Yannic
Brasse
a,
Mariano
Laguna Moreno
a,
Simon
Blum
a,
Tim
Horter
b,
Florian
Janek
b,
Kerstin
Gläser
b,
Carl
Emmerechts
c,
Jean-Michel
Clanet
d,
Michèle
Verhaert
d,
Benoît
Grymonprez
d and
Tobias
Kraus
*ae
aINM – Leibniz Institute for New Materials, Structure Formation Group, Campus D2 2, 66123 Saarbrücken, Germany. E-mail: tobias.kraus@leibniz-inm.de
bHahn-Schickard-Gesellschaft für angewandte Forschung, Allmandring 9b, 70569 Stuttgart, Germany
cSirris, Liège Science Park, Rue Bois Saint-Jean 12, 4102 Seraing, Belgium
dCTP Centre Terre et Pierre, Chau. d'Antoing 55, 7500 Tournai, Belgium
eSaarland University, Colloid and Interface Chemistry, Campus D2 2, 66123 Saarbrücken, Germany
First published on 16th May 2024
Recycling of Waste from Electrical and Electronic Equipment (WEEE) is crucial in preventing resource depletion and promoting a circular economy. The increasing fraction of printed and in-mold electronics is particularly challenging. The combinations of polymers and printed metals are difficult to disassemble due to the strong interfaces that are formed to create reliable in-mold devices. The relatively low metal content makes recycling uneconomical and those valuable materials are then lost to landfill or incineration. Separation layers enable design-for-recycling with minimal modifications during the fabrication process, while preserving product performance and reliability. We present a scalable method for preparing polymer separation layers for printed and in-mold electronics. Slot-die coating is used to prepare water-soluble polymer films with a dry thickness of less than 10 μm on commodity polymer substrates. This separation layer improves the bending stability of inkjet- and screen-printed circuits. Furthermore, it is compatible with typical polymer processing methods, such as thermoforming and injection molding. Various methods, including plasma treatment, are presented to ensure adhesion of the modified interfaces. Finally, we investigate the material recovery and demonstrate the release of the integrated metal within a few minutes by dissolving the separation layer in water. This material recovery process can be readily integrated into current WEEE recycling processes.
Sustainability spotlightPrecious metals and conventional polymers, based on non-renewable resources, are used in most electronic devices as conductive and insulating parts. Therefore, the management of Waste from Electrical and Electronic Equipment (WEEE) in the context of a circular economy is essential. Recycling of polymer-embedded (in-mold) electronics is currently inefficient due to the strong connection between metals and polymers. This makes their recovery uneconomical as recycling is not considered in the design of such products. Here, we introduce a design-for-recycling approach that enables a more efficient recovery of the components with existing recycling processes. We are targeting the action network ‘Green economy’ as part of the UN Sustainable Development Goal ‘Decent work and economic growth’ (SDG 8). The approach also addresses the goals ‘Industry, innovation and infrastructure (SDG 9) and ‘Responsible consumption and production’ (SDG 12). |
Approaches to improve the sustainability of printed electronics in literature focus on the recovery of valuable silver.13 A straightforward solution is to replace the substrate material with water-soluble alternatives such as polyvinyl alcohol (PVA).14 Although this allows for direct release of the silver, it is limited to specialized applications due to the mechanical properties of PVA and its susceptibility to water. Recent approaches utilized degradable materials such as polycaprolactone or polylactic acid for the recycling.15,16 Jaiswal et al. studied cellulose nanocomposites as compostable substrates for flexible electronics.17 Degradation in soil for 3 weeks was sufficient to separate their electronic components and recover them via sieving. These approaches have potential, but will not be immediately economically viable because biodegradation is hardly compatible with the current electronic waste treatment and will require changes to the WEEE directives.4,18
Today, material recovery from WEEE is typically achieved by a series of manual disassembly and presorting, comminution, automated sorting, and finally, hydro- or pyrometallurgical processing.19 Conventional, less integrated electronic waste with PCBs, solder and wiring can be largely separated by shredding and subsequent sorting using density, magnetic, or Eddy current separation.6,19 These methods are inefficient for the separation of integrated materials such as IME due to low metal fractions and their adhesion to the polymer matrix. This results in either loss of the metal or increased amount of polymer impurities in the metallic fraction. Solvent-based methods for depolymerizing or dissolving the matrix materials address this issue and typically yield higher purity materials compared to mechanical recycling.20,21 However, the economic viability of dissolution/precipitation processes is limited by the use of harmful solvents such as dichlormethane (DCM) and the energy consumption for solvent evaporation.22,23 Since this strongly depends on the purity of the waste streams, recent literature promotes the combination of solvent-based and mechanical methods.22,24,25 To facilitate the separation of IME, a straightforward recycling approach that is compatible with the established sorting processes is required.
