| Literature DB >> 32538256 |
Shashi Arya1,2, Sunil Kumar1.
Abstract
Resource Recovery from Waste Electronics has emerged as one of the most imperative processes due to its pressing challenges all over the world. The Printed Circuit Board (PCB) is one of the typical E-waste components that comprise large varieties of metals and nonmetals. Urban Mining of these metals has received major attention all over the world. The existing treatment procedures used extensively for the resource extraction are hydrometallurgy and pyro-metallurgy and crude recycling practices in the informal sector. However, these methods are prone to cause secondary pollutants with certain drawbacks. Also, the existing informal recycling procedures resulted in insignificant occupational health hazards and severe environmental threats. The application of biotechnology is extensively exploited for metal extraction and emerged as one of the sustainable and eco-friendly tools. However, a limited field-scale study is prevailing in the realm of resource recovery from E-waste using bioleaching method. Hence, the application of bioleaching requires more attention and technical know-how in developing countries to curtail crude practices. The application of bioleaching in E-waste, including its available methods, kinetics mechanism associated opportunities, and barriers, have been discussed in this paper. A glance of E-waste management in India and the menace of 95% crude E-waste recycling are also elaborated. The incentives toward profit, socio-economic, and environmentally sustainable approaches have been delineated based on critical analysis of the available literature.Entities:
Keywords: E-waste; bioleaching; hydrometallurgy; informal recycling; printed circuit board; pyro-metallurgy
Mesh:
Year: 2020 PMID: 32538256 PMCID: PMC8291872 DOI: 10.1080/21655979.2020.1775988
Source DB: PubMed Journal: Bioengineered ISSN: 2165-5979 Impact factor: 3.269
Figure 1.Urban mining and its scope toward SDG.
Figure 2.Existing treatment stages for resource recovery from E-waste.
Investment in resource recovery including its treatment method [Adapted and modified from Priya and Hait, 2017 [15], Chatterjee, 2012 [59] and CAMA, 2006 [60]].
| Approximate Investment | |||
|---|---|---|---|
| S. No. | Treatment method | Hydrometallurgy | Pyrometallurgy |
| 1 | E-waste collection | 5.199 | 5.199 |
| 2 | Manpower charges for pretreatment (dismantling and segregation) | 1.039 | 1.039 |
| 3 | Processing and concentration (shredding etc.) | 0.208 | 0.208 |
| 4 | Smelting process | 1.549 | aNA |
| 5 | Recovery and purification | aNA | 1.243 |
aNA 1 USD = INR 60
Typical market value of the resource recovery from E-waste [Adapted and modified from Toxic Link, 2018 [83] and [60–64]].
| E-Waste Material | Resource Recovery | Market Value | US $ |
|---|---|---|---|
| CRT’s | Copper, Plastics, Glass, Lead, Aluminum | Copper: 421.60/kg | 5.48/kg |
| Liquid Crystal Display (LCD) | Indium, tin and Copper | Iron Material: 40–50/kg | 0.52–0.65/kg |
| PCB | Tin, Copper, Lead, Iron, Bromine, Nickel | Lead: 140.50/kg | 1.83/kg |
| Mobile Phones | Copper, Silver, Gold, Palladium, Cobalt | Silver: 1400–1500/kg | 18.21–19.51/kg |
Resource Recovery based on the process treatment
INR and US $ as per 2019 Market Price
Figure 3.Comparative assessment of treatment options for resource recovery from E-waste [Adapted and modified from Priya and Hait, 2017 [15]].
Figure 4.Variations and different steps of bioleaching of E-waste.
Microorganism and conditions for bioleaching.
| Waste Component | Microorganisms | Temp (oC) | pH | Stirring Time | Solid/Liquid Ratio (%w/v) | Time Duration (Days) | Metal Extracted (%) | Authors |
|---|---|---|---|---|---|---|---|---|
| WEEE Shredding dust | 30 | 1.0–3.5 | 150 | 0.5–2 | 8 | Ce, Eu, Ne-99 | [ | |
| 30 | - | 150 | 1 | 30 hours | Au: 48 | |||
| WEEE | 30 | 2.1–0.9 | 150 | 0.5–1 | 21 | Al, Cu, Ni, Zn- 90 | [ | |
| PCBs | 45 | 2.0 | 180 | 1 | 18 | Cu: 89 | [ | |
| PCBs | Ambient | 1.0–1.6 | 150 | 1 | 7 | Cu:98 | [ | |
| TV PCBs | 35 | 1.7 | 175 | 1 | 4.8 | Cu:89 | [ | |
| PCBs | Mixed Acidophilic bacteria | 30 | 2.0 | 160 | 1.2 | 1.8 | Cu: 96.8 | [ |
| PC PCBs | 30 | 3.0 | 170 | 2 | 0.8 | Cu: 100 | [ | |
| PC PCBs | 30 | 2.2 | 170 | 1.5 | 3 | Al: 75.4 | [ | |
| CRT Fluorescent Powder | 30 | 1.7 | 175 | 10 | 16 | Y: 70 | [ | |
| PCBs | 30 | 2.0 | 165 | 2.5 | 4 | Cu: 100 | [ | |
| PCBs (4–10 mm) | 30 | 1.8–2.5 | 170 | 1 | 28 | Cu: 94.8 | [ | |
| PCBs (1 mm) | 30 | 2.0 | 160 | 10(v/v) | 7 | Cu 32.4 | [ | |
| PCB Powder | 55 | 1.2 | 200 | - | 2 hours | Cu: 100 | [ |
Figure 5.Techno-economic and environmental sustainability evaluation of existing methods of resource recovery from waste PCBs [131]. (a) Comparative capital expenditure and revenue generation of different methods of E-waste resource recovery. (b) Influence of the respective technology on climate change and the contribution of carbon dioxide per PCB [92].