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Examensarbete 30 hp October 2018 Evaluating the economic viability of Perovskite – SHJ monolithically integrated PV modules Marwyn Vernon Masterprogrammet i energiteknik Master Programme in Energy Technology

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Page 1: Evaluating the economic viability of Perovskite – SHJ monolithically integrated …uu.diva-portal.org/smash/get/diva2:1276841/FULLTEXT01.pdf · 2019-01-09 · Evaluating the economic

Examensarbete 30 hpOctober 2018

Evaluating the economic viability of Perovskite

– SHJ monolithically integrated PV modules

Marwyn Vernon

Masterprogrammet i energiteknikMaster Programme in Energy Technology

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Teknisk- naturvetenskaplig fakultet UTH-enheten Besöksadress: Ångströmlaboratoriet Lägerhyddsvägen 1 Hus 4, Plan 0 Postadress: Box 536 751 21 Uppsala Telefon: 018 – 471 30 03 Telefax: 018 – 471 30 00 Hemsida: http://www.teknat.uu.se/student

Abstract

Evaluating the economic viability of Perovskite – SHJmonolithically integrated photovoltaic modules

Marwyn Vernon

In this study, the financial and economic viable of perovskite-SHJ tandem solar cells were determined using a detailed bottom-up cost model and energy-yield calculations. Attention to specific advancements in perovskite solar cell layer technology and large-scale deposition have been taken into account to create a realistic, viable commercial scale option for tandem production. A reference tandem technology is used to determine the overall manufacturing cost and minimum sustainable price. Models used show that the tandem technology has the potential to be cost competitive with existing silicon technology given the uncertainty and sensitivity of the values used in this study. It was examined further how non-STC energy yield and service life contributes to the overall economic viability of the tandem module within residential, commercial and utility scale of application. Given the reference tandem module, it is expected to be competitive at the residential level with existing silicon technology if perovskite layers’ service life is greater than 20 years. In commercial and utility application, the tandem model is not economically viable due to the reductions seen in the area- and project-related installation costs for existing technology. This thesis concludes by presenting the current limitations in perovskite technology that would inhibit adaptation of this into commercial-scale production and presents alternative applications in which tandem modules would be more favourable.

MSc ET 18003Examinator: Joakim WidénÄmnesgranskare: Jonathan ScraggHandledare: Lars Korte

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Acknowledgements

Special thanks to the organizers at KIC InnoEnergy Master’s program for the support

financially and experience this wonderful two year journey. I would first like to thank my

thesis supervisor Dr. Lars Korte at Helmholtz-Zentrum Berlin in Berlin, Germany.

Thanks Lars for the office companionship and always helpful attitude. He consistently

allowed this paper to be my own work, but steered me in the right the direction whenever

he thought I needed it.

I would also like to acknowledge Jonathon Scragg of at the Department of Engineering

Sciences at Uppsala University as the second reader of this thesis, and I am grateful to

him for his very valuable comments on this thesis.

Finally, I must express my very profound gratitude to my parents and to my incredible

sisters for providing me with unfailing support and continuous encouragement throughout

my years of study and through the process of researching and writing this thesis. This

accomplishment would not have been possible without them. Thank you.

Marwyn Vernon

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Table of Contents

1. Introduction.......................................................................................................11.1 Aimsofthiswork...................................................................................................1

2. TechnologyBackground......................................................................................22.1 PerovskiteandPerovskiteSolarCells(PSCs)...........................................................22.2 Perovskite/SHJTandemCells..................................................................................52.3 PerovskiteFilmDeposition.....................................................................................6

2.3.1Comparisonofdepositiontechnologies......................................................................72.3.2Solutionbasedperovskitedepositiontechnologies....................................................82.3.3Vapourbaseddepositiontechnology........................................................................112.3.4DifficultiesAssociatedwithUpscalingofPerovskiteSolarCells................................12

3. Methodology....................................................................................................143.1 EconomicApproach..............................................................................................143.2 EconomicOutputs................................................................................................15

3.2.1 LevelizedCostofElectricity(LCOE)....................................................................173.3 TandemCellTechnology.......................................................................................18

3.3.1 StackConfiguration............................................................................................183.3.2 ManufacturingProcess.......................................................................................203.3.3 CostofTechnology(ModuleCost).....................................................................22

4. ModelConfiguration........................................................................................234.1 ModelAssumptions..............................................................................................234.2 ModelValidation..................................................................................................24

5. ModelResults..................................................................................................275.1 ModuleCostandMinimumSustainablePrice.......................................................275.2 SensitivityAnalysis...............................................................................................325.3 EnergyYieldPotentialandLCOE...........................................................................36

6. ConclusionandFutureWork.............................................................................40

References..............................................................................................................42

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List of Figures Figure 1. Crystalline structure of MAPbX3 – perovskite cubic structure with the

formula ABX3. https://mappingignorance.org/2015/10/08/effects-of-defects-and-water-on-perovskite-solar-cells/ .............................................. 3

Figure 2. Illustration of the energy levels of typical ETL, Perovskite, and HTL materials used in the PSC research industry based on most commonly reported values in literature. Reproduced from [10]. .................................. 4

Figure 3. The two architectures are illustrated as the (a) mesoporous and (b) planar structures. The (c) inverted construction of a perovskite solar cell is also depicted. Reproduced from [16]. ......................................................... 5

Figure 4 Four-Terminal and Two-Terminal Configurations .............................. 6Figure 5 Theoretical Tandem Efficiencies as a Function of Cell Band gap [23].

Left: theoretical limits for 4T cells and Right: theoretical limits for 2T cells for variable bandgaps. ................................................................................. 6

Figure 6. Example of spin coating on a 64 cm2 glass substrate with non-uniform application. [28] .......................................................................................... 9

Figure 7. Example of application of thin film via solution based blade coating process. ..................................................................................................... 10

Figure 8. Comparison between the solution based processing technology (from NREL) and literature vapour-deposition perovskite solar cells. ................. 7

Figure 9. The most viable deposition technology in current research and potentially commercial scale with examples from [37]. ............................. 8

Figure 10. Roadmap for bottom-up costing model for proposed solar cell technology. ................................................................................................ 14

Figure 11. Example of total cost breakdown of typical monocrystalline silicone into cost components. Fixed costs shown in blue and variable costs in green. .................................................................................................................. 15

Figure 12. Breakdown of U.S. standard monocrystalline silicon cost components and minimum sustainable price with a WACC equivalent to 14%, reproduced from [38]. ............................................................................... 17

Figure 13. Full Fabrication of Monolithic Tandem Cell for Commercialization. Depicted is a p-i-n,or inverted, cell structure with optimal perovskite subcell layers chosen. ............................................................................... 18

Figure 14. Effect of device area on the PCE [16] ............................................. 20

Figure 15. CHEOPS Perovskite Silicon tandem modules; manufacturer Oxford PV ............................................................................................................. 20

Figure 16. Manufacturing Process of Proposed Solar Tandem Cell ................. 21Figure 17. Discount rates on Renewable Energy Technologies 2017 [67] ....... 26

Figure 18. Breakdown of the manufacturing costs of the production of perovskite-SHJ tandem modules. ............................................................. 27

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Figure 19. Cost of manufacturing for each comparative solar technology to the perovksite tandem. Black squares indicate the MSP - calculated or from literature. [70] ........................................................................................... 29

Figure 20. Distribution for the randomized factors in the Monte Carlo simulation. All except the labour costs and degradation rate follow a normal distribution. Those follow a log-normal distribution. ............................... 31

Figure 21. Results of the Monte Carlo simulation on the fixed total manufacturing cost ($/Wp). 95% of the values fall between 0.36 $/Wp and 0.44 $/Wp. ................................................................................................. 32

Figure 22. Total Manufacturing Costs' sensitivity to individual factors ........... 34Figure 23. Cost Sensitivity to uptime ............................................................... 34

Figure 24. Sensitive Analysis of major variable parameters within the cost model. Top half the graph shows the impact of the cost on ±10% changes for the factors. Bottom half of the graph shows the impact of technological change. ...................................................................................................... 35

Figure 25. LCOE for tandem perovskite-SHJ solar modules for residential application (~5 kW) with average Germany irradiance of 1100 kWh/m2. Left: degradation 0.25%/year, right: 0.50%/year ..................................... 37

Figure 26. Fraunhofer ISE results of LCOE for renewable energy technologies [66]. Solar PV is shown in yellow for residential, commercial, and utility scale installation and use. .......................................................................... 37

Figure 27. Reproduction of stability testing on perovskite solar cells [16] ...... 38Figure 28. Residential, Commercial, and Utility LCOE for tandem

technology ................................................................................................. 39

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List of Tables

Table 1. Input Assumptions WACC for Chinese based polysilicon production ................................................................................................. 16

Table 2. Technologies and application method of analyzed tandem solar cell. 21

Table 3. Manufacturing and associated financial assumptions ......................... 23Table 4. Manufacturing process assumptions ................................................... 24

Table 5. Material Throughput Estimations ....................................................... 24Table 6. Predictive Costs of future tandem module and associated performance

compared along with existing PERC technology. .................................... 28Table 7. Monte Carlo Simulation Input Values ................................................ 30

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List of Abbreviations

PV Photovoltaic SHJ Silicon Heterojunction c-Si crystalline Silicon CIGS Copper Indium Gallium Selenide CdTe Cadmium Telluride PERC Passivated Emitter and Rear Cell PSC Perovskite Solar Cell ET(L/M) Electron Transport (Layer / Material) HT(L/M) Hole Transport (Layer / Material) ITO Indium Tin Oxide CB Conduction Band VB Valance Band PHJ Planar Heterojuntion DSSC Solid State Dye Sensitized Cell 2-T Two Terminal 4-T Four Terminal STC Standard Testing Conditions PCE Power Conversion Efficiency ALD Atomic Layer Deposition PVD Physical Vapour Deposition OLED Organic Light Emitting Device CVD Chemical Vapour Deposition LCOE Levelized Cost of Electricity WC Working Capital MSP Minimum Sustainable Price WACC Weighted Average Capital Cost IRR Internal Rate of Return SG&A Sales, General, and Administration R&D Research and Development BOS Balance of Systems FF Fill Factor CI Confidence Interval WP Peak Watt PIB Polyisobutylene IRENA International Renewable Energy Agency IEC International Electrotechnical Commisson

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1. Introduction Photovoltaic (PV) system costs using traditional c-Si modules have decreased substantially, and as of 2017, they cost close to 1 US dollars per rated watt for large utility-scale systems ($1.03/WP) and less than 3 US dollar per rated watt for residential systems ($2.80/WP) in the United States alone [1]. For future advancements in solar technology, new materials and configurations are being investigated; however, this needs to be considered together with the total energy yield and the total system cost. The advancements in new solar technology efficiency should outweigh the total cost to ensure the technology is economically viable.

