| Literature DB >> 36061036 |
Nayla Ahmad Al-Thani1,2, Tareq Al-Ansari1, Mohamed Haouari2.
Abstract
In 2018, the global annual consumption of Polyethylene terephthalate (PET) bottles was approximately 27.64 million tons, with one million bottles sold worldwide every minute. Unmanaged PET bottles in the environment lead to a series of negative effects on the health of humans and ecosystems. Therefore, the objective of this research was to evaluate the sustainability of eight different PET waste bottle treatment methods using a holistic multi-criteria decision-making approach that combined the technique for order of preference by similarity to ideal solution (TOPSIS) with analytic hierarchy (AHP; TOPSIS-AHP) and coefficient of variation (COV; TOPSIS-COV) approaches. To the best of our knowledge, TOPSIS-COV has not yet been used for waste management. The treatment methods were compared and analyzed against twelve different performance criteria representing three pillars of sustainability: environmental, economic, and social. Both approaches determined closed-loop recycling to be optimal for treating PET waste bottles. The weights of performance indicators obtained using the COV and AHP approaches were comparable, except for cost, photochemical oxidant potential, and human toxicity. The large dispersion in the values of the photochemical oxidant potential causes it to have a higher weight in the COV approach. For cost, the weight was higher using the AHP approach by approximately 12%, which reflects the preference of decision-makers to reduce costs of ventures.Entities:
Keywords: Analytic hierarchy process; Circular economy; Multi-criteria decision making; Performance indicators; Resource management; Sustainable waste management
Year: 2022 PMID: 36061036 PMCID: PMC9434055 DOI: 10.1016/j.heliyon.2022.e10274
Source DB: PubMed Journal: Heliyon ISSN: 2405-8440
Comparison between other research and this research.
| Reference | Method | Performance Criteria | Technology | Material | |||||||
|---|---|---|---|---|---|---|---|---|---|---|---|
| AHP | Fuzzy AHP | TOPSIS | COV | Other | Environment | Economic | Social | Technical | |||
| ( | X | X | Air resources, Water resources, Land resources, Mineral and energy resources, | Economic performance, financial benefits, Trading opportunities, Macro social performance. Managerial ability, Interest support groups, Customer Satisfaction, Managerial effectiveness, Management ability | Health, Potential Internal human resources, External population, Stakeholder population, | Technical capability, New technology acceptance, technical support and training | Mechanical recycling process Chemical recycling process Energy recovery | Mixed Plastic | |||
| ( | Robust mixed- integer linear programming | Pyrolysis | |||||||||
| ( | X | X | Slag Land use Emissions | Employment rate Accessories industry growth Operational cost | Technology level Ease of equipment access Ease of technology use Workplace safety | Plasma Pyrolysis Gasification Incineration | Municipal Solid Waste | ||||
| ( | Multi-Attribute Value Theory | landfilling, incinerating, and recycling | Mixed Plastic | ||||||||
| ( | Hesitant Pythagorean Fuzzy - ELimination and Choice Expressing REality III” | Mechanical, chemical, feedstock and incineration for energy | PET, HDPE, PVC, LDPE, PP, and PS | ||||||||
| This research | X | X | X | Global warming potential, abiotic depletion potential, marine ecotoxicity potential, freshwater ecotoxicity potential, terrestrial ecotoxicity potential, eutrophication potential, terrestrial acidification potential, photochemical oxidant formation, and ozone depletion potential. | Cost Revenue | Human toxicity potential. | Closed-loop, open-loop (mechanical), open-loop (semi-mechanical), landfill, incineration with heat recovery, incineration with heat and power recovery, glycolysis, and pyrolysis. | PET bottles | |||
Figure 1Methodological framework.
