Thermodynamic investigation on M–Te–O (M = Sc, Y) system

The standard Gibbs energy of formation of M₂TeO₆ and M₆TeO₁₂ (where M = Sc, Y), was determined from its vapor pressure measurements by employing thermogravimetry-based transpiration technique. This technique was validated by measuring the vapor pressure of well-studied substances such as TeO₂(s) and CdCl₂(s). The temperature dependence of the vapor pressure of TeO₂(g) over the mixtures M₆TeO₁₂ + M₂O₃ (where M = Sc, Y), generated by the incongruent vaporization reaction, M₆TeO₁₂(s) → 3M₂O₃(s) + TeO₂(g) + ½O₂(g) were measured in the temperature range 1,413–1,473 K and 1,623–1,743 K for Sc₆TeO₁₂(s) and Y₆TeO₁₂(s), respectively. Similarly, the vapor pressure of TeO₂(g) over the mixtures M₂TeO₆(s) + M₆TeO₁₂(s) generated by the vaporization reaction, 3M₂TeO₆(s) → M₆TeO₁₂(s) + 2TeO₂(g) + O₂(g) was measured in the temperature range (1,223–1,293 K) and (1,333–1,423 K) for Sc₂TeO₆(s) and Y₂TeO₆(s), respectively. From the vapor pressure measurements, the standard Gibbs energy of formation of M₆TeO₁₂ and M₂TeO₆ were derived.     

Construction of M–M bonds in late transition metal complexes

The 16-electron Co, Rh and Ir half-sandwich complexes of Cp^#M[E₂C₂(B₁₀H₁₀)] and Cp^#M(E₂S₂C₆H₄) (M = Co, Rh, Ir, Ru; E = S, Se) containing chelating 1,2-dicarba-closo-dodecaborane-1,2-dichalcogenolato ligands and benzenedithiolato ligands are promising precursors to build multimetallic clusters by reactions with low oxidation state late transition metal reagents. Such reactions lead to successful constructions of M–M bonds between iridium, rhodium, cobalt, ruthenium, and other late transition metals. Most of these complexes have been characterized by X-ray single crystal determinations and some have been studied by computational methods. Such theoretical studies reveal the covalent bonding nature of those multinuclear complexes. Some of these clusters have been found to have interesting nonlinear optical properties.     

Thermodynamic studies on the systems M–Te–O (M = Nd,Sm)

The standard Gibbs energies of formation of Nd₂TeO₆ and M₆TeO₁₂ (where M = Nd, Sm) were determined from vapour pressure measurements. The vapour pressure of TeO₂(g) was measured by employing thermogravimetry-based transpiration technique. The temperature dependence of the vapour pressure of TeO₂(g) over the mixtures Nd₂TeO₆+Nd₆TeO₁₂, generated by the incongruent vapourisation reaction, 3Nd₂TeO₆(s) → Nd₆TeO₁₂(s)+2TeO₂(g)+O₂(g), was measured in the temperature range 1,408–1,495 K. Similarly, the vapour pressure of TeO₂(g) over the mixtures M₆TeO₁₂+M₂O₃ (where M = Nd, Sm), generated by the incongruent vapourisation reaction, M₆TeO₁₂(s) → 3M₂O₃(s)+TeO₂(g)+½O₂(g), was measured in the temperature range 1,703–1,773 and 1,633–1,753 K for Nd₆TeO₁₂(s) and Sm₆TeO₁₂(s), respectively. Enthalpy increments of M₂TeO₆(s) (where M = Nd, Sm) were determined by inverse drop calorimetric method in the temperature range 573–1,273 K. The thermodynamic functions, viz., heat capacity, entropy and free energy functions, were derived from the measured values of enthalpy increments. A mean value of ?2,426.2 ± 0.6 and ?2,417.9 ± 1.1 kJ mol^?1 was obtained for $ \Updelta_{\text{f} } H_{298}^{\text{o}} $ (Nd₂TeO₆, s) and $ \Updelta_{\text{f}} H_{298}^{\text{o}} $ (Sm₂TeO₆, s), respectively, by combining the value of $ \Updelta_{\text{f}} G^{\text{o}} $ (Nd₂TeO₆, s) and $ \Updelta_{\text{f}} G^{\text{o}} $ (Sm₂TeO₆, s) derived from vapour pressure data and the free energy functions derived from the drop calorimetric data.     

