrolysis of oil shales were CO₂, CO, H₂, CH₄, C₂H₄, C₂H₆ and C₃H₆, C₃H₈ and minor concentrations of other hydrocarbon gases. The main role of catalysis was to convert the long chain alkanes and alkenes in the oil to lower molecular weight, short chain, alkyl substituted and iso species and high concentrations of aromatic hydrocarbons. Total nitrogen and sulphur contents in the oils were markedly reduced after catalysis. This reduction was reflected in the reduced concentration of nitrogen and sulphur containing aromatic hydrocarbons. The influence of longer VRTs was to increase the formation of aromatic hydrocarbons, reduce the nitrogen, and sulphur compounds in the oils. The influence of catalyst regeneration, involving five regenerations was not significant on the yield and composition of the derived catalytically upgraded oils.     

Ru助剂对Co/SiO_2/HZSM-5催化剂合成航空燃油类烃的影响

以中孔硅胶和微孔HZSM-5分子筛为复合载体,添加Ru制备了钴基催化剂,考察了Ru添加量(1%~4%,质量分数)对催化剂结构和固定床费托合成航空燃油类烃的影响。实验结果表明,制备的复合载体催化剂有一定的微孔和中孔结构,Ru的添加有利于Co分散,Ru促进的催化剂低温还原过程提高了催化剂在150~750℃的还原度和CO转化率,复合载体中HZSM-5分子筛利用其微孔结构,提高了异构烃的收率。当Ru负载量为1%时,CO转化率达到62.8%,航空燃油类烃的收率达到37.7%,包括约10.9%的异构烃。Ru负载量超过2%时,增强的催化剂CO加氢活性和CH4选择性,导致合成产物向低碳烃方向偏移。     

Oxidative dehydrogenation of ethane to ethylene over NiO loaded on high surface area MgO

The oxidative dehydrogenation of ethane over NiO-loaded MgO with high surface area was carried out using a fixed-bed flow reactor at 600 °C under atmospheric pressure.

At 600 °C, the oxidative dehydrogenation of ethane (C₂H₆/O₂ = 1) without dilution with an inert gas resulted in C₂H₆ conversion of 68.8% and a high C₂H₄ selectivity of 52.8%, which corresponds to a C₂H₄ yield of 36.3%. In addition, the catalytic activity did not decrease for at least 10 h. X-ray photoelectron spectra of the catalysts after the reaction exhibited that the initial valence state of Ni²⁺ (NiO) was maintained during the oxidative dehydrogenation of ethane. However, when NiO-loaded MgO was reduced with H₂ prior to the reaction, C₂H₄ selectivity decreased to nearly zero and high CO and H₂ selectivities were observed with the C₂H₆ conversion of 50 %, indicating that partial oxidation of C₂H₆ proceeded. Therefore, it seems important to keep Ni species as an oxide phase on the support, and for this purpose, use of the high surface area of MgO is essential.     

Syn thesis,Characterization of 1,3-Diisopropoxyaloxanes,Their Modification on Calcium Carbonate Filler

Five 1,3-diisopropoxyaloxanes, i. e., (PrⁱO)RO₂AlOAlO₂R(OPrⁱ) [where R=C₁₆H₃₁(Ⅰ)_C₁₈H₃₅(Ⅱ), _C₉H₁₆CH=CHC₇H₁₅(Ⅲ), _P(OCH₂(C₂H₅)CHC₄H₉)₂(Ⅳ), and _C₁₂H₂₃(Ⅴ), respectively] were syn thesized by the hydrolysiscondensation of aluminium isopropoxide with water, exchange reaction with relevant acids. They were characterized by elemental analysis, determination of molecular weight, IR,, ²⁷Al NMR. The results show that the coordination number of Al atom in the compounds is 5, they exist in monomers in benzene. The analyses of TG/DTG, DTA indicated that both the thermal hydrolysis stability, thermal stability of these compounds are in the following order:Ⅰ<Ⅱ<Ⅲ<Ⅳ. The viscosity determinations of light calcium carbonate(L-CaCO₃)/liquid paraffin suspension systems demonstrated that they had an excellent modification effect on the surface of LCaCO₃ filler, the amount needed to form a monomolecular film on the surface of LCaCO₃ particles is in the order:Ⅰ<Ⅱ<Ⅲ<Ⅳ.     

皂荚素的表面活性及其二元体系的热力学研究

通过表面张力的测定研究了皂荚素(GS)的表面活性及其热力学性质随温度的变化.测定了皂荚素分别与十二烷基磺酸钠、十二烷基聚氧乙烯醚硫酸钠、全氟辛酸钠、十二烷基脂肪醇聚氧乙烯(9)醚、辛基酚聚氧乙烯(10)醚及十六烷基三甲基溴化铵等复配的表面张力-浓度对数关系(γ～lgc)曲线,并用二维晶格模型及正规溶液理论计算了含皂荚素的二元表面活性剂溶液表面吸附层的组成、分子相互作用参数及分子交换能.结果表明,皂荚素主要呈现非离子表面活性剂的性质,与阳离子表面活性剂复配呈微弱的离子性.复配后分子交换能均小于零,复配增效.增效顺序为GS/阳离子>GS/非离子>GS/阴离子(表面活性剂复配体系).     