Selected performance indicators.
| Indicator | Description | Reference |
|---|---|---|
| Global Warming Potential (GWP) | Potential change in the earth's temperature due to the release of greenhouse gases. | ( |
| Abiotic Depletion Potential (ADP) | Potential depletion of natural resources. | ( |
| Marine Ecotoxicity Potential (METP) | Potential impact of released toxic substances on marine environments. | ( |
| Freshwater Ecotoxicity Potential (FETP) | Potential impact of released toxic substances on freshwater organisms. | ( |
| Terrestrial Ecotoxicity Potential (TETP) | Potential impact of released toxic substances on land-dependent organisms. | ( |
| Eutrophication Potential (EP) | Potential overgrowth of plankton, algae, and higher aquatic plants due to increased nutrients in the water. | ( |
| Terrestrial Acidification Potential (TAP) | Potential impact of acidifying pollutants on soil, groundwater, surface waters, and biological organisms. | ( |
| Photochemical Oxidant Potential (POFP) | Potential formation of photochemical ozone in the lower atmosphere. | ( |
| Ozone Depletion Potential (ODP) | Potential damage to the protective stratospheric ozone layer due to the human emitted gases. | ( |
| Human Toxicity Potential (HTP) | Potential impact of emitted substances that exist in the environment on human health. | ( |
| Cost | Estimated cost of treating one ton of PET waste. | – |
| Revenue | Estimated revenue of treating one ton of PET waste. | – |
Figure 2Different roots of PET waste treatment alternatives.
Description of the selected technologies.
| Technology | Description |
|---|---|
| Closed-loop recycling | Converting PET waste bottles through physical processes into new bottles with similar properties to the original product. |
| Open-loop recycling (Mechanical recycling) | Converting PET waste bottles using physical and chemical processes into a lower grade plastic product. In mechanical recycling fibers are produced through direct extrusion from flakes. |
| Open-loop recycling (semi-mechanical recycling) | Converting PET waste bottles using physical and chemical processes into a lower grade plastic product. In the semi-mechanical recycling, the first step is to utilize extrusion to make pellets, then the pellets are converted into fibers and other products. |
| Glycolysis | Chemical recycling technique that converts PET waste bottles into oligomer in the presence of a catalyst. Then the oligomers are repolymerized into PET fiber. |
| Pyrolysis | Converting PET waste bottles into other useful products, such as oils and syngas, through thermal decomposition in an inert atmosphere. |
| Incineration with heat recovery | Combustion of PET waste bottles as a fuel to releases heat. The heat is used for heating spaces ( |
| Incineration with heat and power recovery | Combustion of PET waste bottles as a fuel to releases power and heat. The power feeds the grid and the heat is used for heating spaces ( |
| Landfill | Transporting PET waste bottles into landfill sites; the first and most used waste management strategy in most countries including developed countries. |
Figure 3Hierarchical decision structure of PET waste management.
The Performance indicators for the selected end-of-lives.
| Process | Closed-Loop | Open-loop (mechanical) | Open-loop (semi-mechanical) | Landfill | Incineration with heat recovery | Incineration with heat and power recovery | Glycolysis | Pyrolysis |
|---|---|---|---|---|---|---|---|---|
| GWP | −1.70 × 103 | 7.09 × 102 | 1.31 × 103 | 2.91 × 103 | 4.95 × 103 | 1.40 × 103 | 1.84 × 103 | 4.31 × 102 |
| ADP | −1.34 × 10−2 | 4.43 | 7.67 | 3.31 × 10−4 | 8.91 × 10−4 | 8.6 × 10−6 | 1.27 × 101 | 2.53 × 10−6 |
| METP | −1.10 × 104 | 0.00 | 0.00 | 8.62 × 105 | 2.34 × 106 | 1.7 × 104 | 0.00 | 4.86 × 103 |
| FETP | −7.87 × 101 | 2.19 × 102 | 1.74 × 102 | 2.04 × 102 | 5.62 × 102 | 1.2 × 102 | 2.15 × 102 | 3.49 × 101 |
| TETP | −4.44 × 10−1 | 5.17 | 4.88 | 1.70 | 4.72 | 6.7 × 10−1 | 1.21 × 101 | 1.97 × 10−1 |
| EP | −1.04 × 10−1 | 5.91 × 10−1 | 4.88 × 10−1 | 3.60 | 4.90 | −7.2 × 10−2 | 1.63 | 6.11 × 10−2 |
| TAP | −1.84 | 2.22 | 6.28 | 4.34 × 101 | 3.74 × 101 | −3.2 | 9.95 | 8.26 × 10−1 |
| POFP | −2.09 × 101 | 1.48 × 10−1 | 2.09 × 10−1 | 2.39 | 2.10 | −5.9 | 4.26 × 10−1 | 1.16 |
| ODP | 0.00 | 0.00 | 0.00 | 1.18 × 10−5 | 3.16 × 10−5 | 0.00 | 0.00 | 0.00 |
| HTP | −7.16 × 104 | 2.68 × 102 | 2.89 × 102 | 1.46 × 102 | 4.83 × 102 | 1.1E+5 | 5.29 × 102 | 3.17 × 104 |
| Cost | 500 | 500 | 500 | 1.80 × 102 | (4.20 × 102) | (2.1 × 102) | 1300 | 410 |
| Revenue | 1000 | 1000 | 1000 | 0.00 | 41.4 | 41.36 | 1400 | 590 |
(Chilton et al., 2010).