Increasing solar module efficiency can be achieved using multi-junction solar cells. Multi-junction (tandem) cells are solar cells which two or more absorber layers with selective bandgap values capture regions in the sun’s spectrum leading to theoretically increased efficiencies – even above the power conversion limit for a single-junction cell, the so-called Shockley-Queisser limit [1]. One of the most promising tandem cell technologies uses perovskite and silicon heterojunction (SHJ) solar cells in a monolithic construction. Using such a device design, it is aimed to realize efficiencies above 28% using only low temperature processes, which requires optimizing the material design of the tandem configuration [2].

Using a bottom-up cost model along with simulations of different tandem configurations’ performances, the aim is to investigate whether perovskite-SHJ tandem modules have the potential to match or reduce current photovoltaic (PV) system cost ($/WP) comparatively with current and near-future advancements in manufacturing and design configuration.

1.1 Aims of this work

The study will aim to analyse viable market driven options for the acceptance of perovskite – SHJ tandem solar cells into the commercial PV market. To realize this, the study will take a look at the current perovskite technology and optical simulations of state of the art perovskite-SHJ tandem architecture. Using simulation results and literature review for materials and performance, the cost analysis can be used to determine its economic viability. This economic analysis will include the fixed and variable cost of module manufacturing as well as the minimum sustainable price for comparison between existing PV technology on the market, such as PERC c-Si, CIGS, and CdTe. The assessment will also include an uncertainty and sensitivity analysis on important factors such as performance and stability to determine the level of research required for commercialization of this technology.

Finally, this work will determine the levelized cost of electricity to more accurately compare this potential technology with other electricity generating solar modules in residential and commercial operation within Germany.

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2. Technology Background This chapter discusses the current state of perovskite technology including the benefits as to why it makes a good absorber and top cell in a tandem construction, as well as the disadvantages. Furthermore, tandem construction and commercial upscaling options are discussed in order to present the reader with the required background to the challenges and opportunities that are investigated currently.

2.1 Perovskite and Perovskite Solar Cells (PSCs)

Perovskite has itself been identified as an excellent absorber for future solar cell technology whose performance can rival existing marketable PV technology [3]. Since 2009, perovskite solar cell technology has been researched in depth and efficiencies are now reaching 22.1% [4], i.e. those values reaching prevailing c-Si and silicon heterojunction solar cell technology.

Perovskite solar cells (PSCs) consist of an absorbent perovskite layer inserted between an electron transport layer (ETL) and a hole transport layer (HTL) forming a heterojunction solar cell when combined with electrical contacts. Metal contacts like gold or silver are typically used on the back side while transparent conductive oxides, such as indium tin oxide (ITO), are incorporated on the front side due their high optical transmission and high ability to conduct lots of free charge carriers (electrons).

Perovskite cells owe their name to the crystal structure of its absorber material: The materials class of perovskites consists of all crystals having the same structure (but possibly different constituents) as the calcium titanate (CaTiO3), found abundantly in nature. This structure is the ABX3 basic unit cubic structure, shown in Figure 1. In a solar cell context, “A” denotes the cation component typically methylammonium (MA) and/or formamidinium (FA); “B” is for the metal component mainly lead, Pb; and “X” for the halide typically Br or I. Much of the research to date on PSCs has predominately been carried out on CH3NH3PbI3 (MAPbI3); however, recently other perovskite compounds have been tested in order to increase solar cell stability.

Perovskites’ material properties in relation to solar cell application have been studied in detail and show promising optoelectric properties that would enable low cost, high throughput production at low temperatures on various substrates. The perovskite material has a high absorption coefficient across the entire visible range together with a sharp absorption onset and very low sub band-gap absorption [5]. This in addition to other properties such as a direct bandgap, long carrier lifetime and diffusion length [6]–[8] and high electron/hole mobility through the material [9] have enabled the fabrication of highly efficient solar cells.

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Figure 1. Crystalline structure of MAPbX3 – perovskite cubic structure with the formula ABX3. https://mappingignorance.org/2015/10/08/effects-of-defects-and-water-on-perovskite-solar-cells/

Beyond the perovskite layer, the electron and hole transport layers play multiple roles in the stability and performance of the perovskite solar cell. Figure 2 depicts the typical materials used for ETL and HTL within a PSC along with their respective energy levels.

First, these layers are crucial to selectively extract their respective charge carriers while restricting the other charge carrier through appropriate selection of their energetic levels. Secondly they minimize recombination at the surfaces, and lastly they need to be electrically continuous to reduce short-circuiting or shunt pathways [10].

In general, as a necessary condition, an electron transport layer should have a conduction band (CB) aligned with or slightly lower than the one of the absorber. A hole transport layer should have a shallower valence band (VB), with respect to the VB of the perovskite. Typical materials used for the ETL and HTL along with their respective energy levels are also shown in Figure 2 [10]. Early research has favoured TiO2 and spiro-OMeTAD as standard ETL and HTL materials, respectively.

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Figure 2. Illustration of the energy levels of typical ETL, Perovskite, and HTL materials used in the PSC research industry based on most commonly reported values in literature. Reproduced from [10].

There are distinctly two classifying architectures when discussing PSC device design: mesoporous and planar. The mesoporous architecture is based on dye-sensitized solar cells structure in which perovskite is layered on the surface of a nanoparticle mesoporous metal oxide film [11], [12]. This structure, called the scaffold, coupled with an organic small molecule – 2,20,7,70-tetrakis(N,N-di-p-methoxy-phenyl-amine)-9,90-spirobiuorene (spiro-OMeTAD) – as the hole transport material (HTM) or layer is analogous to a solid state dye sensitized cell (DSSC) which has exceeded efficiencies of 9% [13], [14].

A planar heterojunction (PHJ) architecture in turn does not contain a mesoporous scaffold but rather has the perovskite semiconducting layer placed in between two conducting materials – electron and hole selective layers. These discernable layers are similar to existing thin film technology such as CdTe or CIGS. This makes a PHJ architecture ideal in the formation of multi-junction cells. The planar architecture has, however, some disadvantages such as photovoltage loss due to the high density of trap states, resulting in non-radiative electron-hole recombination; and it usually exhibits more severe current-voltage (JV) hysteresis when compared to the mesoporous architecture [15]. Figure 3 shows that within the planar architecture the structure can be inverted, or denoted as a p-i-n device, in which the incoming light would enter and pass through the HTL first as opposed to the ETL.

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Figure 3. The two architectures are illustrated as the (a) mesoporous and (b) planar structures. The (c) inverted construction of a perovskite solar cell is also depicted. Reproduced from [16].

Even with their high radiative recombination efficiencies, excellent absorption and charge-transport characteristics, and their tunable bandgap, there are challenges with perovskite material for solar cell integration [17]–[21]. At this stage in research, the major issues with PSCs are stability and reproducibility. Methylammonium lead iodide (MAPbI3) is unstable making it susceptible to heat and humidity and has yet to hold up consistently to industry standard damp and heat testing. In addition, reproducibility of uniform deposition and crystallization has room for improvement still. It is clear that the choice of interfacial material and method of deposition are amongst the largest factors that influence stability and prevent commercialization.

Despite these ongoing research challenges, the use of perovskite in tandem, multi-junction solar cells has been demonstrated with a high degree of success at the lab scale [2]. Additionally, simulations have suggested that with optimizing PSC material and structure configuration, efficiencies of 30.8% are achievable [22] by minimizing optical and parasitic losses and by optimizing the perovskite bandgap.

2.2 Perovskite/SHJ Tandem Cells

Due to their high, tunable gaps, perovskite solar cells are an ideal top subcell in multi-junction solar cells. There are two major types of multi-junction solar cell constructions: the 2-terminal (2-T) and 4-terminal (4-T). In the 2-terminal configuration, there is only one top and one bottom contact. It is commonly referred to as a monolithic construction. The top and bottom cells are connected in series, meaning the total voltage will be the sum of both voltages, and the current flow between the top cell and the bottom cell will be the same even if the generated current is slightly different, a constraint known as “current matching”. In the 4-terminal configuration, individual contact layers are required and connections for the top and bottom cell. However, it offers the opportunity to harvest the power from each solar cell at its individual maximum power point. Figure 4 shows the structures of the two-terminal and four-terminal configurations. In the 4-T configuration, the top cell is perovskite and the bottom subcell is a lower band gap material, and these two cells are independently connected. Meaning, they are complete cells on their own, with corresponding front and back contacts i.e. four terminals.

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Figure 4 Four-Terminal and Two-Terminal Configurations

In the 2-T configuration the entire cell structure functions as one cell since there is only a front and a back contact. There are some benefits and some challenges with this architecture though. Beneficially, the configuration allows for a simpler electrical connection and the use of only two electrodes. The challenges arise from the current matching needed between the top and bottom cell, and therefore, how the cell operates under non-STC conditions. The highest efficiency of a 2-T c-Si/Perovskite to date is 23.6% [23]; however, the theoretical efficiency potential is much higher, almost 39% for c-Si and MAPIBr (having an ideal band gap around 1.7 eV) as shown in Figure 5.

