A Review on Extrusion Additive Manufacturing of Pure Copper
Abstract
:1. Introduction
2. Feedstocks for Extrusion AM of Pure Copper
2.1. Feedstocks Used in PFSP
2.2. Feedstocks Used in FFRP
2.3. Feedstocks Used in DIWP
3. Manufacturing of Pure Cu Parts
3.1. 3D Printing Processes
3.1.1. PFSP Process
3.1.2. FFRP Process
3.1.3. DIWP Process
3.2. De-Binding and Sintering
3.2.1. For Parts Printed by PFSP
3.2.2. For Parts Printed by FFRP
3.2.3. For Parts Printed by DIWP
4. Performance Characterization of Pure Copper Parts
4.1. Electrical Properties
4.2. Mechanical Properties
4.2.1. Tensile Strength
4.2.2. Density
4.2.3. Surface Roughness
4.2.4. Mechanical Hardness
4.2.5. Flexural Strength
4.2.6. Microstructural Analysis
5. Challenges and Future Prospects Associated with Extrusion AM
6. Conclusions
- The printing processes are classified into three categories: PFSP, FFRP and DIWP, based on the feedstock materials and their feeding mechanisms.
- The binder systems used with copper consist of one polymeric binder component that facilitates the extrusion process and a backbone binder that helps maintain the 3D shape during sintering.
- Depending on the category of the technique, binders may include PEG, TPE, wax, polyolefin, PW–LDPE–SA, or PVA.
- The ranges of the commonly used printing parameters included the following: printing speed: 2–100 mm/s; layer thickness: 0.05–2 mm; bed temperature: 60–90 °C; extrusion temperature: 180–240 °C.
- While PFSP and FFRP required a solvent de-binding step, in DIWP, solvent evaporation at ambient temperature was the only step required to remove the polymeric binder component.
- While most researchers applied a maximum sintering temperature of 1000–1050 °C, only one study used a temperature of 1083 °C.
- The relative density of the final sintered part varied from 89.5% to 95.4% of that of pure copper. Electrical conductivity varied from 51.7% of the IACS to 86.1% of the IACS
- The tensile strength, hardness and surface roughness ranged from 141 MPa to 205 MPa, 54.8 HV to 63 HV, and 2.4 µm to 3.3 µm, respectively.
- Shrinkage was identified as the major challenge for this technology, which was reported to be from 13.1% to as high as 23%.
- However, the studies did not perform any form of fatigue testing on the sintered parts.
- Surface treatment can improve surface roughness and eliminate defects. In addition, CT scans can be used to identify and analyze internal voids and defects.
- The electrical conductivity, tensile strength, and relative density of the parts produced by the DIWP method were found to be lower than those of the parts produced by the other two methods. PFSP and FFRP are preferred when parts with higher electrical conductivity and tensile strength are required.
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
References
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Printing Method | Printing Parameters | Binder System | Solvent De-Binding | Thermal De-Binding | Sintering | Properties of Final Parts | Ref. |
---|---|---|---|---|---|---|---|
PFSP | PS: 20–100 mm/s LT: 0.05–0.25 mm BT: 60 °C ET: 180–220 °C EM: 90–150% | PEG and wax | Placed under water for 14 h, then dried in oven for 2 h at 100 °C | Heated to 500 °C at 1 °C/min and held for 1 h | Heated to 950 °C at 4 °C/min and held for 3 h; heated to 1030 °C at 4 °C/min, held for 3 h, and cooled at 6 °C/min | RD: 90.8% SR: 2.42 ± 0.92 μm | [22] |
