KF对Na3AlF6-Al2O3熔盐电解阴极过程的影响

采用循环伏安法、交流阻抗法和方波伏安法等电化学测量技术,考察了KF对Na₃AlF₆-Al₂O₃熔盐电解体系的阴极过程的影响。研究结果表明：在Na₃AlF₆-Al₂O₃和Na₃AlF₆-Al₂O₃-KF电解质体系的循环伏安曲线中,还原峰随着扫描速率的增大而负移,氧化峰随着扫描速率的增大而正移,在扫描速率较低（25～100 mV·s^-1）的情况下,反应过程不可逆,反应过程相对平缓稳定;随着扫描速率的提高,电极可逆性相对提高。由于电极附近铝离子的聚合现象,使得在无KF的熔盐体系下,交流阻抗的高频区出现了感抗现象;在含KF的体系下,反应是由电化学反应过程和扩散过程共同控制的,且随着KF含量的增加,Warburg阻抗系数减小,电化学反应过程控制逐步取代扩散过程控制;反应电流也随之增大,氧化速率加快,还原和氧化过程可逆性降低。同时KF的加入抑制了铝的沉积,合金化作用比较明显,通过对阴极前波进行高斯拟合,得到不同KF含量（0、3%、5%）体系下的铝离子的电子转移数分别为1.19、1.02、0.75。     

用废弃煤矸石制备高比表面积的SiO2-Al2O3二元复合气凝胶

以兖州煤矸石为原料,经过低温焙烧、酸浸除杂、碱熔活化,采用溶胶-凝胶法和真空干燥法制备完整的块状SiO₂-Al₂O₃二元复合气凝胶。通过X射线衍射、扫描电镜、傅里叶变换红外光谱、氮气吸附等检测手段对原料、SiO₂-Al₂O₃气凝胶及其制备过程中得到的中间产物的物理、化学特性进行表征,研究SiO₂-Al₂O₃凝胶的形成机制。实验结果表明,煤矸石经过酸浸除去了大部分的铁、钾、碱土金属等杂质。在经过碱熔活化后,煤矸石主要组分石英和高岭石均转化为非晶态,反应活性提高。制备得到的SiO₂-Al₂O₃气凝胶是以Si-O-Si、Si-O-Al网络结构为骨架的非晶态纳米颗粒聚集体,其堆积密度0.37 g·cm^-3,比表面积483 m²·g^-1,比孔容1.87 cm³·g^-1,平均孔径10.29 nm,最可几孔径9.32 nm,具有较好的介孔特征。     

柠檬醛在La2O3/γ-Al2O3催化剂上的等温吸附

对柠檬醛-乙酸乙酯溶液中柠檬醛在La₂O₃/γ-Al₂O₃催化剂上等温吸附行为进行了研究。结果表明,30 ℃柠檬醛在La₂O₃/γ-Al₂O₃催化剂上的吸附动力学符合准二阶吸附动力学模型,吸附动力学方程为：1/q_t=2.350/t+0.063 3(R²=0.998 5)。（30~65） ℃柠檬醛在La₂O₃/γ-Al₂O₃催化剂上的等温吸附符合Langmuir方程,温度升高使柠檬醛的饱和吸附量增加,吸附热为32.19 kJ·mol^-1。     

B2O3改性Na2CO3催化剂用于甲醇脱氢制无水甲醛

以B₂O₃为助催化剂,采用研磨混合法改性Na₂CO₃催化剂,在固定床反应器中催化甲醇脱氢制备无水甲醛,考察催化剂的组成和反应条件等对催化反应的影响,采用XRD、TG-DTG、N₂吸附-脱附、SEM和CO₂-TPD等对催化剂进行表征。结果表明,以B₂O₃为助催化剂采用机械研磨混合法改性的Na₂CO₃催化剂,增加了催化剂的比表面积,在(10～30) nm增加了大量的孔道,平均孔径达18.44 nm,比表面积为1.65 m²·g^-1,且B₂O₃分布均匀,改性后的催化剂碱性降低,在催化甲醇脱氢制备无水甲醛的反应中,催化活性明显高于Na₂CO₃催化剂,表明B₂O₃改性Na₂CO₃催化剂能提高甲醇转化率和甲醛选择性。在B₂O₃/Na₂CO₃催化剂中B₂O₃质量分数为30%、甲醇进料质量分数为26%、反应温度为650 ℃和甲醇重时空速为2.94 h^-1条件下,甲醇转化率达59.97%,甲醛选择性达83.28%。     

