| Literature DB >> 30223602 |
Ana Elduque1, Daniel Elduque2, Carmelo Pina3, Isabel Clavería4, Carlos Javierre5.
Abstract
Polymer injection-molding is one of the most used manufacturing processes for the production of plastic products. Its electricity consumption highly influences its cost as well as its environmental impact. Reducing these factors is one of the challenges that material science and production engineering face today. However, there is currently a lack of data regarding electricity consumption values for injection-molding, which leads to significant errors due to the inherent high variability of injection-molding and its configurations. In this paper, an empirical model is proposed to better estimate the electricity consumption and the environmental impact of the injection-molding process. This empirical model was created after measuring the electricity consumption of a wide range of parts. It provides a method to estimate both electricity consumption and environmental impact, taking into account characteristics of both the molded parts and the molding machine. A case study of an induction cooktop housing is presented, showing adequate accuracy of the empirical model and the importance of proper machine selection to reduce cost, electricity consumption, and environmental impact.Entities:
Keywords: electricity consumption; empirical model; environmental impact; injection-molding; manufacturing processes; polymer material
Year: 2018 PMID: 30223602 PMCID: PMC6164802 DOI: 10.3390/ma11091740
Source DB: PubMed Journal: Materials (Basel) ISSN: 1996-1944 Impact factor: 3.623
Figure 1Empirical model.
Estimated electricity consumption in kWh/kg for different values of machine efficiency and % of utilization.
| % of Utilization | Low-Efficiency SEC | Medium-Efficiency SEC | High-Efficiency SEC |
|---|---|---|---|
| 0 | 6.000 | 5.000 | 4.000 |
| 10 | 2.372 | 1.581 | 0.791 |
| 20 | 1.677 | 1.118 | 0.559 |
| 30 | 1.369 | 0.913 | 0.456 |
| 40 | 1.186 | 0.791 | 0.395 |
| 50 | 1.061 | 0.707 | 0.354 |
| 60 | 0.968 | 0.645 | 0.323 |
| 70 | 0.896 | 0.598 | 0.299 |
| 80 | 0.839 | 0.559 | 0.280 |
| 90 | 0.791 | 0.527 | 0.264 |
| 100 | 0.750 | 0.500 | 0.250 |
Machine efficiency values for the empirical model, E.
| Injection-Molding Machine | Clamping Force (kN) | Manufacturing Year | Efficiency (E) |
|---|---|---|---|
| A | 80,000 | 2005 | 70 |
| B | 52,000 | 2005 | 70 |
| C | 30,000 | 2000 | 65 |
| D | 20,000 | 2010 | 75 |
| E | 16,500 | 2010 | 75 |
| F | 12,000 | 1999 | 65 |
| G | 10,000 | 2008 | 70 |
| H | 7500 | 2005 | 70 |
| I | 4000 | 1996 | 60 |
| J | 2000 | 1999 | 65 |
| K | 1250 | 1999 | 65 |
| L | 850 (All-electric) | 2002 | 100 |
Figure 2SEC comparison of the model’s results, measured values, and the EcoInvent data.
Figure 3Comparison of modeled, measured, and EcoInvent data for the environmental impact assessment (ReCiPe).
Figure 4Comparison of modeled, measured, and EcoInvent data for the environmental impact assessment (kg equivalents of CO2).
Figure 5Induction cooktop—internal housing.
Case study data summary.
| Scenario | #1 | #2 | #3 | #4 |
|---|---|---|---|---|
| Polymer Material | Virgin PP | Recycled PP | Virgin PP | Recycled PP |
| Injection-Molding Machine | M | M | N | N |
| Fc (kN) | 8000 (with toggle clamp system) | 8000 (with toggle clamp system) | 5500 | 5500 |
| Manufacturing Date | 2015 | 2015 | 2015 | 2015 |
| E | 85 | 85 | 75 | 75 |
| Vmax (cm3) | 3240 | 3240 | 1500 | 1500 |
| Cycle time (s) | 51.41 | 60.81 | 38 | 39 |
| w (g) | 595 | 603.2 | 606 | 615 |
| ρ (g/cm3) | 1.23 | 1.25 | 1.23 | 1.25 |
| ce (KJ/kg. K) | 1.5 | 1.5 | 1.5 | 1.5 |
| Ti − Ta (K) | 228 | 228 | 228 | 228 |
| Measured SEC (kWh/kg) | 0.838 | 0.785 | 0.59 | 0.601 |
| Modeled SEC (kWh/kg) | 0.835 | 0.861 | 0.578 | 0.580 |
| Model Abs. Error | 0.4% | 9.7% | 2.0% | 3.5% |
| EcoInvent Abs. Error | 75.4% | 87.3% | 149.2% | 144.6% |
Scenarios Assessment: Environmental impact of processing a plastic part.
| Environmental Impact of Part Processing | #1 | #2 | #3 | #4 |
|---|---|---|---|---|
| mPt ReCiPe/Part | 24.41 | 23.24 | 17.80 | 18.38 |
| kg eq. CO2/Part | 0.266 | 0.253 | 0.194 | 0.200 |