Dongchul Choi,
Wan Soo Yun and
Yongkeun Son*
Department of Chemistry and BK21 PLUS School of HRD Centre for Creative Convergence Chemical Science, Sungkyunkwan University, Suwon 440-746, Korea. E-mail: ykson@skku.edu
First published on 19th August 2016
A simple co-precipitation method was used to recover ITO as a nanopowder from the waste ITO target residue in sputtering chambers. The waste ITO target was dissolved in HCl and then ammonia solution was added to make indium tin hydroxide (ITO precursor). After heat treatment up to 400 °C for 6 h, the colour of the ITO precursor changed from white to yellow. The prepared ITO nanopowder was homogeneous with a size of 10 nm and a polycrystalline structure. Over 95 wt% of ITO was recovered using this method. The In/Sn weight ratio was estimated to be 10
:
1, which is very close to commercial ITO. We tried to scale-up the preparation procedure by 20 times to reduce the amount of acid for a more environmentally friendly approach. The particle size was about three times larger than that obtained from the small scale and the In/Sn ratio was slightly different. However, they were still close to commercial ITO.
000 tons while the current annual consumption is about 1400 tons.1 Due to expected indium resource depletion and a subsequent rapid rise in price, several countries have monopolized indium business to control the price. The price of indium has been increasing rapidly. According to the Metal Bulletin, indium price increased by 41.4% from $495/kg in Dec. 2012 to $700/kg in Dec. 2014.2 Therefore, many countries that consume this material without a local supply have difficulties in the production of TCE. Nowadays, the study of TCE without indium has become a hot issue with materials such as graphene,3,4 metal nanowire,5 conducting polymer6 and zinc oxide.7 However, these materials cannot fully replace ITO yet. This is not only because the manufacturing process for TCE is difficult and the cost is high, but also because electrical conductivity and optical transparency problems can occur. ITO can only be used as a basic TCE material until the next decade. Indium is also used in the solar industry. Murphy et al.8 and Chung et al.9 reported that the Copper Indium Gallium Selenide (CIGS) solar industry is expected to increase rapidly and therefore the consumption of indium will increase. Consequently, the global indium resource is being exhausted owing to flat panel display (FPD) and CIGS solar industry growth. One way to avoid the supply difficulty is the recovery or recycling of secondary indium production i.e. discarded liquid crystal display (LCD),10–12 CIGS solar cell13 and waste sputtering target.14–18 Among these, waste sputtering targets are very important because the amount of discarded indium resources is much higher than in other secondary indium productions. ITO targets are usually used for the ITO coated onto glass substrates with the magnetron sputtering method. However, in this process, less than 30% of the ITO target is used and 70% remains in the chamber in the form of sludge.19 For these reasons, many research groups have performed studies on the recovery and recycling of indium (or ITO) from secondary indium production. Several recovery methods have been reported such as solvent extraction,13,14,20–23 spray pyrolysis,16 vacuum metallurgy separation.24,25 Among these, the solvent extraction method using HCl is widely used for the recovery of indium because the HCl shows effective leaching properties of the ITO.14,20,22,23 However, recently most studies of recovery or recycling are solvent extraction and only focused on the recovery of indium itself. Studies related to the recovery of ITO nanopowder from secondary indium production hardly exist. Obviously, the recovery of indium is very important. However, the main demand for indium in related industries is in the form of ITO.26 Therefore, we concluded that the direct preparation of ITO without separating the indium and tin from ITO target waste is economically efficient for the industrial field by reducing the number of steps involved.
Recently, Cha et al.18 reported preparation of ITO ink from waste ITO scrap. However, the formation mechanism of ITO nano powder and scaled up for application to the industrial field were not discussed. In this study, we focused our attention on the recovery of reusable ITO nanopowder from waste ITO targets by using the co-precipitation method and investigation of characteristics such as thermal behavior, crystal structure, particle size, composition, chemical state, and In/Sn ratio for the as-prepared ITO nanopowder. Furthermore, we studied the feasibility of mass production and a more environmentally friendly approach.