Here, we report on a “recyclability by design” strategy that requires only limited adaptations in the IME production process and does not affect the performance of the product until the end of its life. We demonstrate the use of a water-soluble release layer to improve sustainability of printed and in-mold electronics. Our process utilizes polyvinyl alcohol (PVA) to coat PC foils that are subsequently printed with conductive silver, thermoformed, and overmolded with PC (see Fig. 1). After grinding, the PVA layer facilitates the separation of silver and polycarbonate by immersion in water and subsequent sieving. We discuss the impact of the separation layer on the material recovery, the processability of printed electronics and the impact on their electromechanical properties.
A polyvinyl alcohol (PVA) separation layer was prepared by slot-die coating on polycarbonate (PC) foils using aqueous solutions with a polymer mass fraction of 6%. PVA with 88% degree of hydrolysis was applied due to improved cold water solubility compared to fully hydrolyzed alternatives.26 The resulting layer had an area density of 3.2 ± 0.7 g m−2 corresponding to a film thickness of 2.5 ± 0.6 μm. For printing of conductive tracks onto PVA, screen printing (contact method) and inkjet printing (non-contact, drop-on-demand method) were utilized, as these are common techniques that complement each other regarding initial costs, production scale and printing precision.27
Screen printing offers a high layer thickness per transit in the range of few micrometers up to one hundred micrometers, depending on the applied mesh size and paste. It is suitable for medium quantities due to the initial costs of the mask. The viscosity of the paste is typically in the range of 5 × 102 to 103 mPa s.3 Here, two pastes with silver microparticles were applied (Dycotec DM SiP 2002 and Bectron CP 6680). Prints were dried at 130 °C for 30 min in an oven.
Inkjet printing is a digital process without the need for additional masks and is therefore suitable for low quantities, which makes it ideal for prototyping. At less than one micrometer per pass, the thickness of a dried inkjet-printed layer is significantly lower than that of screen-printed structures. The viscosity range for ink jetting is 5–50 mPa s.3 For inkjet printing of tracks on PC and on PVA-coated PC, a commercial ink containing silver nanoparticles was applied (PVNanocell Sicrys I30EG-1). After printing and drying, the ink was sintered at 150 °C for 60 minutes.
Inkjet- and screen-printed silver tracks on PC sheets are shown in Fig. 2a. The layout was designed to test the reliability of printed silver tracks using 4-wire-measurements to investigate the resistivity change of printed tracks, with and without underlying PVA, during bending tests. The test specimen had a dogbone-shape and a total length of 80 mm. Conductive tracks were printed on the 500 μm PC sheets with and without PVA layer.
Bending tests were conducted to investigate the influence of an additional separation layer on the reliability of printed electronics by examining the susceptibility of the layer system to crack under cyclic bending loads. The test rig consisted of an electric motor that drives a crankshaft, which causes deflection of a clamped test specimen against a bolt (see ESI 1†). The deflection was set to 24 mm. By adjusting the position of the bolt, it was possible to adjust the strain on the conductive track. Three different positions were chosen for variation of strain on the test specimen, named as inner position, middle position and outer position as indicated in Fig. 2b. The resulting strains generated during the bending test were determined using finite element method (FEM) simulation. The bending conditions are within the typical fracture limits of 1–2% for metal coatings28 and were chosen because they resulted in failure of the printed conductive tracks within a reasonable number of bending cycles. Strains, rather than stresses, were determined due to limited availability of material data for the used silver inks, namely Young's modulus.