High pressure phase behavior and modeling of CO2–propyl acrylate and CO2–propyl methacrylate systems

High pressure phase behavior are obtained for CO₂–propyl acrylate system at 40, 60, 80, 100 and 120 °C and pressure up to 161 bar and for CO₂–propyl methacrylate systems at 40, 60, 80, 100 and 120 °C and pressure up to 166 bar. The solubility of propyl acrylate and propyl methacrylate for the CO₂–propyl acrylate and CO₂–propyl methacrylate systems increases as the temperature increases at constant pressure. The CO₂–propyl acrylate and CO₂–propyl methacrylate systems have continuous critical mixture curves that exhibit maximums in pressure at temperatures between the critical temperatures of CO₂ and propyl acrylate or propyl methacrylate. The CO₂–propyl acrylate and CO₂–propyl methacrylate systems exhibit type-I phase behavior with a continuous mixture critical curve.The experimental results for CO₂–propyl acrylate and CO₂–propyl methacrylate systems are modeled using both the statistical associating fluid theory (SAFT) and Peng–Robinson equations of state. A good fit of the data are obtained with SAFT using two adjustable parameters for CO₂–propyl acrylate and CO₂–propyl methacrylate systems and Peng–Robinson equation using one and two adjustable parameter for CO₂–propyl acrylate and CO₂–propyl methacrylate system.     

Well-dispersed porous Fe–N–C catalyst towards the high-selective and high-efficiency conversion of CO2 to CO

In this study, through direct pyrolysis of a nitrogen-rich metal-organic framework of Fe-BTT at different temperatures and followed by acid treatment, we prepared a series of Fe–N–C_T (T = 800–1000 °C) composite catalysts with uniform cubic morphology and homogeneously distributed active sites. Acid leaching leads to the removal of excess Fe NPs and the exposure of more pyridinic N and porphyrin-like Fe–N_x sites and creates a higher specific surface area. Structural and electrochemical performance test results showed that Fe–N–C₉₀₀ catalyst exhibited the highest selectivity for CO product at –1.2 V vs. Ag/AgCl, with 496 mV of overpotential and 86.8% of Faraday efficiency, as well as excellent long-term stability, due to the good inheritance from rich-N Fe–BTT precursor.     

The Stabilization Effect of CO2 in Lithium–Oxygen/CO2 Batteries

The lithium (Li)–air battery has an ultrahigh theoretical specific energy, however, even in pure oxygen (O₂), the vulnerability of conventional organic electrolytes and carbon cathodes towards reaction intermediates, especially O₂⁻, and corrosive oxidation and crack/pulverization of Li metal anode lead to poor cycling stability of the Li-air battery. Even worse, the water and/or CO₂ in air bring parasitic reactions and safety issues. Therefore, applying such systems in open-air environment is challenging. Herein, contrary to previous assertions, we have found that CO₂ can improve the stability of both anode and electrolyte, and a high-performance rechargeable Li–O₂/CO₂ battery is developed. The CO₂ not only facilitates the in situ formation of a passivated protective Li₂CO₃ film on the Li anode, but also restrains side reactions involving electrolyte and cathode by capturing O₂⁻. Moreover, the Pd/CNT catalyst in the cathode can extend the battery lifespan by effectively tuning the product morphology and catalyzing the decomposition of Li₂CO₃. The Li–O₂/CO₂ battery achieves a full discharge capacity of 6628 mAh g⁻¹ and a long life of 715 cycles, which is even better than those of pure Li–O₂ batteries.     

Theoretical study of group 11 metal–silonyl complexes: M–SiO and M–(SiO)2 (M = Cu, Ag, or Au)

 The spectroscopic properties of M–SiO and M–(SiO)₂ (1–1 and 1–2 complexes with M = Cu, Ag, or Au) have been theoretically studied. It has been shown that both M–SiO and M–(SiO)₂ compounds in their ground state are bent with a metal–Si bonded structure. The calculated M(ns) spin density agrees well with the electron spin resonance experimental data. From a topological analysis, it has been shown that a rather large charge transfer occurs from the metal towards the SiO moiety, and that the M–Si bond energy correlates with the electron density located at the M–Si bond path (bond critical point). Received: 6 July 2000 / Accepted: 11 October 2000 / Published online: 19 January 2001     

Tautomeric reaction equilibrium of ethyl acetoacetate in CO2–n-pentane and CO2–ethanol mixed solvents in the critical region

The tautomeric equilibrium constant K_C of ethyl acetoacetate (EAA) in CO₂–n-pentane and CO₂–ethanol was studied by UV–VIS spectroscopy at 308.2 K over the pressure range from 6.5 to 9.0 MPa. This work focuses on how the tautomeric equilibrium changes with pressure and composition of the mixed solvents in the near critical region. The results showed that the effect of pressure on K_C was very limited at pressures much higher than the phase separation pressures. However, the K_C increased sharply as the pressure approached the critical point or the bubble point of the mixed solvents.     