Figure 5 Theoretical Tandem Efficiencies as a Function of Cell Band gap [23]. Left: theoretical limits for 4T cells and

Right: theoretical limits for 2T cells for variable bandgaps.

In this study only the monolithic two-terminal planar structure will be considered using PSC and silicon heterojunction solar cells. The fabrication of this tandem cell is layer-by-layer due to its monolithic architecture. Furthermore, physical deposition of perovskite thin film still needs investigation at this moment since lab scale research, and in turn deposition, prevails. The next section will discuss the challenges for upscaling this technology and present an argument for the most viable option at this juncture.

2.3 Perovskite Film Deposition

The technologies explored further relate to solution and vapour based techniques since such techniques have been proven in thin film solar cell manufacturing and exhibited minor success with the small production of perovskite solar cells. Solution deposition examples include blade coating, spraying coating, and slot-die coating; while vapour based techniques proven are thermal evaporation and atomic layer deposition (ALD).

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2.3.1 Comparison of deposition technologies

Most of the research to date for commercial deposition has been developed around solution based deposition as shown in Figure 6. However, recently vapour deposition is being considered for further large-scale application. This is because thin film application with vapour based deposition techniques are used in the OLED industry; however, this too is moving towards a solution-based solution. This move to a solution-based solution is to further reduce capital costs, higher throughput rates, and flexibility of substrate application. For this study, one technology of each deposition technique will be examined and be costed appropriately. A summary of currently the most viable deposition techniques are shown in Figure 7. Slot die coating and PVD will be examined further in this study.

Figure 6. Comparison between the solution based processing technology (from NREL) and literature vapour-deposition perovskite solar cells.

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Figure 7. The most viable deposition technology in current research and potentially commercial scale with examples from

[38].

2.3.2 Solution based perovskite deposition technologies

Ink Formulation

All solution based deposition technology requires a solvent, precursor ions, and the resultant ink for deposition. Normal precursor material is easily accessible. Finding solvents that perovskite is soluble in is more difficult. In the lab, N,N-dimethylformamide (DMF) is the most common solvent used in ink creation. However, DMF is carcinogenic and shows toxicity for reproduction, which can affect personnel during handling and therefore it cannot be used in large scale production. Research on alternative non-hazardous solvent systems is ongoing. Two promising solutions of GBL/ethanol/acetic acid (60/20/20 vol%) [26] and DMSO with co-solvent 2-MP (1:1 ratio) with 5 vol% of 1-pentanol [27] have been identified with results equivalent to reference dimethylformamide-based devices. Additionally the Oxford PV group has formulated a solvent of ACN/MA to completely dissolves the perovskite precursors and have demonstrated uniform, pinhole free films on substrates as large as 125 cm2 [28].

Once the ink has been formulated, it is ready for deposition in which there are a few solution-based technologies that can deposit the required film on a planar substrate. Lab scale deposition of choice is spin coating since high thickness and film quality can be controlled through rotation

Solution

Vapour

Lab

Method MaterialWaste FilmUniformity ModuleExample[37]

- Veryhigh

- Low

- Low

- Lowto

Moderate

- Difficultto

reproduce

- Goodwhen

optimized

- Verygood

when

optimized

- Verygood

when

optimized

13.6%(4cm2)

12.9%(40cm2)

Noreported fabricationon

largescaleasof2017.

4.57%(47.3cm2)

10%(168cm2)

12.2%(64cm2)

$$$

$

$

$$

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speed, time, and ink formulation. Through this method, high levels of reproducibility and good film uniformity are achieved. It is typically limited to a small scale application (currently <10 cm2) since a large amount of material is wasted (90%+) and would equate to high material expenditure. On larger substrates spin coating starts to no longer be economically viable and also cannot be uniformly deposited. Figure 8 shows perovskite spin coated on a 64 cm2 substrate and an uneven application can be seen. Therefore, a more reproducible and uniform application of perovskite film is necessary.

Figure 8. Example of spin coating on a 64 cm2 glass substrate with non-uniform application. [29]

Blade Coating

Blade coating is a cheap and easy application method for solution based films. Figure 7 shows an example of how the film application is distributed via the blade coating process. The blade coating applicator height is set at an adjustable height from the substrate. Besides being very cheap to implement, it is also possible to have control over film thickness and morphology. Drying of the solvent is also something important to consider and this can be controlled by either heating up the substrates to the boiling point or by applying an air flow over the surface during the coating procedure. Blade coating can also be used to deposit HTL and ETL layers.

Use of blade coating in literature has been realized on larger scale cells. More notably application has been successful on mini module size up to 100 cm2 with a PCE of 4.3% [30]. On smaller scales this has been looked at in more detail with blade coating on planar heterojunctions reaching PCEs of up to 12% [31].

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Figure 9. Example of application of thin film via solution based blade coating process.

Slot-die Coating

Slot-die coating is a solution based deposition technology that employs a nozzle head and ink-well reservoir to deposit the solution uniformly onto the substrate. This flow is controlled through constant air or fluid pressure. The nozzle head can move along in one direction at speeds up to 5 m/s. Slot-die coating has shown promising deposition for another thin film application: OLED displays. A continuous nitrogen flow over the surface during deposition helps ensure film uniformity and can control solvent evaporation rate. This is required in order to obtain good perovskite morphology. Similar to blade coating but use is much less at this stage of development since it requires large quantities of ink to fill the reservoir. However, it has higher potential than blade coating since it shows better yield and reproducibility. Recently, Qin et al. employed slot-die coating technique to fabricate all the functional layers in PSCs (except the counter electrode) and obtained a PCE of 14.7% for a device with an active area of 10 mm2 [32].

Spray Coating

Spray coating is another scalable method to fabricate large-area perovskite thin films. A typical spray coating system is composed of a pressure tank for perovskite solution and an air-driven spray nozzle. The ultrafine droplets of perovskite solution are sprayed from the nozzle and deposited on the target substrate which may be heated on a hotplate at a certain temperature. After drying and annealing process, the perovskite film is formed on the substrate.

In order to obtain a perovskite with controlled quality by spray coating, the perovskite solution concentration and viscosity, substrate temperature, the nozzle diameter and spray flow rate should be taken into consideration. A perovskite film with high uniformity, crystallinity, and surface coverage was obtained in a single step with a resulting cell PCE of 13% by Sanjib et al with ultrasonic spray-coating [33].

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Inkjet Printing Inkjet printing is also a non-contact printing process in which ink drops are deposited onto substrate evenly spaced in order to obtain homogenous thickness and uniform coverage. Temperature affects the morphology of the printed perovskite. Post-deposition process Post deposition or post-processing steps need to be considered in the upscaling of perovskite solar cell technology and require optimization in implementation and reducing processing times. One of the major post-processing steps is thermally curing perovskite precursors. In an example in literature, rapid thermal annealing by halogen lamp irradiation was used on FAPbI3 perovskite layers. FAPbI3 has better heat resistivity than MAPbI3, which led to better device reproducibility when treated with rapid thermal annealing. The optimal annealing time using the rapid thermal annealing approach was 40 s at 170 °C, a substantial decrease from the 10 mins required using conventional hot-plates [34]. Post-growth treatments that improve the reproducibility of the process and increase the process tolerance may also be the key to successfully scaling PSC fabrication. These include, but are not limited to, pulsed-light or solvent annealing. Additional success with encapsulation technology can be useful in a scale up scenario. An added fluoropolymer hydrophobic carbon electrode and/or metal oxide barrier layer, or two glass cover sheets sealed with commercial sealants (ethylene vinyl acetate or butyl rubber) have shown success in similar processes and tests.

2.3.3 Vapour based deposition technology

Vapour assisted deposition is conducted under vacuum conditions and such techniques include chemical vapour deposition (CVD), vapour-assisted sequential processing, and sublimation. Layers deposited with vacuum evaporation can be made highly pure, dense, uniform, scalable, and with good reproducibility. Layer thickness is controlled by deposition rate and time, while stoichiometry depends on temperature, pressure, and precursor ratio. In general, vacuum-processed perovskite films are prepared in a high-vacuum chamber (10-5–10-6 mbar), where the precursors are loaded in separated crucibles and heated to their corresponding sublimation temperatures. The stoichiometry and film thickness are controlled by quartz crystal microbalances (QCMs), monitoring the individual material sublimation rate as well as the overall growth of the perovskite compound. The substrate is maintained at room temperature during the deposition, and if the deposition rates of the inorganic and organic precursors are stoichiometrically balanced the perovskite can be prepared without any thermal treatment. The most employed vacuum-based technique is the dual source co-deposition of the perovskite precursors (AX, BX2). This technique is already useful commercially in the production process for OLEDs and application of thin film solar cells. Precursors have high sublimation temperature leading to control of deposition rate and uniform, homogeneous thin films. However, it is difficult to control the MAI sublimation and therefore, this has led research to develop other techniques such as sequential-partial pressure, solution and vapour (CVD), and single source. Although vapour-phase deposition has the potential to be used to deposit

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perovskite thin films over large areas, these methods usually require more sophisticated vacuum equipment and longer processing times, which could potentially hinder their application for the low-cost fabrication of PSCs. An important step in the development of perovskite devices was the demonstration of an efficient (17.6%) fully vacuum-processed solar cell, with the thin-film absorber obtained by controlling the partial pressure of MAI during the conversion of an evaporated PbI2 film [35]. A similar method has been used to prepare monolithic perovskite/Si tandems with 20.5% PCE, using a single-side-textured silicon heterojunction solar cell [36], [37]. Much less research has been done to date with vapour based deposition of perovskite in comparison to the solution based alternative. As such no studies on using mixed-cation, halide perovskites have been reported thus far. Another vapour deposition technique available is atomic layer deposition (ALD). ALD is a low-vacuum technique that can be used to prepare uniform, conformal coatings with atomic-thickness resolution. It has been realized in the commercialization of CIGS cells and in other film technology.

