与半衰期(t1/2)有关问题的探讨

从半衰期通式推导出t_(3/4),7_(7/8)……的通式及其共同表达式,并说明其物理意义: 各级反应半衰期(t_(1/2))的通式: t_(1/2)=k′C_0~(1-n) [1]我们可以根据此式,推导出t_(3/4),t_(4/8)……在各级反应中的通式。如对t_(3/4),可认为是初始浓度为C_0时的半衰期和初始浓度1/2C_0时的半衰期之和,可写为下式:     

热动力学的研究 XV.分数级反主尖的热动力学法

根据热动力学基础理论和n级反应通用的势动力学方程,本文建立了各种分数级反应的热动力学研究法.应用M-340计算机编制了研究法基本公式中有关无量纲参数的各种函数表,并深入讨论了有关函数的基本性质及其图象.同时将本文建立的分数级反应研究法应用于整数级反应的热动力学研究,所得结果与文献报道的一、二级反应的无量纲参数法基本公式完全相同,该研究法还可用于判断化学反应的级数.     

热动力学的研究 XV.分数级反应的热动力学法

根据热动力学基础理论和n级反应通用的热动力学方程,本文建立了各种分数级反应的热动力学研究法.应用M-340计算机编制了研究法基本公式中有关无量纲参数的各种函数表,并深入讨论了有关函数的基本性质及其图象.同时将本文建立的分数级反应研究法应用于整数级反应的热动力学研究,所得结果与文献报道的一、二级反应的无量纲参数法基本公式完全相同,该研究法还可用于判断化学反应的级数.     

流动注射阳极溶出伏安法的中内插标准加入法

探讨在流动注射阳极溶出伏安法中应用内插标准加入法,推导这一非稳定态电积过程的溶出峰电流方程,从而论证了这一方法的定量依据。提出一个快速简易的定量方法,只需在试样载流中分别注入一个空白和标准溶液,就能由导出的一个简单方程得出待测样品浓度。测定一系列水样中ppb级铅,相对标准偏差为3.4％(n=10),回收率为90％～108％。与经典ASV方法对照,结果一致。     

由DTG曲线确定反应级数的新方法

利用动态热重曲线求固相反应动力学参数的方法很多,如微分差分法,微分法和积分法等,有关数据处理方法中,反应级数n的获得尤为重要,因为有的需要预先知道反应级数或通过尝试才能求得反应级数;如Coats-redfern法,最大速率法等。有的方法虽可由实验直接确定反应级数,但精度低。前文曾采用逐步逼进法对Coats-redfern法中最佳n值的获得进行了讨论。本文根据DTG-TG曲线的特点,探求一种简便获得反应级数n的方法,通过研究CaC_2O_4·H_2O的分解反应,对该方法的可靠性进行论证。     

平行反应的热动力学研究法

根据热动力学基本理论, 推导了平行准一级反应和平行准一二级反应的热动力学方程, 建立了热谱解析平行反应动力学参数的热动力学研究法, 并利用该法研究了两个模拟平行反应体系的热动力学, 实验结果验证了方法的正确性.     

由反应机理推导动力学方程的基本方法——对征答(24)的讨论

由反应机理推导反应的动力学方程,现行物理化学教材已有论述。目前应用较广的方法是近似方法——“稳态近似法”或“速率控制步骤法”,文献[1]已明确指出了这种方法适用范围有限且存在严重的不足,但并未给出推导的方法。为此,本文     

非等温法研究TGDDM/DDS体系固化反应动力学

采用DSC对4,4′-四缩水甘油基二氨基二苯基甲烷(TGDDM)和3,3′-二氨基二苯基砜(DDS)体系的固化反应动力学进行了研究.分别通过n级反应法和Malek的最大概然机理函数法确定了固化反应机理函数,求解了固化反应动力学参数,得到了固化反应动力学模型.结果表明,通过Kissinger,Crane方法求解动力学参数所得到的n级反应模型与实验值差别较大;而采用Malek方法判别机理,表明该固化反应按照自催化反应机理进行,实验得到的DSC曲线与模型计算所得到的曲线吻合的较好,所确立的模型在5~20K/min的升温速率下能较好地描述TGDDM/DDS体系的固化反应过程,并为工艺参数的选择和工艺窗口的优化提供了理论依据.     

