Open Access Article
Christian
Sprau
a,
Felix
Buss
b,
Michael
Wagner
a,
Dominik
Landerer
a,
Manuel
Koppitz
a,
Alexander
Schulz
a,
Daniel
Bahro
a,
Wilhelm
Schabel
b,
Philip
Scharfer
b and
Alexander
Colsmann
*a
aLight Technology Institute, Karlsruhe Institute of Technology (KIT), Engesserstrasse 13, 76131 Karlsruhe, Germany. E-mail: christian.sprau@kit.edu; alexander.colsmann@kit.edu
bInstitute of Thermal Process Engineering, Thin Film Technology, Karlsruhe Institute of Technology (KIT), Kaiserstrasse 12, 76131 Karlsruhe, Germany
First published on 16th July 2015
Several high performance polymer:fullerene bulk-heterojunction photo-active layers, deposited from the non-halogenated solvents o-xylene or anisole in combination with the eco-compatible additive p-anisaldehyde, are investigated. The respective solar cells yield excellent power conversion efficiencies up to 9.5%, outperforming reference devices deposited from the commonly used halogenated chlorobenzene/1,8-diiodooctane solvent/additive combination. The impact of the processing solvent on the bulk-heterojunction properties is exemplified on solar cells comprising benzodithiophene-thienothiophene co-polymers and functionalized fullerenes (PTB7:PC71BM). The additive p-anisaldehyde improves film formation, enhances polymer order, reduces fullerene agglomeration and shows high volatility, thereby positively affecting layer deposition, improving charge carrier extraction and reducing drying time, the latter being crucial for future large area roll-to-roll device fabrication.
Broader contextOrganic bulk-heterojunction solar cells are on the cusp of commercialization. Printing and coating techniques are widely considered enablers of low-cost solar module fabrication with excellent carbon footprints. For the transfer of lab-scale processes to an environmentally friendly and sustainable industrial large-scale fabrication of polymer solar cells by printing, non-halogenated solvents and processing additives are mandatory prerequisites. As the choice of solvents is pivotal to the complex formation of the bulk-heterojunction and hence to the device performance, both academia and the solar industry have fostered strong research on “green” device processing in order to advance the market-readiness of organic solar modules. |
| Additive | Hazard statements |
|---|---|
| DIO | H413 chronic aquatic toxicity |
| CN | H302 acute toxicity, oral |
| H315 skin irritation | |
| H319 eye irritation | |
| H335 specific target organ toxicity – single exposure | |
| H400 acute aquatic toxicity | |
| MN | H302 acute toxicity, oral |
| H315 skin irritation | |
| H319 eye irritation | |
| H334 respiratory sensitisation | |
| H335 specific target organ toxicity – single exposure | |
| H411 chronic aquatic toxicity | |
| THN | H315 skin irritation |
| H319 eye irritation | |
| H351 carcinogenicity | |
| H304 aspiration hazard | |
| H411 chronic aquatic toxicity | |
| DPE | H319 eye irritation |
| H411 chronic aquatic toxicity | |
| NMP | H315 skin irritation |
| H319 eye irritation | |
| H360 reproductive toxicity | |
| H335 specific target organ toxicity – single exposure | |
| AA | None |
Besides environmental concerns, more volatile solvent additives than DIO may be beneficial for future roll-to-roll processing due to reduced drying times and temperatures.
In this work, we investigate the deposition of various high-performing polymer:fullerene BHJs from the non-halogenated and production relevant solvents o-xylene or anisole in combination with the eco-compatible additive p-anisaldehyde (AA). The respective solar cells yield PCEs outperforming devices fabricated from common halogenated solvent/additive combinations such as CB and DIO.