2.3.4 Difficulties Associated with Upscaling of Perovskite Solar Cells

Currently, perovskite/tandem solar cell technology is not optimized for commercialization at this time due to a few limitations that need to be addressed at the research level. These are the topic of recent research and are being addressed quickly. Due to the fact that SHJ is a mature technology in the solar industry, these limitations are innately connected to the perovskite material and perovskite solar cell technology in combination with the monolithic tandem cell design. These limitations are associated electrical, cell-related, and tandem specific elements of the system.

Electrical limitations arise from hysteresis of the JV curve of PSC and perovskite/tandem solar cells and through poor deposition. Hysteresis is the phenomenon in which the measured power conversion efficiency during testing are inconsistent depending on the direction they measured. Therefore, the “true” PCE or in turn the total power generation is unknown or variable. Low to negligible hysteresis is required for the commercialization of solar cells since power generation values such as watt peak from PV modules must be precisely quantifiable with a high degree of reproducibility. There are two aspects that impact JV hysteresis in perovskite solar cells. The material should be physically and thermally stable where in the case of MAPbI3, MA is bound loosely to Pb and is thermally unstable. A design of a hysteresis-free perovskite should be investigated that is more stable thermally. Another aspect to hysteresis has to do with the layered materials as well as the perovskite material itself. Typically, heterojunctions with PCBM and polymer HTL provide high-efficiency performance without hysteresis [24].

Furthermore, a major electrical limitation to commercialization of perovskite cells, and in turn perovskite/SHJ tandem cells, is the large-scale deposition of the perovskite material. Currently as described before, lab scale deposition of perovskite uses spin coating for uniform application on the surface. However, this technique does not scale well to large area cells (> 10 cm2). Other thin film deposition techniques are viable options for perovskite deposition. Most importantly these techniques need to provide time for high quality crystallization of the perovskite material and a homogenous film morphology (no pinholes). Development of pinholes in the film promotes paths of low shunt resistance between the electrodes of the solar cell lowering the

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maximum open-circuit voltage and fill factor [25]. The deposition technologies explored previously relate to solution and vapour based techniques since such techniques have been proven in thin film solar cell manufacturing and exhibited minor success with the small production of perovskite solar cells. However, this needs to be proven at large scale and with high reducibility.

In addition, cell stability issues need to be addressed at the research level and demonstrated in order for perovskite/tandem cells to be commercially successful. Limited stability of the traditional perovskite compound (MAPbI3) under heat caused operation of the solar cell in real life situations to be unrealistic. Recent research with multi-halide, cesium doping perovskite material makes the perovskite more inherently stable. Also, the commonly used HTM spiro-OMeTAD has intrinsic stability issues that make commercialization difficult from a longevity and economically viability standpoint. Optimization of perovskite, selective layers and configuration (n-i-p, inverted) still needs research for the stability and commercialization aspects.

While evidence of successful scale-up of single junction cells and tandem cells with perovskite do exist, most of these technologies have experienced some drawbacks and the optimal process has yet to be realized. With analysis of the different deposition methods, the main areas of interest are such to prevent shunt resistances, high voltage loss, and maximize stability of the solar cell. These problems generally are a result of non-uniform film deposition, as discussed before. Additional information like encapsulation and lifetime are also areas of interest since this is a requirement for the development of highly efficient and production scale modules. Through these categories, the ideal deposition process can be realized as one with high application efficiency, uniform distribution, minimal defects, i.e. uniform film morphology, optimal device stability and minimized hysteresis effects.

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3. Methodology This section contains the economic methodology and technological approach for realizing the economic viability of perovskite/tandem solar cells. With regards to the technology used, assumptions were made to the best of the ability with the research to date.

3.1 Economic Approach

A bottom-up cost model is utilized to determine the associated cost and estimate an appropriate range of pricing for perovskite/SHJ solar modules at commercial production scale (>100 MW/year). To achieve the final outputs in determining the economic viability of this technology, initially the key “cost drivers” are identified. The key cost drivers in this economic analysis are the proposed solar cell technology, the manufacturing location, and the manufacturer’s capital structure.

The solar cell technology is described in detail in the next section with underlying assumptions that are applicable to current research endeavors. These assumptions, especially those in terms of thin film technology and deposition methods, are subject to change in the near future since perovskite solar cell technology is still in the research phase. The manufacturing location and capital structure are discussed in further detail in the next section as well but reflect the current trends in solar module production.

With the key cost drivers in place, the cost model categorizing all the necessary inputs that factor into the module cost such as the manufacturing process, direct and indirect labour costs, and tax rates. These steps are considered for every processing layer of the solar module to reflect an accurate price point.

However, the minimum sustainable price (MSP) for the perovskite/Si tandem solar cell alone does not reflect its economic viability into the residential or commercial PV sector. The price point for the new technology neglects two crucial components: the degradation or lifespan of the perovskite material and energy production over its lifespan in operation. These factors are taken account of when calculating the levelized cost of electricity (LCOE) and are valuable in making an accurate comparison between two, or more, existing technologies.

Figure 8. Roadmap for bottom-up costing model for proposed solar cell technology.

ProposedSolarCellTechnology

ManufacturingLocation

Manufacture’sCapitalStructure

KeyCostDrivers

ModelCostCategories&Inputs

ManufacturingProcess• EquipmentandFeedstock• UtilityRequirements• DepreciationofFacilitiesand

Equipment• Labour &Yield• Annualmanufacturingcapacity

Rates• CorporateTaxRates• ElectricityCost• WeightedAverageCapitalCost

(WACC)

ModelOutputs

FixedCosts• DepreciationExpense• SG&AandR&D

VariableCosts• MaterialCosts• Labour Costs

• ElectricityCosts

ProfitMeasures• GrossProfit• EarningsBeforeIncome

Tax(EBIT)• OperatingMargin

MinimumSustainablePrice(MSP)andLCOE

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Finally, since this analysis is an approximation of the costs in the present or near future, the values presented are not absolute and it is necessary to consider the sensitivity and uncertainty of these figures. The sensitivity of the inputs for major unknowns such as the capital cost of cost and material costs for the application of the perovskite top cell will be investigated. Additionally, to provide more clarity into what the range of cost would be, given the variability of values within each costing category, is investigated using Monte Carlo analysis.

3.2 Economic Outputs

This aforementioned “bottom-up” approach to the cost model is employed using the manufacturing costs of the consumables and assumptions for manufacturing processes based on work from Powell [39], Goodrich [40], and Woodhouse et. al [41], [42]. The upfront cost for manufacturing (price of the factory building and equipment) is called the “capital expenditure” (capex) and is usually expressed in dollars per-unit watt ($/W). The definition of capex according to accounting practices is the sum of physical property, plant, equipment, engineering, procurement, and construction of the facility itself. This is the fixed costs associated with the manufacturing facility. The variable cost – also called the working capital (WC) – deals with working materials and required labour. The total investment in a PV manufacturing facility is the sum of the fixed and variable costs as shown in Equation 1.

!"#$#%&!"()*$+)"$ = -#.)/01*$ $3

+ 5%6#%7&)01*$ $3

(1) An example of the total fixed and variable costs for a PV manufacturing plant is shown in Figure 9 below. Depreciation represents the capex for fixed equipment and facilities allocated over the lifespan of the equipment/building per yearly allowed expense. Typically, this follows a straight-line depreciation fixed expense.

Figure 9. Example of total cost breakdown of typical monocrystalline silicone into cost components. Fixed costs shown in blue and variable costs in green.

The successful operation of the PV manufacturing facility requires the sale of the panels for a certain price. The idea of the minimum sustainable price, or MSP, is not equivalent to the manufacturing cost. With any investment, a return on investment is expected based on the current economic environment and risk undertaken. The weighted average capital cost (WACC) is the opportunity rate of return that an investor expects to earn on projects with similar risks and capital structures.

0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1

CostBreakdown(PV)

CostofManufacturing($/Wp)

Materials Labour Electricity Depreciation Maintenance

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WACC is location specific and depends on the availability and cost of debt. For PV manufacturing facilities it is estimated that the WACC for Chinese manufacturing of panels was 14% back in 2016 [42]. In this study, a rigorous calculation is conducted using updated photovoltaic market values for 2018 resulting in a WACC of 12% (11.9%). Using the formula shown in Equation 2; where E is the market value of equity, re is the cost of equity, D is the market value of debt, rd is the pre-tax cost of debt and T is the corporate tax rate; it can be seen that WACC is the cost balance between how heavily the company is leveraged in respect to the amount and cost of equity available. These input values are included in Table 1.

8900 = : ∗ 6< + = ∗ 6> ∗ (1 − B) (2) [43]

Table 1. Input Assumptions WACC for Chinese based polysilicon production WACC Inputs for Chinese based polysilicon production Parameter Value Source Industry’s debt-to-equity ratio D*/E* 0.925 [44] Cost of equity re 18.5% Calculated Average regional unlevered beta bU 1.19 [45] Regional relevered beta b*E 2.13 Calculated Government bond yield curve rate rg 3.70% [46] sovereign default spread rd 0.81% [47] estimated country risk-free rate rf 0.0289 Calculated estimated corporate spread S 3% [48] estimated cost of debt (pretax) rd 0.0549 Calculated effective corporate tax rate rt 15% [49] weighted average cost of capital WACC 11.9% Calculated

The MSP of a PV module is defined as the minimum selling price ($/W) at which the rate of return for the manufacturer, internal rate of return (IRR), equals their WACC. Operating expenses, including Sales, General, and Administration (SG&A) and Research and Development (R&D), taxes, and the profit required to generate the required return on the initial capex and working capital investment expend a portion of the gross profit. The IRR is the rate of return generated by a series of cash flows, such as an initial cash outflow required to construct a manufacturing facility, followed by subsequent cash inflows generated by modules sales. The business objective is to complete projects that have an IRR that is greater than their cost of money (WACC). Figure 10 below shows the final output related to the cost, price, and operating margin. Final prices can be compared on what the market is willing to pay. The MSP for perovskite/silicon tandem cells will be compared against existing and near future PV technology on the market such as PERC, CIGS, CdTe and thin film tandems.

