# Exploring Spray-Coating Techniques for Organic Solar Cell Applications

Authors: Wanyi Nie; Robert Coffin; Jiwen Liu; Christopher M. MacNeill; Yuan Li; Ronald E. Noftle; David L. Carroll
Journal: International Journal of Photoenergy
 (2012)

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## Abstract

We have investigated spray coating as a novel processing method for organic solar cell fabrication. In this work, spraying parameters and organic solvent influences have been correlated with cell performance. Using airbrush fabrication, bulk heterojunction photovoltaic devices based on a new low band gap donor material: poly[(4,8-bis(1-pentylhexyloxy)benzo[1,2-b:4,5-b′]dithiophene-2,6-diyl-alt-2,1,3-benzoxadiazole-4,7-diyl] with the C60-derivative (6,6)-phenyl C61-butyric acid methyl ester (PCBM) as an acceptor, have achieved power conversion efficiencies over 3%. We show that airbrush fabrication can be carried out with simple solvents such as pristine 1,2-dichlorobenzene. Moreover, the influence of device active area has been studied and the 1 cm2 device by spray coating maintained an excellent power conversion efficiency of 3.02% on average.


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## Body

## 1. Introduction

Worldwide, organic photovoltaics are under development as an inexpensive approach for collecting solar energy. Within the field, much effort has been given to the modification of either the absorber chemistry or its structural order. The chemical approach used by most researchers is to modulate the HOMO-LUMO levels of the donor polymer to obtain a low optical band gap (<1.74 eV) and thereby allow for absorption in a range that best matches the solar spectrum [1]. Recently, significant progress has been achieved following these routes, from a starting efficiency of around 1% in 1995 [2] when the bulk-heterojunction architecture was introduced, to 5% in 2007 for the first low band gap donor polymer [3] and most recently record efficiencies of 6%–8% [4–6]. However, these results are generally limited to the laboratory by the experimental requirement of using ultrathin layers that typically means employing spin coating. This method of fabrication only allows for devices on a small scale (usually 2.5 cm × 2.5 cm chips) that would neither control the cost nor satisfy the needs of large-scale manufacturing. Because of this, alternative coating technologies for absorbers have been of significant interest, aimed specifically at cheap, large area coating. These have included ink-jet printing [7], roll-to-roll printing [8], brush painting [9], and spray coating [10, 11]. Among these techniques, spray coating began to gain attention when Vak et al. in 2007 [12] showed they could easily fabricate the active layer with a commercially available hand-held airbrush. Up until now, most of the studies on spray coating OPV have been based on the poly(3-hexyl thiophene) (P3HT): the C60-derivative (6,6)-phenyl C61-butyric acid methyl ester (PCBM) bulk-heterojunction (BHJ) material system and the commonly achieved efficiency was 2-3% with a small active area (10 mm2). Therefore, a natural question is “how will the low band gap polymers with higher efficiencies translate into these scalable techniques?”Previously we reported a newly designed and synthesized low band gap polymer (~1.69 eV) poly[(4,8-bis(1-pentylhexyloxy)benzo[1,2-b:4,5-b′]dithiophene-2,6-diyl-alt-2,1,3-benzoxadiazole-4,7-diyl] (P1) [13]. When optimized with solvent additives in spin coating fabrication, this polymer easily achieves efficiencies exceeding 6%. Based on a similar donor-acceptor architecture as the record polymers referenced above, this polymer provides an excellent opportunity to study correlations in such systems, between spray-coating techniques and device performance for potential large scale applications.


