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Article

An Integrated Planning Framework for Sustainable Water and Energy Supply

by
Esmaeil Ahmadi
1,*,
Benjamin McLellan
1,
Seiichi Ogata
1,
Behnam Mohammadi-Ivatloo
2,3,* and
Tetsuo Tezuka
1
1
Graduate School of Energy Science, Kyoto University, Kyoto 606-8501, Japan
2
Faculty of Electrical and Computer Engineering, University of Tabriz, Tabriz 5157944533, Iran
3
Institute of Research and Development, Duy Tan University, Da Nang 550000, Vietnam
*
Authors to whom correspondence should be addressed.
Sustainability 2020, 12(10), 4295; https://doi.org/10.3390/su12104295
Submission received: 8 May 2020 / Revised: 17 May 2020 / Accepted: 21 May 2020 / Published: 24 May 2020
(This article belongs to the Special Issue Energy Storage Technologies in Future Energy Systems)

Abstract

:
This study aims to reveal the economic, technical, and environmental impacts of different system configurations (centralized or decentralized, components, and technologies) on transition plans to achieve a higher share of renewable energy and desalination supplies for regions facing water scarcity. The main contribution of this research is the comparative evaluation of on-grid decentralized or distributed renewable-powered desalination systems for sustainable water and energy supply planning. Applying a novel nexus approach, an interactive multi-period planning model is developed to highlight synergies and to identify conflicts of planning both energy and water sectors at the same time as endogenous subsystems of one overall system. For studying these synergies in this study, the pace of technology deployment and the path of decline in overall costs are assumed to be a function of experience and knowledge as two-factor learning curves. Using data from 81 projects, the levelized cost and capacity factor of utility-scale photovoltaic and wind supplies in the Middle East were calculated. The results indicate that a scenario with a decentralized water sector and renewable-powered multiple-effect distillation technology has the best overall performance among the proposed scenarios.