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Figure 10. Breakdown of U.S. standard monocrystalline silicon cost components and minimum sustainable price with a WACC equivalent to 14%, reproduced from [39].

3.2.1 Levelized Cost of Electricity (LCOE)

In comparison to other processes of generating electricity, there needs to be a systemized way to look at electricity generation through the lifespan of the power generation technology. This is done through the levelized cost of electricity (LCOE) or the cost per unit of electricity produced. The LCOE can be calculated using the formula seen in Equation 3:

D0E: = FGHIJ G

KGLM

NGHIJ G

KGLM

(3) [50]

Where: LCOE = the average lifetime levelized cost of electricity generation; Ct = Total MSP for solar panel; Et = electricity generation in the year; r = discount rate; and t = life of the system Once the model has evaluated the MSP of tandem solar cells it can be used to determine the LCOE which is location specific and dependent on local solar irradiance, module operating temperature, system discount rate, and local incentive structures. The LCOE will be used to compare against the local monocrystalline silicon PV modules and major local electricity producing plants. Once again, the two major components in this LCOE calculation are the efficiency which denotes the yearly energy production of the system and the degradation rate (lifetime of the system) which is related to the material properties, encapsulation technology, and local environmental conditions (heat, humidity, etc). These parameters will be varied to see how they change the LCOE value and find the area in which this technology is potentially economically viable. For simplicity of this assessment, the balance of systems (BOS) will be remain the same as for a system within the residential, commercial, or utility sector with the same area or power associated costs.

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3.3 Tandem Cell Technology

3.3.1 Stack Configuration

This assessment will focus on a single tandem structure with perovskite and SHJ in a monolithic architecture shown in Figure 11. Ideally to minimize energy loss and maximize power conversion efficiency (PCE), the band gap of each subcell needs to be tuned. This corresponds to a bandgap for the top subcell between 1.5 – 1.8 eV and the bottom subcell bandgap of 0.9-1.2 eV [51] (Silicon having an indirect bandgap of 1.1 eV). Further optical simulations have confirmed that the top subcell should have an even more precise bandgap for optimal efficiency, that between 1.7-1.75 eV [22]. With the tunability of the perovskite material bandgap based on mixed halide selection this can be achieved.

Using a p-i-n or an inverted structure leads to a stable top subcell and also reduces the parasitic absorption present in other n-i-p structures since the layers are thinner and can be constructed without spiro-OMeTAD [22]. This can be seen in the EQE of the two types of cells [22]. The inverted structure also has been seen to reduce hysteresis effects within the structure and leads to constancy in the maximum power point.

Figure 11. Full Fabrication of Monolithic Tandem Cell for Commercialization. Depicted is a p-i-n,or inverted, cell structure with optimal perovskite subcell layers chosen.

With regards to HTL application, NiO and PTAA have been tested as successful alternatives to spiro-OMeTAD. PTAA has been used here at HZB for the creation of inverted tandem largely because of higher voltage obtained in comparison to NiO and due to the lab scale deposition of spin coating. NiO is very stable but inhibits full voltage potential in the cells even with annealing temperature around 300°C. However, PTAA is too expensive for commercialization costing 1903.50 USD/g [52]. NiO has been used before in an inverted

SHJTCO– sputteredandlaserscribed

SnO2 – ALDprocess

Cs-MixedPerovskite[…]– BladeCoating

PCBM– ThermalEvaporation

NiO – ThermalEvaporation

ITO/LiF – Sputtered&ThermalEvap

(a)HTM

(b) Perovskite

(c) ETM

(d) Silicon(SHJ)

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tandem structure and costs about 1% of PTAA. It will be investigated whether or not this high cost for PTAA has an impact on the final cost of the tandem structure since the amount of material consumed is small on per cell manufactured basis.

The ETL observed to work in the inverted structure uses either a combination of SnO2 and PCBM or C60 as the electron selective materials. Previous studies have shown that a thin layer of PCBM in between SnO2 and perovskite increases efficiency [53]. At present, Oxford PV has filed for patents regarding the inclusion of an organic based material in contact with the perovskite layer limiting hysteresis and surprisingly providing more stability than a metal oxide layer like TiO2 under simulated UV light [54]. In addition recent studies have shown that LiF acts as a shunt-blocking layer similar to how thin, insulating, silicon oxide layers have been employed previously in thin-film silicon solar cells to block shunt pathways and increase fill factor (FF) [55]. These layers have good electron extraction properties while reaching high optimal transmission.

A Cs-mixed cation perovskite will be used since it has been demonstrated to offer better stability and reduced effects of degradation. The cell was held under industry standard damp, heat testing 1000 hrs with no degradation. Normal industry standard encapsulation also used. Currently this is achieved with CsFA perovskite having a bandgap of 1.63 eV and a PCE of 23.6% [35]. For example at HZB, the perovskite used is mixture of CsMAFA in a 5:1 ratio of FA to MA and 5% cesium iodide.

Mixed cation lead mixed halide perovskite presented in [53] shows a photostable material, [HC(NH2)2]0.83Cs0.17Pb(I0.6Br0.4)3, with optimal band gap of 1.74 eV reaching an open circuit voltage of 1.2 V. Hypothetically combining this in with the configuration from [35], the potential PCE would be 26.7% (1.2 V + 0.67(SHJ) V = 1.87 V (tandem) * 18.1 mA/cm2 * 0.79 FF). However, with higher bandgap potential, the thickness of the perovskite layer needs to increase since less current is generated – in the range of micro meters rather than nanometers. This may restrict certain thin film deposition methods.

Optical simulations conducted on tandem cell operation under simulated visible light have shown that a reduction in parasitic absorption, thinner films using an inverted structure, and an optimal bandgap perovskite of 1.75 eV could potentially obtain a PCE of 30.8%. For costing purposes, efficiency levels on the module level will be taken as a 3 absolute percentages lower than the cell level efficiency since there will be dead area and shading effects to take into account, amongst higher series resistance and lower shunt resistance. The different types of solar cells all follow an apparent inverse scaling law whereby the absolute PCE value decreases by about 0.8% when the device area increases by an order of magnitude as shown in Figure 12.

Therefore, module efficiencies of 21%, 24%, and 28% will be utilized, for further analysis, corresponding to previous literature testing and optimal simulations.

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Figure 12. Effect of device area on the PCE [16]

3.3.2 Manufacturing Process

Oxford PV currently is working on a commercial process of producing tandem perovskite-SHJ solar cells. The process uses vapour based deposition as seen from the preliminary inventory list in Figure 13. This study will look at the equipment surrounding of the deposition of the layers for the tandem solar cell shown in Table 2 and seen in literature [56]. As stated previously, the application of the perovskite layer will be analyzed for both PVD and Slot die Coating deposition methods. The most cost-efficient method will be taken for further analysis and comparison using LCOE.

Figure 13. CHEOPS Perovskite Silicon tandem modules; manufacturer Oxford PV The fabrication of SHJ can be found in more detail in [57] and was used as the bottom cell component. From the SHJ layer, ITO is sputtered on top with the NiO HTL layer deposited next using ALD technology. Two types of perovskite deposition are of interest: solution based using 1-step deposition and pulse light-annealing and vapour deposition with PVD technology. Between the perovskite and ETL is a thin layer of PCBM deposited via PVD. Then another ALD layer of SnO2 as the ETL, finally, topping off the additional ITO layer via sputtering. This manufacturing process is depicted in Figure 14.

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Layer Thickness (nm) Application Function

Ag front grid - Screen printing Front grid

Indium Tin Oxide 100 Sputtering Top contact layer

Tin Oxide 15 Sputtering Electron transport material

C60 30 PECVD Passivation

Cs-Mixed Perovskite 400 PVD/Slot die Coater Absorber

Nickel Oxide 30 ALD Hole transport material

Indium Tin Oxide 35 Sputtering Recombination junction

n-a-Si:H 8 PECVD Front surface field

i-a-Si 5 PECVD Passivation

n-Si 160 x 103 Wafer manufacturing Silicon substrate

i-a-Si 5 PECVD Passivation

p-a-Si 8 PECVD Back surface field

Ag rear contact 200 Sputtering Back electrode

Table 2. Technologies and application method of analyzed tandem solar cell.

Figure 14. Manufacturing Process of Proposed Solar Tandem Cell

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3.3.3 Cost of Technology (Module Cost)

The cost analysis performed is completed on a stable tandem perovskite/silicon structure at a hypothetical PV manufacturer in China starting operation in 2020. This calculation is using the latest version of the MIT – costModel Powell spreadsheet, that is modified to calculate the costs for silicon heterojunctions and perovskite solar cells rather than for c-Si [58]. It is considered to manufacture PV modules of these tandem cells at production volume of 200 MWP per year at a module size similar to that of silicon modules (60 cells – 1.64 m2 total module area). To provide a realistic and accurate valuation, we chose a relatively conservative approach for developing a cost estimation, and analyzed the uncertainties of the most sensitive assumptions.

The manufacturing cost (MC) per unit area of the perovskite module is calculated by adding up the costs of the steps in the individual manufacturing process:

O0 = (OP + QP + DP + :P + =P)P (3)

where Mi is the cost for materials, Ui is the utility associated with producing that individual step, Li is the engineering and production line labour, Ei is the equipment maintenance and Di is the depreciation of the equipment.