A total of eight conductive tracks were tested for each material combination. The resistivity was measured during the cyclic bending load tests. It should be noted that inkjet- and screen-printed conductive tracks showed different initial resistance values. In ESI 1,† exemplary resistance measurements are shown over bending cycles for screen-printed conductors with Dycotec DM SiP 2002 at 1.93% strain. A rapid increase in resistance was observed at the beginning, which transitions into a constant rise for both layer systems, namely with and without underlying PVA layer. The curves' behavior suggests creep processes in the printed conductive tracks during the bending test. Without underlying PVA, a spike of increasing resistance was measured starting around 6 × 104 cycles. This was interpreted as breakage of the conductive track. In comparison, the track with underlying PVA (blue curve) did not show a sharp rise of resistance. It can be concluded that the PVA layer reduces the stresses in the conductive tracks induced by bending, effectively serving as a compensation layer.28
A statistical analysis of failures using Weibull distributions was conducted using the statistical software Minitab® (see ESI 2†). The failure criterion was a 20% increase in resistance from the initial value.29 From the Weibull distributions, the characteristic lifetime was determined, known as Mean Time To Failure (MTTF), which describes the number of cycles until 63.2% of all components have failed. Fig. 2c displays the MTTF-values in dependence of applied strain at the outer position (1.93%), middle position (1.66%), and inner position (1.46%) for the screen-printing paste Dycotec DM SIP 2002, the screen-printing paste Bectron CP 6880, and the inkjet printing ink Sicrys I30-EG1. Two observations can be made from the plots. (i) The reliability of the printed samples decreases with increasing strain. (ii) An underlying PVA-layer leads to an increase of the number of bending cycles until failure. This effect is most pronounced for the screen-printed sample based on the Bectron paste.
To summarize the impact of PVA layers on the mechanical and electrical properties of printed electronics, there is an improvement in the durability of conductive tracks against mechanical stress. This effect is most prominent for screen-printed samples and is likely dependent on the type of solvent used with the ink/paste.
Printed silver tracks on PVA were overcoated by another PVA layer and subsequently overmolded with 2.5 mm PC. While the samples without PVA layer showed excellent adhesion between the PC foil and the overmold, the PVA-coated samples could be peeled easily. To quantify the adhesion force between PC and PVA, a pull-off test was performed. An adhesive failure between PC and PVA was observed and a tensile strength of 156 ± 15 N cm−2 was determined. Two approaches were tested to improve the adhesion between two polymers: (i) treatment of PC with oxygen plasma and (ii) application of an adhesion-promoting (primer) layer before PVA coating. The first method aims at increasing the hydrophilicity of the PC surface by creating polar species such as hydroxyl, carbonyl and carboxyl groups on the surface, which leads to attractive interactions with the OH-groups of PVA.30,31 The second method utilizes a primer that exhibits strong interactions with both PC and PVA. Here, we used slot-die coated polyvinyl acetate (PVAc) which shows excellent adhesion to PC. Since PVAc is the chemical intermediate in the synthesis of PVA, the same saponification reaction of the acetate group by sodium hydroxide can be used to generate OH-groups on the surface of the primer layer (see Fig. 3a).32 Both methods resulted in an increase of the adhesion that could not be quantified using the pull-off test (see Experimental section for details). Therefore, measurements were performed similar to a standard T-peel test33 as shown in Fig. 3b. To receive symmetrical samples for this test, two PVA-coated sheets were laminated and then peeled. The peel force was measured for PVA on untreated PC, plasma treated PC and PC with saponified PVAc (see Fig. 3c and ESI 5† for detailed setups). By plasma treatment, there is a 51% increase of the peel force whereby the failure is still adhesive between PC and PVA. This situation changes for PC samples with saponified PVAc, where both cohesive failure (rupture of the PVA layer) and adhesive failure between PVA and PVAc could be observed. This is accompanied by a 97% increase of the peel force. The control with the PVAc only (without PVA) revealed that PVAc could not be laminated at 180 °C.
An alternative approach to increasing the adhesion is to reduce the PVA-coated area, which can be achieved by using different slot-die printheads or a different printing technique. This method reduces the use of material significantly and results in the largest possible interfacial area between the PC foil and PC mold, making the influence of the PVA layer on adhesion negligible. Below and above the 30 × 10 mm2 silver tracks, a limited PVA area of 50 × 30 mm2 was applied, which ensures a direct contact between PC foil and 75 × 60 mm2 PC overmold, thus providing good adhesion and protection from humidity. In addition to rectangular coatings under the meander structure, application of PVA patterns by screen and inkjet printing was tested. For inkjet printing, a mixture of dimethyl sulfoxide (DMSO) and water was used to prepare inks, because the high surface tension of pure water prevents droplet formation and its high vapor pressure resulted in clogging of the nozzle. Formulations with a final viscosity of 12–14 mPa s were received using PVA with two different chain lengths (Mw ≈ 31000 g mol−1 and Mw ≈ 130000 g mol−1).