1. Introduction

Over 2 billion people live in countries under high water stress in 2019 [1]. A United Nations study predicted that, by 2050, under the current average economic growth rate and without improvement in the water sector’s efficiency, the global freshwater demand could increase by 20% to 30% [2]. The ongoing pace of improvement in water sector efficiency is not sufficient to close this freshwater supply-demand gap [1]. Moreover, the potential of remaining freshwater resources that can be harnessed sustainably is limited, and due to steep marginal costs, the water prices are expected to rise [3].
Unconventional water supplies such as desalination are becoming a practical option to meet water demand in the future for specific areas due to climate change, natural and physical water scarcity, freshwater resource security, and access to clean water. Currently, more than 150 countries have already started developing desalination units, with production capacity of around 1% of the world’s total drinking water [4]. Desalination technologies are categorized into two main sub-groups based on the processes they utilize, as phase-change or thermal technologies and single-phase technologies. The primary source of energy for phase-change technologies is thermal energy, while single-phase technologies require electricity or hydraulic energy to operate. Table 1 summarizes these desalination technologies. Reverse osmosis (RO), multi-stage flash desalination (MSF), multi-effect desalination (MED), and hybrid desalination are the current dominant commercialized technologies to desalinate saline water [5].
Although desalination costs have dropped significantly because of technological progress and market maturation, and the environmental impacts of the desalination process, such as high carbon footprint and effluent-associated pollution, are somewhat mitigated, the sustainability of these systems are still under question. Energy is one of the chief factors affecting the sustainability and feasibility of desalination projects. From 30% to more than 50% of desalination costs are expended on energy [6]. Energy affects not only the desalination cost, but also technology adoption. The largest desalination plants located in the Middle East are adopting thermal-process-based desalination technologies, making use of their rich fossil fuel reserves [6]. Currently, fossil fuel resources are the main supply for powering desalination facilities in the world [7]. Renewable-powered desalination is a promising solution to mitigate the carbon footprint and eliminate the dependency of desalinated water costs on fuel prices [8]. Table 2 summarizes studies with renewable-powered desalination units with on-grid energy supplies. As can be observed from this table, centralized topology, RO technology, and solar electricity as one of the energy resources are popular ones in the literature. Due to affordability, availability, and zero-water-consumption for energy production compared to other renewable technologies in the regions facing water scarcity, solar and wind supplies are the most widely deployed renewable resources, which are coupled with desalination technologies. Wind resources account for around 32% and solar resources account for 19% of the total renewable-powered desalination facilities worldwide [9].
Variable renewable resources (VREs), including wind and solar power, impose fluctuations on energy systems. The future energy sector, with its high share of renewables, needs to ensure secure energy supply [39] in the event of a crisis such as technical failures or potential political conflicts in the case of exchanging renewable electricity with neighboring countries or regions. Variable renewable energy resources are non-dispatchable, therefore they cannot be controlled by operators. This means the future energy sector needs flexible plans to deal with demand shifts or decline in the case of a crisis such as the COVID-19 outbreak. An IEA report showed that full lockdowns due to the coronavirus outbreak caused an average 25% decline in energy demand per week and this decline is equal to 18% for partial lockdowns [40]. The resilience of energy systems with a high share of VREs hinges on exploring solutions to overcome these fluctuations in power generation to avoid instability caused by an imbalance between the supply side and demand side. Large-scale energy storage units increase the capital cost and could make the whole energy system more complicated due to additional compulsory equipment such as charge and discharge controllers, which could make them impractical for renewable-powered desalination systems [41]. Specifically, utilizing batteries, which have high capital costs and relatively short lifetimes, influences the economic feasibility of renewable-powered desalination projects [41,42]. Authors in some previous studies [43,44] have compared the levelized cost of desalinated water for renewable-powered RO units with and without battery storage. The results revealed estimated cost increases from 8.7 $/m3 to 9.2 $/m3 [43] and from 10 $/m3 to 13 $/m3, respectively [44]. Furthermore, high ambient temperature, which is a characteristic of most of the regions facing water scarcity, increases the self-discharge rate of battery units [45]. Figure 1 illustrates the current state of development, the estimated cost of desalinated water, and the potential capacity of renewable-powered desalination facilities (see Appendix E for details).
Desalination units are capable of compensating for the fluctuating power production of VREs to some extent, as water is desalinated whenever energy is available and is stored as a final product [34]. Studies showed that desalination units could be effectively powered by VREs without applying energy storage systems [46]. Each charge-discharge cycle of energy storage systems causes an amount of energy loss (battery systems operate with a typical charge-cycle efficiency of 75% to 98% [47,48]), so this direct consumption of renewable power could improve the efficiency of the renewable energy systems. The levelized cost of energy (LCOE) was shown to decrease by around 3% for a 100-percent-renewable scenario in Saudi Arabia due to the flexibility provided by RO units and the reduction of required battery capacity [14].
Figure 1 reveals that renewable-powered desalination systems are typically considered to be suitable small-volume desalination, while studies with on-grid energy systems focus on large-capacity desalination facilities. In this study, a centralized desalination system refers to a water system in which saline water is desalinated by one unit and distributed among all target users, while in a decentralized or distributed desalination system, there more than one desalination unitprovide water demand (see Figure 2). As can be seen in Table 2, and to the best of the authors’ knowledge, there is only one study [38], which modeled a water system with more than one unit of desalination for the long-run planning of a water system with on-grid renewable energy resources. This study followed a sequenced approach [38]. After calculating the surplus electricity from roof-top photovoltaics in a region in Australia for only two days during a year through a spatial model, this excess electricity is considered as a yearly fixed energy resource for RO units at zero cost (assumed as waste energy). The proposed system led to the LCOE reduction by 20% for the photovoltaic electricity generation and reducing the levelized cost of desalinated water (LCOW) by 10% compared to the water sector as a fixed electric load.
Moreover, these decentralized desalination systems have the potential to save energy from water distribution by increasing the number of options for site locations of desalination units. Pumps for water distribution are energy-intensive components, which need to be considered for site selection (the location), size of desalination plants, and system configuration (distributed water system with several small-size desalination units or centralized water system with a large-size desalination unit). Studies [49,50] estimated the cost of water transport from coastal desalination plants as summarized in Table 3. It can be seen that for several cases, the cost of water transfer is considerable, relative to the cost of water desalination.
Studies for designing and planning on-grid energy systems with a share of VREs with desalination as a share of the water supply have typically followed a sequenced approach. One sector has been considered as an existing sector with a fixed configuration, based on which the other sector has been planned for the long run. There is a gap in the scope of this field to design and plan both the water and energy sectors at the same time. The operational flexibility of water desalination, transfer, and storage is another key factor that needs to be considered in the long-run planning of VREs, as these flexible loads can help to solve the issues related to the fluctuations of renewable power production. This factor has only been considered in studies that have focused on the operational optimization of these systems. To the best of our knowledge, there is no previous study that compares the long-term planning of centralized and decentralized desalination systems powered by on-grid VREs considering short-term (hourly) operational constraints. These systems have the potential to compensate for the fluctuating power production of variable renewables, to reduce GHG (greenhouse gases) emissions, and to solve effluent-associated environmental issues by providing multiple options for site locations avoiding discharging brine into sensitive ecosystems and distributing the brine.
This study aims to shed more light on potential synergies and conflicts of the transitions to an energy sector with a share of renewables and a water sector with a share of desalination. To this aim, a nexus approach is applied to design the future configuration of both water and energy systems together. More precisely, this study reveals the economic, technical, and environmental impacts of different system configurations (such as centralized, decentralized, and alternative technology mixes) on transition plans to achieve a higher share of renewable energy and desalination supplies for regions facing water scarcity. The authors consider that the current study provides novel insights: (1) Designing and planning both the water and energy sectors at the same time, (2) detailed representation of short-term operational aspects in long-run planning of the water and energy sectors to capture the inherent variability of renewable energy resources, (3) modeling the water sector with centralized and decentralized on-grid renewable-powered desalination systems, (4) proposing a new methodology to study the synergies and conflicts of designing the water and energy sectors as an integrated system/separated system, and (5) estimating the two-factor learning curves for wind, photovoltaic, reverse osmosis desalination, and multi-effect distillation desalination industries in the Middle East.
The remainder of this paper is organized as follows. The research methodology and model developed in this study are explained in Section 2. Furthermore, the case study is introduced in this section. The results of the optimization modules and analysis are illustrated in Section 3 and lastly, the conclusion of this research is summarized in Section 4.