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4. Model Configuration This section explains the way in which the cost model was constructed and the major underlying assumptions that define the final results. Finally, the model constraints from current and future trends within the solar industry and financials surrounding solar modules are discussed.

4.1 Model Assumptions

The costing model, due to the fact that this solar technology has not reached commercial scale yet, relies on numerous assumptions with the most important ones being addressed here. As shown in the economic roadmap for the model, the manufacturing location and capital structure are important and are the basis for financial calculations. Values for the length of depreciation, labour and electricity cost, tax rate, building cost, and additional R&D/SG&A are dictated by the manufacturing location. As such this study defines the location in China where the bulk of manufacturing of traditional silicon based solar cell manufacturing exists today. Whilst comparing this with other forms of technology it is important to understand where they are manufactured since the cost of production varies from location to location. Shipping costs have been neglected in this study for simplicity as they do not add a significant amount to the total overall cost [40]. A summary of the manufacturing location assumptions and associated values can be seen in Table 3 below.

Table 3. Manufacturing and associated financial assumptions Manufacturing Location: China

Parameter Value Units Source

Plant size 200 MW/year Depreciation Equipment and Facilities

10 years [49]

Building 20 years [49] Labour Costs 4.50 / 5.10 $/hr [operator / supervisor] Corporate Tax Rate 25 or 15* % [59] Building Cost O&M 3 / 5 % of capital expense

[building / equipment] [42]

R&D** 9.40 % [42] SG&A** 1.10 % [42]

* 15% for qualified enterprises encouraged by the Chinese government **Estimates of R&D and SG&A based on past models and companies

Additional assumptions besides the manufacturing location and associated financial values are required. These assumptions are in line with the operation of the solar production including uptime, equipment application efficiency, and silicon usage. These assumptions are summarized in Table 4 below.

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In Table 5 material throughput was also estimated based on the past experiences of thin-film deposition technology and acceptable practices for throughput rates [58]. The throughput for each deposition technology was then calculated based on the thickness of the applied film and the corresponding rate. The lowest throughput was determined to be the minimum rate that each factory line could sustain: the rate determining step. Then the number of lines was based off the fact that the minimum throughput without dramatically impacting manufacturing cost would be 1.0 m2/min. With each increase in throughput, the manufacturing cost decreases however it is less of a factor past the 1.0 m2/min point. Typical thin-film manufacturing is approximately 1.44 m2/min [60].

Table 4. Manufacturing process assumptions Panel size : 60 cells; 1.64 m2

Parameter Value Units Source

Silicon wafer size 156 x 156 mm x mm Industry Standard

Plant uptime 96 % [57]

Processing yield of Silicon

92 % [57]

Encapsulation Method

Glass-glass with EVA (or polyolefin alternative) encapsulant

[61]

Table 5. Material Throughput Estimations

4.2 Model Validation

The MIT – costModel Powell spreadsheet was validated personally for silicon heterojunction cells in reference to a previous cost analysis conducted in 2016 [57]. From there, the model was used in combination in ITRPV to approximate costs for SHJ solar cells in the near-future (2020) [62]. This cost reduction is due to usage of thinner silicon wafers (from 180 microns to

Thickness(mm) Technique Rate Throughput(m2/hr) NumberofEquipmentReq'dAgITO 100 Sputtering 1-10A/s 27.8 3SnO2 5 PECVD 20min/mod 20.85 3C60 10 Evaporator 20min/mod 20.85 3

NiO 28 S-ALD 2.4mm/min 139 1ITO 80 Sputtering 1-10A/s 27.8 3

3(4)4.2mm/s(2-10

nm/min)SlotdieCoater

(PVD)

PerovksiteSolarCell

Perovskite 400 27.8

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160 microns), the adoption of diamond wire slurry technology in order to slice the ingot and in turn reduce kerf loss, lower amount of high costing materials such as silver paste and reduced module glass thickness, and higher achievable efficiency (23% vs 20%). This led to a cost reduction from 0.60 $/W (101.55 $/m2) in 2016 to an approximate value of 0.38 $/W (75.97 $/m2) in 2020. After the validation using the trends in ITRPV, it was time to apply the costs associated with the perovskite layer.

The amount of material used in the perovskite layers is calculated from the simulated layer thickness [2] and the density of material across the useful area of the module. The perovskite precusors could be supplied per kilogram by the GreatCell Solar company, formally called Dyesol, and the interstitial layers are costed at the highest attainable bulk amount in terms of weight or volume. In regards to the perovskite absorber layer, the stoichiometry of the film is determined and is based on the required amount for production from bill of materials from the CHEOPS preliminary report [63]. Material usage is taken into account during the application of the layer as well. For instance, the deposition of perovskite via spin coating is lower than deposition with either a slot die coater or PVD since it is in fact less efficient on large areas and there is some material wasted in the process.

The time it takes for application of these layers is crucial to further reducing the cost. The parameter “Deposition Throughput” was incorporated into the model to highlight the major differences that deposition speed has an on the final cost and price between solution and vapour based applications.

The cost for the application of the materials is also dependent on the cost of electricity consumed for each production step. The highest amount of electricity for this process is during the formation of the silicon ingot. Combined, the electricity cost and the capital cost from the formation of the silicon ingot amounts to approximately 10 USD/m2 of the total cost.

Equipment costing for the initial capital cost was based mostly on data from 2016 [57] since it was difficult to gather updated costs from manufacturers. Future costs would only leave room for further reduction in cost and/or leave room for innovation which would reduce overall costs. Since the cost of the equipment is uncertain, a capital cost range is considered in the Monte Carlo analysis. Attention was made to remove equipment from the list that was no longer required for this particular SHJ construction and to include the additional deposition technologies for the top cell component. The equipment was depreciated over the respective depreciation period for equipment and facility costs as previously shown in Table 3.

The MSP is determined using discounted cash flow (DCF) and Net Present Value (NPV) analysis in order to provide the value at which the amount of return is equal to the WACC. In other words, the estimated cost to the customer at which the return equals the cost associated with investing it at 12%. This method of calculating the cost of renewable energy technologies is based on discounting financial flows to a common basis, taking into consideration the time value of money.

The cost of electricity takes into account not only the minimum sustainable price but also for the balance of systems (BOS) for the supporting structure and installation. The BOS for a photovoltaic system is split into three areas: costs that scale with power, costs that scale with area, and fixed costs. Initially BOS data was verified from the NREL and taken from the most recent year 2017 [1], [64]. These are used as estimates into the new tandem configuration. In the US, high BOS costs across the board have resulted in slower cost reductions than in other markets. However, excellent solar resources mean that the LCOE of utility-scale projects in

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the US is not significantly higher than in other markets. However, more precise data on the utility BOS cost for Germany (2014) is approximately 0.53 USD/W [65] for a 1 MWP ground mounted solar project (0.45 €/WP). For residential and commercial installations <10 kW and between 10-100 MWP respectively, the BOS costs are naturally higher. Residential costs around this time are about 1.15 USD/WP (0.98 €/WP) and commercial costs are approximately 0.77 USD/WP (0.66 €/WP) [66].

A rough estimate of how the cost of BOS will change for multi-junction solar cells is used in this study. As the efficiency of the PV modules increases, the required area per WP of installed system capacity and the related BOS price of the system decreases. In 2020 using the estimation for c-Si CAPEX development approximates BOS costs for residential systems to be around 1.00 USD/WP [66]. The costs for the commercial and utility BOS decrease accordingly as well.

LCOE final cost also takes into account the lifetime O&M costs for the installation and ongoing maintenance. For residential, commercial, and utility scale module installations have been reported to be between 33.21, 23.98, 18.92 USD/MWh in 2015 [67].

Discount rate is also a factor and represents the interest rate for the present value of money. In Germany for renewable energy technology production, the discount rate is between 3.5% [68] and 4.25% [69]. The unlevered value of 4.25% was used in this analysis for a conservative calculation and is shown in Figure 15. Using specifically determined discount rates based on the technology, leads to a more accurate representation of the real LCOE.

In terms of where LCOE calculations and comparisons are concerned, it has been concluded that changes in volume growth, learning rate and exchange rate have a relatively small effect (within about +/- 10%) on PV LCOE. The cost of capital (WACC percentage) is by far a more significant factor in PV LCOE than the CAPEX itself [66]. Therefore, for comparison between existing technology and the perovskite-SHJ tandem modules, it is important to find LCOE data using similar WACC values as the cost of additional CAPEX from manufacturing additional layers pose less of a factor.

Figure 15. Discount rates on Renewable Energy Technologies 2017 [69]

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5. Model Results Using the methodology from Section 3 and the costing model described in Section 4, the final tandem cost and minimum sustainable price are obtained in this section. Furthermore, the sensitivity to underlying variable assumptions and major influences to the cost and price point is evaluated in order to determine the confidence in the model results.

5.1 Module Cost and Minimum Sustainable Price

Looking now at the manufacturing cost in more detail of perovskite-SHJ tandem modules, we can see that the cost can be broken down into five major areas, shown in Figure 16. The breakdown includes the cost for maintenance, labour, utilities, materials, and depreciation as shown in Formula 3. Depreciation accounts for the capital cost of equipment associated with deposition and production, depreciated over the allowed timeframe as set by the Chinese government as stated in the assumptions section.

Material costs represent about two-thirds of the cost with the capital cost of equipment is the next largest cost at 18% of the total cost. Breaking down the material cost further it can be shown that the additional cost of perovskite and associated layers contribute only 12% of the total material costs. The perovskite precursors, inks and interstitial layers are not expensive and increasing the demand to be able to purchase in bulk, would reduce the costs but not substantially. This is because majority of the material cost is already inherently built in the cost of manufacturing silicon solar modules such as the cost of metal paste, glass, and encapsulation.

