欢迎访问过程工程学报, 今天是
过程与工艺

钙化提钒溶液沉钒的影响因素及沉钒动力学

  • 张菊花 严哲锋 张力
展开
  • 1. 武汉科技大学钢铁冶金及资源利用省部共建教育部重点实验室,省部共建耐火材料与冶金国家重点实验室,湖北 武汉 430081; 2. 武汉科技大学材料与冶金学院,湖北 武汉 430081;3. 东北大学冶金学院,辽宁 沈阳110004

收稿日期: 2017-02-20

  修回日期: 2017-05-03

  网络出版日期: 2018-01-29

基金资助

钢铁冶金及资源利用省部共建教育部重点实验室开放基金;省部共建耐火材料与冶金国家重点实验室青年基金

Influence Factors and Kinetics of Vanadium Precipitation for the Vanadium Solution from Calcified Vanadium Extraction

  • Juhua ZHANG Zhefeng YAN Li ZHANG
Expand
  • 1. Key Laboratory for Ferrous Metallurgy and Resource Utilization, Ministry of Education, State Key Laboratory of Refractories and Metallurgy, Wuhan University of Science and Technology, Wuhan, Hubei 430081, China; 2. School of Materials and Metallurgy, Wuhan University of Science and Technology, Wuhan, Hubei 430081, China; 3. School of Metallurgy, Northeastern University, Shenyang, Liaoning 110004, China

Received date: 2017-02-20

  Revised date: 2017-05-03

  Online published: 2018-01-29

Supported by

The Open Research Fund of Key Laboratory for Ferrous Metallurgy and Resources Utilization of Ministry of Education;Youth Foundation of the State Key Laboratory of Refractories and Metallurgy

摘要

用(NH4)2SO4对钒渣钙化焙烧、稀酸浸取、化学沉淀净化后的酸性含钒溶液进行沉淀富集,考察了钒浓度、初始pH值、加铵系数(NH3/V摩尔比)、沉钒温度和时间对沉钒率及V2O5含量的影响,研究了沉钒动力学,对沉钒产物进行了表征. 结果表明,在初始pH为2.00?0.05、加铵系数1.5、温度大于95℃、沉钒时间120 min、钒液中V浓度大于20 g/L的条件下,沉钒率超过96%,产品中V2O5含量大于98%,杂质含量符合98级氧化钒的国家标准. 75~99℃下的沉钒过程可由Avrami动力学方程描述,表观活化能Ea=93.23 kJ/mol,指前因子A=9.14×1011 min?1. 铵盐沉钒产物为(NH4)2V6O16?1.5H2O,高温煅烧所得V2O5晶体为柱状,平均粒径1.25 ?m,主要杂质Mn以MnV2O6形式存在.

本文引用格式

张菊花 严哲锋 张力 . 钙化提钒溶液沉钒的影响因素及沉钒动力学[J]. 过程工程学报, 2018 , 18(1) : 111 -117 . DOI: 10.12034/j.issn.1009-606X.217138

Abstract

Vanadium component was precipitated and concentrated by ammonium salt from the acidic vanadium solution obtained by the process comprising of calcium roasting, dilute acid leaching and chemical precipitation purification. The effects of concentration of vanadium, the initial pH of solution, adding amount of ammonium, temperature and time on precipitation rate and quality of vanadium pentoxide were studied and the kinetics of vanadium precipitation was analyzed. The precipitates were characterized. The results showed that under the conditions of initial pH of 2.00?0.05, molar ratio of NH3 to V being 1.5, temperature higher than 95℃, reaction time of 120 min and concentration of vanadium larger than 20 g/L, precipitation rate was higher than 96%, the content of V2O5 in the final product is over 98%, and the contents of impurities meet the standards of Grade 98 vanadiumpentoxide. Avrami kinetic equation well describes the precipitation process occurring at 75?99℃ with apparent activation energy Ea=93.23 kJ/mol and pre-exponential factor A=9.14×1011 min?1. The vanadium precipitate is (NH4)2V6O16?1.5H2O. The crystal of vanadium pentoxide exists in columnar with mean size of 1.25 ?m, and the main impurity of Mn appears as MnV2O6.