## 2. Experiment

Prepatterned ITO substrates were cleaned in an ultrasonication bath with triton water, DI water, acetone, and isopropyl-alcohol for 20 min respectively and dried in a vacuum oven at 100°C for 1 hour. A 30 min UV-Ozone treatment was performed on the ITO surface afterwards and PEDOT : PSS (CLEVIOS 4083) was spun cast at a spin speed of 4000 rpm. The 100 nm active layer was either spun cast or spray-coated from the blend solution ofP1 and PCBM (the optimized ratio of 1 : 2 by weight was previous determined by experiment and IV curve available in Figure 4 in the appendix) dissolved in 1,2-dichlorobenzene (DCB). The substrates with dried films were transferred to a vacuum chamber, pumped down to 1 × 10−6 torr and LiF (~0.25 nm) as hole blocking layer and aluminum (~100 nm) as cathode were added. The resulting organic photovoltaic (OPV) devices were tested in air with a standard A.M 1.5 G solar simulator for I-V characters and external quantum efficiency (EQE) measurement was carried out by a Newport Cornerstone 260 Monochromator connected with a Newport 300 W Xenon light source.


## 3. Results and Discussion

### 3.1. Nozzle to Substrate Distance

Parameter control is the first step in developing this technology for any new polymer. Then, comparisons with standard spin-coating methods can be made between the thin films. From the basic structure of an airbrush in Figure1, the carrier gas brings the polymer solution from a feed cup, along a needle that leads to the nozzle (dia. 0.18 mm in our case). Once the solution passes through the nozzle, a fine line composed of very small droplets will be generated and deposited on the substrate. In this process, a variety of parameters are correlated with the resulting thin film morphology [12, 13]. These include the needle-nozzle distance which determines the size of the spray spot (and density of droplets), the carrier gas pressure which controls the deposition rate, and the nozzle to substrate distance which determines the droplet drying time during flight. A detailed study on the nozzle to substrate distance was carried out in the first study in spray coating on OPV by Vak et al. [12]. In that work, they defined the three regions between airbrush nozzle and substrate as “wet”, “intermediate,” and “dry” and they found the best linear control over thickness as a function of spraying time was in the “intermediate zone.” They also suggested that the “intermediate zone” varied with the boiling point of the solvent used.Figure 1
Airbrush spraying polymer on top of a device.Initially, as a control, we fabricated devices using P3HT : PCBM as the absorbing layer and the performance was quit close to that reported elsewhere [10] and shown in Table 1 for the spray distance of 15 cm. A detailed study was then carried out for our P1 polymer [14] and based on this, the “intermediate zone” was found to be very similar to the P3HT system; around 15 cm, using the fixed solution made by dissolving 2.5 mg P1 and 5 mg PCBM in DCB. We note that the DCB solution will dry the film slower than chlorobenzene due to the higher boiling point and therefore gives us a wider window for film thickness control [15].Table 1
AverageJV characteristics by spraying coating. P1 : PCBM solutions dissolved by CB, DCB and TCB under room temperature and spin coated from DCB. The maximum value of PCE over 8 devices under each condition is given in the last column as Peak PCE.
SolventVoc (V)Jsc (mA/cm2)FFPCEPeak PCESpray coatingCB0.9465.670.4552.37%2.53%DCB0.9606.880.4042.68%3.00%TCB0.9023.880.3771.31%1.40%Spin coatingCB0.9782.580.5641.38%1.42%DCB0.9237.610.4963.49%3.72%Spray coating P3HTUn-annealed0.6284.590.3160.91%Annealed0.6249.390.4262.5%2.72%


