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在高压釜反应器中通过炼钢炉渣碳酸化实现 CO2 捕集。

CO2 sequestration by carbonation of steelmaking slags in an autoclave reactor.

机构信息

Department of Biochemistry, Taipei Medical University, Taipei, Taiwan.

出版信息

J Hazard Mater. 2011 Nov 15;195:107-14. doi: 10.1016/j.jhazmat.2011.08.006. Epub 2011 Aug 10.

DOI:10.1016/j.jhazmat.2011.08.006
PMID:21889848
Abstract

Carbon dioxide (CO(2)) sequestration experiments using the accelerated carbonation of three types of steelmaking slags, i.e., ultra-fine (UF) slag, fly-ash (FA) slag, and blended hydraulic slag cement (BHC), were performed in an autoclave reactor. The effects of reaction time, liquid-to-solid ratio (L/S), temperature, CO(2) pressure, and initial pH on CO(2) sequestration were evaluated. Two different CO(2) pressures were chosen: the normal condition (700 psig) and the supercritical condition (1300 psig). The carbonation conversion was determined quantitatively by using thermo-gravimetric analysis (TGA). The major factors that affected the conversion were reaction time (5 min to 12h) and temperature (40-160°C). The BHC was found to have the highest carbonation conversion of approximately 68%, corresponding to a capacity of 0.283 kg CO(2)/kg BHC, in 12h at 700 psig and 160°C. In addition, the carbonation products were confirmed to be mainly in CaCO(3), which was determined by using scanning electron microscopy (SEM) and X-ray powder diffraction (XRD) to analyze samples before and after carbonation. Furthermore, reaction kinetics were expressed with a surface coverage model, and the carbon footprint of the developed technology in this investigation was calculated by a life cycle assessment (LCA).

摘要

采用超细化渣(UF 渣)、粉煤灰(FA 渣)和掺合水硬渣水泥(BHC)三种炼钢渣进行了二氧化碳(CO2)封存实验,在高压釜反应器中进行了加速碳酸化反应。考察了反应时间、液固比(L/S)、温度、CO2压力和初始 pH 值对 CO2封存的影响。选择了两种不同的 CO2 压力:正常条件(700 psig)和超临界条件(1300 psig)。采用热重分析(TGA)定量测定碳酸化转化率。主要影响因素为反应时间(5 min 至 12 h)和温度(40-160°C)。在 700 psig 和 160°C 下,BHC 的碳酸化转化率最高,约为 68%,相应的 CO2 封存容量为 0.283 kg CO2/kg BHC,反应 12 h 后达到。此外,通过扫描电子显微镜(SEM)和 X 射线粉末衍射(XRD)分析碳酸化前后的样品,证实碳酸化产物主要为 CaCO3。还通过表面覆盖模型表达了反应动力学,并通过生命周期评估(LCA)计算了本研究中开发技术的碳足迹。

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