双电极法现场快速检测地下水和湖水中碳酸氢根和碳酸根

地下水和湖水中碳酸氢根( HCO-3)和碳酸根( CO2-3)含量是地球化学碳行为和碳循环的重要表征,但两种离子的浓度易受环境影响而改变,因此,地下水和湖水中HCO-3和CO2-3真实含量的测定一直是个难题。实验利用CO2的水解平衡,通过pH电极和二氧化碳电极联用,建立了HCO-3和CO2-3现场快速测定的新方法,解决了地下水和湖水中HCO-3和CO2-3真实含量的测定难题。研究结果表明,在pH=4.8±0.1的底液中, HCO-3和CO2-3的线性范围分别为0.027~570 mg/L和1.25×10-8~39.7 mg/L。共存的金属离子、强酸阴离子(K+、Na+、Mg2+、Cl-、SO2-4,100 mg/L)、弱酸阴离子和弱酸(HSO-3、NO-2、HOAc,50 mg/L)对测定干扰小于5%。实际水样加标实验回收率在95.2%~99.2%之间,相对标准偏差为2.6%~3.7%。与酸碱滴定法进行对比,本方法的准确性良好。但方法受温度影响,因此标准溶液与样品应在同一温度下测量。总体而言,双电极法灵敏、快速、经济且电极携带方便、操作简单、对环境要求不高,十分适合现场和室内一般自然水体的快速检测。本方法已成功应用于青海省地下水和青海湖湖水中HCO-3和CO2-3的现场测定。实验表明,海东地区地下水样品pH在6.4~7.4之间,HCO-3含量为234~4096 mg/L,CO2-3含量为0.16~1.89 mg/L；青海湖湖水样品pH≈8.7,HCO-3含量范围在1.36~1.86 g/L,CO2-3含量在32.3~43.9 mg/L,与文献结果吻合。     

Reactive Polymer as Artificial Solid Electrolyte Interface for Stable Lithium Metal Batteries

Lithium (Li) metal anodes have the highest theoretical capacity and lowest electrochemical potential making them ideal for Li metal batteries (LMBs). However, Li dendrite formation on the anode impedes the proper discharge capacity and practical cycle life of LMBs, particularly in carbonate electrolytes. Herein, we developed a reactive alternative polymer named P(St-MaI) containing carboxylic acid and cyclic ether moieties which would in situ form artificial polymeric solid electrolyte interface (SEI) with Li. This SEI can accommodate volume changes and maintain good interfacial contact. The presence of carboxylic acid and cyclic ether pendant groups greatly contribute to the induction of uniform Li ion deposition. In addition, the presence of benzyl rings makes the polymer have a certain mechanical strength and plays a key role in inhibiting the growth of Li dendrites. As a result, the symmetric Li||Li cell with P(St-MaI)@Li layer can stably cycle for over 900 h under 1 mA cm⁻² without polarization voltage increasing, while their Li||LiFePO₄ full batteries maintain high capacity retention of 96 % after 930 cycles at 1C in carbonate electrolytes. The innovative strategy of artificial SEI is broadly applicable in designing new materials to inhibit Li dendrite growth on Li metal anodes.     