:
1.5 w/w, polymer concentration 10 g L−1) in either chlorobenzene (CB, anhydrous, 99.8%,), o-xylene (anhydrous, 97%) or anisole (anhydrous, 99.7%) and stirred overnight at elevated temperatures (CB: 50 °C, o-xylene and anisole: 85 °C). All solvents and additives were used as purchased (Sigma-Aldrich). The solvent additives, either 1,8-diiodooctane (DIO, 98%) or p-anisaldehyde (AA, 98%), were then added to the stock solution. The non-filtered warm solution was spun onto the samples (1500 rpm, 60 s) to form the photo-active layer. After initial film drying at room temperature (10 min), the films were annealed on a hotplate (60 °C, 20 min) to remove the residual additive. Then the devices were transferred into a vacuum chamber (base pressure 10−6 mbar) to deposit the molybdenum oxide hole extraction layer (MoO3, 10 nm) and the silver top electrode (Ag, 100 nm) by thermal evaporation, using a shadow mask defining the active solar cell area (3 × 3.5 mm2). The same device architecture and fabrication procedure were employed to investigate all other polymer:PC71BM photo-active layers. Poly[[4,8-bis[5-(2-ethylhexyl)thiophen-2-yl]benzo[1,2-b:4,5-b′]dithiophene-2,6-diyl][3-fluoro-2-[(2-ethylhexyl)carbonyl]thieno[3,4-b]thiophenediyl]] (PTB7-Th, 1-Material Inc., Mw = 108 kg mol−1, ĐM = 2.5), poly[[2,7-(5,5-bis-(3,7-dimethyloctyl)-5H-dithieno[3,2-b:2′,3′-d]pyran)-alt-4,7-(5,6-difluoro-2,1,3-benzothiadiazole)]] (PDTP-DFBT, 1-Material Inc., Mw = 37 kg mol−1, ĐM = 2.4) and poly[(5,6-difluoro-2,1,3-benzothiadiazol-4,7-diyl)-alt-(3,3′′′-di(2-octyldodecyl)-2,2′;5′,2′′;5′′,2′′′-quaterthiophen-5,5′′′-diyl)] (PffBT4T-2OD, 1-Material Inc., Mw = 100 kg mol−1, ĐM = 2.5) were dissolved and mixed with PC71BM according to the blend ratios and polymer concentrations listed in Table 4. All solids were sufficiently dissolved in all solvents and the solutions were deposited without filtering. PTB7-Th:PC71BM solutions and films were prepared following the PTB7:PC71BM deposition protocol. PDTP-DFBT:PC71BM solutions were stored overnight on a hotplate (85 °C) and spun (1200 rpm, 60 s; 800 rpm from o-DCB solution) from warm solution (60 °C). PffBT4T-2OD:PC71BM solutions were stirred overnight (110 °C) and spun (800 rpm, 120 s) onto warm substrates (solution and substrates were stored on a 95 °C hotplate prior to spin casting) followed by subsequent annealing (80 °C, 5 min).
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| Fig. 1 (a) Solar cell device architecture. (b) Active layer components PTB7 and PC71BM. (c) Chemical structures of the solvents and additives investigated in this work. | ||
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| Main solvent | Additive | t (nm) | J SC (mA cm−2) | V OC (mV) | FF (%) | PCEa (%) | R q (nm) | α 1/α2 |
|---|---|---|---|---|---|---|---|---|
| a PCE of the best performing devices in parentheses. | ||||||||
| CB | — | 90 | 8.8 ± 0.1 | 762 ± 7 | 42 ± 1 | 2.8 ± 0.1 (2.9) | 5.1 | 1.03 |
| o-Xylene | — | 90 | 6.2 ± 0.2 | 736 ± 5 | 45 ± 1 | 2.0 ± 0.6 (2.2) | 12.7 | 0.96 |
| Anisole | — | 80 | 9.3 ± 0.2 | 750 ± 1 | 46 ± 2 | 3.2 ± 0.2 (3.5) | 5.1 | 1.01 |
| CB | 4% DIO | 85 | 14.0 ± 0.1 | 739 ± 4 | 67 ± 2 | 6.9 ± 0.2 (7.3) | 2.5 | 1.07 |
| o-Xylene | 3% DIO | 85 | 14.2 ± 0.2 | 737 ± 5 | 67 ± 2 | 7.0 ± 0.2 (7.1) | 2.6 | 1.07 |
| Anisole | 2% DIO | 80 | 13.4 ± 0.2 | 738 ± 3 | 66 ± 1 | 6.5 ± 0.1 (6.7) | 1.9 | 1.08 |
| CB | 2% AA | 90 | 13.6 ± 0.6 | 748 ± 5 | 69 ± 2 | 7.0 ± 0.3 (7.5) | 2.7 | 1.07 |
| o-Xylene | 2% AA | 85 | 14.3 ± 0.1 | 738 ± 4 | 70 ± 1 | 7.4 ± 0.1 (7.6) | 2.4 | 1.07 |
| Anisole | 1% AA | 80 | 13.5 ± 0.2 | 747 ± 4 | 65 ± 1 | 6.6 ± 0.2 (6.9) | 4.1 | 1.05 |
Whereas BHJs from pure solvents did not yield efficient polymer solar cells, the addition of the processing additive DIO enhanced both Jsc and FF significantly. Fig. 2b depicts the J–V curves of solar cells deposited from CB, o-xylene and anisole with individually optimized DIO concentrations as noted in the graph. The corresponding key performance data are summarized in Table 2. The BHJ deposition from all three solvent/DIO combinations yields high PCEs of ≈7% due to an excellent FF >65% and a Jsc ≈ 14 mA cm−2. Whereas the solar cells that were deposited from pure solvents show different properties, the performance of all devices that were deposited utilizing the additive DIO yields very similar J–V curves. The voltage dependent current densities under reverse bias when using pure solvents indicate poor charge carrier extraction and field dependent recombination. In contrast, upon using the additive DIO, the current density under reverse bias saturates, indicating excellent extraction of free charges and low recombination losses even at low internal fields, being in good agreement with previous studies.24
This drastic device performance improvement upon using the additive DIO emphasizes the importance of the solvent additive for efficient PTB7:PC71BM solar cells. Although DIO is used in small amounts only, it is a hazardous substance that is not suitable for industrial large-area device processing. Furthermore, DIO residues are suspected to be remaining in the active layer after film formation, due to the high DIO boiling point (bp = 332.5 °C).