The inkjet printing process was strongly influenced by the PVA chain length since only short chain length PVA was printable with the comparable small nozzle sizes of the Samba printhead. For high chain lengths, a rapid clogging of nozzles limited the printability. The wetting behavior on polycarbonate was ideal, therefore no pre-treatment was performed. For screen printing, an optimal viscosity of 2–5 Pa s was obtained using an aqueous solution with the high molecular weight PVA at mass fractions of 13–15%. The printing resulted in pronounced dewetting on PC and formation of bubbles in the PVA layer (see ESI 6†) due to air entrapment during the filling stroke (flooding of the mesh) and lifting of the mesh from the printed paste. To prevent these effects, PC was treated with atmospheric plasma and the surfactant 2,4,7,9-tetramethyl-5-decyne-4,7-diol ethoxylate (TMDD-E) was added to the formulation (10 mmol kg−1). TMDD-E is a non-ionic surfactant that acts both as wetting agent and defoamer by displacing PVA from the air–water interface, which facilitates drainage and bubble coalescence. The resulting prints showed neither bubbles nor dewetting after printing and had an average height of 6 ± 2 μm (see Fig. 4b and c). Subsequently, silver tracks were printed on such PVA layers by screen printing and a second PVA layer was deposited on these tracks. The properties and processibility of these prints regarding thermoforming and injection molding did not differ significantly from silver prints without PVA. The increased contact area between the PC foil and the overmold improves mechanical stability through cohesion and protects the separation layer from humidity, preventing limitations in products that use the separation layer.
The separation of the printed silver layer was tested using the wide silver tracks and meander structures before thermoforming/overmolding. Both samples showed separation of the silver layer within 10 min after immersion in water (see Fig. 5a and ESI 7†). This is caused by the high solubility of PVA, its comparably large surface area and low film thickness. The situation changes for overmolded structures where the available surface area for dissolution is limited by the layer thickness and the perimeter of the sample. Overmolded samples with a fully coated PVA layer were kept pendant in water at various temperatures from ambient to 80 °C for 60 minutes. Separation of foil and overmold was not observed for these tests. Therefore, the dissolution of such confined PVA layers was studied in more detail. Laminated PC/PVA/PC samples were cut into squares of either 6 mm or 12 mm side lengths. The polymer release into the aqueous phase under slow stirring was determined using a photometric assay.34 The results are summarized in Fig. 5b. For larger pieces, the released amount of PVA is 2.4 ± 0.5% whereas for smaller pieces the release is about 9.1 ± 0.3% within 8 hours. An increase is expected as the mass transfer rate is proportional to the available area, which grows linearly with decreasing size of the polymer chunks. We attribute the deviation from a proportional behavior to differences in the mixing due to greater movement of the small pieces. This influences the PVA concentration gradient and thus the rate of dissolution. The findings on the dissolution speed of confined PVA suggest that a size reduction of the overmolded samples (initial size of 75 × 60 mm2) is required for industrial recycling.
Three different types of overmolded samples (see Table 1) were analyzed for silver recovery using industrial methods: (a) Wide tracks (30 × 10 mm2 silver) with a 50 × 30 mm2 PVA layer below and above silver, (b) Wide tracks without PVA layer, and (c) meander structures with PVA deposited below and above silver by screen printing. A comminution step was required to make the separation layer accessible to water. Knife milling was tested for size reduction but resulted in clogging of the mill. Thus, samples were comminuted with a shredder, which is typically used for recycling of materials such as plastics and wires.35 Shear forces between rotating drums equipped with knifes lead to fragmentation of the samples. A 10 mm calibration grid was used to adjust the size of the milled particles. Beyond size reduction, delamination effects were noticed on the structures. The PC foil and overmold were separated through friction induced by the mills. This delamination was particularly noticeable for sample type (a), which is due to the lowered adhesion in the PVA-coated area.
The dissolution of PVA and the release of silver was tested by immersing shredded samples in water with an agitator at ambient temperature (20 °C) and in hot water (90 °C). In both cases, water dissolved the PVA separation layer on sample type (a) and the ink was released from the PC components within minutes (see Fig. 6). The temperature had a direct effect on the kinetics of the separation. At ambient temperature, the ink separation was achieved in 30 minutes whereas the process was completed in only 5 minutes at 90 °C. The fragments from sample (b) did not undergo further separation of silver and PC due to absence of the release layer. For sample (c) only the delaminated PC pieces were affected by dissolution of PVA, and thus, silver was partially released (see ESI 7†). We conclude that (i) the PVA layer is necessary for proper separation of printed silver and (ii) the layer is required to be in the same size range as the fragmented polymer to ensure delamination of polymer foil and overmold. The delamination occurs either during shredding or by dissolution of the PVA layer under agitation, and is required for the silver release.