载体表面酸碱性质对无碱水溶液中Au催化的甘油氧化反应产物选择性的调控作用

甘油(GL)是一种重要的生物平台分子,通过催化选择氧化反应将其转化为具有高附加值化学品是可持续发展化学化工的重要课题之一.以Au为催化剂的GL水相选择氧化反应可以生成甘油酸(GLA)、二羟基丙酮(DHA)、羟基丙二酸(TTA)、羟基乙酸(GCA)和乳酸(LA)等多种产物.通常,该反应需要碱(NaOH)存在时才能进行,产物往往以GLA为主(选择性40%-70%),副产物主要有GCA, TTA和草酸(OA).一般认为,可溶性碱(OH-)是通过夺取GL分子中羟基上的质子而诱发反应的.尽管在Au催化的反应体系中从未检测到有甘油醛(GLD)生成, GLD和/或DHA被认为是该反应的中间物种.本课题组前期工作表明,氧化物(TiO2, Al2O3, ZrO2, CuO等)负载的纳米Au催化剂能够在无碱(无外加OH-)水溶液中选择性催化GL氧化生成DHA(而不是GLA).因此, OH-的存在与否很可能会改变水溶液中Au催化剂上GL氧化反应的途径.本文试图回答当GL的水溶液中不存在NaOH时, Au催化剂载体的表面酸碱性质是否也会对GL氧化反应的选择性产生调控作用.我们选用Mg/Al比(x)不同的MgO-Al2O3样品为Au催化剂的载体,以尿素为沉淀剂,采用沉积沉淀法制备了相应的Au/MgO-Al2O3(x)催化剂样品.采用X射线衍射、电感耦合等离子体-原子发射光谱仪、透射电镜以及N2吸附-脱附等温线等对MgO-Al2O3(x)和/或Au/MgO-Al2O3样品的物相、元素组成、Au颗粒大小以及比表面积等进行了表征分析;采用NH3和CO2程序升温脱附(TPD)分别对MgO-Al2O3(x)载体表面的酸、碱性进行了测定. NH3-TPD和CO2-TPD结果表明,随着Mg/Al比x从0增加至4.8, MgO-Al2O3(x)的表面酸量从0.94降到0.20μmol/m2,而其表面碱量却从0.05剧增至0.80μmol/m2.因此,载体中MgO含量越多或Mg/Al比越大,其酸性越弱而碱性越强.在无碱水溶液中的催化反应结果表明, Au/MgO-Al2O3(x)上GL氧化反应的主要产物为DHA, GLA以及GCA等.随着x值(催化剂表面碱性)不断增大,产物DHA的选择性从约80%下降到10%左右,而GLA的选择性却从约4%增加至约50%.当载体为酸性最强的Al2O3(x =0)时,产物DHA的选择性为最高(80%).由此可见,载体表面的酸碱性质决定了无碱水溶液中Au催化剂上的GL氧化产物的分布. 此外,当保持Au粒子的尺寸基本不变(如3.1或6.6 nm左右),而改变载体的酸碱性质时, Au/MgO-Al2O3催化GL氧化反应的活性(TOF)可相差8-9倍.本文还通过改变Au/MgO-Al2O3样品焙烧温度,制备了表面酸碱性质相同而颗粒大小不同的三个Au/MgO-Al2O3(0.2)催化剂,考察了Au粒径对GL氧化反应选择性的影响.在这三个催化剂上, Au颗粒的平均尺寸分别为2.8,3.2和6.6 nm, GL氧化反应的产物选择性近乎相同(DHA和GLA的选择性分别为65%和15%左右),但平均尺寸为6.6 nm Au粒子的催化活性(TOF)是3.2 nm Au粒子的1.6倍,2.8 nm Au粒子的2.7倍.因此,本文建立了载体表面酸碱性质与无碱水溶液中GL氧化产物选择性之间的关系,通过改变载体表面酸碱性质实现了对无碱水溶液中Au催化剂上GL氧化反应选择性的调控.尽管载体酸碱性质和Au粒子尺寸都对Au/MgO-Al2O3催化剂的本征活性有重要影响,但载体酸碱性质的影响更显著.     

预处理温度对甘油氢解双金属Ir-Re催化剂性能的影响

在生物柴油生产过程中大量副产的甘油是重要的生物质转化平台化合物.通过甘油氢解制备高附加值的1,3-丙二醇是甘油的资源化利用的重要途径,能够显著提高生物柴油产业的经济效益,同时也是探究更复杂的糖醇类化合物氢解的模型反应.因此,甘油氢解制备1,3-丙二醇成为当前学术界的研究热点.通常,以Re或W为助剂修饰的贵金属催化剂是有效的甘油选择性氢解制1,3-丙二醇的催化剂,其中,双金属Ir-Re催化剂是目前最高效的催化剂之一.甘油氢解反应是典型的结构敏感性反应,它的催化性能依赖于双金属催化剂的结构,而后者受制备工艺条件如热处理方式及条件的影响.最近,我们报道了以直接还原法(即浸渍-还原法)制备的Ir-Re催化剂为合金结构,在甘油氢解中表现出更为优越的反应活性及目前报道中最高的1,3-丙二醇生成速率,并提出了可能的双功能反应机理,即催化剂表面的Re-OH酸性位和Ir均为甘油氢解的活性位.本文采用直接还原法制备KIT-6(具有三维有序介孔孔道结构的SiO2)负载的双金属Ir-Re催化剂,进一步研究还原温度对Ir-Re/KIT-6的结构及其催化性能的影响,揭示催化剂表面酸性在甘油氢解反应中的重要作用并阐明其构-效关系.结果显示不同还原温度(400–700 oC)制备的催化剂的比表面积、孔体积及孔径数据基本一致,表明还原温度对Ir-Re/KIT-6的织构性质的影响很小.根据程序升温还原和透射电镜-能量散射点扫描结果可知,不同温度还原后的催化剂表面Ir和Re均以金属态形式存在,同时两者存在直接的相互作用,形成了Ir-Re合金;而漫反射红外图谱上CO吸附峰的红移以及峰形的显著变化也印证了Ir-Re合金结构的形成. TEM结果显示,在400–700oC还原后得到的Ir-Re合金纳米粒子均匀分布于KIT-6上,尺寸基本一致(2.5–2.8 nm),与CO化学吸附结果一致.此外, NH3-程序升温脱附结果表明催化剂的酸量随着还原温度的升高而逐渐增大,但酸强度没有明显变化,这可能是由于高温还原进一步促进了Ir和Re的相互作用,在原子尺度上混合更为均匀所致. Ir-Re催化剂上甘油氢解反应结果显示,随着还原温度由400提高到600 oC,所制催化剂的活性先增加而后趋于稳定.由此可以认为Ir-Re催化性能的差异与Ir分散度和酸强度的关联较小,主要是由于催化剂表面酸量所致.直接关联酸量与反应活性(以反应时间内的平均1,3-丙二醇生成速率表示)可以看到,反应活性随着酸量的增加而线性增大,表明Ir-Re/KIT-6的表面酸量直接影响了甘油氢解反应速率的快慢,即酸位Re-OH直接参与了催化反应.众所周知, Re金属活化H2的能力很弱,而金属Ir在反应中起到催化加氢的作用.实验结果很好地印证了Ir-Re合金催化甘油氢解反应的双功能反应机理,即酸位Re-OH与金属Ir协同参与氢解反应,分别作为甘油吸附位和H2活化中心,因此提高催化剂的表面Re-OH的数量将是进一步提高催化活性的途径之一.总的来说,在400–700 oC还原得到的Ir-Re/KIT-6催化剂具有Ir-Re合金结构.还原温度对催化剂的织构性质、金属纳米粒子的尺寸、Ir的分散度及表面酸强度的影响不大,但还原温度的升高有利于Ir和Re的相互作用,显著提高了催化剂的表面酸量,因而提高催化活性.此外,表面酸量和反应活性的线性关系表明酸位Re-OH参与Ir-Re合金催化甘油氢解反应,印证了双功能反应机理.     