2. Methodology

The nexus approach is deemed necessary to design future, inherently interlinked systems from the starting point of planning in a holistic manner [51]. Concepts such as integrated management consider at least one of the systems as an existing system and are therefore different from the nexus approach. This approach identifies the future systems as inherently interconnected. The nexus approach aims to highlight potential synergies and identify critical conflicts to be dealt with [52]. These outcomes are benchmarks for trade-offs among system integration, increasing complexity to the point where the decision making is delayed or incapacitated; and designing these systems as separated systems with less complexity, but potentially lower efficiency. Moreover, different system configurations could influence the extent of these synergies, conflicts of interests, and complexity.
Two system types (integrated and separated) and two system configurations for the water sector (see Figure 2) are assumed, making a total of four scenarios for investigation in this study, including:
  • Base Scenario: The water sector is considered as a centralized system with MED desalination technology.
  • C_RO Scenario: The water sector is studied as a centralized system with RO desalination technology.
  • D_RO Scenario: The water sector is assumed as a decentralized system with RO desalination technology.
  • D_MED Scenario: The water sector is considered as a decentralized system with MED desalination technology.
In the base scenario, the water sector is studied as an exogenous factor for the energy system, in which there is no control over it. In C_RO, D_RO, and D_MED scenarios, both energy and water systems are studied as an integrated system, which are endogenous parts of one integrated system. The energy sector is considered as centralized in all of the above scenarios because of the data limitation for descaling learning curves for variable renewable resources to give sensible differentiation between a set of small-scaled systems and an equivalent large-scaled system.
As shown in Figure 3, there are four modules within the model proposed in this study: (1) Proposing a supply-demand module, (2) developing an energy storage module, (3) estimating the learning curves for the region of the case study, and (4) conducting economic analysis and calculating GHG emissions reduction.
I Supply-demand module
A supply-demand module is developed as the first step of the proposed model, to study the technical aspects of the proposed scenarios. The energy demand is estimated based on demographic trends and historical data. System configuration and national plans and targets are taken into account in this optimization module, which is described in detail in Appendix A. The module is developed and solved as a linear problem. The objective function is to minimize the electricity exchange with the national grid, as follows:
Min t , y | p g r i d ( t , y ) |
where p g r i d is the absolute value of hourly electricity exchange with the electric grid. p g r i d includes both negative (selling electricity to the grid) and positive values (purchasing electricity from the grid).
II Energy storage module
The energy storage module is developed to find the required battery capacity equivalent to the operational capacity of the flexible water sector. This optimization model is described in detail in Appendix B. The new required capacity of battery storage for each year and the cost of this battery storage for a unit of variable renewable energy generation (MWh) are calculated using the results of the supply-demand module. The objective function is to minimize the capacity of batteries ( C a p b a t ( y ) ) equivalent to the operational capacity of the flexible water sector in each year as:
Min y C a p b a t ( y )
III Learning curves
Learning curves have been applied as a practical approach of looking at the pace of technology deployment and the path of cost reduction. As the underlying assumption of the learning curve, experience, knowledge, and other factors can improve technology performance that leads to unit cost reduction with the accumulation of factors mentioned above. The one-factor learning curve, which was popular in the mid-1970s, only reflects the effect of experience (cumulative production), whereas the two-factor learning curve considers the influence of both experience and knowledge. Studies have shown that the one-factor learning curve overestimates the impact of experience [53].
Modeling the pace of technology deployment and the path of cost reduction just as a function of time f ( t i m e ) , which is the most frequent approach among studies [54], is not practical, because it does not allow the consideration of synergistic effects of an integrated energy-water transition study but supports a separation of the systems because both energy and water systems will see cost reductions at the same rate regardless of integration. In this study, the path of cost reduction is modeled by the two-factor learning curve and is assumed to be a function of experience and knowledge ( f ( e x p e r i e n c e , k n o w l e d g e ) ), which is explained in Equation (3) [55]. The two-factor learning curve is described in more detail in Appendix C.
C t = C 0 × C C α × K S β
where C t describes the unit cost of technology, C 0 is the initial unit cost, C C is the cumulative production, α depicts the learning-by-doing elasticity, K S is the knowledge stock, and β is the learning-by-searching elasticity.
Based on this learning curve, the technology cost decreases by increasing the cumulative production as well as investment in research and development (R&D). In the two-factor learning curve, learning-by-doing (LDR) and learning-by-searching (LSR) illustrate this decreasing technology cost denoting the percentage of variation in cost as a result of doubling the cumulative production and R&D investment, respectively. The LDR is calculated as 1 2 α and the LSR is obtained as 1 2 β .
Due to a lack of data, a new approach is developed to estimate the learning-by-searching ratio of the two-factor learning curve and the average R&D budget using particle swarm optimization. The details of this approach are described in Appendix C.
IV Economic analysis and GHG emissions
To reveal the synergistic effects, conflicts, and the influence of the system type and shape, the results of the previous modules are used to assess the future cost of variable renewable energy and desalinated water for the proposed scenarios for the region of the case study. Furthermore, the potential of each scenario in decreasing GHG emissions is calculated. Finally, a sensitivity analysis is conducted to evaluate the effect of R&D investment on the technologies.

Case Study

The southern coast of Iran, which is facing severe water scarcity [56], is chosen as a case study. This region has ready access to seawater for desalination from the Persian Gulf and the Gulf of Oman. As can be seen in Figure 4 [56], Iran has 6 main and 31 secondary water basins. The six main drainage basins include the Caspian Sea basin in the north, the Central Plateau in the middle of the country, the Persian Gulf and Gulf of Oman basin in the west and south, the Kara-Kum basin in the north-east, the Lake Urmia basin in the north-west, and Lake Hamoon basin in the east [56].
The Persian Gulf and Gulf of Oman basin has ready access to seawater, giving four provinces inside this water basin, which are considered as the region of the present case study, to deploy desalination as a source of freshwater.
The region of the case study also has great potential to generate solar and wind power, which are taken as the VRE resources in the current study. In this region, the hourly average wind speed is 3.26m/s and the daily average solar radiation is equal to 5.63KWh/m2/day [58].
Jask county has a hot desert climate with sweltering summers and little precipitation, situated on the Gulf of Oman. A port town (see Figure 4), the capital of the county, also named Jask, is the case study as an urban area (small town) with a population of 16,860 at the 2017 census [59]. To model a decentralized water sector for rural areas, 19 rural districts are selected (see Figure 4), which are inside Jask county and have access to seawater for desalination. The total population of these districts is 16,855 in order to be readily comparable with the centralized case (see Appendix D for details) [59]. Due to a lack of data, it is assumed that the water demand of these 19 rural districts is equal to Jask port and distributed as a proportion of their population.

3. Results and Discussion

In this section, first the results of the supply-demand module and the energy storage module for the proposed scenarios the case study (Jask, Iran) are explained. These outcomes are the baseline for technical, economic, and environmental analysis for the whole region in the southern coast of Iran.
All water, energy, and technology-related costs in this study were converted to 2018 United States dollars ($).