| In3+ + Sn4+ → In(OH)3 + Sn(OH)4 | (1) |
| In(OH)3 + Sn(OH)4 → (In1–xSnx)OOH + H2O | (2) |
| (In1–xSnx)OOH → In2Sn1–xO5–y + H2O | (3) |
The thermal behaviour of the as-prepared ITO precursor including chemical decomposition and phase transition was confirmed by using TGA/DTA. As shown in Fig. 1, TG analysis showed three weight loss stages in the temperature range of 23–1000 °C. In the first stage, weight loss of 9.2% was observed in the range of 23–170 °C corresponding to the evaporation of physically adsorbed water and solvent.29 Therefore, a small and broad endothermic DTA peak was also observed. Greater weight loss of 10.4% between 170 and 252 °C was observed in the second stage, during which the DTA curve showed an endothermic reaction. These results indicate that phase transition from the mixture of In(OH)3 and Sn(OH)4 to In1–xSnxOOH (InSnOOH) (eqn (2)). InSnOOH was formed as an intermediate phase from low heat treatment (<252 °C). For the last stage, weight loss of 1.8% occurred between 252 to 350 °C, which indicates phase transition from InSnOOH to ITO (eqn (3)).30 The DTA curve showed an exothermic peak for the same temperature range due to the formation of crystallized metal oxide at 350 °C.30–33 Therefore, crystallized In2Sn1–xO5–y (ITO) was obtained at higher temperatures (>350 °C). Based on this thermal analysis, the ITO precursor was thermally treated with 400 °C to obtain well crystallized ITO.
Fig. 2 shows the X-ray diffraction patterns of the waste ITO target powder and the white precipitate before and after heat treatment at 400 °C. Before heat treatment (ITO precursor) appeared amorphous with a little crystalline phase in Fig. 2(a). The heat treatment caused a structural transformation as shown in Fig. 2(b). The peaks with 2θ values of 30.4°, 35.5°, 50.9°, and 60.7° were associated with the crystal planes of (222), (400), (440) and (622), respectively, for ITO.34,35 These planes matched the cubic bixbyite structure of In2O3 (JCPDS no. 06-0416).
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| Fig. 2 Comparison of XRD patterns before heat treatment (a), after heat treatment (b) at 400 °C and waste ITO target powder (c). | ||
The sharp and strong diffraction peaks such as the (222) plane showed that the ITO was well crystallized. This pattern was compared to that obtained from a waste ITO target as in Fig. 2(c). The two patterns had similar structures. The crystallite sizes of the sample after heat treatment and the waste ITO target powder were estimated with the Debye–Scherrer equation:36
![]() | (4) |
XPS spectra before (top) and after (middle) heat treatment are compared with that of waste ITO target powder (bottom) in Fig. 3. Table 1 summarizes the binding energies (BE) in Fig. 3. As shown in Fig. 3(a), there are two peaks located at 444.4 eV and 451.9 eV for each sample, corresponding to spin–orbit splitting of the In 3d5/2 and In 3d3/2 states, respectively. These correspond to the In3+ bonding state, specifically In2O3. Furthermore, the Sn BE for each sample is shown in Fig. 3(b). The Sn 3d5/2 and Sn 3d3/2 peaks are located at ∼486.5 eV and 494.9 eV, respectively. These values are attributed to the Sn4+ bonding state from SnO2. The In 3d and Sn 3d BEs from the as prepared ITO nanopowder were in excellent agreement with the waste ITO target (Table 1). Fig. 3(c) shows the O 1s XPS spectrum. The spectrum was deconvoluted to three Gaussian–Lorentzian peaks. The original sample showed three component peaks based on OI at 529.0 eV, OII at 531.0 eV, and OIII at 533.3 eV. This demonstrated that the small OI peak was primarily on the outer surface of the ITO precursor.39 The maximum intensity OII peak at 531.0 eV was attributed to the oxygen in metal hydroxide (metal = In, Sn).40 The highest BE of the 533.3 eV peak from OIII may be due to adsorbed water molecules.39,40 On the other hand, OII after heat treatment and in the ITO target powder were not easily assigned as shown in Fig. 3(d). The BE of oxygen in metal hydroxide was overlapped despite the hydroxide to oxide phase transition caused by thermal dehydration. According to the ITO ionic structure (see Fig. 3(e)), the O2− lattice ion was located in two different regions, which were full complements of the six nearest-neighbour O2− ions (OI2−) and oxygen deficient regions (OII2−).41 The BEs after heat treatment were 529.9 and 531.6 eV while those for the waste ITO target powder were 529.9 and 531.5 eV. BEs from the sample after heat treatment were approximately equal to those of the waste ITO target powder. However, the OII peak from the sample after heat treatment showed lower intensity then the OII peak of the waste ITO target because the number of oxygen vacancies differed with the heat treatment temperature. From this result, we can conclude that the number of oxygen vacancies in different samples differed from each other. The lower BE of 529.9 eV indicated a full complement of six nearest-neighbour O2− ions (OI) and the higher BE of 531.5 and 531.6 eV indicated oxygen deficient regions (OII). According to XPS analysis, the chemical states of the as-prepared ITO nanopowder did not change compared with a typical ITO.