Figure 16. Breakdown of the manufacturing costs of the production of perovskite-SHJ tandem modules.

Table 6 shows the cost of the perovskite-SHJ tandem solar modules and other comparable technology in terms of manufacturing cost in $/m2 and $/WP and the market minimum sustainable price in $/WP. Since the efficiency is variable, it is more comparable to evaluate the technology manufacturing cost is in terms of $/m2. Therefore, the four tandem cell

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technologies within Table 6, whose only differing attribute is the PCE variances, have a total manufacturing cost of 97.15 $/m2. Comparing this with silicon heterojunction technology, it can be seen that the difference is the cost of producing additional layers in the modules, an additional 21.18 $/m2. This is lower than the theoretical cost of production of perovskite solar modules on their own [60] since the cost of contacts and encapsulation are already included into the cost of manufacturing the SHJ modules and only account for the production of additional layers for the perovskite absorber layers.

Table 6. Predicted Costs of future tandem module and associated performance compared along with existing PERC & SHJ technology.

Configuration PCE (%) Total Cost

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Source

Perovskite-SHJ Tandem 21 0.46 97.15 0.60 Model

Perovskite-SHJ Tandem 24 0.41 97.15 0.53 Model

Perovskite-SHJ Tandem 28 0.35 97.15 0.45 Model

Perovskite-SHJ Tandem 31 0.31 97.15 0.41 Model

SHJ - 2020 23 0.38 75.97 0.49 Model

PERC (2018) 21 0.4 72.73 0.56 [70], [71]

The future cost of PERC could not be determined and so it is reported as it appears in the 2018 market. Therefore, the comparison is not exact since future PERC modules will also benefit from of the expected cost reductions inherent in the perovskite-SHJ tandem model (thinner wafers, etc.). It can be seen that SHJ modules and higher efficient tandem modules are expected to be cheaper in terms of module price and have the potential to surpass PERC modules. This is especially true for tandem modules since they generate higher energy yields for the same lifetime due to their higher efficiencies. The threshold where the price of the tandem module is cheaper than the PERC module is around 24% efficiency. Add same comparison to the SHJ module, between 24 and 28% efficiency. Figure 19 shows the manufacturing cost comparison between existing thin-film and silicon technologies already or soon to be in the market. Thin-film tandem are also included even though they are not already on the market to provide another layer of comparison. Thin-film technology in general is cheaper from a spot price perspective since the material and cost of fabrication is quite low compared to silicon based modules. The five additional solar module technologies are lower in cost except for SHJ, which is created with mature solar technology.

The thin-film technology, tandem and single junction, costs less to make and can be therefore priced at a lower MSP. The thin-film tandem is approximately the same efficiency and costs about 10 cents per Watt cheaper given the cheaper bottom cell construction. This makes it a more cost effective solar module compared to the SHJ-perovskite tandem. However, when compared to the existing silicon competitor, it is comparable in cost with the tandem at a higher efficiency. This gives the tandem module potential to be more economically viable if it can

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operate over a typical silicon lifespan (25-30 years) since it will produce more energy over its lifespan.

Figure 17. Cost of manufacturing for each comparative solar technology to the perovksite tandem - calculated [Calc] or from literature [#]. Black squares indicate the MSP.

The manufacturing costs and minimum sustainable prices produced by the cost model are developed based on one value for each variable category. For estimation, this proves to be not extremely valuable when the value itself has a degree of uncertainty attached to it. In order to understand how the variability in the variables affect the overall manufacturing cost can be determined via a method known as the Monte Carlo analysis. A Monte Carlo simulation was conducted in order to determine how the changes in key parameters together affect the overall cost of production for the tandem cells. In essence, the Monte Carlo simulation is a stochastic method, repeated random sampling, to obtain a deterministic result. Each factor that is altered in the system is randomized to reflect the probability function and behavior of that factor. By using probability distributions, variables can have different probabilities of different outcomes occurring. Probability distributions are an informative method for describing uncertainty. These probabilities are chosen based on literature [73] and the nature of the factor themselves. The random variables and their corresponding distribution type are shown as the simulation input in Table 7 and Figure 18. Most of them assume a normal distribution centered around the mean for each factor. The resulting range of all calculation results form a distribution from which uncertainty information can be derived with basic statistical methods. In this way, Monte Carlo simulation provides a much more comprehensive view of what may happen. It tells you not only what could happen, but also how likely it is to happen. In this work, we use 10,000 iterations for the uncertainty analysis.

The results from the Monte Carlo analysis are based on the assumption that all the factors are independent from each other. This is not entirely correct since for example the type of encapsulation will affect the degradation rate and perhaps the PV equipment costs; however, it is appropriate assumption for initial research purposes.

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Table 7. Monte Carlo Simulation Input Values

Random Variable Distribution Type

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Module Efficiency Normal 24% 21% 28%

Labour Costs Log-Normal 4.2 $/m2 3 $/m2 7 $/m2

Electricity Cost Normal 5 $/m2 4 $/m2 6 $/m2

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Capital Cost Normal $16.2*106 $14.2*106 $18.2*106

Encapsulation Cost Normal 3.7 $/m2 3 $/m2 4.7 $/m2

Degradation of PV Modules

Log-Normal 0.5 0.25 1.0

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Figure 18. Distribution for the randomized factors in the Monte Carlo simulation. All except the labour costs and degradation rate follow a normal distribution. Those follow a log-normal distribution.

The results of the probability distribution for the manufacturing cost based on 10,000 randomized iterations and using a module efficiency at 24% as reference can be seen in Figure 19. The overall cost of the tandem solar cell varies from 0.34 to 0.47 $/W. For the tandem module, the manufacturing cost determined initially is 0.41 $/W, therefore, the uncertainty accounts for approximately ±15% of the cost.

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Noting that a 95% CI shows that the manufacturing cost for the tandem cell falls between 0.36 and 0.44 $/W or about 0.41±10% $/W. This shows that the original estimation of the parameters are good approximation for the cost of these materials, the uncertainty is relatively low.

Figure 19. Results of the Monte Carlo simulation on the fixed total manufacturing cost ($/Wp). 95% of the values fall between 0.36 $/Wp and 0.44 $/Wp.

5.2 Sensitivity Analysis

Denoting which variables contribute the overall manufacturing cost is one step in identifying areas in which researchers can devote their time and energy. However, using a cost model with fixed values can fall short when these values are no longer accurate. In this case we can determine how the manufacturing cost would react to such changes – how relative changes in the variable costs affect the overall manufacturing cost. This is done through a sensitivity analysis. The material cost has the highest contribution to the overall manufacturing cost of which perovskite only accounts for a small portion. However, it would be beneficial for this study to see how the cost reacts to changes in perovskite material expenditure (i.e. in the case of new technology that is more or less expensive). The next biggest expenditure is the depreciated cost or the cost associated with the capital cost of equipment. And overall the efficiency and uptime of the factory all play a big factor in the overall cost of the module. Once again, a sensitivity analysis can determine the effect of each component on the overall manufacturing cost.

Figure 20 shown below depicts how the total manufacturing costs (fixed + variable costs) reacts to increasing capital cost increase in the indicated factors. The sensitivity between the capital cost of deposition equipment and the cost associated with perovskite material costs is examined. The blue line in the graphs at the 100% level indicates the price point at the reference

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tandem condition and efficiency of 24%. Therefore, at capital cost increase at the 200% level, this indicates that the price of the factor has doubled.

As can be seen in the first graph, with each relative percentage increase in the capital cost it has a greater effect on the overall manufacturing cost of the solar cell. Doubling the cost of perovskite material from the current cost (from 100% to 200%) represents only a 10% increase in the manufacturing cost of the solar cell; however, when it comes to the capital cost increase, this represents an increase of approximately 27%. This suggests that differing compositions of the perovskite layer, i.e. with Cs or multi-halide solution, which would result in relatively higher costs, do not largely impact the overall manufacturing cost. However, a deposition technology that is very expensive or low throughput will put pressure on the economic viability of the technology.

If we look further into this phenomenon, the second graph includes the impact of efficiency on the manufacturing cost. As will be shown later, efficiency not only has an impact on the manufacturing cost but the lifetime energy yield (energy generation) for LCOE valuations. This second graph shows that efficiency has a much higher impact than both changes to perovskite material costs or capital costs – inversely so. Also, this shows that if there is a process that increases the capital investment cost for equipment this can be balanced by a suitable, increase in the cell efficiency. A 50% increase to capital cost equates to a necessity to achieve at least a 13% relative increase in efficiency to keep the manufacturing cost from increasing. This results in a few absolute percentage points added to the efficiency.

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Figure 20. Total Manufacturing Costs' sensitivity to individual factors

In Figure 21, the manufacturing cost for the module is plotted against the uptime of the plant. There seems to be a point around uptime of 40% where the cost rising dramatically with values lower than that. However, above this it seems that the cost of manufacturing does not change dramatically with the plant uptime. A similar curve has been found in literature following the processing throughput in which the inflection point is at 1.0 m2/min [60]. In this study, the processing throughput was estimated to be approximately 1.05 m2/min for thin film production, slightly greater than the point where costs start to increase dramatically and therefore not subject to that much cost fluctuations.

Figure 21. Cost Sensitivity to uptime

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Besides altering the cost of the highest contributing factors in the overall manufacturing cost, key parameters in the model were identified and then varied to see the effect of changing one parameter on the final module manufacturing cost ($/WP). The parameters and their effect on the manufacturing cost can be seen in Figure 22. The most noticeable factor in this would be the module efficiency; changing this by +10% from 24% to 26.4% results in a reduction of the overall manufacturing cost of 0.05 $/Wp. Perovskite material utilization, electricity and labour costs have little impact on the overall cost and should be not be considered in determining the economic viability of this tandem technology. It can be seen that changes in technology can have an impact on the resulting cost of the tandem cell. For instance, changing the HTL from NiO to PTAA results in an absolute increase of 0.25 USD/W or 61% increase even though it only constitutes a 30 nm layer in the cell. However, this is due to the 100-fold cost increase above NiO. PTAA has been researched in the lab and successfully decreasing hysteresis and maintaining a high VOC but would not translate to being commercially available unless bulk material costs decrease dramatically.