### 3.2. Polymer Ink Properties

The properties of the spray solution not only affects the choice of nozzle-substrate distance for thickness optimization, but also plays an important role on film morphology. This is based primarily on the choice of solvent boiling point and vapor pressure. The basic concept is to choose a fast drying solvent to prevent droplets from redissolving sublayers but not so fast so as to allow for a homogenous and pin-hole free film to form. Green et al. [15] found chlorobenzene (CB) to be an excellent choice for a good film quality and achieved efficiencies ~2.36% using P3HT : PCBM as the sprayed active layer. In 2009, Hoth et al. [16] adjusted the polymer solution viscosity by using a solvent mixture combining DCB and 1,3,5-trimethylbenzene in order to prevent the droplets from drying before touching the substrate as pristine CB does. This approach allowed for efficiencies up to 3.1% in the same BHJ material system with the resulting reduced surface tension allowing for the formation of a preferred morphology. Very recently, Susanna et al. used the mixed solvent of DCB and CB to achieve a similar morphology and obtained a PCE~4.2% [13].However, the choice of solvent varies the solution viscosity, which is then related to the specific material to be sprayed. So it was necessary to determine the best solvent for the blended solution ofP1 and PC61BM. Considering both the solubility of the polymer and the boiling point (bp) (related to the drying rate) of the host solvent, we initially investigated three solvents: CB (bp = 131°C), DCB (bp = 180.5°C), and 1,2,4-trichlorobenzene (TCB, bp = 241.4°C). The optimum ratio of P1 : PC61BM was previously determined to be 1 : 2 and this was held constant for this study. Absorbing layers were sprayed at room temperature (RT) with constant volumes (200 μL) and concentrations (3.00 mg/mL), yielding a film thickness of 90 ± 33.5 nm.The current density-voltage (JV) characteristics are summarized in Table 1. Active layers sprayed from DCB gave the best results with average power conversion efficiency (PCE) of 2.68%, and a peak value of 3.00%. Comparing to data from the devices sprayed from CB and TCB solution, we find that differences in performance are largely a result of differences in short-circuit current density, which is 20% and 77% lower for the devices sprayed from CB and TCB, respectively. Similar to our previous work with P1 we find that the fill factor (FF) is higher for the devices sprayed from CB (~0.455) compared with DCB (~0.405), though this difference is not significant enough to offset the Jsc difference.Figure2 shows the JV curve under illumination and the corresponding external quantum efficiency and indicating that the performances are quite close between spin cast devices and sprayed devices. The slightly lower fill factor can be explained by observing in the atomic force microscopy (AFM) images of Figures 2(c) and 2(d), which show a similar morphology, but a much higher height variation for spray-coated films (0~192 nm) than spun cast films (0~82 nm) (refer to Figure 5 in the appendix). A variation in film thickness and roughness will result in a charge recombination due to the limited charge mobility for conjugated polymers. Therefore, the thicker parts in the spray-casted film will lower the total shunt resistant and affect the device filling factors. However, this confirms that spray coating does present an approach to large-scale fabrication for OPV using this materials system.(a)I-V character under illumination and (b) EQE for spin and spray-coated device using difference solvents; AFM images for (c) spray-coated and (d) spin-coated device; the scale bar for AFM is in units of nm.
(a)(b)(c)(d)