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| Fig. 3 XPS spectra of the samples before heat treatment and after heat treatment at 400 °C alongside waste ITO target powder; (a) indium 3d, (b) Tin 3d, (c) oxygen 1s before heat treatment (d) oxygen 1s after heat treatment and (e) schematic diagram of ITO ionic structure.41,42 | ||
| Sample | In (3d5/2) (eV) | Sn (3d5/2) (eV) | O (1s) (eV) |
|---|---|---|---|
| Before heat treatment | 444.4 | 486.4 | 529.0 |
| 531.0 | |||
| 533.3 | |||
| After heat treatment | 444.4 | 486.5 | 529.9 |
| 531.6 | |||
| 533.0 | |||
| Waste ITO target | 444.4 | 486.5 | 529.9 |
| 531.5 | |||
| 533.2 |
The shape and composition of the as-prepared ITO nanopowder were characterized by using FESEM, HRTEM, SAED and EDS. Fig. 4(a), the waste ITO target powder shows irregular shapes in micro size. On the other hands, as-prepared ITO powder showes an aggregated form of the homogeneous spheres of and nano scale as shown in Fig. 4(b). According to EDS analysis in the Fig. 4(c), the prepared ITO consists of O, In, and Sn. The weight ratio of In and Sn was estimated to be 11.5
:
1, which is in good agreement with the original ITO target. The HRTEM image in Fig. 4(d) shows that the interplanar d spacing of the prepared ITO nano particle was about 2.85 Å, which corresponds to the (222) lattice plane of In2O3. Fig. 4(d) inset, the SAED pattern of the as-prepared ITO nanopowder shows the polycrystalline diffraction rings indexed to the (222), (400), (440) and (622) planes indicating the polycrystalline structure of the ITO. This results show good agreement with the XRD pattern.
The average particle sizes and distribution were determined by measuring 200 particles in random regions as shown in Fig. 4(e). The average size of the ITO nano particles was 10.3 ± 2.1 nm. Fig. 4(f) shows the nitrogen adsorption–desorption isotherms curve at 77 K for ITO nanopowder and a surface area of 87.69 m2 g−1 was obtained. The BET curve shows a typical type II isotherm, which indicated a non-porous material.43 BET analysis can also be used to approximate the particle size by using following equation.44
![]() | (5) |
The weight percentages of the In and Sn compositions were determined for each sample by ICP analysis and are summarized in Table 2. The composition of In and Sn in the as-prepared ITO nanopowder were about 72.6 wt% and 7.4 wt%, respectively. The In and Sn weight ratio were estimated to be 9.8
:
1, which is in good agreement with the ITO target.
| Elements | Unit: (wt%) | ||
|---|---|---|---|
| ITO target | In/SnOH | Prepared ITO | |
| In | 70.2 | 56.5 | 72.6 |
| Sn | 6.9 | 5.8 | 7.4 |
| In/Sn | 10.2 | 9.7 | 9.8 |
The prepared ITO nanopowder should be scaled up for application to the industrial field. We carried out an experiment to scale up the powder preparation 20 fold. The prepared ITO powder is shown in Fig. 5 inset and has a similar colour to commercial ITO. We obtained the prepared ITO nanopowder (19.1 g) from waste ITO target (20 g) with a high recovery yield (95.5%). In this case, the particle size was about three times larger than the 1 g scale as shown in Fig. 5. Even though the particle size changed, the samples still had similar or smaller sizes compared to commercial ITO nanopowder.
The acid is absolutely necessary material in industrial field such as semiconductor cleaning/etching and metal smelting/refining etc. Critical environmental problems such as soil acidification and acid rain have been partly attributed to the use of the acid. We considered that reducing the use of the acid is helping to solve these environmental problems. In this study, HCl is necessary for dissolution of the waste ITO target. 600 mL of HCl was needed to dissolve 20 g of waste ITO target powder using the conventional process. Therefore, we reduced to half the amount of HCl required, creating an environmentally friendly approach. The In and Sn compositions and the In/Sn ratio were determined for each sample by ICP analysis and are summarized in Table 3. 20 g of waste ITO target powder was dissolved in 600 mL of HCl and the composition of In and Sn were determined to be 72.5 wt% and 7.3 wt%, respectively. After reduction of the amount of HCl to half, the composition of In and Sn were 73.3 wt% and 7.5 wt% respectively. Furthermore, the dissolution time for the ITO target powder was increased by 2.3 times, and we could prepare large scale ITO nanopowder with a more environmentally friendly process. With a reduced amount of HCl, longer reaction times and energy are required for dissolving the ITO target. According to our results, the compositions changed slightly after reducing the amount of HCl used, however, the In/Sn ratio was very close to commercial ITO.
| Sample | Unit (%) | |
|---|---|---|
| Prepared ITO using HCl 600 mL (scale-up) | Prepared ITO using HCl 300 mL (scale-up) | |
| In | 72.5 | 73.3 |
| Sn | 7.3 | 7.5 |
| In/Sn ratio | 9.9 | 9.8 |
| This journal is © The Royal Society of Chemistry 2016 |