Al-MCM-41介孔分子筛吸附喹啉的性能

在碱性条件下,采用水热晶化法,以偏硅酸钠为硅源,铝酸钠为铝源,CTAB为结构模板剂,成功合成出了含铝介孔分子筛Al-MCM-41。采用XRD、BET等手段对合成的Al-MCM-41进行表征,对柴油中的氮化物喹啉进行了吸附实验,考察了Al-MCM-41介孔分子筛对氮化物喹啉的吸附能力,探究了硅铝比为60的Al-MCM-41分子筛对喹啉溶液吸附的热力学和动力学行为,测得353.15～393.15 K 温度范围内的吸附等温线数据,用Langmuir、Freundlich方程对此进行拟合,并根据热力学原理计算得到吸附过程中的ΔH、ΔG、ΔS值和吸附表观活化能。结果表明, 硅铝比为60的Al-MCM-41具有较大的孔容、比表面积和较窄的孔径分布,结晶度和有序性高。等温吸附平衡符合Freundlich 等温线模型,其ΔH -0.7682 kJ·mol^-1,ΔG -28.1215 kJ·mol^-1, ΔS 73.2434 J·mol^-1·K^-1,吸附动力学符合Pseudo拟二级方程,E_a为2.8575 kJ·mol^-1。     

Al2O3/ACF复合电极材料的制备及性能表征

以H₃PO₄预处理后的活性炭纤维(ACF)毡为原料,采用浸渍煅烧法制备Al₂O₃/ACF复合电极材料;通过扫描电镜(SEM)、比表面积及孔径分析仪(BET)、X射线衍射(XRD)、X射线光电子能谱(XPS)、傅里叶红外光谱分析仪(FTIR)对负载Al₂O₃前后活性炭纤维的微观结构与电化学性能进行表征,利用自制的电吸附装置对NaCl模拟废水进行电吸附性能测试。结果表明,采用浸渍煅烧法成功制备了Al₂O₃/ACF复合电极材料,Al₂O₃/ACF复合体表面及孔道中有絮状或颗粒状的Al₂O₃存在,比表面积从1244.37 m²·g^-1降为974.59 m²·g^-1;同时,Al元素含量为1.06%,Al₂O₃以无晶相无定形态存在于纤维表面;Al₂O₃/ACF表面形成一些Al O键的官能团,其比电容比ACF提高76.5%。负载Al₂O₃后的ACF电极材料电吸附性能增强,除盐效率较ACF原样电极提升了2.3倍,且电极具有可再生性。Al₂O₃/ACF复合材料可以作为电极材料用于去除废水中的无机盐离子。     

超顺磁核-壳结构催化剂在裂化汽油烷基化脱硫中的应用

通过可控液相沉积制备具有超顺磁性能的介孔核-壳结构Fe₃O₄@nSiO₂@mSiO₂-Al₂O₃和H₃P₁₂W40/Fe₃O₄@nSiO₂@mSiO₂-Al₂O₃催化剂。以噻吩和异戊烯组成的模拟汽油烷基化反应作为探针反应,考察催化脱硫性能,并采用FT-IR、N2等温吸附-脱附、NH₃-TPD、VSM和SEM等方法对催化剂进行表征。结果表明,Fe₃O₄@nSiO₂@mSiO₂-Al₂O₃催化剂是具有超顺磁性和介孔结构特征的固体酸催化剂,其饱和磁化强度为46.3 emu·g^-1,低矫顽力为零,比表面积为342.6 m²·g^-1。模拟汽油在Fe₃O₄@nSiO₂@mSiO₂-Al₂O₃催化剂上170 ℃反应2 h,噻吩转化率为72.2%,负载质量分数40%的磷钨酸后,噻吩转化率达96.9%,催化活性、选择性和催化剂寿命均提高。     