Being able to dissolve fullerenes in high concentrations25 and having a higher boiling point (>200 °C) than most main solvents, non-halogenated (substituted) benzaldehydes appear as an interesting alternative material class.26 Being a representative of this material class, we have focused on the eco-compatible additive AA (bp = 248 °C) to improve the formation of the photo-active layer. The J–V curves of the corresponding solar cells comprising photo-active layers deposited from CB, o-xylene or anisole with an individually optimized additive concentration are shown in Fig. 2c. The key performance data are summarized in Table 2. The drastic PCE enhancement over devices that were deposited from pure main solvents is comparable to the effect of DIO on the device performance. Best Jsc and FF were yielded upon BHJ deposition from o-xylene/AA, resulting in an average PCE of 7.4%.
We note that, with respect to future process upscaling, we have performed preliminary doctor blading experiments on PTB7:PC71BM in o-xylene/AA solution with the devices yielding similar performance (data not provided here).
To further analyze and compare the impact of the solvent additives DIO and AA on the film properties, we studied the film surface topography by atomic force microscopy (AFM) as depicted in Fig. 4. When depositing the PTB7:PC71BM film from the pure solvents CB, o-xylene or anisole, we observed protruding nano-spheres with a lateral size of about 150–200 nm and a height of approximately 10–20 nm above the average film surface. For the films cast from o-xylene, these features are even larger, measuring about 300 nm in diameter, with a typical height of about 30 nm. In contrast, when using the additives DIO or AA together with any of the three main solvents, these features are not visible in the AFM images and the surface is rather smooth.
These observations are in good agreement with earlier AFM and transmission electron microscopy (TEM) studies on PTB7:PC71BM films that were cast from CB or CB/DIO.15,22,23 By X-ray diffraction experiments, these spherical features in PTB7:PC71BM films were identified to be almost pure fullerene agglomerates embedded in a polymer:fullerene matrix, with the 200 nm agglomerates when cast from CB being reduced to 30 nm upon deposition from CB/DIO.23 In additive free bulk-heterojunctions, the fullerene agglomeration therefore leads to enhanced recombination, with the detailed processes still being discussed.23,24,29 These interpretations match our optoelectronic device study in Section 3.1, where we found reduced recombination as well as enhanced FF and Jsc for devices with photo-active layers that were deposited from solvent/DIO or solvent/AA.
We note that we found shallow depression features with a diameter of about 150–300 nm instead (depth 5–10 nm), upon film deposition from CB/AA, o-xylene/AA and, most pronounced, from anisole/AA. Taking into account the excellent performance of the corresponding solar cells, we attribute these features to surface inhomogeneities that form during the drying process rather than material separation.