碘促进的苯并咪唑及其衍生物的合成

在碘的氧化作用下,由伯醇和邻苯二胺一步合成了苯并咪唑及其衍生物。考察了碘和碳酸钾用量及温度对反应产率的影响,反应较佳的条件为n(o-ClC6H4CH2OH)∶n(o-phenylenediamine)∶n(I2)∶n(K2CO3)=1.0∶1.1∶5.0∶5.0,反应温度70℃,反应时间5 h。用方法A在较佳的反应条件下2-(2-氯苯基)苯并咪唑的产率可达86%,用方法B其产率达69%。没有选择传统的醛或酸作为反应底物,而是选择了伯醇在碘的氧化作用下直接合成了目标产物,反应为合成苯并咪唑及其衍生物的一个新方法,探讨了可能的反应机理。     

n级反应的热动力学对比进度法

在化学反应的热动力学研究中,根据一次实验的热谱曲线来确定一个未知反应的级数,是一项很有理论和实际意义的工作.本文建立了n级反应的热动力学对比进度法.应用此法可判定反应级数和计算速率常数,并用实验及文献数据验证了本文方法的正确性.     

有序介孔Ru-MgZr复合氧化物合成及催化亚油酸异构化性能

筛选高效、高选择性多相催化剂异构化亚油酸是共轭亚油酸(CLA)研究的重点。 本文采用溶剂挥发自组装改进的溶胶-凝胶法,合成有序介孔Ru掺杂的MgO-ZrO₂固体碱催化剂。 考察了催化剂中不同Mg物质的量对催化剂孔径、比表面积和表面碱性以及Ru等的结构和性能对催化性能的影响。 对比了催化剂的形貌、表面碱性及Ru组分对催化性能的影响程度。 结果表明,n(Zr)∶n(Mg)=3∶1时,Ru掺杂的MgO-ZrO₂固体碱催化剂具有高度有序的介孔结构和高的比表面积。 而n(Zr)∶n(Mg)=1∶1时, MgO-ZrO₂固体碱催化剂合成CLA产率较高,反应时间4 h,产率达到85%,催化效率为0.099 g(CLA)·L^-1(solvent)·min^-1,并且催化产物主要为具有生物活性的3种共轭亚油酸异构体。 催化剂的强碱性位点和晶格Ru是催化异构化反应的两个活性位点,强碱性位点是提高催化性能的关键。 固体碱复合氧化物催化效率高、制备方法简单、反应产物生物活性高等优点,具有较好的应用前景。     

瓜环基金属纳米催化剂的电化学研究进展（英文）

金属纳米材料在电催化应用中展示出良好的性能,但是它们依旧面临着稳定性差和调控策略有限的问题。引入第二组分是一种有效的策略,能够很好的改善其催化活性与稳定性。在这篇综述中,我们概述了结合金属纳米材料和瓜环（CB[n]）用于电催化应用。瓜环是一系列的具有刚性结构、高稳定性、与金属配位的官能团的大环,它们适合稳定金属纳米材料并对其进行调控。本文讨论按照瓜环的功能分类,包含瓜环作为保护剂、瓜环基的超分子自组装体以及瓜环作为前驱体制备氮掺杂多孔碳。多种金属纳米催化剂,包括金属纳米颗粒（Pt,Ir,Pd,Ru,Au）、金属单原子（Fe,Co,Ni）以及过渡金属碳化物（TMCs）成功与瓜环或瓜环衍生的碳材料复合,这些复合材料在许多电催化反应中展示出优异的性能和稳定性,反应包括了氧还原反应（ORR）、析氧反应（OER）、析氢反应（HER）、二氧化碳还原反应（CO2RR）、甲烷氧化反应（MOR）、乙醇氧化反应（EOR）。其中,一些金属-瓜环复合物可进一步作为双功能催化剂用于全水解和燃料电池中。瓜环基的纳米催化剂具有媲美商用催化剂的性能,甚至其稳定性可优于商用催化剂。实验分析以及密度泛函理论（DFT）计算...     