载体焙烧温度对Ni/SiO2-Al2O3催化剂稳定性的影响

为了获得高水热稳定的负载Ni催化剂,延长催化剂在含水液相体系中的使用寿命,以不同温度焙烧的SiO₂-Al₂O₃为载体,采用浸渍法制备Ni/SiO₂-Al₂O₃催化剂,通过吡啶-原位傅立叶变换红外光谱、X射线衍射、NH₃-程序升温脱附和H₂-程序升温还原等方法进行表征,以水相1,4-丁炔二醇加氢为探针反应,研究载体焙烧温度对Ni/SiO₂-Al₂O₃催化剂催化加氢性能及含水体系中稳定性的影响。结果表明,在(400~800) ℃,随着载体焙烧温度升高,活性组分Ni存在状态及催化剂加氢活性变化较小,但催化剂的水热稳定性下降,造成这一现象的原因是随着载体焙烧温度升高,载体表面SiO₂聚集,暴露的Al³⁺增加,载体水合程度增大。载体焙烧温度400 ℃时,Ni/SiO₂-Al₂O₃催化剂表现出最佳的水热稳定性。     

绝缘衬底上化学气相沉积法生长石墨烯材料

利用化学气相沉积法,在Si衬底、蓝宝石衬底和SiC衬底上生长石墨烯材料,研究石墨烯的表面形貌、缺陷、晶体质量和电学特性。原子力显微镜、光学显微镜和拉曼光谱测试表明,Si₃N₄覆盖层可以有效抑制3C-SiC缓冲层的形成;低温生长有利于保持材料表面的平整度,高温生长有利于提高材料的晶体质量。5.08 cm蓝宝石衬底上石墨烯材料,室温下非接触Hall测试迁移超过1000 cm²·V^-1·s^-1,方块电阻不均匀性为2.6%。相对于Si衬底和蓝宝石衬底,SiC衬底上生长石墨烯材料的表面形态学更好,缺陷更低,晶体质量和电学特性更好,迁移率最高为4900 cm²·V^-1·s^-1。     

D301大孔吸附树脂吸附甘氨酸

通过静态吸附法研究了树脂D301对水溶液中甘氨酸的吸附行为。采用单因素实验法确定了最佳吸附条件为pH 7.5,温度35℃,时间45 min,吸附剂用量为0.1 g,在此条件下最大平衡吸附量可达794.81 mg·g^-1。同时探究了D301对甘氨酸溶液吸附的热力学行为,测得了303.15～318.15 K温度范围内的吸附等温线数据,用Langmuir、Freundlich、Temkin方程对此进行拟合,并根据热力学原理计算得到吸附过程中ΔH^θ、ΔG^θ、ΔS^θ值和吸附表观活化能。结果表明等温吸附平衡符合Langmuir等温线模型,其ΔH^θ 134.75 kJ·mol^-1,ΔG^θ-6.312 kJ·mol^-1, ΔS^θ 450.806 J·mol^-1·K^-1,E_a为81.27 kJ·mol^-1。研究结果表明D301对甘氨酸的吸附为化学吸附和物理吸附共存且为自发进行的吸热过程。     

The NaF-AlF3-Al2O3-Na2O system—I standard free energy of formation of α-aluminium oxide from emf measurements

The behaviour of oxygen and aluminium electrodes was studied by means of emf measurements in Na₃AlF₆ melts saturated with α-Al₂O₃ in the temperature range of 1233–1310 K. The results indicate that the electrodes are reversible when they are separated by an α-Al₂O₃ diaphragm. However, the aluminium electrode reacts with the melt to a certain extent. This means that the standard free energy data for α-Al₂O₃ are not easily derived from emf measurements in Na₃AlF₆ melts saturated with α-Al₂O₃. However, the emf for the following cell (Pt)O₂/Li₃AlF₆₍₁₎, AlF_3(s), Al₂O_3(s)//Li₃AlF₆₍₁₎, AlF_3(s), Al₂O_3(s)/Al was in excellent agreement with values derived from standard free energy data for α-Al₂O₃ formation in the JANAF Tables in the range of 1020–1275 K.     

Influence of fluorides on phase transition of α-Al2O3 formation

Homogeneous α-Al₂O₃ particles have been synthesized by introducing fluorides in the alumina precursor. The effects of LiF, ZnF₂ and AlF₃ additives on the phase transformation and the micrograph of the prepared α-Al₂O₃ particles are investigated. It is shown that, at a heating rate of 5 °C min⁻¹, addition of 2% fluoride relative to the initial mass of the precursor decreases the transformation temperature by 300 °C for LiF and AlF₃ and well-dispersed α-Al₂O₃ powders with average particle size of ∼2 μm were obtained. The mechanism of the influence can be explained by the formation of intermediate compound (AlOF), which was considered to accelerate the mass transportation from θ- to α-Al₂O₃. The addition of ZnF₂ can slight reduce the θ- to α-Al₂O₃ phase transition temperature. However, the effect on the phase transition of α-Al₂O₃ formation is not obvious.     