To analyze and compare the drying of PTB7:PC71BM/o-xylene solutions containing either additive, DIO or AA (2% v/v), we investigate the evaporation kinetics of additive residues from freshly prepared PTB7:PC71BM layers on a quartz crystal microbalance (QCM). On the QCM, we record the resonance frequencies over time. An increasing resonance frequency reflects a loss of mass due to solvent/additive evaporation. Fig. 5a and b shows the relative resonance frequency change of the first harmonics (n = 1, 3, 5, 7, 9) Δfn/n of both material systems over time. These resonance frequencies during additive evaporation are given relative to the resonance frequency of the uncoated crystal. We note that the time frame differs by a factor of 10, that is, 40 h for o-xylene/DIO and 4 h for o-xylene/AA. For the as-cast o-xylene/DIO film we find a linearly increasing Δf within the first 5 h of the experiment. During the early stages of drying, henceforth referred to as constant rate period, the thermodynamics at the vapor–liquid interface and the gas-phase mass transport are dominant. The observed linear increase is characteristic of single solvents that evaporate during the constant rate period, inferring that the high-boiling additive DIO is still present in the as-cast film whereas o-xylene has evaporated earlier, during spin casting. Simultaneous evaporation of two solvents would yield a drying curve that is either non-linear or features a kink at the transition from low- to high-boiling solvent dominated drying.32,33 At low additive content, that is, at a later stage of drying, which we henceforth refer to as the falling rate period, the diffusion coefficient in polymer solutions can decrease by orders of magnitudes, hampering the removal of trace solvent. The measurements were discontinued after 40 h when only little frequency variation was noted, that is, the film was effectively dry. The experiment was repeated with another film that was annealed on a hotplate (1 min at 60 °C) directly after spin coating, leading to a reduced constant rate period of ≈2 h. Here, after initial sample drying on the hotplate, the subsequent drying at 25 °C shows the same constant evaporation rate as the as-cast film, confirming the presence of only DIO in the film.
In contrast, QCM measurements of films deposited from o-xylene/AA showed almost no frequency change over time and no constant rate period. We conclude that AA had almost completely evaporated earlier, during spin coating.
To quantitatively determine and compare the evaporation rates and the corresponding mass loss from the resonance frequency change, we use the Sauerbrey equation. These mass losses and the corresponding thickness decrease due to additive evaporation are depicted in Fig. 5c and d and summarized in Table 3 for both solvent mixtures versus time. Fig. 5e and f shows a zoom in the relevant mass regime of the falling rate period. Within 4 hours of drying, about 125 ng cm−2 of the additive AA evaporated from the PTB7:PC71BM film at room temperature, yielding an average evaporation rate of 31 ng cm−2 h−1. In contrast, it takes 22.7 hours for the same amount of DIO to evaporate, yielding an average evaporation rate of 5.5 ng cm−2 h−1. Only at the end of the measurements, that is, after 4 h of AA evaporation and 40 h of DIO evaporation, the evaporation rates of both additives have equalized (2.5 ng cm−2 h−1). If we assume additive diffusion within the film to limit the additive evaporation and a dry film at the end of the experiment, we can conclude that the diffusion coefficient of DIO is lower than the diffusion coefficient of AA in the PTB7:PC71BM matrix.
| Additive | Drying time (h) | Solvent mass Δm–Δmdry (ng cm−2) | Thickness difference t–tdry (nm) |
|---|---|---|---|
| DIO | 0 | 9766 | 53 |
| 5 | 600 | 3.5 | |
| 10 | 244 | 1.5 | |
| 20 | 101 | 0.8 | |
| 30 | 41 | 0.4 | |
| 40 | 0 | 0 | |
| AA | 0 | 125 | 1.1 |
| 2 | 6 | 0.2 | |
| 4 | 0 | 0 | |
Moreover, the relationship of mass with frequency change allows for calculating the film thickness of the dry layers tdry. In all experiments the frequencies Δfn/n approached about −410 Hz at the end of the measurement procedures, which corresponds to a dry film thickness of 60 nm, assuming a density of 1.2 g cm−3 for typical organic semiconductors.34 This allowed us to determine the mass of the initial wet layer before solvent and additive evaporation, taking into account the initial composition of the PTB7:PC71BM/o-xylene/additive solutions and the respective densities. After spin coating, about 96 wt% of the o-xylene/DIO solution had evaporated from the PTB7:PC71BM layer, whereas 99.9 wt% of the o-xylene/AA solution had evaporated under equal conditions.
