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首页> 外文期刊>Journal of thermal analysis and calorimetry >Thermogravimetric analysis of kinetic characteristics of K2CO3-impregnated mesoporous silicas in low-concentration CO2
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Thermogravimetric analysis of kinetic characteristics of K2CO3-impregnated mesoporous silicas in low-concentration CO2

机译:低浓度CO2中K2CO3浸渍介孔二氧化硅动力学特性的热重分析

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摘要

The requirement for self-sustained and long-duration human operations in confined spaces including submarines, spacecrafts, or underground citadels has made ambient removal of low-concentration CO2 a critical technology. Mesoporous silica materials have been regarded as promising carriers to support active components for CO2 sorption. The CO2 sorption kinetic of mesoporous silica-supported adsorbent is an important parameter to be assessed. In this paper, K2CO3-impregnated mesoporous silicas were prepared by impregnating K2CO3 on MCM-41, SBA-15, and silica gel (SG) in ethanol solution, respectively. The CO2 sorption experiments were performed in a simulated confined space atmosphere of 1.0 % CO2, 2.0 % H2O, and 293-333 K using thermogravimetric analysis. The kinetic performances of the sorbents were evaluated by fitting the experimental data to the shrinking core model. K2CO3/SG exhibited the optimum carbonation kinetic performance. The apparent activation energies for chemical reaction-controlled region and internal diffusion-controlled region are 3.95 and 64.87 kJ mol(-1), respectively. To obtain the specific carbonation kinetic mechanism, a double exponential model was used to simulate the carbonation process of K2CO3/SG. The apparent activation energies for H2O diffusion-hydration and CO2 diffusion-carbonation stages are 8.40 and 4.32 kJ mol(-1), respectively. H2O diffusion-hydration is the rate limiting step in the whole carbonation process.
机译:在包括潜艇,航天器或地下citadels在内的密闭空间中,对人类自我维持和长时间操作的要求已使在环境中去除低浓度的CO2成为一项关键技术。介孔二氧化硅材料被认为是有希望的载体,可以支持活性成分吸附CO2。介孔二氧化硅负载的吸附剂的CO2吸附动力学是需要评估的重要参数。本文通过将K2CO3分别浸渍在乙醇溶液中的MCM-41,SBA-15和硅胶(SG)上制备了K2CO3浸渍的中孔二氧化硅。使用热重分析法在1.0%CO2、2.0%H2O和293-333 K的模拟密闭空间气氛中进行了CO2吸附实验。通过将实验数据拟合到收缩芯模型来评估吸附剂的动力学性能。 K2CO3 / SG表现出最佳的碳化动力学性能。化学反应控制区和内部扩散控制区的表观活化能分别为3.95和64.87 kJ mol(-1)。为了获得特定的碳酸化动力学机理,使用双指数模型来模拟K2CO3 / SG的碳酸化过程。 H2O扩散水合和CO2扩散碳酸化阶段的表观活化能分别为8.40和4.32 kJ mol(-1)。 H2O扩散水合是整个碳酸化过程中的限速步骤。

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