Molten salt synthesis of α-Al2O3 platelets using NaAlO2 as raw material

α-Al₂O₃ platelets were prepared by a molten salt synthesis method when NaAlO₂ was used as raw material. The effects of the stirring rate during the gel preparation, heating temperature, type and addition amount of molten salts, addition of plate-like α-Al₂O₃ seeds, additives such as TiOSO₄ and Na₃PO₄·12H₂O on the morphology of α-Al₂O₃ were studied. High stirring rate during the gel preparation and high heating temperature not only help to restrain the overlapping of α-Al₂O₃ platelets, but also improve the size distribution. When the heating temperature increases to 1200 °C, most of α-Al₂O₃ platelets are hexagonal in its morphology, and the size of platelets becomes relatively uniform. When Na₂SO₄-K₂SO₄ flux is used instead of NaCl-KCl flux, it is easy to obtain α-Al₂O₃ platelets with a big size. When the molar ratio of salt to final Al₂O₃ powders increases to 4:1, most of α-Al₂O₃ platelets are hexagonal, and the overlapping of powders is inhibited. The addition of a small amount of plate-like seeds has a significant effect on the size of α-Al₂O₃ platelets. With the increase of seed amount, the diameter of α-Al₂O₃ platelets tends to decrease. The addition of 5.45 wt.% TiOSO₄ results in the formation of hexagonal α-Al₂O₃ platelets with an average diameter of 5.1 μm and an average thickness of 1.4 μm. Thin α-Al₂O₃ platelets with a discal shape are obtained owing to the co-addition of 0.51 wt.% Na₃PO₄·12H₂O and 3 wt.% TiOSO₄.     

The solubility of selenate-AFt (3CaO·Al2O3·3CaSeO4·37.5H2O) and selenate-AFm (3CaO·Al2O3·CaSeO4·xH2O)

The Se(VI)-analogues of ettringite and monosulfate, selenate-AFt (3CaO·Al₂O₃·3CaSeO₄·37.5H₂O), and selenate-AFm (3CaO·Al₂O₃·CaSeO₄·xH₂O) were synthesised and characterised by bulk chemical analysis and X-ray diffraction. Their solubility products were determined from a series of batch and resuspension experiments conducted at 25 °C. For selenate-AFt suspensions, the pH varied between 11.37 and 11.61, and a solubility product, log K_so=61.29±0.60 (I=0 M), was determined for the reaction 3CaO·Al₂O₃·3CaSeO₄·37.5H₂O+12 H⁺⇔6Ca²⁺+2Al³⁺+3SeO₄²⁻+43.5H₂O. Selenate-AFm synthesis resulted in the uptake of Na, which was leached during equilibration and resuspension. For the pH range of 11.75 to 11.90, a solubility product, log K_so=73.40±0.22 (I=0 M), was determined for the reaction 3CaO·Al₂O₃·CaSeO₄·xH₂O+12 H⁺⇔4Ca²⁺+2Al³⁺+SeO₄²⁻+(x+6)H₂O. Thermodynamic modelling suggested that both selenate-AFt and selenate-AFm are stable in the cementitious matrix; and that in a cement limited in sulfate, selenate concentration may be limited by selenate-AFm to below the millimolar range above pH 12.     

L'electrolyse de l'alumine dans la cryolithe fondue. Etude du mecanisme de decharge cathodique a l'aide de l'electrode a disque tournant

The use of a rotating disk platinum electrode, on which aluminium has been previously deposited, has allowed us to determine the mechanism of the cathodic reaction during the electrolysis of cryolite—alumina melts. This mechanism requires three stages within the Nernst's diffusion layer. The first of these is the dissociation of the ion AlF^3?₆, at δ′ from the electrode, forming the ions Al³⁺ and F^?. The second one is the discharge of ions Al³⁺ diffusing towards the cathode and the third one, at δ″ from the electrode, is the reaction of the ions F^? with the ions AlF^?₄ to give again the ions AlF^3?₆. The ions Na⁺, which transport most of the current serve to maintain electro-neutrality.     

