Hydrometallurgical process for the recovery of yttrium from spent fluorescent lamp: Leaching and crystallization experiments

被引:18
|
作者
Saratale, Rijuta Ganesh [1 ]
Kim, Hee-Young [2 ]
Park, Yooheon [3 ]
Shin, Han Seung [3 ]
Ghodake, Gajanan [4 ]
Bharagava, Ram Naresh [5 ]
Mulla, Sikandar, I [6 ]
Kim, Dong-Su [2 ]
Saratale, Ganesh Dattatraya [3 ]
机构
[1] Dongguk Univ Seoul, Res Inst Biotechnol & Med Converged Sci, Goyang Si 10326, Gyeonggi Do, South Korea
[2] Ewha Womans Univ, Dept Environm Sci & Engn, New 11-1, Seoul 120160, South Korea
[3] Dongguk Univ Seoul, Dept Food Sci & Biotechnol, Goyang Si 10326, Gyeonggi Do, South Korea
[4] Dongguk Univ Seoul, Coll Life Sci & Biotechnol, Dept Biol & Environm Sci, Goyang Si 10326, Gyeonggi Do, South Korea
[5] Babasaheb Bhimrao Ambedkar Univ, Dept Microbiol DM, Lab Bioremediat & Metagen Res LBMR, Raebareli Rd, Lucknow 226025, Uttar Pradesh, India
[6] REVA Univ, Sch Appl Sci, Dept Biochem, Bangalore 560064, Karnataka, India
关键词
Fluorescent lamp waste; Yttrium; Leaching; Crystallization; Rare earth metals; Hydrometallurgical process; RARE-EARTH-ELEMENTS; OXALATE POWDERS; METALS; WASTE; DEMAND; ZINC; END; CRITICALITY; EXTRACTION; GADOLINIUM;
D O I
10.1016/j.jclepro.2020.121009
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Present day rising necessity for rare earth elements (REE) is of great interest for its recovery through processing various waste materials concerning both economic and environmental benefits. The present study investigates the recovery potential of yttrium from fluorescent lamp waste using a hydrometallurgical process. Leaching of metals from the waste was studied by applying acids viz. hydrochloric acid (HCl), nitric acid (HNO3) and sulfuric acid (H2SO4). Influence of various factors (solid:liquid ratio, reaction temperature, reaction time, and acid concentration) were conducted by full factorial design for the recovery of yttrium. Experimental variables such as decomposition, leaching and the oxide preparation were studied and the mechanisms responsible during the progress in each step was systematically investigated. The optimal experimental conditions attained with 40% solid/liquid ratio, at 45 degrees C in 0.5 h at 150 rpm, with 3N H2SO4 concentration. Whereas, HCl and HNO3 leachants showed poor performance. Leaching process conducted in this study were best suited to 'ash diffusion control dense constant size-spherical particles model', which means that the diffusion process through the ash is the rate regulatory step in the leaching process. With increase in the concentration of oxalic acid as precipitating agent, a reduction in the nuclear induction period resulted indicating a higher sedimentation rate and shorter equilibration time. In addition, crystal nucleation rate and crystal growth rate, showed that the reaction velocity of the crystal nucleation 'p' is 2.88 and the crystal growth degree and value increases with the increase in the concentration of oxalic acid (n: 0.3437-0.4872). The precipitation rate was improved with the rise in temperature (from 25 degrees C to 45 degrees C) while the sedimentation rate was found negligible above 45 degrees C. This detailed study methodology can be considered as a feasible process thus creating a possibility to treat fluorescent waste lamp powders for various industrial applications. (C) 2020 Elsevier Ltd. All rights reserved.
引用
收藏
页数:15
相关论文
共 50 条
  • [41] Hydrometallurgical recovery of lead from spent lead-acid battery paste via leaching and electrowinning in chloride solution
    Xing, Peng
    Wang, Chengyan
    Wang, Ling
    Ma, Baozhong
    Chen, Yongqiang
    HYDROMETALLURGY, 2019, 189
  • [42] Recyclables recovery of europium. and yttrium metals and some salts from spent fluorescent lamps
    Rabah, Mahmoud A.
    WASTE MANAGEMENT, 2008, 28 (02) : 318 - 325
  • [43] Hydrometallurgical recovery of platinum-group metals from spent auto-catalysts-Focus on leaching and solvent extraction
    Paiva, Ana Paula
    Piedras, Francisco Vega
    Rodrigues, Pedro G.
    Nogueira, Carlos A.
    SEPARATION AND PURIFICATION TECHNOLOGY, 2022, 286
  • [44] Hydrometallurgical leaching and recovery of cobalt from lithium ion battery
    Sethurajan, Manivannan
    Shirodker, Mandar G. Prabhu
    Rene, Eldon R.
    van Hullebusch, Eric D.
    ENVIRONMENTAL TECHNOLOGY & INNOVATION, 2022, 28
  • [45] Nickel and aluminium recovery from spent reforming catalyst through selective leaching, crystallization and precipitation
    Batti, Naga Raju
    Mandre, N. R.
    TRANSACTIONS OF NONFERROUS METALS SOCIETY OF CHINA, 2022, 32 (01) : 345 - 353
  • [46] Recovery of cadmium from hydrometallurgical zinc smelter by selective leaching
    Aparajith, B.
    Kumar, Ashish
    Hodder, Duncan
    Gupta, M. L.
    HYDROMETALLURGY, 2010, 102 (1-4) : 31 - 36
  • [47] Hydrometallurgical process for recovery of metal values from spent nickel-metal hydride secondary batteries
    Japan Science and Technology Corp, Japan
    Hydrometallurgy, 1 (61-75):
  • [48] Vacuum pyrolysis and hydrometallurgical process for the recovery of valuable metals from spent lithium-ion batteries
    Sun, Liang
    Qiu, Keqiang
    JOURNAL OF HAZARDOUS MATERIALS, 2011, 194 : 378 - 384
  • [49] Integrated process development for the recovery of Europium and Yttrium from waste fluorescent powder
    Ching-Hwa Lee
    Ching-Hua Liao
    Srinivasa R. Popuri
    Chi-En Hung
    Journal of Material Cycles and Waste Management, 2017, 19 : 1235 - 1243
  • [50] Integrated process development for the recovery of Europium and Yttrium from waste fluorescent powder
    Lee, Ching-Hwa
    Liao, Ching-Hua
    Popuri, Srinivasa R.
    Hung, Chi-En
    JOURNAL OF MATERIAL CYCLES AND WASTE MANAGEMENT, 2017, 19 (03) : 1235 - 1243