碱式碳酸锌在二氧化碳气氛下的热分解动力学

运用TG/SDTA同步分析仪, 研究了碱式碳酸锌在流动二氧化碳气氛中的热分解过程及热分解动力学. 探讨了加热速率对反应过程的影响. 采用Friedman法对实验数据进行分析,结果表明,反应的活化能数值随着分解率的不同而变化, 由此推断该反应是由多步反应组合而成的,其平均表观活化能E_a为286.84 kJ/mol.     

In situ time-resolved FTIR investigation on the reaction mechanism of partial oxidation of methane to syngas over supported Rh and Ru catalysts

In situ time-resolved FTIR spectroscopy was used to study the reaction mechanism of partial oxidation of methane (POM) to synthesis gas and the reaction of CH₄/O₂/He (2/1/45, molar ratio) gas mixture with adsorbed CO species over Rh/SiO₂, Ru/γ-Al₂O₃ and Ru/SiO₂ catalysts at 500—600℃. It was found that CO is the primary product of POM reaction over reduced and working state Rh/SiO₂ catalysts. Direct oxidation of CH₄ is the main pathway of synthesis gas formation over Rh/SiO₂ catalyst. CO₂ is the primary product of POM over Ru/γ-Al₂O₃ and Ru/SiO₂ catalysts. The dominant reaction pathway for synthesis gas formation over Ru/γ-Al₂O₃ catalyst is via the reforming reactions of CH₄ with CO₂ and H₂O. For the POM reaction over Rh/SiO₂ and Ru/γ-Al₂O₃ catalysts, consecutive oxidation of surface CO species is an important pathway of CO₂ formation.     

pH值对砂岩中CO_2示踪矿物的稳定性影响实验研究

研究片钠铝石形成后保持稳定的pH值临界条件,对含片钠铝石砂岩展开了不同pH值条件下水-岩反应实验。结果表明:在封闭反应体系条件下,相同pH值(pH值为4)、不同体积(10、80、500 m L)条件下,随着反应溶液体积的增大,片钠铝石溶蚀程度增强,片钠铝石稳定性降低;相同体积(500 m L)、不同pH值(4pH9)条件下,pH值的增大对片钠铝石溶解速率影响不显著;pH值不是片钠铝石溶解程度发生改变的主控因素,在研究天然片钠铝石稳定性时,可以排除pH值造成的影响。     

全氧煤粉低氧浓度燃烧动力学参数的热重实验

利用热重分析仪研究了四种煤粉在低氧惰性气氛(即O2/CO2)下的着火特性、燃尽特性.实验在O2体积分数为7.5%~20%,升温速率20℃·min-1条件下进行.通过对Arrhenius和Coats Redfern方程进行最小二乘法的二元一次线性回归,求得煤粉在不同低氧浓度下的动力学参数.结果表明:随着O2体积分数降低,着火温度基本不变,燃尽温度增大;活化能、指前因子和反应级数都随着O2体积分数降低而不同程度地减小;活化能和指前因子之间存在补偿效应,计算可得等动力学温度和反应速率常数;当O2体积分数小于12.5%,随O2体积分数减小,煤粉的反应速率常数随反应温度增大而增大的趋势越来越平缓.     

Effect of CO<Subscript>2</Subscript> and H<Subscript>2</Subscript>O on gasification dissolution and deep reaction of coke

To more comprehensively analyze the effect of CO₂ and H₂O on the gasification dissolution reaction and deep reaction of coke, the reactions of coke with CO₂ and H₂O using high temperature gas-solid reaction apparatus over the range of 950-1250℃ were studied, and the thermodynamic and kinetic analyses were also performed. The results show that the average reaction rate of coke with H₂O is about 1.3-6.5 times that with CO₂ in the experimental temperature range. At the same temperature, the endothermic effect of coke with H₂O is less than that with CO₂. As the pressure increases, the gasification dissolution reaction of coke shifts to the high-temperature zone. The use of hydrogen-rich fuels is conducive to decreasing the energy consumed inside the blast furnace, and a corresponding high-pressure operation will help to suppress the gasification dissolution reaction of coke and reduce its deterioration. The interfacial chemical reaction is the main rate-limiting step over the experimental temperature range. The activation energies of the reaction of coke with CO₂ and H₂O are 169.23 kJ·mol-1 and 87.13 kJ·mol-1, respectively. Additionally, water vapor is more likely to diffuse into the coke interior at a lower temperature and thus aggravates the deterioration of coke in the middle upper part of blast furnace.     