### 3.3. Active Area

Researchers have also begun to focus on the realistic processes for larger area production. Na et al. [17] reported fully spray-coated, ITO-free, solar cells using the anode (PEDOT : PSS) and the active layer (P3HT : PCBM). They were able to achieve PCE~2.17%, thereby moving towards a cost-effective deposition method. At the same time, Girotto et al. [11] have developed a physical model for understanding droplet dynamics. In this work, they were able to spray a uniform PEDOT : PSS followed by a spray-coated absorbing layer with a fill factor over 70%, which is comparable to that achieved experimentally on spun-coated films. Taken together, these suggest that spray-coating can lead the OPV device to market without sacrificing efficiency but morphological considerations may be different from the spun cast approach.However, we note that most of the studies [11, 12, 15, 18, 19] for spray coating OPV were carried out with an active area of around 10 mm2 so scalability has not been demonstrated. Importantly, the roughness and thickness of sprayed films may reduce the final performance in large devices due to the increased internal resistance. In fact, it has been demonstrated that a 50% decrease occurs in a very large device (over 12 cm2) [20], whereas on a 4 cm2 device very little loss of performance (2.64%) from the smaller devices was observed. In our study, we observed a 1% decrease as well when larger device sizes (to 1 cm2) were fabricated by spraying. This is due to the rougher surface.In order to scale up our device by spray coating, we studied theJV performance as a function of active area statistically in Figure 3. Each point in Figure 3 refers to the average over 8 electrodes (2 chips of 4-electrode devices). Each electrode is an active area of the film. The error was estimated by the difference between the average and maximum. Again, the Voc is not affected by active area as shown in Figure 3 with voltages ranging from 0.957 V to 0.970 V. Jsc is also relatively constant at 8.52±0.5 mA/cm2 up to the active area of 34 mm2. It dropped to 0.45 mA/cm2 when device sizes were increased to 100 mm2, which is only a 5% sacrifice in performance. The fill factor also decreased at 100 mm2 as expected to 0.395±0.007 but the device with an active area of 34 mm2 still maintains a good fill factor of 0.49 that is comparable to the spun-casted devices. Because of the variation in thickness across the active are, the polymer solar cell can be viewed as a number of devices connected in parallel. When the active area increases, the shunt resistant was reduced from 853 ohm·cm2 for the 0.3 cm2 device down to 585 ohm·cm2 due to this film thickness variation which leads to charge recombination (AFM analysis is available in Figure 5 in the appendix). We suggest that this dominates the change in device filling factor. Surprisingly, the 100 mm2 devices show an average PCE of 3.02% in spraying coated devices. For such large active area devices this is quite good even though there is a 1.1% drop compared to the peak value of 4.12% for an active area of 34 mm2.Statistical study with scale bars on (a) open-circuit voltage (Voc square) and short-circuit current (Jsc diamond). (b) Filling factor (triangle) and power conversion efficiency (circle) tested under a standard AM 1.5 solar simulator for sprayed devices as a function of active area.
(a)(b)Figure 4
JV characteristics under 100 mW/cm2 illumination by standard A.M. 1.5 solar simulator with P1 : PCBM ratio at 1 : 1 (black solid), 1 : 2 (red dash), 1 : 3 (blue dot), and 1 : 4 (green dash-dot).AFM topology analysis of (a) a spun-casted film and (b) a spray-casted film using DCB as carrier solvent.
(a)(b)


## 3.1. Nozzle to Substrate Distance

Parameter control is the first step in developing this technology for any new polymer. Then, comparisons with standard spin-coating methods can be made between the thin films. From the basic structure of an airbrush in Figure1, the carrier gas brings the polymer solution from a feed cup, along a needle that leads to the nozzle (dia. 0.18 mm in our case). Once the solution passes through the nozzle, a fine line composed of very small droplets will be generated and deposited on the substrate. In this process, a variety of parameters are correlated with the resulting thin film morphology [12, 13]. These include the needle-nozzle distance which determines the size of the spray spot (and density of droplets), the carrier gas pressure which controls the deposition rate, and the nozzle to substrate distance which determines the droplet drying time during flight. A detailed study on the nozzle to substrate distance was carried out in the first study in spray coating on OPV by Vak et al. [12]. In that work, they defined the three regions between airbrush nozzle and substrate as “wet”, “intermediate,” and “dry” and they found the best linear control over thickness as a function of spraying time was in the “intermediate zone.” They also suggested that the “intermediate zone” varied with the boiling point of the solvent used.Figure 1
Airbrush spraying polymer on top of a device.Initially, as a control, we fabricated devices using P3HT : PCBM as the absorbing layer and the performance was quit close to that reported elsewhere [10] and shown in Table 1 for the spray distance of 15 cm. A detailed study was then carried out for our P1 polymer [14] and based on this, the “intermediate zone” was found to be very similar to the P3HT system; around 15 cm, using the fixed solution made by dissolving 2.5 mg P1 and 5 mg PCBM in DCB. We note that the DCB solution will dry the film slower than chlorobenzene due to the higher boiling point and therefore gives us a wider window for film thickness control [15].Table 1
AverageJV characteristics by spraying coating. P1 : PCBM solutions dissolved by CB, DCB and TCB under room temperature and spin coated from DCB. The maximum value of PCE over 8 devices under each condition is given in the last column as Peak PCE.
SolventVoc (V)Jsc (mA/cm2)FFPCEPeak PCESpray coatingCB0.9465.670.4552.37%2.53%DCB0.9606.880.4042.68%3.00%TCB0.9023.880.3771.31%1.40%Spin coatingCB0.9782.580.5641.38%1.42%DCB0.9237.610.4963.49%3.72%Spray coating P3HTUn-annealed0.6284.590.3160.91%Annealed0.6249.390.4262.5%2.72%