Co–Cu–La catalysts for selective CO2 hydrogenation to higher hydrocarbons

Copper and lanthanum promoted cobalt catalysts for CO₂ hydrogenation to higher hydrocarbons are described. The catalysts were prepared by the self-propagating high-temperature synthesis followed by alkaline leaching. They are active in CO₂ hydrogenation at 200 °C under 10 bar pressure (CO₂ : H₂ = 1 : 3) with selectivity to C₂₊ alkanes up to 39%; no alkenes and alcohols are formed under these experimental conditions.     

Enhanced thermal properties of Li2CO3–Na2CO3–K2CO3 nanofluids with nanoalumina for heat transfer in high-temperature CSP systems

Nanofluids of Li₂CO₃–Na₂CO₃–K₂CO₃ improved by three nano-Al₂O₃ samples are firstly prepared by means of two-step aqueous method to enhance thermal properties for high-temperature heat transfer, when used as heat transfer fluids and thermal energy systems for concentrating solar power systems. Specific heat of ternary carbonates containing Al₂O₃ of 0.2, 0.4, 0.8, 1.0, 1.4 and 2.0 mass% is measured, and nanofluids with 1.0 mass% of 20-nm Al₂O₃, 1.0 mass% of 50-nm Al₂O₃ and 0.8 mass% of 80-nm Al₂O₃ are selected as superior candidates. The maximum enhancement of specific heat is 18.5% in solid and 33.0% in liquid, 17.9% in solid and 22.7% in liquid, 13.2% in solid and 17.5% in liquid for nanofluids containing 20-, 50- and 80-nm Al₂O₃. Thermal conductivity is, respectively, improved by 23.3, 28.5 and 30.9% under the addition of Al₂O₃. New chemical bonds and crystals are scarcely formed in composites through FT-IR and XRD determination. SEM images certify that nano-Al₂O₃ are homogeneously mixed into nanofluids and this structure may be a critical incentive for enhancing thermal properties. There are no significant changes with respect to the heat flow, melting/freezing point and latent heat after the 30 circles of determination. Briefly, it can be speculated that these nanofluids will exhibit tremendous potential in the coming applications of heat transfer and thermal storage for concentrating solar power systems.

     

Ionic liquid–formulated hybrid solvents for CO2 capture

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Selective catalytic reduction of NO with CO on Pt/W–Ce–Zr catalysts

Various Pt catalysts (Pt/ZrO₂, Pt/CeO₂, Pt/CeZrO, Pt/WO₃/ZrO₂ and Pt/WO₃/CeZrO) were prepared and characterized, and their catalytic reduction reactions of NO by CO, with or without the presence of excess oxygen, were investigated. The results of temperature-programmed experiments showed that CO could be easily oxidized over Pt/CeO₂ and Pt/CeZrO while the introduction of WO₃ into the catalyst (Pt/WO₃/CeZrO) inhibited the reduction of catalyst surface; NO could not dissociate over those catalysts in oxidized state but after CO reduction at a low temperature, NO dissociation took place only over Pt/CeO₂ and Pt/CeZrO catalysts. For NO + CO reaction, those easily reduced catalysts Pt/CeO₂ and Pt/CeZrO exhibited better catalytic performances, and NO could be rapidly converted below 350 °C. For the reaction with the presence of excess O₂, the NO conversions were significantly inhibited, but better NO conversions were obtained over the tungstate-contained catalysts when compared with Pt/CeO₂ and Pt/CeZrO. The higher activities of Pt/W–Ce–Zr catalysts were attributed to their high acidities.     

Franck–Condon breakdown in core-level photoelectron spectroscopy of chemisorbed CO

The photon energy dependence of the vibrational fine structure in the C1s and O1s X-ray photoelectron main lines of chemisorbed CO on Ni(100) and Ru(0001) has been measured from 6 to 150 eV above the core-level thresholds. Significant deviations from the behavior in gas-phase CO are found. A strong dominance of the adiabatic peak towards threshold is found for the C1s, but not the O1s, lines. In the C1s lines, we observe a broad maximum of vibrational excitation 5 eV above the shape resonance. At high photon energies, Franck–Condon behavior is observed in both the C1s and O1s lines. This behavior is discussed in terms of the adsorbate electronic structure and the dynamic metallic screening upon core ionization.     