参考文献

[1] PERRON L.Vanadium, Natural Resources Canada [M]. Ottawa: Minerals & Resources Sector, 2001: 59.1-59.3. [2]孙朝晖.钒新技术及钒产业发展前景分析[J].钢铁钒钛, 2012, 33(1):1-7 [3]SUN Z H.Analysis on New Vanadium Technologies and Prospects of Vanadium Industry[J].Iron Steel Vanadium Titanium, 2012, 33(1):1-7 [4] POLYAK D E.U.S. Geological Survey 2009 Minerals Yearbook-vanadium [M]. Virginia: Geological Survey, 2011: 80.1-80.10. [5]范鹤林,陈登福,徐松,等.高钙钒比钒渣钠化焙烧熟料浸出条件研究[J].过程工程学报, 2013, 13(6):958-962 [6]FAN H L, CHEN D F, XU S, et al.Research on Leaching Conditions of Sodium Roasted Vanadium Slag with High CaV Ratio[J].The Chinese Journal of Process Engineering, 2013, 13(6):958-962 [7]ZHANG J H, ZHANG W, ZHANG L, et al.A Critical Review of Technology for Selective Recovery of Vanadium from Leaching Solution in V2O5 Production[J].Solvent Extr. Ion Exc., 2014, 32(3):221-248 [8]李千文,刘丰强,邓孝伯,胡力.攀钢转炉钒渣钠化焙烧实验室研究[J].钢铁钒钛, 2012, 33(4):8-11 [9]LI Q W, LIU F Q, DENG X B, et al.Study on Roasting of Pangang Converter Vanadium Slag with Soda in Laboratory[J].Iron Steel Vanadium Titanium, 2012, 33(4):8-11 [10]LI X S, XIE B, WANG G E, et al.Oxidation Process of Low-grade Vanadium Slag in Presence of Na2CO3[J].T. Nonferr. Metal Soc., 2011, 21(8):1860-1867 [11]LIU B, DU H, WANG S N.A Novel Method to Extract Vanadium and Chromium from Vanadium Slag Using Molten NaOH-NaNO3 Binary System[J].AIChE J., 2013, 59(2):541-552 [12]LIU H B, DU H, WANG D W, e al.Kinetics Analysis of Decomposition of Vanadium Slag by KOH Sub-molten Salt Method[J].T. Nonferr. Metal Soc., 2013, 23(5):1489-1500 [13]WANG Z H, ZHENG S L, WANG S N, et al.Electrochemical Decomposition of Vanadium Slag in Concentrated NaOH Solution[J].Hydrometallurgy, 2015, 151:51-55 [14]ZHANG G Q, ZHANG T A, LV G Z, et al.Extraction of Vanadium from LD Converter Slag by Pressure Leaching Process with Titanium White Waste Acid[J].Rare Metal Mat. Eng., 2015, 44(8):1894-1898 [15] LIU Z H, LI Y, CHEN M L, et al.Enhanced Leaching of Vanadium Slag in Acidic Solution by Eletro-oxidation[J].Hydrometallurgy, 2016, 159:1-5 [16] MIRAZIMI S M J, RASHCHI F, SABA M.A New Approach for Direct Leaching of Vanadium from LD Converter slag [J].Chem. Eng. Res. Des., 2015, 94:131-140 [17] ZHANG J H, ZHANG W, ZHANG L, et, al.Mechanism of Vanadium Slag Roasting with Ccalcium Oxide[J].Int. J. Miner. Process., 2015, 138:20-29 [18]张菊花,张伟,张力,等.酸浸对钙化焙烧提钒工艺钒回收率的影响[J].东北大学学报自然科学版, 2014, 35(11):1574-1578 [19]ZHANG J, ZHANG W, ZHANG L, et, al.Effect of Acid Leaching on the Vanadium Leaching Rate in Process of Vanadium Extraction Using Calcium Roasting[J].Journal of Northeastern University (Natural Science), 2014, 35(11):1574-1578 [20] 张菊花.转炉钒渣制备V2O5清洁工艺的研究 [D]. 沈阳:东北大学,2014. 1-141. [21]ZHANG J H.A Cleaner Process for Preparation of V2O5 from Converter Vanadium Slag [D]. Shenyang: Northeastern University, 2014. 1-141. [22]李大标.酸性铵盐沉钒条件实验研究[J].过程工程学报, 2003, 3(1):53-56 [23]LI D B.Experiment of Acidic Precipitation of Vanadate-leaching Solution[J].The Chinese Journal of Process Engineering, 2003, 3(1):53-56
文章导航

/