## 3.2. Polymer Ink Properties

The properties of the spray solution not only affects the choice of nozzle-substrate distance for thickness optimization, but also plays an important role on film morphology. This is based primarily on the choice of solvent boiling point and vapor pressure. The basic concept is to choose a fast drying solvent to prevent droplets from redissolving sublayers but not so fast so as to allow for a homogenous and pin-hole free film to form. Green et al. [15] found chlorobenzene (CB) to be an excellent choice for a good film quality and achieved efficiencies ~2.36% using P3HT : PCBM as the sprayed active layer. In 2009, Hoth et al. [16] adjusted the polymer solution viscosity by using a solvent mixture combining DCB and 1,3,5-trimethylbenzene in order to prevent the droplets from drying before touching the substrate as pristine CB does. This approach allowed for efficiencies up to 3.1% in the same BHJ material system with the resulting reduced surface tension allowing for the formation of a preferred morphology. Very recently, Susanna et al. used the mixed solvent of DCB and CB to achieve a similar morphology and obtained a PCE~4.2% [13].However, the choice of solvent varies the solution viscosity, which is then related to the specific material to be sprayed. So it was necessary to determine the best solvent for the blended solution ofP1 and PC61BM. Considering both the solubility of the polymer and the boiling point (bp) (related to the drying rate) of the host solvent, we initially investigated three solvents: CB (bp = 131°C), DCB (bp = 180.5°C), and 1,2,4-trichlorobenzene (TCB, bp = 241.4°C). The optimum ratio of P1 : PC61BM was previously determined to be 1 : 2 and this was held constant for this study. Absorbing layers were sprayed at room temperature (RT) with constant volumes (200 μL) and concentrations (3.00 mg/mL), yielding a film thickness of 90 ± 33.5 nm.The current density-voltage (JV) characteristics are summarized in Table 1. Active layers sprayed from DCB gave the best results with average power conversion efficiency (PCE) of 2.68%, and a peak value of 3.00%. Comparing to data from the devices sprayed from CB and TCB solution, we find that differences in performance are largely a result of differences in short-circuit current density, which is 20% and 77% lower for the devices sprayed from CB and TCB, respectively. Similar to our previous work with P1 we find that the fill factor (FF) is higher for the devices sprayed from CB (~0.455) compared with DCB (~0.405), though this difference is not significant enough to offset the Jsc difference.Figure2 shows the JV curve under illumination and the corresponding external quantum efficiency and indicating that the performances are quite close between spin cast devices and sprayed devices. The slightly lower fill factor can be explained by observing in the atomic force microscopy (AFM) images of Figures 2(c) and 2(d), which show a similar morphology, but a much higher height variation for spray-coated films (0~192 nm) than spun cast films (0~82 nm) (refer to Figure 5 in the appendix). A variation in film thickness and roughness will result in a charge recombination due to the limited charge mobility for conjugated polymers. Therefore, the thicker parts in the spray-casted film will lower the total shunt resistant and affect the device filling factors. However, this confirms that spray coating does present an approach to large-scale fabrication for OPV using this materials system.(a)I-V character under illumination and (b) EQE for spin and spray-coated device using difference solvents; AFM images for (c) spray-coated and (d) spin-coated device; the scale bar for AFM is in units of nm.
(a)(b)(c)(d)