Figure 22. Sensitive Analysis of major variable parameters within the cost model. Top half the graph shows the impact of the

cost on ±10% changes for the factors. Bottom half of the graph shows the impact of technological change. In addition to the notable changes to the efficiency variation and HTL technology choice, there are also other interesting observations here. One being terms of encapsulation. Using PIB, or polyisobutylene, as an encapsulant has shown promise in providing effective edge seal and limiting moisture ingress [61]. From an economic standpoint, a polyolefin alternative may be beneficial if the service life of the perovskite thin film is improved since the additional manufacturing cost is minimal. There is incentive to investigate how the encapsulant impacts lifetime in order to produce more cost-efficient modules and lower LCOE.

It is important to note as well the differences seen in the solution versus vapour price. The two factors that produced an increase of roughly 0.10 USD/W is the result of more expensive capital cost for equipment for the vacuum deposition equipment and for the decreased throughput using this equipment. However, this may be avoided if large scale commercialization is available. One industry source has determined the cost of an additional 0.26 €/wafer (equates to 12.84 $/m2 or ~0.05 $/WP) for the perovskite layer using a vapour based deposition process in a large-scale production (1 GW/year) [74]. This is in comparison with a solution deposition cost of 9.10 $/m2. Therefore, solution deposition is the cheapest option however, at higher rates vapour deposition is competitive and may be the best result for reproducibility. Reproducibility

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is not directly modelled in this case, as the cells that are discarded due to manufacturing defects, but should be included in future work.

5.3 Energy Yield Potential and LCOE

In the analysis of this device, as stated before, the monolithic construction of the perovskite-silicon tandem device requires current matching. Values obtained for the current and voltage were primarily taken from simulation work using STC, AM1.5 spectral distribution which is not always representative of outdoor conditions. The precise spectral composition depends on many factors such as atmospheric dust, humidity and cloud cover. In addition, a cloudy day on which the majority of the light is diffuse will result in a different spectrum hitting the solar panel at a range of angles. Therefore, spectral irradiance distribution and the angle of incidence play a factor in whether the charge carrier generation rates induced in the two absorbers produce the optimal current.

Modelling of the effects of these factors on current matching of the tandem devices show that they combine to decrease the energy yield of the device by 4.5% per year compared to simulated values [75]. Other research and simulation with regards to three different real world locations that differ from AM1.5 states that the tandem devices will deliver 98 to 103 % of the expected energy yield [76]. This is using optical simulations in combination with real weather data.

The reason the energy yield is almost unaffected is due to an enhancement of the fill factor (FF) of the JV curve when current mismatch occurs and this largely compensates for the drop of photocurrent. Both the IR and UV rich spectra result in photocurrent mismatch between top and bottom cells. In addition, during simulations it was discovered that there is a slight shift in optimal bandgap - for instance with an IR rich irradiance, a lower bandgap perovskite top cell is ideal for peak performance.

The most influential parameters with regards to the LCOE calculation for new technology perovskite will be the service life and the degradation rate. Since this fairly new technology and the stability of the perovskite is currently being researched, this will be varied to see what the effect is and at what point this technology is economically feasible.

Figure 23 below shows the range of LCOE prices for the tandem perovskite- SHJ tandem values in Germany residential energy production with two different degradation rates. A competitive achievable rate of 11 cents/kWh is the dark blue region in the top right regions of the graph. This rate is found in Fraunhofer’s LCOE for renewable energy [68] and an insert of the LCOE is shown in Figure 24. Fraunhofer ISE uses a comparative discount rate of approximately 4% which is close enough for the study that is presented here (4.25%). This is important for an accurate comparison as explained before.

At a reference tandem module effiency of 24%, it is equally as competitive to existing solar technology around a service life of 21 years. Using another reference for renewable energy LCOE as reference, in 2016 Germany PV LCOE was stable around 0.15 cents/kWh [77]. This can be achieved with the tandem device with a service life of 15 years. However, it is important to note that the IRENA LCOE values are based on a discount rate of 7.5% which would then naturally inflate their reported values. But ideally a tandem module with an efficiency of 24% would be economically viable with a service life between 15 and 21+ years. Conversely, if we

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look at a tandem module with an efficiency of 30%, the minimum service life would just under 19 years. It would seem that working towards producing a tandem module to last more than 20 years would be ideal in making it cost competitive especially with an increasingly cost competitive silicon market.

Figure 23. LCOE for tandem perovskite-SHJ solar modules for residential application (~5 kW) with average Germany irradiance of 1100 kWh/m2. Left: degradation 0.25%/year, right: 0.50%/year

Figure 24. Fraunhofer ISE results of LCOE for renewable energy technologies [68]. Solar PV is shown in yellow for residential, commercial, and utility scale installation and use.

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Over the past decade, there has been a rapid increase in the stability of perovskite solar cells (PSCs). This is shown in Figure 25. The average lifetime of a PSC has increased from hours in 2009 to about a year in 2017. Stability of perovskite solar cells/modules are a combination of proper structural composition and careful encapsulation. Modules have shown to pass the IEC test for damp heat and humidity 85C, 85% for 1000 hours with optimizing these designs [78].

Figure 25. Reproduction of stability testing on perovskite solar cells [16]

In Figure 26 there are three LCOE graphs for different applications of solar modules: residential, commercial, and utility based applications. For each scenario, the tandem parameters stayed the same; however, the cost of BOS and the amount of installed power changed accordingly. For the reference tandem at 24% efficiency, the installed power assume were <10 kW, 50kW, and 5 MW for residential, commercial, and utility applications respectively. LCOE is depicted as both a function of module efficiency and service life. In addition, the high-mid range values for solar PV LCOE from the Fraunhofer ISE report are included on the graphs for reference.

In terms of economic viability in comparison with existing technology, it is more viable to install tandem module equipment in residential applications. For commercial and utility use, there is no scenario in which the cost of electricity production meets or exceeds those demonstrated with existing technology. The same conclusion has been reported recently with thin film tandem solar modules in differing US weather conditions [72]. The economic study found that commercial and utility scale 2-T thin film solar modules were not economically viable since area and project system costs decrease with increasing production size and reduce the feasibility window created by the increased energy production.

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Figure 26. Residential, Commercial, and Utility LCOE for tandem technology

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6. Conclusion and Future Work

In this study, the financial and economic viability of perovskite-SHJ tandem solar cells were determined using a detailed bottom-up cost model and energy-yield calculations. Attention to specific advancements in perovskite solar cell layer technology and large-scale deposition have been taken into account to create a realistic, viable commercial scale option for tandem production. In doing so, this tandem technology is used in the bottom-up cost model to determine the overall manufacturing cost, minimum sustainable price, and LCOE. A reference tandem is used for comparison in which the efficiency is 24% after taking into account losses due to scaling up, module arrangement, and electrical losses.

In terms of manufacturing cost, the additional cost for perovskite layers on top of a silicon heterojunction bottom cell is about 15-20% of the total fixed and variable costs. The majority of the total cost is associated with the material selection but in regard to the silicon bottom cell. Perovskite materials contribute 12% of the material cost, or about 8% of the total manufacturing cost. The total cost for the tandem module is between 0.36 – 0.44 $/WP. This is at the reference efficiency of 24%. When comparing tandem versus silicon heterojunction solar modules, it is best to compare without efficiencies and so the cost becomes 97.15 $/Wp and 75.97$/Wp, respectively. A difference of 21.18 $/Wp for the manufacturing of the perovskite layers.

In comparing the minimum sustainable price, the tandem module was compared against thin film technologies such as CIGS and CdTe, PERC, and silicon heterojunctions. Thin film technologies have a lower market entry price due to absence of silicon ingot formation, an expensive capital venture. The reference tandem proved price competitive with PERC solar modules and has potential to be economically viable given the potential for additional energy generation.

Energy yield and service life contribute to the overall economic viability of two terminal solar modules with perovskite. Previous literature simulations show that there is a minimal energy loss in comparison with STC and real-world irradiance conditions due to limitations in current matching and variations in the light spectrum. Given the reference tandem module, it is expected to be competitive at the residential level with existing silicon technology if the tandem service life is greater than 20 years. Degradation issues need to be resolved to able to reach this goal since the current work has only shown a lifetime of approximately 1 year. Research into this is critical in reaching an acceptable level of feasibility. In commercial and utility application, the tandem model is not economically viable due to the reductions seen in the area- and project-related installation costs for existing technology.

In terms of market price entrance, a tandem efficiency greater than 24% is required; however, this alone is not enough to consider. Further investigation into perovskite stability issues is required since this a major roadblock for commercialization. Silicon has been proven to last at least 25 years and now even reaching 30+ years in operation. Perovskite material degrades under heat and humidity and would need to last as long as silicon to be cost competitive. Another aspect to commercialization to consider would be the consistent deposition of perovskite and associated layers. Furthermore, every process must induce as few defects as possible. In the present context, the power output of each solar cell in a PV module and the power output of each PV module in a PV system must lie within very narrow bands of

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acceptability. This is because in a series/parallel connection of multiple solar cells to get the desired voltage/current, the component with the minimum voltage/current will dictate the power output of the PV module. Any manufacturing variability that affects the performances of solar cells will result in lower yields of modules, and is one of the main technical reasons for the failures of several thin-film solar cell companies. Additional work to explore would be to determine how the tandem modules operate and the LCOE in different climates (i.e. dry, humid) in which the spectrum will alter the energy production. Also, the economics of specific technology such as CSP or using tracked devices could be explored.

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