| Literature DB >> 33885343 |
Neelam Rathore1, Narayan Lal Panwar1.
Abstract
Solar energy has become a leading solution to meet the increasing energy demand of growing populations. Solar photovoltaic technology is an efficient option to generate electricity from solar energy and mitigate climate change. Although the development and growth of solar photovoltaics has had a positive impact on energy system decarbonization, but end-of-life solar panels might become toxic waste if not properly disposed of. Presently in India, approximately 200,000 tonnes of solar photovoltaic waste are expected to be produced by 2030 and 1.8 million tonnes by 2050, by which time solar waste could grow to 60 million tonnes globally. Solar waste has recently been included in the category of waste electrical and electronic equipment to restrict the negative influence of continual development. Recent advancements have been focused only on increasing the efficiency of solar photovoltaic panels without considering the impact of waste solar panels on the environment and the issue of appropriate disposal of waste panels. Effective and ecofriendly methods for recycling end-of-life waste are rarely considered. There is a need to critically investigate and manage the disposal and recycling of solar panels waste. This review article addresses handling and recycling of solar waste, which will be present in large quantities after 25 years. We review multiple adopted technologies to recycle solar waste and technological advancement achieved while recycling photovoltaic waste. Further life cycle assessment of recycling technologies is also discussed.Entities:
Keywords: Waste generation; end of life; environmental impact; life cycle assessment; recycling; solar photovoltaic technology
Mesh:
Year: 2021 PMID: 33885343 PMCID: PMC9016676 DOI: 10.1177/0734242X211003977
Source DB: PubMed Journal: Waste Manag Res
Figure 1.Total installed power capacity in India.
RES: renewable energy sources.
Source: MNRE, 2019.
Figure 2.Estimation of cumulative solar PV module waste (million tonnes), 2020–2050.
Source: Chowdhury et al., 2020.
Constituents of crystalline silicon solar panels.
| Recyclable material | Content (kg kWp−1) |
|---|---|
| Frame | Al 12.77 |
| Silver bar line | Ag 0.03 |
| Glass | Glass 54.72 |
| Polycrystalline silicon chips | Si 3.10 |
| Background | Plastic 17.09 |
| Adhesive sealant | 10% |
| Tinned wire | Cu 0.45 |
Source: Xu et al., 2018.
Hazardous materials used in PV manufacturing.
| Type of cell | Material used | Critical issues if disposed of improperly |
|---|---|---|
| GaAs | Arsenic (As) | Poisonous, cancer promoting, lung affecting. |
| Arsine (As H3) | Toxic gas, blood, kidney damaging | |
| Trimethyl gallium | Pyrophoric liquid | |
| Hydrochloric acid | Corrosive material | |
| Methane | Flammable gas | |
| a-Si | Diborane (as dopant) | Flammable gas |
| Pulmonary problem | ||
| Diethylsilane (in deposition) | Flammable liquid | |
| Silane (in deposition) | Pyrophoric gas, irritant, fire hazard | |
| Hydrofluoric acid | Corrosive material | |
| Silicon tetrafluoride (in deposition) | Toxic and corrosive gas | |
| Hydrogen | Flammable gas and fire hazard | |
| CuSe.InSe | Selenium | Poisonous and irritant |
| CdTe | Tellurium | Adverse effect on liver |
| Cadmium | Can cause lung cancer, also affects bones and kidneys |
Source: Nkuissi et al., 2020.
Figure 3.Waste classification of PV modules along with their environmental impact.
Source: Suresh et al., 2019.
Figure 4.PV recycling methods.
Source: Chowdhury et al., 2020.
Method for recycling of modules. .
| Methods | Recovery aim | Treatment condition | References |
|---|---|---|---|
| Nitric acid dissolution | Wafer from module | 60°C and 25 hours |
|
| Fluidized bed combustion | Wafer from module | 450–470°C, 30 minutes |
|
| Thermal decomposition in inert gas | Cell from 1 cell module | 520°C, 90 minutes |
|
| Dense acids like H2SO4, HNO3, HCL | PV layer separation | 50°C, 40 min with high agitation rate |
|
| Vacuum decomposition | Recycling of gallium | 850°C, 1 Pa and 40 minutes |
|
| Combustion | Glass, Si cells and electrode metal | Combustion at 500–550°C |
|
| Pre-treatment of glass and EVA surfaces |
EVA: ethylene vinyl acetate.
Favourable treatment conditions in thin film and CIS panels.
| Type of panel | Parameters | |||
|---|---|---|---|---|
| Acid mixture and ratio | Temperature | Stirring | Time | |
| Thin film (a-Si:H and µ-Si:H) | H2SO4: H2O | 50°C | 100 rpm | 60 min |
| 1:1 | ||||
| H2SO4: H2O (serial elution) | Reaction temperature | 0 rpm | 40 min | |
| 1:1 | ||||
| CuSe.InSe | Lactic acid: H2O | 25°C | 100 rpm | 4 days |
CIS: copper-indium-selenide.
Source: Savvilotidou et al., 2017.
Figure 5.Technologies for solar panel recycling.
Source: Xu et al., 2018.
Figure 6.Separation of layers in furnace: (a) before thermal process, (b) after thermal process, (c) the front surface and (d) back surface of solar cells.
Source: Shin et al., 2017.
Figure 7.(a) the PV cell surface after the swelling of the EVA resin and (b) the remained PV cell after the EVA resin was removed.
Source: Kang et al., 2012.
Figure 8.Summary of reported recycling process.