Converting Thiophene in Simulated Coking Crude Benzene to N,N-Dimethyl-2-thiophenecarboxamide by Dimethylcarbamyl Chloride Under Mild Conditions

Since the content of thiophene in coking crude benzene is high, it is necessary to remove it from coking crude benzene for efficient utilization. In this study, an important intermediate, N,N-dimethyl-2-thiophenecarboxamide, was synthesized from thiophene and dimethylcarbamyl chloride. The influences of the dosages of dimethylcarbamyl chloride and ZnCl2 catalyst, reaction temperature and time on the removal rate were further explored based on the reaction kinetics.The structure of the target product was characterized by means of MS,NMR and 13C NMR.The removal rate of thiophene was 98.14% after the reaction for 2 h and thiophene was almost removed after the reaction for 3 h under the optimal reaction conditions [a molar ratio of n(thiophene):n(dimethylcarbamyl chioride):w(ZnCl2)=1:12:10,300 r/min, 318 K and 101.325 kPa].The acylation of thiophene with dimethylcarbamyl chloride was approximately in accord with the first order kinetic equation at 303-323K.The activation energy was 53.9850 kJ/mol and the pre-exponential factor was 1.4521×10^9 h^-1.     

有机溶剂/缓冲液双相体系中固定化Acetobacter sp.CCTCC M209061细胞催化1-(4-甲氧基)-苯基乙醇不对称氧化反应

在有机溶剂/缓冲液双相体系中, 利用固定化醋酸杆菌Acetobacter sp.CCTCC M209061细胞高对映体选择性地催化1-(4-甲氧基)-苯基乙醇(MOPE)的不对称氧化反应, 成功地拆分外消旋MOPE得到对映体纯(S)-MOPE. 与游离细胞相比, 固定化细胞催化反应速度有所降低, 但其稳定性(包括操作稳定性、 热稳定性和储藏稳定性)明显提高. 固定化细胞连续使用10批次(每批次12 h)后, 仍能保留其初始催化活性的58%以上, 而游离细胞仅保留约20%的相对活性. 在所考察的不同有机溶剂中, 正己烷不仅能较好地溶解底物, 而且对细胞的生物相容性相对较好, 因而提高了反应底物浓度、 反应初速度、 对映体回收率及残留底物e.e.值, 是反应体系中最适宜的有机相. 该反应的最适宜正己烷体积分数为60%, 辅底物为50 mmol/L丙酮, 底物浓度为40 mmol/L, 缓冲液pH=6.5, 反应温度为30 ℃; 在此条件下, 反应初速度为80.4 μmol/min, 反应12 h后, 对映体回收率和残留底物e.e.值分别为51.0%和99.9%, 明显好于水单相反应体系.     