PS: 20 mm/s LT: 0.05 mm BT: 60 °C ET: 196 °C EM: 120% | Placed under water for 12 h with stirring at 40 °C and 60 °C, then dried in over at 100 °C for 2 h | Heated to 500 °C at 1 °C/min and held for 1 h, then cooled to RT at 4 °C/min | Heated to 950 °C–1050 °C at 4 °C/min with 96% He and 4% H2 and held for 3 h, then cooled to RT at 4 °C/min | RD: 94.5% SR: ~2.9 μm | [37] | ||
FFRP | LT: 0.129 mm | Thermoplastic polymer and wax | Washed in proprietary solvent Opteon SF-79 | Placed in proprietary furnace filled with H2 and Ar | Parameters set per manufacturer’s specifications | RD: 94.51 ± 0.4% SR: 3.3 ± 0.02 μm EC: 86.11 ± 6.92% of IACS TS: 205.87 ± 0.07 MPa | [9] |
LT: 0.129 mm ET: 220 °C | Paraffin wax and high-molecular-weight (HMW) polymer | Immersed in OpteonSF-79 solvent to remove the paraffin wax using the washing equipment for 10 h | 30 h long thermal cycle in presence of 2.8% H2 and 97.8% Ar | RD: 95.3 ± 0.5% EC: 48 ± 1 × 106 S/m (82% of IACS) TS: 205.8 ± 5.0 MPa SH: 54.8 ± 2.1 HV | [5] | ||
PS: 30 mm/s LT: 0.3 mm BT: 90 °C ET: 240 °C EM: 120% ND: 0.6 mm | TPE and grafted polyolefin | Submerged in cyclohexane at 60 °C for a fixed period of time, and dried at room temperature in a fume hood for at least 4 h | Heated up to 450 °C for about 8 h in H2 atmosphere at 2 K/min with 1 h holding at 250 and 450 °C | Heated up to 1050 °C in H2 atmosphere. Heating rate: 2 K/min; 1 h de-binding plateau at 1050 °C | Flexural strength and modulus increased with increase in mass | [47] | |
DIWP | 1 gm of acrylic dissolved in 10 mL of acetone | Evaporation | Heating and cooling cycle at 5 °C/min in presence of flowing forming gas (95% N2 and 5% H2). Held for 2 h at peak temperatures. Highest temp.: 1000 °C. | RD: 89.28% EC: 30 × 106 S/m (51.7% of IACS) TS: 141 ± 19 MPa. | [48] | ||
LT: 0.35, 0.45, 0.55, 0.65, 0.75 mm | Paraffin wax | Heated up to 750 °C, 800 °C, 850 °C, 900 °C, 950 °C, 1000 °C and 1050 °C at 10 °C/min. Holding time for 30 min (best temperature at 950 °C with holding time of 120 min) | RD: 90.4% SH: 60 HV | [49] | |||
PS: 2–10 mm/s LT: 0.4 mm Tip Size: 0.5 mm Fill density: 50–90% Screw Extruder RPM: 45 RPM | Polyvinyl carboxy polymer and PVA | Dried in air at room temperature. Later, heat treatment conducted in a box furnace with charcoal at 950 °C for 2 h | With the increase in Cu content, viscosity increased but volumetric flow rate decreased | [51] | |||
PS: 6 mm/s LT: 2 mm ET: 160 °C Piston Speed: 0.047 mm/s | Paraffin wax, polyethylene, and stearic acid | No solvent de-binding | Heated up to 500 °C in a vacuum atmosphere furnace at 2 °C/min with holding period of 150 min | Heated up to 1083 °C; heating rate: 3 °C/min, holding time: 3 h (optimal combination from nine samples) | RD: 90.95% EC: 0.114940 Ω mm2/m TS: 175 MPa SH: 63 HV Decrease of viscosity with the increase of shear rate | [50] |
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Sakib-Uz-Zaman, C.; Khondoker, M.A.H. A Review on Extrusion Additive Manufacturing of Pure Copper. Metals 2023, 13, 859. https://doi.org/10.3390/met13050859
Sakib-Uz-Zaman C, Khondoker MAH. A Review on Extrusion Additive Manufacturing of Pure Copper. Metals. 2023; 13(5):859. https://doi.org/10.3390/met13050859
Chicago/Turabian StyleSakib-Uz-Zaman, Chowdhury, and Mohammad Abu Hasan Khondoker. 2023. "A Review on Extrusion Additive Manufacturing of Pure Copper" Metals 13, no. 5: 859. https://doi.org/10.3390/met13050859
APA StyleSakib-Uz-Zaman, C., & Khondoker, M. A. H. (2023). A Review on Extrusion Additive Manufacturing of Pure Copper. Metals, 13(5), 859. https://doi.org/10.3390/met13050859