The dispersed PC fragments and ink particles from sample (a) were segregated by using a dense medium. Namely, a ZnCl2 solution was adjusted to a specific gravity of 1.3 to make the PC pieces float at the surface (specific gravity of 1.2), whereas the silver ink sedimented. The pieces with ink remaining on the PC, as in samples (b) and (c), also floated because the amount of ink was not sufficient to result in a specific gravity greater than 1.3 (see ESI 8†). A more scalable industrial process for the segregation of PC and ink particles is sieving. Most of the ink particles were recovered as fine particles (<3 mm), while the PC particles were recovered on a 5 mm screen. Some larger ink particles remained with PC particles in the 3–5 mm fraction. An additional breakage step was performed by agitation in an attrition cell to reduce the size of these large ink particles. The dispersion was subjected to high rotation speed for 1 minute and sieved again. Thereafter, the ink particles passed through the 3 mm aperture while the PC particles remained unchanged and were recovered in the oversized fraction (see ESI 8†). Chemical analysis of both fractions revealed that 93.8% of the silver was recovered in the <3 mm fraction, while the residual amount of silver remained in the oversized fraction with the polymer.
Fig. 7 Proposition of a recycling process for Waste from Electrical and Electronic Equipment (WEEE). In the current process, a mixed fraction containing polymers and metallic residues (such as in-mold electronics) is incinerated or disposed because their separation is too energy-intensive. Our process complements the waste treatment to increase recovery of metals and recyclable polymers. Color coding: blue (processing steps), green (recovered materials), yellow (material losses). This figure is based on information from ref. 6 and 19. |
For inkjet printing, a solution of PVA with a mass fraction of 3% was prepared in a 9:1 DMSO/water mixture. 180 mL DMSO were added to 20 mL water in a Schott bottle. 90 g of this mixture were added to 10 g of Mowiol 4-88 and stirred for 3 days until a homogeneous stock solution (10%) was yielded. The stock solution was partially diluted to PVA mass fractions of 1–9% with the DMSO/water mixture for viscosity measurements.
For screen printing, solutions of PVA with a mass fraction of 15% were prepared in water. 37.5 g Mowiol 18-88 were added to a Schott bottle containing 212.5 g water at 85% under vigorous stirring. The addition was made stepwise over two hours to avoid aggregation. The mixture was allowed to cool down to room temperature overnight under stirring, yielding a highly viscous solution. It was partially diluted to mass fractions of 1–15% with water for viscosity measurements. 1 g of a 1 mol L−1 solution of 2,4,7,9-tetramethyl-5-decyne-4,7-diol ethoxylate (TMDD-E) was added to the 100 g of the PVA solution and mixed with a speed mixer at 2800 rpm, yielding a 15% Mowiol 18-88 solution with 10 mmol kg−1 TMDD-E.
For preparation of a primer layer, 40 g PVAc were dissolved in 160 g of an ethanol/water mixture (94% mass fraction of ethanol) by stirring for 72 h. The solution was diluted to a PVAc mass fraction of 17%. Slot-die coating was done on 10 × 5 cm2 PC foils using a coating width of 30 mm at a speed of 0.2 m min−1 and a pump rate of 0.6 mL min−1, resulting in a theoretical wet film thickness of 100 μm. The theoretical layer thickness is 14.4 μm after drying of PVAc (density of 1.18 g cm−3).
Plasma-treated, PVAc-coated, and untreated PC foils were slot-die coated with 6% PVA using a coating width of 30 mm at a speed of 0.2 m min−1 and a pump rate of 0.6 mL min−1, resulting in a theoretical wet film thickness of 100 μm. The theoretical layer thickness is 4.7 μm after drying of 6% PVA (density of 1.27 g cm−3).