(Shen et al., 2010).
(Aryan et al., 2019).
(Willard, 2019).
(Yoshioka et al., 2004).
(Gradus et al., 2016).
Figure 4Importance of environmental impact criteria.
Pairwise comparison matrix of the criteria which hold the preference value.
| Criteria | Economic | Environment | Social |
|---|---|---|---|
| Economic | 1 | 0.25 | 2 |
| Environment | 4 | 1 | 4 |
| Social | 0.50 | 0.25 | 1 |
Normalized matrix.
| Criteria | Economic | Environment | Social |
|---|---|---|---|
| Economic | 0.182 | 0.17 | 0.286 |
| Environment | 0.727 | 0.67 | 0.571 |
| Social | 0.091 | 0.17 | 0.143 |
Normalized principal Eigen vector (i.e. weights/priority vector).
| Criteria | Wj |
|---|---|
| Economic | 0.211 |
| Environment | 0.655 |
| Social | 0.133 |
Weights of the criteria and sub-criteria weights calculated using AHP.
| Criteria | Sub-Criteria | Weight (W) |
|---|---|---|
| Social | Human Toxicity Potential | 10.22% |
| Economic | Cost | 14.85% |
| Revenue | 6.28% | |
| Environment | Global warming | 8.22% |
| Abiotic Depletion | 6.63% | |
| Marine ecotoxicity | 8.60% | |
| Freshwater ecotoxicity | 8.97% | |
| Terrestrial ecotoxicity | 8.70% | |
| Eutrophication | 6.81% | |
| Terrestrial acidification | 6.53% | |
| Photochemical oxidant formation | 6.66% | |
| Ozone depletion | 7.54% | |
Calculated weights using the COV method.
| Process | COVj | Wj |
|---|---|---|
| GWP | 1.3 | 5.82% |
| ADP | 1.557 | 6.96% |
| METP | 2.0899 | 9.33% |
| FETP | 1.024 | 4.57% |
| TETP | 1.13 | 5.05% |
| EP | 1.358 | 6.07% |
| TAP | 1.528 | 6.83% |
| POFP | 3.09 | 13.81% |
| ODP | 2.092 | 9.35% |
| HTP | 5.66 | 25.29% |
| Cost | 0.67 | 3.08% |
| Revenue | 0.8637 | 3.85% |
Measurement of the ideal separation (), negative-ideal separation (), and relative closeness for TOPSIS-AHP.
| Process | Rank | ||||
|---|---|---|---|---|---|
| Closed-loop | 3.01 × 10−2 | 2.61 × 10−1 | 2.91 × 10−1 | 0.897 | 1 |
| Open-loop (mechanical) | 1.09 × 10−1 | 1.89 × 10−1 | 2.98 × 10−1 | 0.635 | 3 |
| Open-loop (semi-mechanical) | 1.12 × 10−1 | 1.86 × 10−1 | 2.99 × 10−1 | 0.624 | 4 |
| Landfill | 1.42 × 10−1 | 1.75 × 10−1 | 3.16 × 10−1 | 0.553 | 6 |
| Incineration with heat recovery | 2.01 × 10−1 | 1.33 × 10−1 | 3.34 × 10−1 | 0.397 | 8 |
| Incineration with heat and power recovery | 1.57 × 10−1 | 1.98 × 10−1 | 3.55 × 10−1 | 0.558 | 5 |
| Glycolysis | 1.70 × 10−1 | 1.61 × 10−1 | 3.31 × 10−1 | 0.485 | 7 |
| Pyrolysis | 1.12 × 10−1 | 2.04 × 10−1 | 3.16 × 10−1 | 0.646 | 2 |
Measurement of the ideal separation (), negative-ideal separation (), and relative closeness for TOPSIS-COV.
