Arid
DOI10.1021/ie3030642
Solid-Liquid Equilibrium and Process Design of CuSO4 + NaCl + (H2O or H2SO4/H2O) Systems at 298.15 K
Rocha, O. A.1; Claros, M.1; Graber, T. A.1,2; Flores, E. K.2; Taboada, M. E.1,2
通讯作者Taboada, M. E.
来源期刊INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH
ISSN0888-5885
出版年2013
卷号52期号:20页码:6803-6811
英文摘要

The low availability of fresh water in Chilean deserts has encouraged research into new alternative water sources in the mining industry. One of alternative is the use of saline water; however, there are few data about this new approach. For the production of copper sulfate pentahydrated (CuSO4 center dot 5H(2)O) crystals, the effect of NaCl in the crystallization area must be known; therefore, the solid liquid equilibrium of the CuSO4 + NaCl + (H2O or H2SO4/H2O) system at 298.15 K was experimentally determined by the wet residue method. The density and refractive index of saturated solutions were also measured. The addition of NaCl has a clear effect on the solid liquid equilibrium, promoting the formation of solid phases. In the phase equilibrium diagram that includes sulfuric acid, the pH affects the solubility curve. Using the information of the new phase diagrams, six simulation cases, varying in NaCl content and the addition of sulfuric acid in the feed, were evaluated in terms of mass and energy balance. The addition of sulfuric acid increases the total fluxes but decreases the heat requirement. Contrary to the expected results, the yields for the cases that include sulfuric acid were lower. The best results were obtained using a 50% NaCl pulp, which,produced the lowest total flux and a high yield of 75.6%.


类型Article
语种英语
国家Chile
收录类别SCI-E
WOS记录号WOS:000319551400021
WOS关键词CRYSTALLIZATION ; SOLUBILITY ; SEAWATER
WOS类目Engineering, Chemical
WOS研究方向Engineering
资源类型期刊论文
条目标识符http://119.78.100.177/qdio/handle/2XILL650/177625
作者单位1.Univ Antofagasta, Dept Ingn Quim, Antofagasta, Chile;
2.Ctr Invest Cient & Tecnol Mineria CICITEM, Antofagasta, Chile
推荐引用方式
GB/T 7714
Rocha, O. A.,Claros, M.,Graber, T. A.,et al. Solid-Liquid Equilibrium and Process Design of CuSO4 + NaCl + (H2O or H2SO4/H2O) Systems at 298.15 K[J],2013,52(20):6803-6811.
APA Rocha, O. A.,Claros, M.,Graber, T. A.,Flores, E. K.,&Taboada, M. E..(2013).Solid-Liquid Equilibrium and Process Design of CuSO4 + NaCl + (H2O or H2SO4/H2O) Systems at 298.15 K.INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH,52(20),6803-6811.
MLA Rocha, O. A.,et al."Solid-Liquid Equilibrium and Process Design of CuSO4 + NaCl + (H2O or H2SO4/H2O) Systems at 298.15 K".INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH 52.20(2013):6803-6811.
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