Source: Lunardi et al., 2018b.
Summary of various recycling processes of crystalline PV panels.
| Process | Result | References |
|---|---|---|
| Pyrolysis (fluidized bed reactor or conveyer belt) | This process separates 100% of glass sheets and 80% of wafers |
|
| Pyrolysis (at different oxidizing atmosphere and at different heating rates) to separate EVA | The content of acetate in EVA strongly influences the pyrolysis behaviour (melting point and pyrolysis gas amount) of EVA |
|
| Nitrogen pyrolysis process | Decompose plastic. Organic conversion rate approached 100% for the condition of 500°C, 30 min, and 0.5 L min−1 N2 flow rate |
|
| Removal of EVA using trichloroethylene | When single cell module was dissolved in organic solvent at 80°C for 10 days, silicon cell was separated without any dent |
|
| Deutsche Solar’s process including chemical and thermal treatment | This process yields about 76% of recovered cells which can be reutilized |
|
| Removal of EVA layer and silicon by thermal treatment along with etching treatment | Pure silicon was recycled where adjustment of chemical conditions is necessary |
|
| Two step heating process of EVA along with chemical treatment with acid and alkali | This process separated 62% silicon and 85% copper |
|
| Treatment with chemical etching followed by dissolution of EVA in organic solvent | High purity silicon up to 86% could be recovered | |
| Separation of glass sheets from panels using prototype induction method | Satisfactory results were obtained but it does not provide any quantitative information |
|
EVA: ethylene vinyl acetate.
Comparison of various recycling processes of silicon module.
| Technology | Process | Advantages | Limitations | References |
|---|---|---|---|---|
| Delamination | Physical disintegration | Various types of waste can be obtained by splitting modules and laminated modules. | It could break solar cells | |
| Glass cannot be separated from EVA | ||||
| Dissolution in nitric acid | EVA and metal layers can be removed. | Release of harmful emissions. | ||
| Whole cell can be recovered. | ||||
| Thermal treatment | Removal of EVA completely. | Requirement of large amount of input energy. | ||
| Removal of EVA | ||||
| Ultrasonic irradiation | Recovery of Si without any damage | Waste solution treatment. | ||
| Dissolution in organic solvent | Module separation | It produces organic liquid waste |
| |
| Heat treatment and chemical etching | Recovered silicon wafers are not very pure | |||
| Materials separation | Erosion | Glass can be recovered | Pre-purification of panels is necessary. |
|
| No need for any chemicals. | ||||
| Vacuum blasting | Glass can be recovered completely | Release of metallic fractions. | ||
| Semiconductor layer is removed without any use of chemicals. | Time consuming process. | |||
| Leaching | Metal is completely removed from glass. | Large amount of chemicals is used. | ||
| Flotation | Less chemicals are required | Recovered materials are not very pure. | ||
| Simpler method. | Materials are separated at various stage of process. | |||
| Dry and wet chemical process | Less chemicals and simple process requiring less energy. | Dissolved solids cannot be removed. | ||
| Low and controllable emissions. | ||||
| Materials purification | Hydrometallurgical | Commercially applicable. | It involves large absorption and separation steps. |
|
| Applicable to industries. | High throughput is required. |
| ||
| Pyrometallurgical | Feedstock can contain different materials. | Few materials can be missed in slag. |
|
EVA: ethylene vinyl acetate.
Figure 9.Comparison of different PV technologies by valuation with Eco-indicator 99.
Source: Jungbluth et al., 2007.
LCA assessment of 1000 kg of PV waste generated by 73 m2 of panels.
| Fuels/chemicals required | Process | Emission | Scraps |
|---|---|---|---|
| DieselDiesel (1.14 L)Electricity (5.33 kWh) |
| Yes | |
| Diesel (1.14 L) | Yes | ||
| Electricity (5.33 kWh) | Yes | 3.3 kg of copper scrap and 180 kg of aluminium scraps | |
| Electricity (48.01 kWh) |
| Yes | Glass scrap |
| Electricity (0.25 kWh) |
| Yes | |
| Electricity (56.76 kWh) |
| Emissions from transportation of bottom ash (from incinerator to sieving) | Aluminium scrap and 34.68 kg of metallurgical grade silicon scrap |
| 100 kg water | Electrolysis | 2 kg of NOx | 0.50 kg of silver scrap and 1.08 kg of copper scrap |
| 36.5 kg of water and 36.5 kg Ca(OH)2 |
| Emissions from transportation of 306.13 kg of liquid waste and 50.25 kg sludge to landfill site |
LCA: life cycle assessment.
Source: Latunussa et al., 2016.
Figure 10.Environmental impact of 1000 kg silicon PV waste recycling.
Source: Latunussa et al., 2016.
Comparison of various studies of recycling for climate change scenario.
| Process | Impact and savings | Reference |
|---|---|---|
| FRELP | Impact: 461 kg CO2 eq. per tonne of treated waste |
|
| Saving: 2400 kg CO2 eq. per tonne | ||
| Baseline | Impact: 116 kg CO2 eq. per tonne of treated waste |
|
| Saving: 2025 kg CO2 eq. per tonne | ||
| Treatment of Si PV module with 72 cells | Impact: 59.2 kg CO2 eq. GWP |
|
| Acidification: 0.4 kg SO2 eq. | ||
| Recycling of 1 m2 CdTe PV plant | Energy demand: 81 MJ, GWP: 6 kg CO2 eq. |
|
| Acidification: 9.1 kg SO2 eq. |
GWP: global warming potential.