| Process | Rank | ||||
|---|---|---|---|---|---|
| Closed-loop | 9.0 × 10−3 | 4.10 × 10−1 | 4.19 × 10−1 | 0.979 | 1 |
| Open-loop (mechanical) | 1.94 × 10−1 | 2.56 × 10−1 | 4.50 × 10−1 | 0.569 | 2 |
| Open-loop (semi-mechanical) | 1.97 × 10−1 | 2.53 × 10−1 | 4.50 × 10−1 | 0.563 | 3 |
| Landfill | 2.21 × 10−1 | 2.32 × 10−1 | 4.53 × 10−1 | 0.512 | 5 |
| Incineration with heat recovery | 2.56 × 10−1 | 2.14 × 10−1 | 4.70 × 10−1 | 0.456 | 7 |
| Incineration with heat and power recovery | 3.55 × 10−1 | 1.73 × 10−1 | 5.29 × 10−1 | 0.328 | 8 |
| Glycolysis | 2.10 × 10−1 | 2.48 × 10−1 | 4.57 × 10−1 | 0.542 | 4 |
| Pyrolysis | 2.41 × 10−1 | 2.21 × 10−1 | 4.62 × 10−1 | 0.479 | 6 |
Figure 5Difference between the rank of the processes using subjective and objective weights. Global Warming Potential (GWP), Abiotic Depletion Potential (ADP), Marine Ecotoxicity Potential (METP), Freshwater Ecotoxicity Potential (FETP), Terrestrial Ecotoxicity Potential (TETP), Eutrophication Potential (EP), Terrestrial Acidification Potential (TAP), Photochemical Oxidant Potential (POFP), Ozone Depletion Potential (ODP), and Human Toxicity Potential (HTP).
Figure 6Sensitivity analysis (Green: Closed-Loop Recycling, Red: Pyrolysis).
List of the weights for the main criteria for each scenario.
| Scenario | Environment | Economic | Social |
|---|---|---|---|
| S1 | 1 | 0 | 0 |
| S2 | 5/6 | 1/6 | 0 |
| S3 | 5/6 | 0 | 1/6 |
| S4 | 2/3 | 0 | 1/3 |
| S5 | 2/3 | 1/3 | 0 |
| S6 | 2/3 | 1/6 | 1/6 |
| S7 | 1/2 | 1/2 | 0 |
| S8 | 1/2 | 0 | 1/2 |
| S9 | 1/2 | 1/6 | 1/3 |
| S10 | 1/2 | 1/3 | 1/6 |
| S11 | 1/3 | 2/3 | 0 |
| S12 | 1/3 | 0 | 2/3 |
| S13 | 1/3 | 1/3 | 1/3 |
| S14 | 1/3 | 1/6 | 1/2 |
| S15 | 1/3 | 1/2 | 1/6 |
| S16 | 1/6 | 5/6 | 0 |
| S17 | 1/6 | 0 | 5/6 |
| S18 | 1/6 | 2/3 | 1/6 |
| S19 | 1/6 | 1/6 | 2/3 |
| S20 | 1/6 | 1/3 | 1/2 |
| S21 | 1/6 | 0.5 | 1/3 |
| S22 | 0 | 1 | 0 |
| S23 | 0 | 0 | 1 |
| S24 | 0 | 1/3 | 2/3 |
| S25 | 0 | 2/3 | 1/3 |
| S26 | 0 | 5/6 | 1/6 |
| S27 | 0 | 1/6 | 5/6 |
| S28 | 0 | 1/2 | 1/2 |