Butane isomerization over platinum promoted sulfated zirconia catalysts

The isomerization of n-butane to i-butane has been studied at 11 bar in a microflow reactor over sulfated zirconia (SZ) and platinum containing sulfated zirconia (Pt-SZ) catalysts. In the presence of H₂ a significantly higher temperature is required for isomerization over SZ than in its absence. The rate over SZ is higher with n-butane containing 33 ppm butene as an impurity than with a feed that is pre-equilibrated over a Pt/SiO₂ catalyst to a much lower butene content. Over Pt-SZ the reaction rate is higher, because any butene consumed is rapidly regenerated; the conversion is perfectly stable in 83 h runs, selectivity to i-butane is 95%; i-pentane and propane are the main byproducts. The activation energy is 53 kJ mol⁻¹. Upon increasing the pressure of H₂ from 1.1 to 6.6 bar, the reaction rate was found to decrease in a perfectly reversible fashion. Kinetic analysis reveals that the reaction order is negative in H₂ (−1.1 to −1.3 depending on the temperature) and positive in n-butane (+ 1.3 to +1.6), indicating that the mechanism of this isomerization is intermolecular: butene is formed and reacts with adsorbed C₄-carbenium ions to adsorbed C₈ intermediates which isomerize and undergo β-fission to fragments with i-C₄ structure. This mechanism is confirmed over Pt-SZ by isotopic labelling experiments, though at much lower pressure, using double labelled ¹³CH₃---CH₂---CH₂---¹³CH₃. The primary reaction product consists of i-butane molecules, containing zero, one, two, three and four ¹³C atoms in a binomial distribution.     

Mesomorphic phase transitions of a series of D-phase compounds

Mesomorphic phase transitions of 4'-n-alkoxy-3'-nitrobiphenyl-4-carboxylic acids (ANBC) with numbers of carbons (n) in the alkoxy group ranging from 11 to 22 have been studied by differential scanning calorimetry (DSC) and polarizing optical microscopy. The D phase, a mesophase of particular interest through its being optically isotropic, was observed for the n = 17, 19, 20, 21, and 22 members of the ANBCs, as well as for the n = 16 and 18 members, as reported previously. The S_c-D phase transition temperature decreased with increasing n, so that the temperature range of the D phase extended over 64° at n = 22. In the n = 15 member, the D phase was certainly observed on first heating, but was not seen on subsequent cooling and second heating processes.     

Organotin-oxometalate coordination polymer catalyzed oxyfunctionalization of monoterpenes

The organotin-oxometalate coordination polymers [(nBu₃Sn)₂MO₄]·nH₂O (where, M = Mo or W) were prepared by the interaction of nBu₃SnCl with sodium salts of molybdate or tungstate and tested in oxyfunctionalization of monoterpenes with urea hydroperoxide (UHP) as an oxidizing agent. The oxyfunctionalization of monoterpenes gave commercially important products such as epoxides, ketones and hydroxyl derivatives. Among the two catalyst, organotin-oxomolybdate [(nBu₃Sn)₂MoO₄] showed higher activities and epoxide selectivities under selected liquid phase oxyfunctionalization conditions with most of the monoterpenes such as limonene, -pinene, β-pinene, carene, camphene, gerniol and linalool. The integrity of the organotin-oxometalates polymers were confirmed by X-ray diffraction BET surface area, FT-IR, FT-Raman, SEM, TG/DTA and MAS NMR (¹³C, ¹¹⁹Sn) analysis. The effects of reaction parameters on limonene conversions and product selectivities have been studied in detail using [(nBu₃Sn)₂MoO₄] catalyst. There was no leaching of the active catalyst into the reaction medium and catalyst was recyclable without loss in its activity in the oxidation reaction.     