气相质谱法研究 Fe 与 CO2-- CO 氧化反应动力学

采用气相质谱在线监测反应气体成分变化的方法,研究了1273~1473 K 范围内,不同比例 CO2- CO 混合气体对铁片恒温氧化的反应动力学.结果表明,氧化反应速率与二氧化碳分压呈线性关系,反应速率常数随 CO2/ CO 体积比值增大而减小,铁片氧化反应的表观活化能为(137.7±15.8) kJ·mol -1.该方法得到的结果与文献相比较,结果是可靠的,表明该方法可以用来在线研究气-固反应的动力学.     

Isothermal reduction kinetics of Panzhihua ilmenite concentrate under 30vol% CO-70vol% N2 atmosphere

The reduction of ilmenite concentrate in 30vol% CO-70vol% N₂ atmosphere was characterized by thermogravimetric and differential thermogravimetric (TG-DTG) analysis methods at temperatures from 1073 to 1223 K. The isothermal reduction results show that the reduction process comprised two stages; the corresponding apparent activation energy was obtained by the iso-conversional and model-fitting methods. For the first stage, the effect of temperature on the conversion degree was not obvious, the phase boundary chemical reaction was the controlling step, with an apparent activation energy of 15.55-40.71 kJ·mol-1. For the second stage, when the temperatures was greater than 1123 K, the reaction rate and the conversion degree increased sharply with increasing temperature, and random nucleation and subsequent growth were the controlling steps, with an apparent activation energy ranging from 182.33 to 195.95 kJ·mol-1. For the whole reduction process, the average activation energy and pre-exponential factor were 98.94-118.33 kJ·mol-1 and 1.820-1.816 min-1, respectively.     

淀粉水热还原铬酸钠过程动力学研究

为避免传统氧化铬工艺所产生的含铬副产物对环境的污染,本文提出了用淀粉水热还原铬酸钠生产氧化铬的新工艺。在对水热还原过程的反应规律及反应机理进行分析的基础上,对淀粉水热还原铬酸钠过程的动力学进行了研究,调查了影响六价铬还原转化率的因素。结果表明,反应温度、反应物浓度和反应时间是主要因素。选择等温、恒容、不可逆反应动力学模型来描述其反应过程,其动力学方程为：r=-d［Cr(Ⅵ)］/dt=1.367×10¹³e^{-100.566×1000/RT}［Cr(Ⅵ)］［St］,即指前因子、表观活化能和总反应级数分别为1.367×10¹³L/(mol·h)、100.566kJ/mol和二级或拟二级。该反应属化学反应控制,对Cr（Ⅵ）和淀粉均表现为一级或拟一级。     

基于胺法的旋流喷淋气液吸收烟气CO2的性能

为了强化CO_2捕集过程的气液传质,设计了一类多级旋流喷淋反应器,实验研究了典型的醇胺(乙醇胺(MEA)、二乙醇胺(DEA))脱除CO_2的分离效率和传质系数,并分析了操作条件的影响.结果表明:在相同的实验条件下,MEA的脱碳效率(最大值95%)大于DEA的脱碳效率(最大值92.3%).与相关研究数据的对比表明,多级旋流喷淋可以有效增强醇胺-CO_2喷淋反应系统的传质过程.醇胺溶液旋流气液吸收烟气CO_2的脱碳效率受操作条件的影响,其随着吸收剂质量分数、吸收剂流量和反应温度的增加而提高,随着烟气中CO_2体积分数和烟气流量的增加而降低.     

A model for estimating the rate constant between CO2-CO gas and molten slag containing iron oxides using optical basicity

A simple model for estimating the rate constant between CO₂-CO gas and molten slag containing iron oxides was developed using optical basicity only. In this model, the temperature dependence of the rate constant can be described by the Arrhenius law, and the activation energy can be expressed with a linear function of the slag??s optical basicity. The model was applied to some molten slag systems, such as FeO, FeO-CaO, FeO-SiO₂, FeO-Na₂O, FeO-CaO-SiO₂, FeO-SiO₂-P₂O₅, FeO-SiO₂-Na₂O, and FeO-CaO-SiO₂-P₂O₅. A comparison between the predicted results and measured data showed that the model worked well.     

The v-v energy transfer of highly vibrationally excited states (I)

The relaxation of the highly vibrationally excited CO (v = 1–8) by CO₂ is studied by timeresolved Fourier transform infrared emission spectroscopy (TR FTIR). 193 nm laser photolysis of the mixture of CHBr₃ with O₂ generates the highly vibrationally excited CO(v) molecules. TR FTIR records the intense infrared emission of CO(v→v-1). The vibrational populations of each level of CO(v) have been determined by the method of spectral simulation. Based on the evolution of the time resolved populations and the differential method, 8 energy transfer rate constants of CO(v = 1–8) to CO₂ molecules areobtained: (5.7±0.1), (5.9±0.1), (5.2±0.2), (3.4±0.2), (2.4±0.3), (2.2±0.4), (2.0±0.4) and (1.8±0.6) (10¹⁴ cm³ · molecule⁻¹ · s⁻¹), respectively. A two-channel energy transfer model can explain the feature of the quenching of CO(v) by CO². For the lower vibrational states of CO, the vibrational energy transfers preferentially to the u³ mode of CO² For the higher levels, the major quenching channel changes to the vibrational energy exchange between CO(v→v-1) and the u¹ mode of CO².     