3.1. Supply-Demand Module

In the 2015 Paris Climate Agreement, COP21, Iran pledged to meet a target of 7.5 GW of renewable electricity generation capacity by 2030 [60]. According to the Iranian Sixth National Development Plan, the Ministry of Energy and the Renewable Energy Organization, which are Iran’s leading electric utility and subsidiaries, are assigned a target of supplying 5% of total electricity demand from renewables by 2021 [61]. Moreover, according to the Iranian National Strategic Energy Plan, Iran aims to reach competitive costs for renewable power production by 2040 and increase the current renewable deployment rate, which is around 1% yearly. The Iranian Ministry of Energy has proposed comprehensive plans to hit the aforementioned targets, such as a feed-in tariff mechanism and long-term contracts at guaranteed prices, extended from five-year contracts to 20-year contracts from 2015 [62]. In this study, the growth rate of VREs’ share of total electricity supplies is assumed to be 2% per year by 2040.
For the water sector, according to the Iranian Sixth National Development Plan, the Ministry of Energy is assigned to propose a plan for transferring required knowledge and providing sufficient financial support toward supplying 70% of the urban water demand on the shoreline of the Persian Gulf and the Gulf of Oman by 2021 from desalination [61]. This study assumes a linear increase for the expansion of desalination across the period to meet the 70% target.
Ten days in each season, for a total of 40 days as representative of each year, are chosen (due to a software limitation) as the short-term operation horizon for each year between 2020 to 2040 as the long-run planning horizon to solve the linear supply-demand module. The module is coded into GAMS 26.3.5 [63] and solved by CPLEX solver for the sample county (Jask, Iran).
The total renewable electricity production for each scenario is the same (68,371 MWh from 2020 to 2040, 40 days each year). The optimal yearly capacity of wind supply, photovoltaic (PV) supply, and desalination plants are obtained for the proposed scenarios. The hourly water production of each desalination plant, the amount of stored water in the city’s reservoir (for the base and C_RO scenarios), the amount of water stored in the desalination unit’s reservoir, the amount of water pumped from the desalination reservoir (for the base and C_RO scenario), and the amount of hourly water extraction from the conventional water sources are the other variables of this model to meet the mentioned target share of VRE and desalination production. The share of PV and wind in the total VRE electricity production is depicted in Figure 5 and Figure 6. For D_RO and D_MED scenarios, the share of solar electricity rises from 32% and 0% of total renewable electricity generation in 2020 to 86% and 85% in 2040, respectively, while for the base and C_RO scenarios, the share of solar electricity production from the total VRE electricity production declines from 100% in 2020 to 85% and 88% in 2040, respectively. As can be seen in Figure 5 and Figure 6, solar electricity performs better in following the electrical load pattern in this case study and with a share of more than 85% of total VRE, electricity production is the dominant renewable resource for all the scenarios.
Mismatches between VRE electricity generation profiles and electric demand due to the variability of VRE power generation can cause instability in electricity grids. The portion of VRE electricity generation exceeding the electric load is defined as the excess renewable electricity generation in this study, and self-consumption refers to a portion that is consumed directly by the county of the study and is not fed into the national electricity grid. Figure 7 shows the amount of excess electricity generation and share of self-consumption from the entire VRE electricity generation for all the scenarios. The amount of excess power generation from VREs in 2040 reaches about 17.4% of total renewable electricity generation for the base scenario, while this excess energy generation is around 14.3% for the C_RO and D_RO scenarios and 16.1% for the D_MED scenario.
Figure 8 depicts the electricity demand of the water sector and its share from the total electricity demand. Although the water sector’s electricity demand is rising for all the scenarios from 2020 to 2040 (due to a higher portion of desalination and demand growth in proportion to Iran’s population growth [64]), its share from the total electricity demand shrinks from 6.6% in 2020 to 3.9%, 6.3%, and 2.9% for the base, D_RO, and D_MED scenarios in 2040, respectively. For the C_RO scenario, this share rises slightly from 6.6% in 2020 to 7.1% in 2040. This comes from differences between the yearly growth rate of water demand influenced by the population growth in the current module and the growth rate of electricity demand, which is a constant (a 6.5% yearly growth based on national data predictions [59]). The RO desalination technology requires more electricity to desalinate water (4 KWh/m3) compared to the electricity consumption of MED technology, 1.5 KWh/m3 in this study. As a result, scenarios with RO technology, the C_RO and D_RO scenarios, have a higher electricity demand compared to the scenarios with MED technology, the base and D_MED scenarios. Furthermore, as can be seen in Figure 8, the scenarios with the decentralized water sector, the D_RO and D_MED scenarios, benefit from energy-saving due to less electricity consumption for water distribution.

3.2. Energy Storage

In the next step, based on the results of the supply-demand module, an optimization problem was solved using GAMS software [63] to find the required batteries equivalent to the operational capacity of the flexible water sector. Annual equivalents of the lump sum unit investment cost of the required batteries are determined to calculate the cost of batteries for a unit of VRE electricity production (MWh/$). This annual equivalent of the lump sum unit investment cost of each technology is defined as a stream of equal annual debts over the lifetime of the technology, in such a way that the present value of the stream is equivalent to the lump sum unit investment cost for each technology. The results of this optimization module are summarized in Figure 9.
The flexibility of the water sector as an electric load in D_RO and D_MED reaches its highest capacity between 2030 to 2034, at about 18 MWh and 15 MWh, respectively. This flexibility is lower in the C_RO scenario compared to the scenarios with the decentralized water sector in most of the studied time horizon, which was not expected due to stricter constraints on the decentralized water sector (see Appendix A). This flexibility is sensitive to the share of each VRE supply in the total renewable power generation. In the scenarios with the decentralized water sector, by reaching above 90% share of solar electricity in total VRE power generation in 2030 (see Figure 5), the equivalent capacity of batteries reaches the highest value and starts declining after 2035, when the portion of wind electricity is increasing (see Figure 6). This means the decentralized water sector has local optimum flexibility around 90% share of solar electricity in the total VRE power generation. For the C_RO scenario with the centralized water sector, the equivalent battery capacity is growing with the rising share of wind electricity in total VRE power generation (see Figure 9d). This shows that the centralized water sector operates more flexibly with a higher percentage of wind electricity compared to the decentralized water sector. It is noteworthy to mention that the objective function of the supply-demand module, the results of which are the baseline for the current storage module, is to find the optimal capacity of VRE supplies for reaching minimum overall electricity exchange with the national grid, which is not identical with finding the maximum flexibility of the water sector as an electric load.
The cost of batteries for a unit of VRE electricity generation falls in several periods, although the equivalent capacity is constant or decreasing, for instance, in Figure 9b for the D_RO scenario, from 2030 to 2035. This is due to an assumption in this study that the cost of lithium-ion batteries will decrease by 40% by 2040 [65,66] causing a lowering of costs while the equivalent battery capacity is constant or decreasing.

