Y. Katsuyama, A. Yamasaki, A. Iizuka, M. Fujii, K. Kumagai, Y. Yanagisawa
{"title":"Development of a process for producing high‐purity calcium carbonate (CaCO3) from waste cement using pressurized CO2","authors":"Y. Katsuyama, A. Yamasaki, A. Iizuka, M. Fujii, K. Kumagai, Y. Yanagisawa","doi":"10.1002/EP.10080","DOIUrl":null,"url":null,"abstract":"A new type of process for producing high-purity calcium carbonate from waste cement powder was developed. The process consists of two main reactions; extraction of calcium in the form of calcium ions from waste cement powder in a water slurry by pressurized CO2 (typically at several MPa), and precipitation of calcium carbonate (CaCO3) from the extracted solution by reduction of the CO2 pressure. The process can be recognized as the emission reduction process of CO2 as well. Laboratory-scale experimental studies were conducted for both the extraction reaction and the precipitation reaction, to examine the feasibility of the process. The extraction process was found to proceed at a relatively high rate, especially during the initial 10 min. The concentration of calcium ions exceeded the thermodynamic solubility of CaCO3 (supersaturation) when abundant waste cement was available. After filtration of the residues, CaCO3 particles with >98% purity were obtained by depressurizing the CO2. The dependency of the reaction rates on the operating conditions, such as the ratio of waste cement to water, CO2 pressure, and particle size of waste cement particles, was investigated. A process design was carried out based on the experimental results, assuming that the present process is applied to two types of CaCO3 production process: flue gas desulfurization and production of ultrahigh-purity CaCO3. The estimated costs per 1 metric ton of CaCO3 were USD 136 for desulfurization and USD 323 for high-purity CaCO3. © 2005 American Institute of Chemical Engineers Environ Prog, 2005","PeriodicalId":11769,"journal":{"name":"Environmental Progress","volume":null,"pages":null},"PeriodicalIF":0.0000,"publicationDate":"2005-07-01","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"101","resultStr":null,"platform":"Semanticscholar","paperid":null,"PeriodicalName":"Environmental Progress","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.1002/EP.10080","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"","JCRName":"","Score":null,"Total":0}
引用次数: 101
开发利用加压CO2从废水泥中生产高纯碳酸钙(CaCO3)的工艺
开发了一种利用废水泥粉生产高纯碳酸钙的新工艺。该过程包括两个主要反应;通过加压CO2(通常在几兆帕)从废水泥粉中提取钙离子形式的钙,并通过降低CO2压力从提取的溶液中析出碳酸钙(CaCO3)。这个过程也可以看作是二氧化碳的减排过程。对萃取反应和沉淀反应进行了实验室规模的实验研究,以检验该工艺的可行性。研究发现,萃取过程以相对较高的速率进行,特别是在最初的10分钟内。当有大量废水泥可用时,钙离子浓度超过了CaCO3的热力学溶解度(过饱和)。残渣过滤后,减压CO2得到纯度为> ~ 98%的CaCO3颗粒。考察了废水泥与水比、CO2压力、废水泥颗粒粒径等操作条件对反应速率的影响。根据实验结果,假设本工艺适用于烟气脱硫和生产超高纯度CaCO3两种CaCO3生产工艺,进行了工艺设计。估计每公吨CaCO3的脱硫成本为136美元,高纯CaCO3的脱硫成本为323美元。©2005美国化学工程师学会环境项目,2005
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