水矿物碳酸化固碳化学及实验结果解释

Zhongxi Chen, W. O'connor, S. Gerdemann
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引用次数: 123

摘要

在固碳的水矿物碳酸化中,将高压CO2注入与橄榄石或蛇纹石混合的水或碳酸氢钠溶液中,以生产碳酸镁。因此,二氧化碳气体被固定在固体碳酸盐中进行隔离。这种反应通常是缓慢的,为了提高反应速率,人们进行了大量的研究。本文是用基本热力学分析来理解这一复杂的非均相化学过程,并解释一些实验结果的初步尝试。该方法首先将该过程分解为两个基本步骤:从橄榄石或蛇纹石中溶解镁离子,以及沉淀菱镁矿。然后用热力学计算来评估这两个步骤的两个重要参数:pH值和碳离子浓度。计算结果解释了CO2压力升高、温度升高和碳酸氢钠的加入对碳酸化反应的促进作用,与实验结果吻合较好。分析还表明,在同一反应器中浸出硅酸镁和形成碳酸镁的反应路线中,降低pH有利于硅酸镁离子的溶解,但降低了碳离子浓度,限制了菱镁矿的析出;仔细平衡这两个步骤是至关重要的。可以在这个模型的基础上进一步改进。©2006美国化学工程师学会环境项目,2006
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Chemistry of aqueous mineral carbonation for carbon sequestration and explanation of experimental results
In aqueous mineral carbonation for carbon sequestration, high-pressure CO2 is injected into water or sodium bicarbonate solution mixed with olivine or serpentine to produce magnesium carbonate. Thus, CO2 gas is fixed in a solid carbonate for sequestration. Such reactions are generally slow, and a significant amount of research was conducted to increase the reaction rate. This article is an initial effort using basic thermodynamic analysis to understand this complicated heterogeneous chemical process, and to explain some experimental results. The approach started with decomposing the process into two basic steps: magnesium ion dissolution from the olivine or serpentine, and magnesite precipitation. Thermodynamic calculation then is used to assess two important parameters for each of these two steps: the pH and carbonic ion concentration. The calculations explain the roles of increased CO2 pressure, elevated temperature, and adding sodium bicarbonate for enhancing the carbonation reaction, and these results agreed well with the experimental data. The analysis also indicates that for reaction routes in which leaching magnesium silicate and forming magnesium carbonate occur in the same reactor, lowering the pH helps dissolve magnesium ions from silicate, but it lowers carbonic ion concentration and limits precipitation of magnesite; careful balance of these two steps is critical. Further improvement may be built upon this model. © 2006 American Institute of Chemical Engineers Environ Prog, 2006
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