4.7 Article

O2-enriched microbial activity with pH-sensitive solvo-chemical and electro-chlorination strategy to reclaim critical metals from the hazardous waste printed circuit boards

Journal

JOURNAL OF HAZARDOUS MATERIALS
Volume 416, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.jhazmat.2021.125769

Keywords

Hybrid technology; Green recycling process; Electronic waste; Bio-solvo-and electro-chemical approach; Strategically-critical metals

Funding

  1. Brain Pool Program through the National Research Foundation of Korea (NRF) - Ministry of Science and ICT [2019H1D3A2A02101993]
  2. National Research Foundation of Korea [2019H1D3A2A02101993, 5199990214022] Funding Source: Korea Institute of Science & Technology Information (KISTI), National Science & Technology Information Service (NTIS)

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An innovative process integration for sustainable recovery of critical metals from waste printed circuit boards is demonstrated, involving acid pre-treatment and microbial activity for base metals' liberation. Through optimization, efficient separation and extraction of copper, nickel, zinc, and gold are achieved.
An innovative process integration for the sustainable recovery of critical metals from waste printed circuit boards (WPCBs) is demonstrated. In the acid pre-treatment of WPCBs, > 95% of highly toxic metals lead and tin could dissolve after 240 min of contact in 4.0 mol L-1 HNO3. Thereafter, the microbial activity of Sulfobacillus ther-mosulfidooxidans (strain RDB) under intense aeration is found favorable for base metals' liberation. similar to 92% copper, 89% nickel, and 93% zinc get extracted at the optimal condition of O-2-mixed-aeration, 30%; pulp density, 10 g L-1; aeration rate, 0.5 L min(-1); sulfur dosage, 2%; temperature, 45 degrees C; and duration, 21 days. Quantitative separation of base metals is achieved using ketoxime as a function of equilibrium pH that yielding pH(0.5) order: Cu (1.45) < Ni (5.7) < Zn (8.1). The residual gold from WPCBs is uniquely leached (similar to 99% efficiency) in brine solution (2.0 mol L-1 NaCl) under the electro-chlorination rate, 0.62 mmol min(-1); dissolution pH, 1.0; pulp density, 20 g L-1; temperature, 30 degrees C; and time, 60 min. Subsequently, gold from brine solution is solvated with tri-butyl-phosphate at pH(eq), <= 0.5, forming <([2( RP = O)center dot HAuCl4 center dot H2O])over bar> complex in the organic phase. Finally, > 99% of high-purity gold is stripped from loaded organic while contacting ammoniacal thiosulfate solution in two-stages of counter-current flow.

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