3.3. Learning Curve

The parameters of the two-factor learning curve for utility-scale photovoltaic, wind, MED, and RO technologies have been estimated in the current study. The results of these estimations are illustrated in Figure 10, Figure 11 and Figure 12. The levelized cost and capacity factor of wind and photovoltaic supplies were obtained using data from 49 photovoltaic projects and 32 wind projects in the Middle East, as explained in detail in Appendix C.
The estimated LDR and LSR for the utility-scale photovoltaic industry between 2013 to 2019 in the Middle East were 15.3% and 33.9%, respectively, with a goodness of fit (R2) of 96.9% based on the average LCOE and 86.9% based on overall data. Figure 10 shows that the obtained LCOE of the utility-scale photovoltaic electricity is equal to 55.2 $/MWh in 2020. Previous studies [67] obtained an LDR of 18% for 26 regions in North Africa, South America, and Australia using the one-factor learning curve to estimate the LCOE of PV. Authors in other studies [68] adopting a similar two-factor learning curve found an LDR of 17% and an LSR of 10% for the photovoltaic technology. Other studies [55] (using data from 2009 to 2016 for the US) and [69] (using data from 1975 to 2000 using worldwide data) estimated these rates as 6.7% and 18.4% for LDR and 75.2% and 14.3% for LSR, respectively, by including a time lag between investment in R&D and subsequent declines in cost for the photovoltaic technology.
The estimated LDR and LSR for the wind industry between 2010 to 2018 in the Middle East were 13.5% and 36.6%, respectively, with a goodness of fit (R2) of 90.0% based on the average LCOE and 67.4% based on overall data. For the wind industry, the overall LDR span is a broad range, from −11% to 35% among studies [53]. As can be seen in Figure 11, the obtained LCOE of wind energy in this study reaches 34.6 $/MWh in 2020. Other studies, [55,69] adopting a similar two-factor learning curve to obtain future wind energy costs, estimated an LDR of 14.2% and an LSR of 18.0% using data from 1991–2000 and an LDR of 17.5% and LSR of 37.1% using data from 2009 to 2016.
The learning rates of the two-factor learning curve for the utility-scale photovoltaic and wind technologies in the Middle East, which are obtained in the current study, were higher than the previous studies. This indicates that, in this region with large-scale investments and commercialization, the learning ability of the utility-scale photovoltaic and wind technologies have substantially improved. Moreover, the estimated LSR rates were higher than the LDR rates for the technologies mentioned above, showing that these technologies are undergoing an explosion of knowledge-driven cost reductions. In consequence, investment in R&D can play a chief role in the development of these technologies in the Middle East.
The estimated levelized cost of water for the RO and MED desalination technologies is also obtained by applying the two-factor learning curve, which is depicted in Figure 12. The estimations indicate that the LCOW for RO technology reaches 2.19 $/m3 and 2.46 $/m3 for the MED technology. The obtained LDR and LSR rates for the RO desalination technology are equal to 9.1% and 49.6% with a goodness of fit (R2) of 99.2% using data from 2012 to 2020 [70]. For the MED desalination technology using data between 2012 to 2020 [70,71], the obtained LDR is 12.9%, and the LSR is 57.2% with a goodness of fit (R2) of 98.9%. Previous studies, [72] adopting a one-factor learning curve to estimate the learning rate for the CAPEX of RO technology, found an LDR of 15% for RO desalination technology using worldwide empirical data. Other studies [73], estimated a range of 6% to 20% for LDR of the RO desalination technology with a goodness of fit (R2) of 98.0% and a range of 12% to 23% for LDR of the MED technology with a goodness of fit (R2) of 99.1%.