高碳烃宽温度范围燃烧机理构建及动力学模拟

发动机中燃料点火特性以及燃烧能量的释放对于发动机设计具有非常重要的作用,为了提高燃料的燃烧效率以及减少燃料在燃烧过程中污染物的排放,基于反应动力学机理对燃料燃烧过程的模拟就显得十分必要。因此需要更加深入的认识碳氢燃料的燃烧机理,探索其在燃烧过程中十分复杂的化学反应网络。为了发展能够适用于实际燃料多工况条件(宽温度范围、宽压力范围和不同当量比)燃烧的燃烧机理,基于碳氢燃料机理自动生成程序ReaxGen构建了正癸烷燃烧详细机理(包含1499个物种,5713步反应)和正十一烷燃烧详细机理(包含1843个物种,6993步反应)。详细机理主要由小分子核心机理和高碳烃类(C5以上)机理两部分组成。为了验证机理的合理性与可靠性,本文对于高碳烃燃烧新机理在点火延时时间以及物种浓度曲线进行了动力学分析,并与实验数据及国内外同类机理进行了对比,结果表明本文提出的正癸烷和正十一烷燃烧新机理在比较宽泛的温度、压力和当量比条件下都具有较高的模拟精度,为发展精确航空煤油燃烧模型提供了基础数据。同时考虑到详细机理的复杂性以及机理分析的计算量大和时耗长,本文基于误差传播的直接关系图形(Directed Relation Graph with Error Propagation,DRGEP)方法简化得到的包含709组分2793反应的正癸烷和包含820组分3115反应的正十一烷简化机理,使用DRGEP方法时所采用的数据点选自压力范围从1.0×10~5 Pa到1.0×10~6Pa,当量比范围从0.5到2.0,初始温度范围从600到1400时恒压点火的模拟结果在点火延迟时间附近区域的抽样,同时在正癸烷机理简化中选取正癸烷、O_2和N_2作为初始预选组分,正十一烷的机理简化中主要选取正十一烷、O_2和N_2作为初始预选组分,得到的简化机理在比较宽泛的条件下的预测结果与详细机理吻合很好。最后结合敏感度分析方法分析了正癸烷和正十一烷的点火延迟敏感性,考察了机理中影响点火的关键反应。结果表明:这些机理能够合理描述正癸烷和正十一烷的自点火特性,在工程计算流体力学仿真设计中有很好的应用前景。     

ortho-Selective ethylation of phenol with ethanol catalyzed by bimetallic mesoporous catalyst, CoAl-MCM-41

CoAl-MCM-41 (X) catalysts with X = n_Si/(n_Co + n_Al) various ratios were synthesized and ethylation of phenol with ethanol was studied in vapor-phase at temperatures between 250 and 450 °C. The products obtained were O-alkylated product (ethyl phenyl ether), C-alkylated products (2-ethylphenol and 4-ethylphenol), and C-/O-alkylated products (ethyl ethylphenyl ether). The phenol conversion increased significantly with reaction temperature over all the catalysts. The activity of the catalysts followed the order CoAl-MCM-41 (20) > CoAl-MCM-41 (50) > CoAl-MCM-41 (80). Selectivity between the C-alkylation and the O-alkylation depended on the factors such as acidity of the catalyst and the reaction temperature. CoAl-MCM-41 (20) catalyst displayed a phenol conversion of 40% and a selectivity of more than 80% for 2-ethylphenol under the optimized reaction condition. The ethanol to phenol ratios and the reactant flow rate are also influential for both activity and selectivity of CoAl-MCM-41 catalysts.     

A theoretical study of protonated OCnOH ions, n=3–8

Since ion-neutral reactions are a major component of the processes driving interstellar chemistry, most reaction network include protonated species. Besides, these ions are able to initiate chemical processes that would not occur with their neutral parents. In this contribution we report a systematic study of the protonated adducts of the OC_nO series (n=3–8) using the B3LYP level of theory. The structures of all possible O-protonated and C-protonated isomers of [OC_nOH⁺] have been determined together with their rotational constants, vibrational frequencies and intensities. Although it appears that these ions belong to two different series, odd-n and even-n, it is found that protonation occurs at the carbons second to the terminal oxygens for all n. The most stable structure is found to be the singlet ion whatever the singlet or triplet spin state of the parent species. However, due to the lack of efficient spin–orbit coupling, only the odd series [OC_nOH⁺] with n=3,5,7 should be formed on the singlet ground state surface. Analysis of the infrared intensities shows that the spectra are dominated by only one or two very strong bands (CC stretching) that carry most of the overall intensity in the 2200–2350 cm⁻¹ region.