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砷铁水热共沉淀制备大颗粒臭葱石

  • 余自秀 李存兄 魏昶 樊刚 李兴彬 邓志敢 李旻廷
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  • 1. 昆明理工大学冶金与能源工程学院,云南 昆明 650093;2. 昆明高聚科技有限公司,云南 昆明 650106

收稿日期: 2017-03-17

  修回日期: 2017-05-05

  网络出版日期: 2018-01-29

基金资助

压力场下高硅氧化锌矿高温酸转化及硅沉淀机理研究;湿法炼锌高铁溶液水热沉铁及铁资源化利用基础研究;湿法冶金含砷铁废水水热矿物化沉砷及砷物相转变机制研究;湿法炼锌浸出渣与高铁锌精矿协同浸出及相互作用机理研究;湿法炼锌高铁溶液水热沉铁及铁资源化利用基础研究;战略有色金属非传统资源清洁高效提取的基础研究

Preparation of Large-sized Scorodite Based on Arsenic and Iron Hydrothermal Co-precipitation

  • Zixiu YU Cunxiong LI Chang WEI Gang FAN Xingbin LI Zhigan DENG Minting LI
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  • 1. Faculty of Metallurgy and Energy Engineering, Kunming University of Science and Technology, Kunming, Yunnan 650093, China; 2. Kunming Gaoju Science and Technology Co., Ltd., Kunming, Yunnan 650106, China

Received date: 2017-03-17

  Revised date: 2017-05-05

  Online published: 2018-01-29

摘要

开展了硫酸体系中砷铁水热共沉淀为大颗粒晶型臭葱石的研究,考察了初始Fe/As摩尔比、初始pH、反应温度、搅拌速度和氧分压等因素对砷铁沉淀率、臭葱石晶型形成及臭葱石粒度的影响. 结果表明,Fe/As摩尔比、初始pH及反应温度降低有利于形成纯净大颗粒臭葱石,臭葱石颗粒粒度与氧分压关系不大. 高搅拌速度有利于形成纯净臭葱石,但不利于大颗粒臭葱石晶体的形成. 在Fe/As摩尔比1.5、初始pH 1.0、反应温度160℃、搅拌速度500 r/min和氧分压0.4 MPa的优化条件下,除砷率高于97%,沉砷渣中砷含量大于30%,平均粒度大于20 ?m.

本文引用格式

余自秀 李存兄 魏昶 樊刚 李兴彬 邓志敢 李旻廷 . 砷铁水热共沉淀制备大颗粒臭葱石[J]. 过程工程学报, 2018 , 18(1) : 126 -132 . DOI: 10.12034/j.issn.1009-606X.217178

Abstract

Coprecipitation of arsenic and iron in sulphuric acid system to produce large particle sized scorodite was carried out. The effects of initial Fe/As molar ratio, initial pH, temperature, agitation speed and oxygen partial pressure on scorodite crystalline formation, particle size distribution and the precipitation rates of As and Fe were investigated. The results showed that the decrease of Fe/As molar ratio, initial pH and temperature was beneficial to large and purified scorodite formation which was independent of oxygen partial pressure. Higher agitation speed was available for the formation of more purified scorodite but small-sized scorodite. The precipitation of As was higher than 97%, the content of arsenic in residue was larger than 30% and the average size of scorodite was larger than 20 ?m under the optimum conditions of Fe/As molar ratio 1.5, initial pH 1.0, temperature 160℃, agitation speed 500 r/min, oxygen partial pressure 0.4 MPa.

参考文献

[1]Mandal B K, Suzuki K T.Arsenic round the world: a review[J].Talanta, 2002, 58(1):201-235
[2]熊珊.含砷废液臭葱石沉砷研究[D]. 长沙:中南大学. 2012.
[3]Han F X, Su Y, Monts D L, et al.Assessment of global industrial-age anthropogenic arsenic contamination[J].The Science of Nature, 2003, 90(9):395-401
[4]庄明龙, 柴立元, 闵小波, 等.含砷废水处理研究进展[J].工业水处理, 2004, 24(7):13-16
[5]Riveros P A, Dutrizac J E, Spencer P.Arsenic disposal practices in the metallurgical industry[J].Canadian metallurgical quarterly, 2000, 40(4):395-420
[6]Gonzálezcontreras P, Weijma J, Buisman C J.Continuous bioscorodite crystallization in CSTRs for arsenic removal and disposal[J].Water Research, 2012, 46(18):5883-5892
[7]Krause E, Ettel V A.The solubility and stability of ferric arsenate compounds[J].Hydrometallugy, 1989, 22(3):311-337
[8]Itou H, Takasu T, Ueno Y.Crystallization of the amorphous ferric arsenate in the saturated steam atmosphere[J].High Temperature Materials Process, 2011, 30(4-5):473-483
[9]Dutrizac J E, Jambor J L.The synthesis of crystalline scorodite,FeAsO4?2H2O[J].Hydrometallugy, 1988, 19(3):377-384
[10]Kitamura Y, Okawa H, Kato T, et al.Size and morphology of scorodite particles synthesized using ultrasound irradiation[J].Japanese Journal of Applied Physics, 2014, 53(7S):467-468
[11]Kitamura Y, Okawa H, Sugawara K.Synthesis of large scorodite particles using short period time sonication to enhance agglomeration of precursor[J].Japanese Journal of Applied Physics, 2015, 54(7S1):07-H
[12]Fujieda S, Shinoda K, Inanaga T, et al.Dissolution Characteristics and Morphology of Large-sized Scorodite Particles Synthesized from Fe(II) and As(V) in Aqueous Solution[J].High Temperature Materials & Processes, 2012, 31(4-5):451-458
[13] Kitamura Y, Okawa H, Kato T, et al.Size and morphology of scorodite particles synthesized using ultrasound irradiation[C]. Meeting of the Japan Society of Sonochemistry. The Japan Society of Sonochemistry, 2013:85-86.
[14]Welham N J, Malatt K A, Vukcevic S.The stability of iron phases presently used for disposal from metallurgy systems-a review[J].Minerals Engineering, 2000, 13(8-9):911-931
[15]Dutrizac J E, Jambor J L, Chen T T.The behavior of arsenic during jarosite precipitation: reaction at 150℃ and the mechanism of arsenic precipitation[J].Canadian Institute of Mining, 1987, 26(2):103-115
[16]朱义年, 张学洪, 解庆林, 等.砷酸盐的溶解度及其稳定性随值的变化[J].环境化学, 2003, 5(22):478-484
[17]Sahu N K, Dash B, Sahu S, et al.Extraction of copper by leaching of electrostatic precipitator dust and two step removal of arsenic from the leach liquor[J].Korean journal of Chemical Engineering, 2012, 29(11):1638-1642
[18]Doerfelt C, Feldmann T, Daenzer R, et al.Stability of continuously Fe(II)Fe(III)As(V) co-precipitates under periodic exposure to reducing agents[J].Chemosphere, 2015, 138(1):239-246
[19]Fujita T, Taguchi R, Abumiya M, et al.Effect of pH on atmospheric scorodite synthesis by oxidation of ferrous ions: Physical properties and stability of the scorodite[J].Hydrometallurgy, 2009, 96(3):189-198
[20] Papangelakis V G, Blakey B C, Liao H.[20] Papangelakis V G, Blakey B C, Liao H. Hematite solubility in sulphate process solutions[M]// Hydrometallurgy ’94. Springer Netherlands, 1994:159-175.
[21]李洪桂.湿法冶金学[M].长沙:中南大学出版社. 2002, 171-248.
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