As a structural advancement of PTB7, the polymer PTB7-Th was reported in the literature, enabling enhanced PCEs exceeding 9%, when deposited from CB/DIO on top of a modified ZnO interfacial layer, or yielding PCEs of more than 10%, when using an organic interlayer instead.35,36 Following the experimental protocol of Section 3.1, the J–V curves of these solar cells deposited from either CB/DIO, o-xylene or o-xylene/AA are depicted in Fig. 6. All key performance data are listed in Table 4. Whereas PTB7-Th:PC71BM reference solar cells cast from CB and 4% DIO (v/v) show PCEs of 7.5%, which is in good agreement with literature known results on plain ZnO,35 the PCEs of solar cells that were processed from o-xylene and 2% AA (v/v) improved to 8.3%.
| Polymer | Blend ratio | c (g L−1) | Main solvent | Additive | t (nm) | J SC (mA cm−2) | V OC (mV) | FF (%) | PCEa (%) |
|---|---|---|---|---|---|---|---|---|---|
| a PCE of the best performing device in parentheses. b Cells with up to 600 nm thickness and similar device performance. | |||||||||
| PTB7-Th | 1 : 1.5 |
10 | CB | 4% DIO | 125 | 15.1 ± 0.2 | 791 ± 3 | 62 ± 1 | 7.5 ± 0.1 (7.6) |
1 : 1.5 |
10 | o-Xylene | — | 120 | 10.0 ± 0.1 | 772 ± 1 | 31 ± 1 | 2.3 ± 0.1 (2.4) | |
1 : 1.5 |
10 | o-Xylene | 2% AA | 100 | 15.3 ± 0.2 | 783 ± 1 | 69 ± 1 | 8.3 ± 0.1 (8.5) | |
| PDTP-DFBT | 1 : 2 |
8 | o-DCB | — | 95 | 10.6 ± 0.2 | 712 ± 3 | 53 ± 1 | 4.0 ± 0.1 (4.2) |
1 : 1.5 |
9.6 | o-Xylene | — | 90 | 2.6 ± 0.1 | 720 ± 4 | 45 ± 1 | 0.9 ± 0.1 (0.9) | |
1 : 1.5 |
9.6 | o-Xylene | 1.5% AA | 105 | 12.4 ± 0.1 | 704 ± 5 | 54 ± 1 | 4.7 ± 0.2 (5.0) | |
| PffBT4T-2OD | 1 : 1.2 |
10 | CB : o-DCB 1 : 1 |
3% DIO | 440 | 17.5 ± 0.4 | 736 ± 3 | 60 ± 1 | 7.7 ± 0.3 (8.1) |
1 : 1.2 |
9 | o-Xylene | — | 450 | 4.0 ± 0.2 | 775 ± 15 | 48 ± 2 | 1.5 ± 0.1 (1.7) | |
1 : 1.2 |
9.5 | o-Xylene | 1% AA | 300b | 18.0 ± 1.0 | 738 ± 3 | 68 ± 3 | 9.0 ± 0.2 (9.5) | |
Similar observations were made for photo-active blends comprising the narrow bandgap polymer PDTP-DFBT and PC71BM, which can yield PCEs of up to 8% when cast from pure o-DCB,37 and which were also employed in highly efficient tandem solar cells.38–40 It was pointed out in the literature that the deposition of PDTP-DFBT:PC71BM BHJs from o-DCB, omitting any additives, is sufficient to yield high PCEs. However, we found that this concept does not apply to the deposition from the non-chlorinated solvent o-xylene. In contrast, adding AA to the o-xylene solution (1.5% v/v), we yielded PDTP-DFBT:PC71BM (1
:
1.5) solar cells with PCEs of up to 5.0%, clearly outperforming both reference devices deposited from pure o-DCB (PCE = 4%, blend ratio 1
:
2) or o-xylene (PCE = 1%). We note that we found significantly higher PDTP-DFBT solubility in o-xylene than in o-DCB, making o-xylene – besides the environmental aspect – much more favorable towards improved processability of this polymer.
As a third example, we investigated o-xylene/AA for the deposition of a blend comprising PffBT4T-2OD and PC71BM. Very recently, this polymer was reported to enable PCEs exceeding 10%. It exhibits high crystallinity and performs very well in thick active layers (≈300 nm).1 Following the previously published preparation protocol, we built reference solar cells incorporating a PffBT4T-2OD:PC71BM photo-active blend from a CB
:
o-DCB 1
:
1 solvent mixture with the addition of 3% DIO, resulting in an average device efficiency of 7.7%. Using the solvent o-xylene plus 1% of AA instead, we yielded PCEs of 9.0% (hero device: 9.5%), with the improvement originating mainly from a higher FF. Again, without employing AA, the efficiency of the solar cells is drastically lower.
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