3.4. Economic Analysis and Emissions

Based on the results of the supply-demand module, storage module, and the estimated rates of the two-factor learning curve and costs of the utility-scale photovoltaic, wind, RO, and MED technologies from the previous sub-section, an economic analysis has been conducted for the region of the case study. Furthermore, the reduction of GHG emissions for the proposed scenarios has been calculated. Lastly, a sensitivity analysis has been conducted to investigate the role of R&D in the development of the mentioned technologies. The electricity and water demand in 2020–2040 have been obtained based on national predictions [59] and the World Bank’s population estimation [64] for the region of the case study.
The cost of batteries for a unit of VRE electricity generation (see Figure 9), which was obtained for the C_RO, D_RO, and D_MED scenarios due to a lower required capacity of batteries compared to the base scenario, is considered as a saved budget for the energy sector in these scenarios. Countries have pledged to increase public and private R&D spending substantially by 2030 as part of the Sustainable Development Goals. The latest available data from the UNESCO Institute for Statistics show that the current maximum R&D spending as a percentage of GDP is around 5% [74]. Therefore, 5% of this saved budget is assumed to be invested in R&D of the wind and photovoltaic technologies in proportion to the share of each supply in VRE electricity generation. It is assumed that the rest of this saved budget (95%) finances further generation of renewable electricity from utility-scale photovoltaic and wind. This budget covers all the fixed and variable costs of the VRE electricity generation during the lifetime of these technologies, which is 20 years.
Studies [3,49,75] showed that about 40% and 7% of LCOW of the RO desalination technology and the MED desalination technology goes to electricity consumption, respectively. As a result, a lower cost of electricity in the C_RO, D_RO, and D_MED scenarios compared to the levelized cost of electricity in the base scenario causes a cost-saving in the water sector. Moreover, the scenarios with the decentralized water sector benefit from energy-saving due to less electricity consumption for water distribution, causing additional cost-saving for these scenarios. These cost-savings are considered as a saved budget for the water sector in the C_RO, D_RO, and D_MED scenarios. Similar to the energy sector, it is assumed that 5% of this saved budget is invested in R&D of desalination technologies and 95% of this budget finances more water desalination to increase the share of desalination from water supplies. This budget covers all the fixed and variable costs of the desalination water production during the lifetime of the RO and MED technologies, which is considered 20 years in this study.
Table 4 summarizes the LCOE of renewable supplies and LCOW of the MED and RO desalination technologies for the proposed scenarios from 2020 to 2040 in the region of the case study.
Table 4 shows that the levelized cost of wind electricity generation will reach 17.8 $/MWh, 18.6 $/MWh, 17.5 $/MWh, and 17.4 $/MWh for the base, C_RO, D_RO, and D_MED scenarios, respectively. In the base, C_RO, D_RO, and D_MED scenarios, 94%, 92%, 89%, and 90% of this cost reduction in 2040, compared with the cost of wind electricity in 2020, is driven by the experience effect of cumulative production, and 6%, 8%, 11%, and 10% is driven by the knowledge stock of the cumulative increase in R&D spending, respectively. In the C_RO scenario, the share of wind electricity generation from the total VRE electricity production in 2040 is the lowest amongst the proposed scenarios, with 12% (see Figure 5) causing the highest LCOW for the wind supply in the C_RO scenario due to the effect of production experience.
For utility-scale photovoltaics, the LCOE in 2040 is equal to 17.3 $/MWh, 15.0 $/MWh, 13.5 $/MWh, and 14.1 $/MWh, for the base, C_RO, D_RO, and D_MED scenarios, respectively. About 96%, 83%, 76%, and 78% of this cost reduction in 2040 as compared with 2020 is caused by the experience of cumulative production, and 4%, 17%, 24%, and 22% comes from the knowledge stock of the cumulative increase in R&D spending for the base, C_RO, D_RO, and D_MED scenarios, respectively.
The cost reduction of wind electricity is lower than the cost reduction of photovoltaic electricity. For instance, in the D_MED scenario, the LCOE of photovoltaic electricity reduces from 55.2 $/MWh in 2020 to 14.1 $/MWh, while the wind electricity experiences a cost reduction from 34.7 $/MWh in 2020 to 17.4 $/MWh in 2040. Several factors cause this difference, including, first, the share of wind power from total renewable electricity generation varies from 11% to 15% in 2040, affecting the cost reduction by the experience of cumulative production. Moreover, in this proposed module, the VRE technologies are gaining budget from the saved budget for spending on R&D and adding new capacity in proportion to their share of total VRE generation (see Figure 5 and Figure 6) based on the results of the previous technical modules in this study. In other words, the photovoltaic technology gets more share from the saved budget because it is more attractive based on the technical modules.
Even though the LSR is higher than the LDR for both photovoltaic and wind technologies, the main percentage of the cost reduction is driven from the experience of cumulative production showing these technologies are facing an inadequate R&D budget for development. The circumstances are improved for the C_RO, D_RO, and D_MED compared to the base scenario. For example, the share of cost reduction due to knowledge stock increased from 4% in the base scenario to 22% for the D_RO scenario for the photovoltaic technology because a fraction of the saved budget is dedicated to spending on R&D.
Table 4 shows that the levelized cost of desalinated water for the base, C_RO, D_RO, and D_MED scenarios will reach 0.79 $/m3, 1.01 $/m3, 0.98 $/m3, and 0.74 $/m3, respectively. For MED desalination technology in the base and D_MED scenarios, about 55% and 56% of the cost reduction is caused by the knowledge stock in 2040 as compared with 2020 and around 45% and 44% is driven by the experience effect of cumulative production, respectively. Around 36% and 39% of the RO desalinated water reduction cost is driven by the experience of the cumulative production for the C_RO and D_RO scenarios, respectively. These results indicate that RO and MED desalination technologies received adequate R&D budget compared to photovoltaic and wind technologies.
Figure 13 depicts the synergy results of the integration of the water and energy sectors for the energy sector. The C_RO, D_RO, and D_MED scenarios, with the integrated water and energy sectors, generate 32%, 64%, and 53% more renewable electricity, respectively, during the lifetime of the newly installed capacities in 2020–2040 compared to the renewable electricity generation of the base scenario with the separated water and energy sectors. These scenarios have 7%, 14%, and 12% less required budget, respectively, compared to the required budget for the base scenario. As can be seen in Figure 13, for the water sector, only the D_MED scenario shows a synergistic effect from the integration of the water and energy sector. This scenario produces 4% more desalinated water during the lifetime of the newly installed facilities with 3% less required budget compared to the desalinated water production and required budget in the base scenario while the C_RO and D_RO scenarios require 18% and 16% more budget compared to the budget in the base scenario to meet the same targets. Furthermore, the D_MED scenario reaches a levelized cost of desalinated water of 0.74 $/m3, which is 5% lower than the cost in the base scenario in 2040.
Figure 14 indicates that the D_MED scenario with 444 Mt of CO2, 7913 tons of CH4, and 794 tons of NO2 reduction by 2040 has a better performance in GHG emissions reduction compared to the other scenarios. These reductions were calculated based on the Iranian electricity mix and with an assumption of providing the thermal energy for the desalination process from Iranian natural gas in the base scenario and from solar thermal resources for the D_MED scenario [59,76]. Although the C_RO scenario generates more renewable electricity compared to the D_MED scenario (see Figure 13), the D_MED scenario, as explained in the introduction, has the potential to provide thermal energy for the desalination process from the solar thermal resources due to distributed water sector and its size compatibility.
As can be seen in Table 4, the obtained LCOE in the scenarios with the integrated water and energy sectors, the C_RO, D_RO, and D_MED is lower the LCOE in the base scenario with separated water and energy sectors. Even though the VRE costs are likely to decrease dramatically, these costs will remain more expensive than natural gas power plants in 2040 for Iran producing electricity with an LCOE of 10 $/MWh [60,77]. The levelized cost of renewable electricity is equal to 17.6 $/MWh, 16.8 $/MWh, 15.5 $/MWh, and 15.7 $/MWh for the base, C_RO, D_RO, and D_MED scenarios, respectively. Even though the D_RO reaches a cheaper LCOE and higher penetration of VRE (see Figure 13) compared to the D_MED scenario, in this scenario, the LCOW will be 13% more expensive than the base scenario, and the required budget to meet the same targets in the water sector is 16% higher than the base scenario.
The United Nations addressed water resource management and deployment of renewable energy among focal targets to achieve sustainable development goals (SDG) in Iran [78]. Currently, planning for the water and energy sector is being conducted separately in Iran [78]. This study shows the integrated planning of these sectors brings potential technical, economic, and environmental synergistic benefits while avoiding conflicts. Moreover, even when considering all cost reductions and developments, renewable power and desalination (as one of the proposed strategies to achieve SDGs in Iran [79]) remain expensive energy and water supplies compared to other conventional resources. It needs heavy national investment and subsidies from governments for the next few decades. The proposed renewable-powered desalination system in this study gives the rural areas of Iran an opportunity to benefit from these investments and subsidies. Such rural areas are given priority for development in the suggested strategies for achieving SDGs in Iran [79].