Comparative analysis of the dissolution kinetics of galena in binary solutions of HCl/FeCl<Subscript>3</Subscript> and HCl/H<Subscript>2</Subscript>O<Subscript>2</Subscript>

A comparative study of the dissolution kinetics of galena ore in binary solutions of FeCl₃/HCl and H₂O₂/HCl has been undertaken. The dissolution kinetics of the galena was found to depend on leachant concentration, reaction temperature, stirring speed, solid-to-liquid ratio, and particle diameter. The dissolution rate of galena ore increases with the increase of leachant concentration, reaction temperature, and stirring speed, while it decreases with the increase of solid-to-liquid ratio and particle diameter. The activation energy (E _a) of 26.5 kJ/mol was obtained for galena ore dissolution in 0.3 M FeCl₃/8.06 M HCl, and it suggests the surface diffusion model for the leaching reaction, while the E _a value of 40.6 kJ/mol was obtained for its dissolution in 8.06 M H₂O₂/8.06 M HCl, which suggests the surface chemical reaction model for the leaching reaction. Furthermore, the linear relationship between rate constants and the reciprocal of particle radius supports the fact that dissolution is controlled by the surface reaction in the two cases. Finally, the rate of reaction based on the reaction-controlled process has been described by a semiempirical mathematical model. The Arrhenius and reaction constants of 11.023 s⁻¹, 1.25×10⁴ and 3.65×10² s⁻¹, 8.02×10⁶ were calculated for the 0.3 M FeCl₃/8.06 M HCl and 8.06 M H₂O₂/8.06 M HCl binary solutions, respectively.     

CuO/CeO2催化剂在温度变动过程中的CO-PROX催化性能

采用浸渍方法制备不同Cu/Ce原子比的CuO/CeO₂催化剂,用于富氢气体中CO优先氧化反应(CO-PROX),考察其在温度变动情况下的催化性能. 利用X射线衍射(XRD)、程序升温还原(TPR)方法对反应前后催化剂样品进行了表征. XRD测试表明,催化反应后的催化剂中有金属Cu0生成. 这与文献结果一致. 与不含CO₂的情况比较,当模拟富氢气体中含有CO₂时,低温段催化活性明显下降. Cu/Ce原子比为10%的催化剂在温度变动过程中具有较稳定的催化性能.      

摩擦化学反应活化能对CMP的影响

根据质量作用定律,测定了铜膜在静态腐蚀和化学机械抛光（Chemical Mechanical Polishing,CMP）两种反应条件下的化学反应速率常数;通过Arrhenius方程,测定了铜膜在两种反应条件下的化学反应活化能.结果表明：当抛光液温度为298.15 K,工作压力为13 780 Pa时,静态腐蚀条件下体系化学反应速率常数是114.80 s^-1,而CMP条件下体系的化学反应速率常数是412.11 s^-1,同时,CMP条件下的反应活化能为4 849.80 J,静态腐蚀条件下的反应活化能为31 870.30 J,由此得出,反应活化能的降低是CMP过程中的机械摩擦作用所致.因此,根据CMP过程中铜膜和抛光垫各自克服滑动摩擦力所作的系统功,推导出CMP过程中活化能降低值的系统功表达式,并通过改变工作压力和转速来验证该表达式的适用性.     

超声波下酸化碘酸钾和亚硫酸钠反应的反应速率研究

分别测定在有超声波作用和在无超声波作用条件下 ,酸化碘酸钾 (KIO3 )和亚硫酸钠 (Na2 SO3 )反应的反应速率方程式及活化能 ,从而研究该反应的机理以及超声波在该反应中的作用 ,并确定反应的最佳条件。实验得出 ,超声波对该反应有一定的促进作用 ,但是这种促进作用只提高反应的速率常数和降低反应的活化能 ,并没有改变反应机理。在超声波功率为 30 0W时 ,反应的速率方程表示式为 :v =k·c1 0 9(KIO3 ) ·c1 0 0 (Na2 SO3 )·c1 0 8(H+ ) ,其中 :k =95 0 (mol-1·L) 2 ·s-1,活化能为 17 35kJ·mol-1。实验还得出 ,在温度为2 98K时 ,当KIO3 与Na2 SO3 的初始浓度比为 2∶5 ,H+ 的初始浓度为 0 0 4 2 8mol·L-1,超声功率为 30 0W时 ,反应速率为最快 ,即v =4 31× 10 -4mol·L-1·s-1)。     