## 3.3. Active Area

Researchers have also begun to focus on the realistic processes for larger area production. Na et al. [17] reported fully spray-coated, ITO-free, solar cells using the anode (PEDOT : PSS) and the active layer (P3HT : PCBM). They were able to achieve PCE~2.17%, thereby moving towards a cost-effective deposition method. At the same time, Girotto et al. [11] have developed a physical model for understanding droplet dynamics. In this work, they were able to spray a uniform PEDOT : PSS followed by a spray-coated absorbing layer with a fill factor over 70%, which is comparable to that achieved experimentally on spun-coated films. Taken together, these suggest that spray-coating can lead the OPV device to market without sacrificing efficiency but morphological considerations may be different from the spun cast approach.However, we note that most of the studies [11, 12, 15, 18, 19] for spray coating OPV were carried out with an active area of around 10 mm2 so scalability has not been demonstrated. Importantly, the roughness and thickness of sprayed films may reduce the final performance in large devices due to the increased internal resistance. In fact, it has been demonstrated that a 50% decrease occurs in a very large device (over 12 cm2) [20], whereas on a 4 cm2 device very little loss of performance (2.64%) from the smaller devices was observed. In our study, we observed a 1% decrease as well when larger device sizes (to 1 cm2) were fabricated by spraying. This is due to the rougher surface.In order to scale up our device by spray coating, we studied theJV performance as a function of active area statistically in Figure 3. Each point in Figure 3 refers to the average over 8 electrodes (2 chips of 4-electrode devices). Each electrode is an active area of the film. The error was estimated by the difference between the average and maximum. Again, the Voc is not affected by active area as shown in Figure 3 with voltages ranging from 0.957 V to 0.970 V. Jsc is also relatively constant at 8.52±0.5 mA/cm2 up to the active area of 34 mm2. It dropped to 0.45 mA/cm2 when device sizes were increased to 100 mm2, which is only a 5% sacrifice in performance. The fill factor also decreased at 100 mm2 as expected to 0.395±0.007 but the device with an active area of 34 mm2 still maintains a good fill factor of 0.49 that is comparable to the spun-casted devices. Because of the variation in thickness across the active are, the polymer solar cell can be viewed as a number of devices connected in parallel. When the active area increases, the shunt resistant was reduced from 853 ohm·cm2 for the 0.3 cm2 device down to 585 ohm·cm2 due to this film thickness variation which leads to charge recombination (AFM analysis is available in Figure 5 in the appendix). We suggest that this dominates the change in device filling factor. Surprisingly, the 100 mm2 devices show an average PCE of 3.02% in spraying coated devices. For such large active area devices this is quite good even though there is a 1.1% drop compared to the peak value of 4.12% for an active area of 34 mm2.Statistical study with scale bars on (a) open-circuit voltage (Voc square) and short-circuit current (Jsc diamond). (b) Filling factor (triangle) and power conversion efficiency (circle) tested under a standard AM 1.5 solar simulator for sprayed devices as a function of active area.
(a)(b)Figure 4
JV characteristics under 100 mW/cm2 illumination by standard A.M. 1.5 solar simulator with P1 : PCBM ratio at 1 : 1 (black solid), 1 : 2 (red dash), 1 : 3 (blue dot), and 1 : 4 (green dash-dot).AFM topology analysis of (a) a spun-casted film and (b) a spray-casted film using DCB as carrier solvent.
(a)(b)


## 4. Conclusion

In summary, a review of the recent achievements in large-scale OPVs (mainly based on P3HT : PCBM BHJ structures) by spray coating technology, has identified several important parameters such as nozzle-substrate distance, choice of solvent, mixture of cosolvent that influence morphology optimization. Using these parameters in this work, we have explored the possibility of fabricating solar cell devices by a hand-held airbrush with an active layer composed of a new low band gap copolymer poly[(4,8-bis(1-pentylhexyloxy)benzo[1,2-b : 4,5-b′]dithiophene-2,6-diyl-alt-2,1,3-benzothiadiazole-4,7-diyl] and phenyl-C61-butyric acid methyl ester (PC61BM). 1,2-Dichlorobenzene is shown as an appropriate carrier solvent by comparing the solar cell performance with other two solvents (chlorobenzene, 1,2,4-trichlorobenzene) under identical conditions, and we obtain a promising PCE~3.00% on average without any special treatment under room temperature conditions. We believe these results may give some guidance to spray approaches in this class of donor acceptor polymers.



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*Source: 175610-2012-05-14.xml*