Addendum to “Volumetric properties of binary liquid-phase mixture of (water + glycerol) at temperatures of (278.15 to 323.15) K and pressures of (0.1 to 100) MPa” [J. Chem. Thermodyn. 79 (2014) 135–158]: Effect of pressure on excess thermodynamic characteristics of mixture water + glycerol

Experimentally determined volumetric properties of the liquid binary mixture of {water (1) + glycerol (2)} were processed to calculate the changes of the following thermodynamic parameters with pressure: excess molar Gibbs free energy, ${\mathrm{\Delta }}_{P_o\to P}{G}_m^E$, excess molar entropy, ${\mathrm{\Delta }}_{P_o\to P}{S}_m^E$, excess molar enthalpy, ${\mathrm{\Delta }}_{P_o\to P}{H}_m^E$, as well as the enthalpy of mixing of water and glycerol, $H_m^E$, at 100 MPa. The mixing enthalpies of water and glycerol, $H_m^E$, became more exothermic with pressure increasing at all temperatures studied.     

Graded regulation technology for enhanced oil recovery and water shutoff in pore-cavity-fracture carbonate reservoirs

Although a single type of chemical agent (eg, gels, microspheres, surfactants, etc.) has achieved some effects in enhanced oil recovery of carbonate reservoirs, for pore-cavity-fracture carbonate reservoirs, the use of a single type of chemical agent does not perform well. The main objective of this study is to study the effect of different types of chemical agents in enhanced oil recovery of complex carbonate reservoirs. In order to determine the screening principle of chemical agents, the types of water channeling in the North Troyes reservoir were analyzed. For complex fractures, step by step plugging, multi-agent and multi-slug comprehensive intervention is carried out to ensure the plugging of high-permeability channels and inhibit the seepage of large channels. It can plug channeling fracture channel, adjust secondary dominant channel and reduce matrix flow resistance, so as to expand macroscopic swept volume and improve microscopic water flooding efficiency. The results show that it is difficult to comprehensively control water channeling in pore-cave-fracture carbonate reservoir, and the reservoir heterogeneity in the test area can be improved by mixing different types of control and flooding agents and carrying out deep profile control. The plugging rate of gel is 97.18 %, and the oil–water selection ratio is 0.45 in fractured core; the expansion rate of nano - microspheres is more than 3 times; the wetting modifier can improve the imbibition oil displacement efficiency by 14.76%, and the test result shown that nano - microspheres and wetting modifier have good synergistic oil displacement effect. The field application result shown that daily oil production of oil well in the test area increased by 5.0 m³/d and the daily water rate decreased by 19.0% compared with that before the control flooding. The findings of this study can help for better understanding of enhanced oil recovery in pore-cave-fracture carbonate reservoir.     

