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具有丰富晶界的铜催化剂在气-液平衡扩散电极上高效电还原CO_(2)制C_(2)H_(4)
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作者 卞磊 张紫阳 +3 位作者 田昊 田娜娜 马智 王中利 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 2023年第11期199-211,共13页
电催化二氧化碳还原反应(CO_(2)RR)可以将二氧化碳转化为具有高经济价值的碳氢化合物,被认为是实现碳中和并缓解能源危机的一种有潜力的技术.铜(Cu)作为一种最有应用前景的非贵金属催化剂之一,表现出较高的催化CO_(2)RR转化为多碳产物(C... 电催化二氧化碳还原反应(CO_(2)RR)可以将二氧化碳转化为具有高经济价值的碳氢化合物,被认为是实现碳中和并缓解能源危机的一种有潜力的技术.铜(Cu)作为一种最有应用前景的非贵金属催化剂之一,表现出较高的催化CO_(2)RR转化为多碳产物(C_(2+))的活性.然而,电催化CO_(2)还原成C_(2+)产物涉及一个动力学过程缓慢的C-C偶联反应,这导致C_(2+)产物的选择性较低,电流密度低,阻碍了其在工业电解槽中的实际应用.同时,CO_(2)RR产物的选择性不仅取决于热力学速率决定步骤,还取决于传质控制动力学.CO_(2)RR发生在固-气-液三相反应界面,气-液的平衡扩散可以有效抑制析氢竞争反应,进而提高CO_(2)RR的反应效率.本文设计合成了一种富晶界的Cu纳米带催化剂,并构建了气-液平衡扩散的电极结构,用于高效电催化二氧化碳还原制备乙烯(C_(2)H_(4)).以一种碱式碳酸铜(Cu_(2)CO_(3)(OH)_(2))纳米带为前驱体,在原位电化学还原条件下,前驱体中的Cu2+离子获得电子被还原为金属Cu,而释放的CO_(3)2-和OH-混合阴离子调节金属Cu的生长.生成的Cu纳米带由细小的纳米颗粒堆积而成,并暴露出大量的由Cu(111),Cu(200)和Cu(220)晶面形成的富晶界结构(GBs).同时,在CO_(2)RR测试中发现催化剂层的厚度是影响CO_(2)和电解质传质的关键因素.通过调整催化层厚度,CO_(2)和电解质可以同时到达催化剂表面,参与到CO_(2)RR中,实现了气-液平衡扩散,有效抑制了氢析出副反应.在晶界效应和气-液平衡扩散的协同作用下,优化后的电极在电流密度为700 mA cm^(-2)时,对C_(2)H_(4)和C_(2+).产物的法拉第效率分别高达67.2%和82.1%.此外,C_(2)H_(4)的部分电流密度可高达505 mA cm^(-2),高于大多数文献报道的结果.原位拉曼光谱和衰减全内反射表面增强红外吸收光谱结果表明,丰富的晶;界结构增强了CO_(2)在催化剂表面的活化,显著促进了*CO中间体的形成和吸附,加速了C-C偶联过程形成*OCCO和*OCCOH中间体,提高了C_(2)H_(4)和其他C_(2+)产物的产率.综上,本文设计了一种高活性Cu催化剂和电极结构,为高效电催化CO_(2)还原为C_(2)H_(4)等C_(2+)产物提供参考. 展开更多
关键词 电催化二氧化碳还原 乙烯 C_(2+)产物 晶界 气-液扩散
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采空区碳封存条件下CO_(2)-水界面特性及溶解传质规律 被引量:1
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作者 李树刚 张静非 +5 位作者 林海飞 包若羽 丁洋 白杨 周雨璇 朱冰 《煤炭学报》 EI CAS CSCD 北大核心 2024年第1期513-527,共15页
采空区CO_(2)封存作为解决煤炭行业碳排放难题的重要负碳技术储备,在采空区废弃资源二次利用、CO_(2)封存等方面具有广泛的应用前景。利用原位界面张力测定仪开展了不同温压、地层水矿化度及阳离子溶液类型对CO_(2)地层水系统的界面张力... 采空区CO_(2)封存作为解决煤炭行业碳排放难题的重要负碳技术储备,在采空区废弃资源二次利用、CO_(2)封存等方面具有广泛的应用前景。利用原位界面张力测定仪开展了不同温压、地层水矿化度及阳离子溶液类型对CO_(2)地层水系统的界面张力(IFT)影响规律实验,明晰了CO_(2)注入含水碎胀煤岩体中的气液界面扩散效应,并将基于统计缔合理论结合兰纳−琼斯势能模型的状态方程(SAFT-LJ状态方程)与密度梯度理论(DGT)结合预测了IFT理论值;利用自主研发的地质封存地化反应模拟实验平台对相同条件下的CO_(2)溶解性进行了探究实验,得到了采空区储层环境下CO_(2)溶解度变化特征,采用D-S模型计算了对应CO_(2)溶解度理论值。实验结果表明:环境温度一定时,采空区储层压力与IFT呈线性负相关关系,储层温度升高,IFT相应增加,但变化幅度较小;温压条件一定时,矿化度与IFT存在正相关性,且在本实验范围内,低压、高温、高矿化度会促使IFT升高;CO_(2)−盐溶液之间的IFT呈现出随着阳离子价态升高而增大的现象(K^(+)<Na^(+)<Ca^(2+)<Mg^(2+));采空区储层压力与CO_(2)溶解度呈正相关关系,当温度为25℃、纯水条件下,压力由0.5 MPa增至2.5 MPa,对应CO_(2)溶解度由0.1627 mol/kg升至0.7141 mol/kg;CO_(2)溶解度随着温度与矿化度的升高而降低;相同质量分数下,一价阳离子溶液(NaCl、KCl)比二价阳离子溶液(CaCl_(2)、MgCl_(2))可溶解更多的CO_(2)。注入采空区中的游离相CO_(2)克服界面张力通过扩散溶解传质作用打破了采空区地层的地球化学平衡,通过明确环境温压条件、采空区水环境对IFT及CO_(2)溶解度的影响规律,阐明CO_(2)地层水气液界面效应及溶解传质机理,以期为采空区CO_(2)封存安全性及封存量评估提供理论基础。 展开更多
关键词 采空区 CO_(2)封存安全性 界面扩散-溶解 界面张力 溶解度
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Diffusion-controlled Adsorption Kinetics of Surfactant at Air/Solution Interface 被引量:3
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作者 刘俊吉 徐芸 孙红秀 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2013年第9期953-958,共6页
For the diffusion-controlled adsorption, the expression of dynamic surface adsorption P(t) was ob- tained by solving the diffusion equation. Two cases, i.e. the short and long time limits, were mainly discussed in t... For the diffusion-controlled adsorption, the expression of dynamic surface adsorption P(t) was ob- tained by solving the diffusion equation. Two cases, i.e. the short and long time limits, were mainly discussed in this paper. From the measured dynamic surface tension of aqueous surfactant sodium dodecyl sulfate (SDS) solutions at 25 ℃, the adsorption kinetics of SDS at air/solution interface was studied. It was proved that for both of the short and long time limits, the adsorption process of SDS was controlled by diffusion. 展开更多