Sensitivity Analysis

For investigating the role of R&D budget in the deployment wind, solar MED, and RO technologies, a sensitivity analysis has been conducted in this study. To this end, the share of R&D investment from the saved budgets (explained in the previous subsection) is assumed to differ by up to 10%. The resulting LCOE of VRE electricity and LCOW of desalination technologies in 2040 for the proposed scenarios are summarized in Table 5. The levelized cost of photovoltaic electricity (around 20% for the C_RO scenario, 32% for the D_RO scenario, and 28% cost reduction for the D_MED scenario) was most affected by increasing the share of R&D budget compared to the LCOE of wind power (around 2% for the C_RO scenario, 6% for the D_RO scenario, and 4% cost reduction for the D_MED scenario) and LCOW of MED and RO desalination technologies (around 1% for the C_RO scenario, 8% for the D_RO scenario, and 14% cost reduction for the D_MED scenario) due to the higher effect of cumulative production and receiving a higher share of the R&D budget. As mentioned, in the C_RO scenario, the share of wind electricity generation from the total VRE electricity production in 2040 is the lowest amongst the proposed scenarios causing higher LCOW for the wind supply as can be seen in Table 5.
As mentioned, it is assumed in this study that a share of the saved budget goes into the renewable and desalinated water production, adding new capacities to the supply sides of the water and energy sector. This budget covers all the fixed and variable costs of the VRE electricity generation and desalinated water production within the lifetime of these technologies, which is 20 years. The renewable generation and desalinated water production of these new capacities from the saved budget are described in Figure 15 and Figure 16 for the proposed scenarios. By increasing the share of R&D in Figure 16, as expected, the VRE electricity generation is diminished because the budget for the VRE generation is reduced and invested in R&D instead. For the water sector in the D_MED scenario, although the MED water production rises from 1% for no R&D share to 8% for 10% R&D share because of the same reason, the required budget decreases 17% because of the high cost reduction of photovoltaic electricity (around 28%). This reveals the role of LCOE in the cost of water desalination, indicating that with a 17% lower budget compared to the budget for no share of R&D in the D_MED scenario, the MED water production rises about 7%.

4. Conclusions

In the Middle East, the water and energy sectors are planning to transition towards a higher share of renewable resources and desalinated water supplies. A novel methodology is developed to model synergies of integrated planning of inter-linked sectors. The nexus approach in this study revealed that the configuration of each sector has direct impacts on the other sector. Designing the water sector and energy sector as endogenous parts of one system can decrease the cost of the fluctuating renewable power generation for the energy sector in all the proposed scenarios. Among these scenarios, in only one scenario, the scenario with the decentralized water sector and multiple effect distillation desalination technology, the water sector experienced synergistic results, causing a lower required budget and levelized cost of desalinated water compared to the base scenario with the separated water and energy sectors. On the other hand, other scenarios imposed a higher levelized cost of desalinated water and required budget on the water sector, revealing a conflict between the water and energy sectors. The synergy results for a 5% research and development share from the saved budget showed that by modeling the water and energy sectors at the same time, the levelized cost of variable renewable electricity decreased 4% for the scenario with the centralized reverse osmosis water sector, 12% for the scenario with reverse osmosis decentralized water sector, and 11% for the multiple effect distillation decentralized water sector compared to the 17.6 $/MWh for the base scenario with the separated sectors. Meanwhile, renewable electricity generation grows 32%, 64%, and 53% with 7%, 14%, and 12% less budget, respectively. Although the scenario with the reverse osmosis decentralized water sector has a better performance in the energy sector, this scenario requires 16% more budget for the water sector and reaches levelized cost of desalinated water of 0.98 $/m3, which is 24% higher compared to the base scenario to meet same targets. In the meantime, the scenario with the multiple effect distillation decentralized water sector reaches levelized cost of desalinated water of 0.74 $/m3, which is 6% lower the base scenario while producing 4% more desalinated water with 3% less required budget. Furthermore, this scenario showed a better performance in reducing greenhouse gas emissions due to its size compatibility with renewable-powered desalination facilities. As a result, the scenario with the decentralized water sector and renewable-powered multiple effect distillation desalination technology showed the best overall performance among the proposed scenarios. Moreover, the sensitivity analysis revealed the role of levelized cost of energy in the cost of water desalination, indicating that with a 17% lower budget compared to the budget for no share of research and development, the multiple effect distillation water production rises about 7%. In summary, the integrated planning of the water and energy sectors, as focal target sectors in sustainable development goals for Iran, could bring technical, economic, and environmental synergic benefits while it is necessary for avoiding conflicts.
It is noteworthy to mention that the estimated learning rates of the two-factor learning curves in this study showed that the research and development investment have a significant role in deployment and cost reduction of photovoltaic, wind, multiple effect distillation, and reverse osmosis technologies due to higher learning-by-searching rates comparing to learning-by-doing rate. Despite the fact that the learning-by-searching rate is higher than the learning-by-doing rate for all these technologies, the main percentage of the cost reduction is driven from the experience of production for the wind and photovoltaic technologies showing these technologies are facing an inadequate research and development budget for development. Nevertheless, in the proposed scenarios in this study, investing a portion of the saved budgets on research and development solved this issue to some extent.
Finally, considering all technology developments, renewable energy and desalination supplies remain more expensive than conventional resources for the next few decades. The proposed renewable-powered desalination system in this study enables the rural regions, as a priority area for development in the strategies for sustainable development goals in Iran, to benefit from required massive national investment and subsidies.