多环芳烃与不饱和自由基氢提取反应类的动力学研究

对2~6个环的多环芳烃的氢提取反应类进行了系统研究, 提取氢原子的不饱和自由基包括丙炔基自由基（C₃H₃）、 烯丙基自由基（C₃H₅）、 丁二烯基自由基（nC₄H₅, iC₄H₅）、 环戊二烯基自由基（C₅H₅）以及苯基自由基（C₆H₅）. 采用M06-2X/cc-pVTZ方法得到了多环芳烃的电子结构信息, 利用过渡态理论并结合Eckart隧道校正, 计算了所有反应在500~2500 K范围内的反应速率常数.考察了多环芳烃的大小、 结构对反应速率常数的影响, 对比了不同氢提取自由基及不同氢提取反应类型的速率常数. 结果表明, 多环芳烃的大小对反应速率常数影响不大, 但是多环芳烃的环结构对反应速率常数影响较大. 将不同的氢提取反应类简化为发生在五元环上的C₅类和发生在六元环上的C₆类两类, 结果表明, C₆类的反应活性高于C₅类. 研究了nC₄H₅, iC₄H₅以及C₆H₅自由基与多环芳烃的氢提取反应, 它们的氢提取反应活性大小顺序为C₆H₅>nC₄H₅>iC₄H₅. 通过对每类典型反应的速率常数取平均值, 总结出相应类型的速率规则, 可用于构建多环芳烃和碳烟机理.     

Measurement of mass attenuation coefficients for four mixtures using X-rays from 13 keV up to 40 keV

The total absorption coefficients for some selected organic compounds relevant to health physics, Triaflol BN (C₃H₄O₂)_n, Triaflol TN (C₁₂H₁₈O₇)_n, Kapton (C₄₄H₂₀O₁₀)_n, and Melinex (C₁₀H₈N₄O₄)_n were measured in the X-ray energy range from 13 keV up to about 40 keV using a collimator, high purity germanium detector with thin Be window and variable energy X-ray source. The measured values are compared with the theoretical ones obtained using the XCOM code. The agreement is generally good within a few percent.     

机械球磨制备三苯胺基PAF-106s及C2烃吸附性质

以三苯胺为单体, 无水三氯化铁为催化剂, 二甲醇缩甲醛为外交联剂, 通过机械球磨不同比例的三苯胺、 三氯化铁和二甲醇缩甲醛, 合成了PAF-106s(PAF-106a~PAF-106c, PAF: porous aromatic framework). 红外光谱、 元素分析、 X射线光电子能谱和固体核磁共振波谱等表征结果证明发生了聚合反应. 氮气吸附结果表明, 三苯胺、 三氯化铁和二甲醇缩甲醛的比例影响PAF-106s的多孔性能. 三氯化铁和三苯胺摩尔比从3∶1增加到12∶1时, PAF-106c的BET比表面积从PAF-106a的135 m²/g增加到280 m²/g. 引入二甲醇缩甲醛后, PAF- 106d~PAF-106g的BET比表面积随三氯化铁和二甲醇缩甲醛摩尔比的增加而逐渐降低. 在273和298 K下, 测试了PAF-106c的C2烃吸附性能, 并采用理想吸附溶液理论计算了C₂H₂/C₂H₄和C₂H₆/C₂H₄分离比.     

Theoretical Study on the Kinetics for the Reactions of Heptyl Radicals with Methanol

Ab initio study of the reactions of n-heptyl radicals(1-C₇H₁₅, 2-C₇H₁₅, 3-C₇H₁₅, and 4-C₇H₁₅) with methanol was conducted over the temperature range of 300-1500 K. Transition states for the reaction channels producing C₇H₁₅OH, CH₃, C₇H₁₅OCH₃, H, C₇H₁₆, CH₂OH and CH₃O were identified and the geometries of all stationary points were calculated at BB1K/MG3S level of theory. The potential barrier heights of the corresponding transition states were predicted by the CBS-QB3//BB1K and G4//BB1K methods, indicating that the eight H-abstraction channels are more kinetically favorable than the channels where OH transfers from CH₃OH to C₇H₁₅ and where the C₇H₁₅OCH₃+H products are given. The rate constants of H-abstraction channels were calculated with TST and TST/Eck. Both the forward and reverse rate constants have positive temperature dependence and the tunneling effect is only important at the temperature lower than 700 K. For the reactions of H-atom abstraction from methyl in CH₃OH by n-heptyl, a reverse and the corresponding forward rate constant are roughly equal. For the reactions of H-atom abstraction from OH in CH₃OH by n-heptyl, a reverse rate constant is larger by several orders of magnitude than the corresponding forward one.     

阴离子功能化生物柴油离子液体抗氧化剂[X][C6H5COO]的制备

设计合成了两种阴离子功能化离子液体抗氧化剂（[MI][C₆H₅COO]、[Ch][C₆H₅COO]）,采用核磁共振氢谱、傅里叶红外光谱对其结构进行了表征,并研究了两种离子液体抗氧化剂对小桐子生物柴油抗氧化性、铜片腐蚀性和油溶性能的影响。结果表明,离子液体抗氧化剂可有效提高生物柴油氧化稳定性,在添加量为0.3‰时,[MI][C₆H₅COO]的小桐子生物柴油诱导期提高了238%,超过了中国国家标准（6 h）,[Ch][C₆H₅COO]的小桐子生物柴油诱导期提高了141%,未达到中国国家标准。进一步研究了两种离子液体抗氧化剂的油溶性,油溶性能从大到小的顺序为[MI][C₆H₅COO] > [Ch][C₆H₅COO] > GA（合成离子液体抗氧化剂的原料）。实验表明,合成的两种离子液体抗氧化剂中含有亲油阳离子的[MI][C₆H₅COO]综合性能明显优于含有亲水阳离子的[Ch][C₆H₅COO]。