Life Cycle Assessment of Reusable Plastic Crates (RPCs)
Abstract
:1. Introduction
2. Materials and Methods
2.1. Goal definition
- to assess the environmental and energy performances related to the life cycle of RPCs as a function of the number of deliveries;
- to identify the contribution of the reconditioning stage to the overall environmental indicators and indicate methods for a more sustainable management of RPCs.
2.2. RPCs System Description and Analyzed Scenarios
- the percentage of crates that are washed after the first inspection;
- the type and amount of chemicals used in the washing step.
2.3. Functional Unit
2.4. System Boundaries
- the production of the crates (100 input crates plus those replacing the discarded ones during the reconditioning process);
- the reconditioning process, i.e., the transportation of the crates from the users to the reconditioning plant, the consumption of electrical energy, water, fuel, and chemicals for the process (including the transport of chemicals to the facility), the wastewater treatment, and the incineration of the solid residues removed from the crates;
- the end of life of the crates through a recycling process (both the crates after n deliveries and those discarded in the reconditioning process);
- the transportation of the crates, the solid residues, and the sludge (from the wastewater treatment) to their final treatment.
- avoided production of PP primary granulate due to the recycling of the RPCs after n deliveries;
- avoided production of the electric energy from the Italian distribution grid due to the recovery of electricity in the incineration processes (incineration of sludge, solid residues, and plastic scraps from recycling);
- avoided production of heat from a domestic gas boiler due to the recovery of heat in the incineration processes.
2.5. Data Quality
2.6. Selected Indicators
- International reference life cycle data system—ILCD [26], considering 12 impact categories: climate change (CC), ozone depletion (OD), human toxicity (non-cancer effects; HTNC), human toxicity (cancer effects; HTC), particulate matter (PM), photochemical ozone formation (POF), acidification (A), terrestrial eutrophication (TE), freshwater eutrophication (FE), marine eutrophication (ME), freshwater ecotoxicity (FEC), and mineral, fossil, and renewable resources depletion (RD).
- Cumulative energy demand—CED [27], to evaluate the energy performance of the system.
2.7. Inventory
2.7.1. RPCs Production
2.7.2. Reconditioning Process
2.7.3. End of Life
3. Results
- the production step of (100 + 0.55 × (n − 1)) crates in case of the scenarios W1 and (100 + 0.46 × (n − 1)) crates for the scenarios W2;
- the reconditioning process of 100 × (n − 1) crates. This step includes the transportation of the crates from the users to the reconditioning plant, the washing step (consumption of electric energy, chemicals, and hot water), the wastewater treatment, and the incineration of the solid residues removed by the crates;
- the end of life of [100 + 0.55 × (n − 1)] crates in case of the scenarios W1 and of (100 + 0.46 × (n − 1)) crates for the scenarios W2.
3.1. Impact assessment
- the transportation of the crates from the users to the reconditioning plant (this is valid especially for the impact categories particulate matter, photochemical ozone formation, terrestrial and marine eutrophication, and resource depletion);
- the electricity consumption of the reconditioning plant in case of freshwater eutrophication and ecotoxicity impact categories;
- the washing stage, especially for the climate change and ozone depletion impact categories and the CED and water depletion indicators. In this stage, the most impacting processes are the heating of the water, the consumption of the disinfectant based on peracetic acid (only for the scenario RE1), and the consumption of water.
3.2. Reconditioning System (RPCs) vs. Single-Use System (SPCs)
3.3. Sensitivity Analysis
- the production of the electricity used in the reconditioning plant;
- the production of the heat used in the reconditioning plant;
- the substitution ratio between secondary and virgin PP granulate.
3.3.1. Production of the Electricity Used in the Reconditioning Plant
3.3.2. Production of Heat Used in the Reconditioning Plant
3.3.3. Substitution Ratio between Secondary and Virgin Polypropylene Granulate
4. Discussion and Conclusions
Supplementary Materials
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
References
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Parameter | Analyzed Scenarios | |
---|---|---|
Percentage of crates that are washed | W1: After the first inspection, all the crates are washed. The breakage rate 1 of the overall process (before and after washing) is 0.55% | W2: After the first inspection, only 55% of the crates are washed, whereas the others are considered in sufficient hygienic conditions to be re-used without being washed. The breakage rate 1 of the overall process is 0.46% |
Chemicals used in the washing step | RE1
| RE2
|
Input | Scenario | |||
---|---|---|---|---|
W1-RE1 | W1-RE2 | W2-RE1 | W2-RE2 | |
Water for washing | 0.055 m3 | 0.030 m3 | ||
Heating of water (gas conventional boiler) | 32.2 MJ | 17.7 MJ | ||
Electric energy | 2.48 kWh | 1.37 kWh | ||
Disinfectant RE1 (16% acetic acid, 15% peracetic acid, 23% hydrogen peroxide, 1% stabilizer, 45% deionized water) | 0.099 kg | - | 0.054 kg | - |
Disinfectant RE2 (sodium hypochlorite, 14% solution) | - | 0.043 kg | - | 0.024 kg |
Detergent RE1 (40% soda, 0.6% alkyl alcohol alkoxylate, 59.4% deionized water) | 0.523 kg | - | 0.288 kg | - |
Detergent RE2 (soda, 30% solution) | - | 0.179 kg | - | 0.099 kg |
Stabiliser (10% citric acid, 5% lactic acid, 0.25% potassium iodate, 84.75% deionized water) | - | 0.011 kg | - | 0.006 kg |
Transport for the supply of chemicals (light commercial vehicle) | 0.62 kg transported for 100 km | 0.23 kg transported for 100 km | 0.34 kg transported for 100 km | 0.13 kg transported for 100 km |
Solid residues removed from crates (sent to incineration for municipal waste—100 km distance) | 46 g | 199 g | ||
Wastewater (sent to a physical–chemical pre-treatment and then to a wastewater treatment plant) | 0.055 m3 | 0.030 m3 |
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Tua, C.; Biganzoli, L.; Grosso, M.; Rigamonti, L. Life Cycle Assessment of Reusable Plastic Crates (RPCs). Resources 2019, 8, 110. https://doi.org/10.3390/resources8020110
Tua C, Biganzoli L, Grosso M, Rigamonti L. Life Cycle Assessment of Reusable Plastic Crates (RPCs). Resources. 2019; 8(2):110. https://doi.org/10.3390/resources8020110
Chicago/Turabian StyleTua, Camilla, Laura Biganzoli, Mario Grosso, and Lucia Rigamonti. 2019. "Life Cycle Assessment of Reusable Plastic Crates (RPCs)" Resources 8, no. 2: 110. https://doi.org/10.3390/resources8020110
APA StyleTua, C., Biganzoli, L., Grosso, M., & Rigamonti, L. (2019). Life Cycle Assessment of Reusable Plastic Crates (RPCs). Resources, 8(2), 110. https://doi.org/10.3390/resources8020110