An Isolable Silicon Dicarbonate Complex from Carbon Dioxide Activation with a Silylone

The first isolable molecular silicon dicarbonate complex (bis‐NHC)Si(CO₃)₂ 2 (bis‐NHC=H₂C[{NC(H)=C(H)N(Dipp)}C:]₂, Dipp=2,6‐iPr₂C₆H₃) was synthesized by facile reaction of the bis‐N‐heterocyclic carbene stabilized silylone (bis‐NHC)Si 1 , bearing a zero‐valent silicon atom, with carbon dioxide. The monomeric silicon dioxide complex (bis‐NHC)SiO₂ 3 supported by the bis‐NHC ligand was proposed as a key intermediate resulting from double oxygenation of the zero‐valent silicon atom in 1 by two molar equivalents of CO₂ under liberation of CO; its subsequent Lewis acid–base reaction with CO₂ leads to 2 which has been fully characterized including an single‐crystal X‐ray diffraction analysis. Its electronic structure, spectroscopic data and the thermochemistry of the formation have been studied quantum‐chemically.     

Role of preparation parameters of Cu–Zn mixed oxide catalyst in solvent free glycerol carbonylation with urea

Solvent-free carbonylation of glycerol with urea to glycerol carbonate (GC) was achieved over heterogeneous Cu–Zn mixed oxide catalyst. Cu–Zn catalysts with different ratios of Cu:Zn were prepared using co-precipitation (CP) and oxalate gel (OG) methods. As compared to CuO–ZnO(2:1) catalyst prepared by oxalate gel (OG) method, much higher conversion of glycerol and highest selectivity towards glycerol carbonate (GC) was achieved with CuO–ZnO_CP(2:1) catalyst. Physicochemical properties of prepared catalysts were investigated by using XRD, FT-IR, BET, TPD of CO₂ and NH₃ and TEM techniques. The effect of stoichiometric ratio of Cu/Zn, calcination temperature of CuO–ZnO catalysts and effect of reaction parameters such as molar ratio of substrates, time and temperature on glycerol conversion to GC were critically studied. Cu/Zn of 2:1 ratio, glycerol–urea 1:1 molar ratio, 145 ​°C reaction temperatures were found to be optimized reaction conditions to achieve highest glycerol conversion of 86% and complete selectivity towards GC. The continuous expel of NH₃ from reaction the mixture avoided formation of ammonia complex with CuO–ZnO catalyst. As a result of this, CuO–ZnO catalyst could be recycled up to three times without losing its initial activity.     

Ultrasound-assisted fast encapsulation of metal microparticles in SiO2 via an interface-confined sol-gel method

Although the traditional Stoˇber process-based methods are widely used for encapsulation of metal nanoparticles in SiO₂, these time-consuming methods are not effective for coating metal microparticles with a uniform SiO₂ layer of desired thickness. Herein, an ultrasound-assisted, interface-confined sol–gel method is proposed for fast encapsulation of metal microparticles in SiO₂, and the encapsulation of Sn microparticles is chosen as an example to illustrate its feasibility. The proposed method involves covering metal microparticles with liquid films that contain water, alcohol, surfactant (Span-80) and catalyst (NH₄F) and then ultrasonically dispersing these particles into cyclohexane, where tetraethylorthosilicate (TEOS) is added. To ensure the hydrolysis-condensation reactions of TEOS occurring at the particle-cyclohexane interface so that the formed SiO₂ is coated on the particles, the microparticles should be well dispersed into cyclohexane with the liquid films being not broken away from their surfaces. It is found that the assistance of probe sonication and the addition of surfactant are crucial to achievement of a good dispersion of metal microparticles in cyclohexane. And using high-viscosity alcohol (namely glycerol), controlling the volume ratio of water to alcohol and the amount of water, and choosing a suitable ultrasonic power are essential for preventing the formation of free SiO₂ (namely SiO₂ that is not coated on the particles), which is a result that the liquid films escape from the particle surfaces under ultrasonic cavitation. Our results have also revealed that the thickness of SiO₂ layer can be adjusted by changing the reaction time or the total amount of water. In particular, the thickness of SiO₂ layer can be easily raised by simply repeating the encapsulation procedure. Compared with the traditional Stoˇber process-based methods, the proposed method is time-saving (reaction time: about 30 min vs. more than 12 h) and extremely effective for coating microparticles with a continuous, uniform SiO₂ layer of desired thickness.     

CuI/l-proline catalyzed click reaction in glycerol for the synthesis of 1,2,3-triazoles

Despite the apparent simplicity of the copper(I) iodide catalyzed CuAAC reaction, the conversion of the catalytic species, i.e. Cu(I) to thermodynamically more stable Cu(II), via aerial oxidation or disproportionation is a major issue. To stabilize the Cu(I) species, the reaction is ideally carried out under an inert atmosphere in the presence of additives such as alcohols, amines, thiols, and aldehydes. Herein, we report the first CuI catalyzed click reaction without an inert atmosphere by employing the CuI/l-proline system in glycerol. The method showed remarkable stability towards sensitive functional groups such as acetonides and 1,2,4-trioxanes.