Lamination of samples (two of each type, receiving a PC/PVA/PC sandwich) was conducted with the universal testing machine Zwick (ZwickRoell) equipped with an oven and ceramic heaters. The oven was pre-heated to 100 °C overnight and the heaters were set to 180 °C. Lamination was achieved by pressing the samples between two 10 × 10 cm2 ceramic heaters. The process comprised a 30 s settling phase at 5 N cm−2, a 15 s unloading phase at 1 N cm−2 and a 300 s loading phase at 100 N cm−1.
These samples were measured with a T-peel test similar to ISO 11339:2022. Samples were cut into 2.5 cm wide strips with a laminated length of 7 cm with 5 cm peel arms. The initial separation of the clamps was 50 mm and the separation rate was set to 100 mm min−1. The peel force was averaged over 50 mm of the laminated length (disregarding the first 10 mm and last 10 mm). The average values were 5.6 ± 0.1 N m−1 for untreated samples, 8.4 ± 1.0 N m−1 for plasma treated samples, and 11.1 ± 1.0 N m−1 for samples with hydrolyzed PVAc layer. Three measurements were performed for each sample type.
PVA based inks were printed on PC Lexan 8B35 foil using the same printer and printhead with a drop spacing of 15 μm. For high Mw PVA, a rapid clogging of nozzles limited the printability. Only low Mw PVA was printable with the comparable small nozzle sizes of the Samba printhead. The printhead temperature as well as the substrate temperature were set to 43 °C. The wetting behavior on PC was ideal, therefore no pre-treatment was performed. An influence of surfactant was not noticeable.
PET screen mesh with 110 wires per cm (34 μm wire diameter, 54 μm aperture), 22.5° tension orientation; 20 cm squeegee; printing angle 75°; 4 bar pressure; 100 mm s−1 velocity; 3 mm snap-off distance. Prints were cured at 130 °C for 30 min.
PVA was printed using high Mw PVA at mass fractions of 13–15%, having an optimal viscosity of 2–5 Pa s. Formulations were degassed for several hours at 2 mbar. PC Lexan 8B35 foils were cleaned with isopropanol and treated with atmospheric plasma before printing. Printing was conducted with settings as mentioned above but 3 layers were deposited with 30 s drying at ambient temperature between prints. PVA layers of 5 μm thickness were received without bubble formation using formulations with 15% PVA and 10 mmol kg−1 TMDD-E.
Overmolding of PC was performed on an injection molding press, an Allrounder 420C-1000-350 (Arburg, Germany) with a clamping force of 100 tons. The overmolded PC is Makrolon 2805 (Covestro). The melt temperature is 290 °C and the mold temperature 115 °C. The thermoformed sheets are put on the core side and held by vacuum. After closing of the mold, an idle time is set 40 seconds before molding. This allows the sheet to reach the temperature of the mold and to improve the welding of the overmolded PC on the PC sheets. The total cycle time was 1 minute.
(a) Wide ink track with PVA layer: PC sheet Lexan 8B35 125 μm (100 × 80 mm2) coated on the smooth side with 3 layers in a sandwich structure (50 × 30 mm2) slot-die coated PVA 6 wt%, screen-printed silver 30 × 10 mm2 (Elantas Bectron CP 6680), (50 × 30 mm2 slot-die coated PVA 6%), overmolded with polycarbonate Makrolon 2805 (75 × 60 mm2).
(b) Wide ink track without PVA layer: PC sheet Lexan 8B35 125 μm without PVA coating, screen-printed silver 30 × 10 mm2 (Elantas Bectron CP 6680), overmolded with polycarbonate (Makrolon 2805).
(c) Meander structure with printed PVA layer: PC sheet Lexan 8B35 125 μm (100 × 80 mm2) coated on the smooth side with 3 layers in a track sandwich structure (screen-printed PVA 15% with TMDD-E, screen-printed silver meanders (Elantas Bectron CP 6680), screen-printed PVA 15% with TMDD-E) overmolded with polycarbonate Makrolon 2805 (75 × 60 mm2).
(d) Wide ink track with fully coated PVA layer: PC sheet Lexan 8B35 125 μm (100 × 80 mm2) coated on the smooth side with 3 layers in a sandwich structure (full area slot-die coated PVA 6%, screen-printed silver 30 × 10 mm2 (Elantas Bectron CP 6680), full area slot-die coated PVA 6%), overmolded with polycarbonate Makrolon 2805 (75 × 60 mm2).
Footnote |
† Electronic supplementary information (ESI) available. See DOI: https://doi.org/10.1039/d4su00092g |
This journal is © The Royal Society of Chemistry 2024 |