过渡金属团簇M+2(M=Fe、Co、Ni)与CO的化学反应

利用离子讲质谱计和激光溅射技术相结合,研究了Fe2＋、CO2＋、Ni2＋与CO气体的吸附反应,比较了它们的反应活性,给出了化学反应的速率常数及随反应气体压强的变化关系,并从理论上模拟了化学反应过程,测量结果与已有的实验值符合较好．     

Accurate CO2 Joule–Thomson inversion curve by molecular simulations

We present simulation of the Joule–Thomson inversion curve (JTIC) for carbon dioxide using two different approaches based on Monte Carlo (MC) simulations in the isothermal–isobaric ensemble. We model carbon dioxide using a two-center Lennard–Jones (LJ) plus point quadrupole moment (2CLJQ) potential. We show that a precision of four significant figures in ensemble averages of thermodynamic quantities of interest is needed to obtain accurately the JTIC. The agreement between the experimental data, Wagner equation of state (EOS) and our simulations results indicates that the 2CLJQ potential represents an excellent balance between simplicity and accuracy in modeling of carbon dioxide. Additionally, we calculate the JTIC using the BACKONE EOS (that uses the same intermolecular potential as in our simulations) and show that the BACKONE EOS performs very well in predicting the JTIC for carbon dioxide.     

（CH3）3NO存在下M（CO）5（M＋Fe,Ru,Os）的CO取代反应动力学研究

在(CH_3)_3NO存在下,PPh_3取代M(CO)_5(M=Fe,Ru,Os)中CO的反应速度遵循二级速度定律,分别与[M(CO)_5]和[(CH_3)_3NO]的一次方成正比,与[PPh_3]无关。反应速度按FeRu>Os的次序约减小4倍。 1 实验方法 典型的动力学实验中,将(CH_3)_3NO的C_2H_5OH溶液和PPh_3的己烷溶液分别用注射器加到体积合适的烧瓶中,再注入Fe(CO)_5并迅速震荡烧瓶,再取出一部分反应液立即注入充N_2     

Decoupling microporosity and nitrogen content to optimize CO2 adsorption in melamine–resorcinol–formaldehyde xerogels

Selected melamine–resorcinol–formaldehyde (MRF) xerogels have been synthesized and analyzed to determine the influence of nitrogen (N) incorporated into the gel structure and resorcinol-to-catalyst (sodium carbonate) and resorcinol-to-formaldehyde molar ratios. The aforementioned factors were varied, and their effect on gel properties was characterized, allowing for a better understanding of how gel characteristics can be tailored and their impact on gel performance. MRF gels, produced in this study, were characterized using volumetric and gravimetric analyses to determine porous structure and quantify CO₂ capture capacities and kinetics, allowing determination of heats of adsorption and activation energies for CO₂. MRF10_200_0.25 has exhibited the largest CO₂ capacity (1.8 mmol/g at 0 °C) of the sample tested. Thermal stability was tested by proximate analysis, and MRF xerogels exhibited high thermal stability; however, it was found that volatile matter increases as [M] increases, particularly for [M] 20%w/w and higher. Working capacity was determined from a series of cycling studies, and capacities of 0.55, 0.58, and 0.56 mmol/g at 60 °C were observed for [M] of 10, 20, and 30%w/w, respectively. The measured heat of adsorption showed that incorporation of nitrogen functionalities results in a low energy penalty, demonstrating that the adsorption mechanism is still driven by physical forces. The results obtained indicate that the family of materials studied here offer potential routes for carbon capture materials, through a combination of micropore structure development and incorporation of favorable Lewis acid–base interactions.     

Electrochemical CO2 reduction reaction on cost-effective oxide-derived copper and transition metal–nitrogen–carbon catalysts

The electrochemical CO₂ reduction reaction (CO₂RR) either to generate multicarbon (C₂₊) or single carbon (C₁) value-added products provides an effective and promising approach to mitigate the high CO₂ concentration in the atmosphere and promote energy storage. However, cost-effectiveness of catalytic materials limits practical application of this technology in the short term. Herein, we summarize and discuss recent and advanced works on cost-effective oxide-derived copper catalysts for the generation of C₂₊ products (hydrocarbons and alcohols) and transition metal–nitrogen–doped carbon electrocatalytic materials for C₁ compounds production from CO₂RR. We think they represent suitable electrocatalyst candidates for scaling up electrochemical CO₂ conversion. This short review may provide inspiration for the future design and development of innovative active, cost-effective, selective and stable electrocatalysts with improved properties for either the production of C₂₊ (alcohols, hydrocarbons) or carbon monoxide from CO₂RR.