关键词 ADSORPTION air/solution interface dynamic surface tension
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Measurement of Diffusion Coefficients of Air in Silicone Oil and in Hydraulic Oil 被引量:6
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作者 丁川 范毓润 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2011年第2期205-211,共7页
A piston-cylinder apparatus was established to measure the solubility and diffusivity of air in dimethyl silicone oils and in hydraulic oils based on the PVT state equation of air and the solution of unsteady one-dime... A piston-cylinder apparatus was established to measure the solubility and diffusivity of air in dimethyl silicone oils and in hydraulic oils based on the PVT state equation of air and the solution of unsteady one-dimensional diffusion equation.The measured diffusivity-temperature relation can be well fitted by the Arrhenius equation for engineering applications.The correlation between the solute diffusivity D and solvent viscosity μ is examined.In terms of Eyring's activation theory,the activation in the air-silicone-oil diffusion process is quite different from that in the momentum transport of the silicone oil:the activation entropy of the former is positive while that of latter is negative.However,the activation enthalpies of the two processes are in the same order of magnitude,which leads to the observation that Dμ/T is roughly constant. 展开更多
关键词 AIR silicone oil hydraulic oil diffusion coefficient VISCOSITY
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A Reynolds mass flux model for gas separation process simulation:Ⅰ. Modeling and validation 被引量:2
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作者 李文彬 余国琮 +1 位作者 袁希钢 刘伯潭 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2015年第7期1085-1094,共10页
Separation process undertaken in packed columns often displays anisotropic turbulent mass diffusion. The anisotropic turbulent mass diffusion can be characterized rigorously by using the Reynolds mass flux(RMF) model.... Separation process undertaken in packed columns often displays anisotropic turbulent mass diffusion. The anisotropic turbulent mass diffusion can be characterized rigorously by using the Reynolds mass flux(RMF) model.With the RMF model, the concentration and temperature as well as the velocity distributions can be simulated numerically. The modeled Reynolds mass flux equation is adopted to close the turbulent mass transfer equation,while the modeled Reynolds heat flux and Reynolds stress equations are used to close the turbulent heat and momentum transfer equations, so that the Boussinesq postulate and the isotropic assumption are abandoned. To validate the presented RMF model, simulation is carried out for CO2 absorption into aqueous Na OH solutions in a packed column(0.1 m id, packed with 12.7 mm Berl saddles up to a height of 6.55 m). The simulated results are compared with the experimental data and satisfactory agreement is found both in concentration and temperature distributions. The sequel Part II extends the model application to the simulation of an unsteady state adsorption process in a packed column. 展开更多
关键词 Mathematical modelingComputational fluid dynamics (CFD)Computational mass transfer (CMT)Anisotropic turbulent mass diffusionPacked bedAbsorption
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