Interfacial tension between aluminum and cryolite melts during electrolysis of the systems Na3AlF6–AlF3 (NaF)–Al2O3

The interfacial tension between aluminum and cryolite melts containing different salt additions has been measured by the capillary depression method. The technique is based on the measurement of the capillary depression occurring when the capillary, which is moved vertically down through the molten salt layer, passes through the salt/metal interface. The depression is measured by simultaneous video recording of the immersion height of the alumina capillary. The interfacial tension was found to be strongly dependent on the n(NaF)/n(AlF₃) ratio (cryolite ratio, CR). At the cryolite ratio 2.28 (80 wt.% Na₃AlF₆ + 10 wt.% AlF₃ + 10 wt.% Al₂O₃ // Al, t = 1000 °C) the interfacial tension was 546 mN m⁻¹, while it was 450 mN m⁻¹ at the cryolite ratio 4.43 (80 wt.% Na₃AlF₆ + 10 wt.% NaF + 10 wt.% Al₂O₃ // Al, t = 1000 °C). Experiments under current flow conditions were also performed. During the electrolysis the interfacial tension at n(NaF)/n(AlF₃) ratio 2.28 decreased from 546 mN m⁻¹ at zero current to 518 mN m⁻¹ at 0.112 A cm⁻². The same trend was observed in the system with a cryolite ratio 4.43. The interfacial tension decreased from 450 mN m⁻¹ at zero current to 400 mN m⁻¹ at 0.112 A cm⁻². The consequent increase in interfacial tension of these systems caused by interruption of electrolysis was observed. Electrolysis of the system 25 wt.% NaF + 75 wt.% NaCl (eutectic mixture)/Al indicated no influence of applied current on the interfacial tension at 850 °C.     

Electrochemical micromachining using a solid electrochemical reaction at the metal/β″-Al2O3 microcontact

A simple solid state technique for electrochemical micromachining of metal substrates using a metal ion conductor (Na-β″-Al₂O₃) was proposed. The fundamental solid electrochemical cell consists of a (anode) metal substrate (M = Ag, Cu, Zn, and Pb)/pyramidal Na-β″-Al₂O₃/Ag (cathode) system, where the contact diameter between M/Na-β″-Al₂O₃ was extremely small, on the order of a few micrometer. Under an applied electric field, the metal substrate was electrochemically oxidized to metal ions (Mⁿ⁺) at the M/Na-β″-Al₂O₃ microcontact. These Mⁿ⁺ ions migrated into the Na-β″-Al₂O₃. As a result of continuous electrolysis, the metal substrate was locally consumed at the microcontact, and thus solid state electrochemical micromachining was accomplished. As expected, the machining size or depth depended on the electrolysis conditions (current, operating time) and the apex configuration of pyramidal Na-β″-Al₂O₃. Moreover, the scanning of the Na-β″-Al₂O₃ pyramid during electrolysis produced a fine patterned metal substrate. In the present paper, solid state electrochemical micromachining was performed for several metal substrates, and its advantages and disadvantages vis-a-vis the conventional electrochemical micromachining method are discussed in detail.     

Effects of the surface treatment of the Al2O3 filler on the lithium electrode/solid polymer electrolyte interface properties

The lithium deposition-dissolution process in solid polymer electrolytes containing Al₂O₃ filler treated under different conditions has been investigated comparing with the ionic conduction behavior of the electrolyte. The composite electrolytes were prepared from poly(ethylene oxide) (PEO), LiBF₄ and α-Al₂O₃ filler by using a dry process, where the surface of α-Al₂O₃ was beforehand modified by a wet process. The exchange current densities, i₀, of the lithium electrode process in P(EO)₂₀LiBF₄ with and without Al₂O₃ filler were determined by a micro-polarization method. The temperature dependence of i₀ provided similar values for activation energy, ca. 25 and 70 kJ mol⁻¹ in both temperature regions above and below 60 °C, respectively. The effect of the surface treatment of the filler on the lithium electrode process gave a different tendency from that on the ionic conductivity. The Al₂O₃ surface treated by alkali solution enhanced the electrode process to the largest extent among the fillers used here, while it led to rather poor cycling stability in voltammetry. The enhanced reaction rate at the lithium electrode/solid polymer electrolyte interface has probably resulted in the improved ion dissociation by the surface groups of the Al₂O₃ filler.     

Viscosity of NaFAlF3Al2O3 melt mixtures

Melt viscosities for the system NaFAlF₃Al₂O₃ over the experimentally accessible range are reported, the limiting factors being the solubility of Al₂O₃ and the vapour pressure. The temperature extends from the liquidus temperature to 1100°C. A recently developed precision oscillation viscometer is utilized. The results are discussed in a qualitative fashion.