Density functional study on mechanism of CO oxidation with activated water on O/Au （1 1 1 ） surface

With density functional theory, the mechanism of water-enhanced CO oxidation on oxygen pre-covered Au （111） surface is theoretically studied. First, water is activated by the pre-covered oxygen atom and dissociates to OHads group. Then, OHads reacts with COads to form chemisorbed HOCOads, Finally, with the aid of water, HOCOads dissociates to CO2. The whole process can be described as 1/2H2Oads ＋ H2Oads ＋ 1/2Oads＋ COads→H3Osds ＋ CO2, gas. One CO2 is formed with only 1/2 pre-covered oxygen atom. That is why more CO2 is observed when water is present on oxygen pre-covered Au （111） surface. Activation energy of each elementary step is low enough to allow the reaction to proceed at low temperature.     

Effect of H2S concentration on the corrosion behavior of pipeline steel under the coexistence of H2S and CO2

The effect of H2S concentration on H2S/CO2 corrosion of API-X60 steel was studied by scanning electron microscopy, a weight-loss method, potentiodynamic polarization tests, and the electrochemical impedance spectroscopy technique. It is found that the cor-rosion process of the steel in an environment where H2S and CO2 coexist at different H2S concentrations is related to the morphological structure and stability of the corrosion product film. With the addition of a small amount of H2S, the size of the anode reaction region is de-creased due to constant adsorption and separation of more FeS sediment or more FeHS＋ions on the surface of the steel. Meanwhile, the dou-ble-layer capacitance is diminished with increasing anion adsorption capacity. Therefore, the corrosion process is inhibited. The general cor-rosion rate of the steel rapidly decreases after the addition of a small amount of H2S under the coexistence of H2S and CO2. With a further increase in H2S concentration, certain parts of the corrosion product film become loose and even fall off. Thus, the protection provided by the corrosion product film worsens, and the corrosion rate tends to increase.     

CO_2对煤低温氧化反应过程的影响实验研究

为了深入研究CO2对煤低温氧化反应的影响,利用程序升温油浴实验装置,研究在不同CO2浓度下煤样的自燃特性。采集南屯矿煤样,破碎并筛分出混合平均粒径为4.18 mm的煤样,向试验管煤样中通入不同配比的混合气体,实验控制升温速度为0.3℃/min,供气量为190 mL/min.测定在6种不同浓度CO2气氛下的煤样低温氧化特性,实验结果表明:CO2浓度越高,煤样耗氧速率越小,CO产生率降低。在起始阶耗氧速率相差不大,煤氧复合作用以物理吸附和化学吸附为主,后期阶段以化学反应为主,变化明显。相比于空气气氛下,CO2气氛下煤样活化能有所提高,在40~100℃的温度范围内煤氧作用的活化能值由17.85 kJ/mol升高至22.71 kJ/mol,氧化反应速率降低,表明CO2的加入降低了煤的氧化反应速率,抑制了煤的氧化反应。     

Ab initio MO study of reaction mechanism for carbonyl migration of Co complex

Ab initio method under the effective core potential (ECP) approximation is employed to study the reaction mechanism of carbonyl migration of the cycle of olefin hydroformylation catalyzed by a carbonyl cobalt HCo(CO)₃ at Hartree-Fock (HF) level. The structures of the reactant, transition state and product for the reaction are determined. The energy of each stationary point is corrected at MP2/LAN2DZ//LANL2DZ+ZPE (zero-point energy) level. The calculated activation barrier is 28.89 kJ/mol.     

Preferential Oxidation of CO in a Hydrogen-Rich Gas Through Au/NaY Catalytic Membranes

This paper describes novel Au/NaY catalytic membranes for preferential oxidation of CO (CO-PROX) in an H2-rich gas. NaY zeolite membranes with a high CO2/N2 separation factor were loaded with nanosized Au particles using an ion-exchanged method. X-ray diffraction analyses showed that the structure of the NaY zeolite was not damaged by the ion exchange process. CO-PROX experiments showed that the catalytic membranes had excellent catalytic performance for selective oxidation of CO. The CO/H2 molar ratio on the permeate side decreased with increasing operating temperature in the range of 80-200℃. At 200℃, almost no CO was detected from the permeate stream of a catalytic membrane with the feed con-taining 0.67% CO, 1.33% O2, 32.67% H2, and He in balance. Thus, these Au/NaY catalytic membranes show a promise for CO removal from hydrogen fuels.