Author Contributions

E.A. designed, conceptualized, and developed the simulation model, analyzed the simulation results, visualized, and wrote the manuscript. B.M. reviewed, edited, and visualized. B.M., S.O., B.M.-I., and T.T. gave guidance, provided the materials, and helped to improve the quality of the work. All authors have read and agreed to the published version of the manuscript.

Funding

This research received no external funding.

Conflicts of Interest

The authors declare no conflict of interest.

Nomenclature

SubscriptsDescription
tSet of time, hour
dSet of time, day
ySet of time, year
lSet of location for the decentralized water sector
rReservoir
pmpPump
desRO desalination
convConventional
wWater
VariablesDescription
w r ( l , d , y ) Amount of water in the reservoir
w c o n v ( l , t , y ) Amount of water extraction from conventional water supplies
w p m p , d e s ( t , y ) Pumped water from the desalination plant’s reservoir
w r , d e s ( t , y ) Amount of water in the desalination reservoir
w d e s ( l , t , y ) Water production by the desalination plant
C a p c o n v ( l , y ) Water production capacity of conventional water supplies
C a p d e s ( l , y ) Water production capacity of desalination plants
C a p w i n d ( y ) Wind energy capacity
C a p p v ( y ) Capacity of the photovoltaic panels
C a p b a t ( y ) Capacity of battery unit
p c h ( t , y ) Electricity charge of battery unit
p d c h ( t , y ) Electricity discharge of battery unit
C n e w ( y ) Unit cost
P r d n e w ( y ) Cumulative production
K n e w ( y ) Cumulative investment
ParametersDescription
w d ( l , d , y ) Water demand
C a p r ( l , y ) Capacity of the water reservoir
C a p r , d e s ( y ) Capacity of the desalination unit’s reservoir
C a p p m p , d e s ( y ) Capacity of the pumping from the desalination’s reservoir
D e s s h a r e ( y ) Share of desalination from total water demand
p d e s Required energy for producing a unit of desalinated water
p p m p Required electricity for pumping unit of water from a desalination plant to the reservoir
p c o n v Energy needed to extract and transfer unit of water from conventional water resources
p w i n d ( t , y ) Wind electricity production
v ( t ) Wind speed
p p v ( t , y ) Electricity production from photovoltaic panels
I ( t ) Solar radiation
p R E ( t , y ) Renewable energy production
R E s h a r e ( y ) Target share of renewable energy production
p d ( t , y ) Electricity demand
p w ( t , y ) Electricity consumption of the water sector
p g r i d ( t , y ) Electricity exchange with the national grid
e f f b a t Efficiency of the battery storage
E b a t ( t , y ) Energy stored in the battery unit
C i n i t i a l Initial unit cost
α Learning-by-doing elasticity
β Learning-by-searching elasticity
P r d i n i t i a l Initial cumulative production
K S Knowledge stock
I n Investment expenditures
O M Operations and maintenance expenditures
F Fixed expenditures
C f Capacity factor
d r Discount rate
L f Lifetime of the technology

Appendix A. Supply-Demand Module

Appendix A.1. Water Module

Appendix A.1.1. Integrated System

The amount of water in the water reservoir in each location should be more than the water demand for the next day, which is described as:
w d ( l , d , y ) w r ( l , d 1 , y )
where w d is the daily water demand in each location and w r is the amount of water in the water reservoirs. For the centralized water sector, there is only one location.
For the decentralized water sector, the hourly amount of water in the water reservoir for each location is obtained as Equation (A2).
w r ( l , t , y ) = w r ( l , t 1 , y ) + w c o n v ( l , t , y ) + w d e s ( l , t , y )
where w c o n v describes the amount of water extraction from conventional water supplies, which are underground and surface water resources, and w d e s is the amount water production from the desalination supply.
For the centralized water sector, the hourly amount of water in the desalination reservoir follows Equation (A3).
w r , d e s ( t , y ) = w r , d e s ( t 1 , y ) + w d e s ( t , y ) w p m p , d e s ( t , y )
where w p m p , d e s is the amount of pumped water from the centralized desalination plant’s reservoir.
The amount of stored water in each reservoir cannot exceed the capacity of the reservoir, which can be described as (A4) and (A5).
w r ( l , t , y ) C a p r ( l , y )
w r , d e s ( t , y ) C a p r , d e s ( y )
The capacity of water production from the desalination plant, conventional resources, and the amount of pumped water are limited based on (A6)–(A8).
w c o n v ( l , t , y ) C a p c o n v ( l , y )
w d e s ( l , t , y ) C a p d e s ( l , y )
w p m p , d e s ( t , y ) C a p p m p , d e s ( y )
The share of desalination from the total water demand needs to meet the target for each year, which is imposed on the model as Equation (A9).
t , l w d e s ( l , t , y ) = D e s s h a r e ( y ) × l , d w d ( l , d , y )
To become economically and technically feasible, desalination facilities are required to operate more than 80% of their total capacity through a year [80]. This constraint is considered in the model as:
t w d e s ( l , t , y ) C a p d e s ( l , y ) × 365 × 0.8
The hourly electricity consumption of the centralized water sector for each year is calculated as Equation (A11). It is assumed that for the decentralized water sector, the desalination is located exactly at the demand location; as a result, there is no need to transfer the desalinated water. The hourly electricity consumption of the decentralized water sector is obtained from Equation (A12).
p w ( t , y ) = t p c o n v × w c o n v ( t , y ) + p p m p × w p m p , d e s ( t , y ) + p d e s × w d e s ( t , y )
p w ( t , y ) = l , t p c o n v × w c o n v ( l , t , y ) + p d e s × w d e s ( l , t , y )
where p w depicts the electricity demand of water sector, p d e s shows the required electricity to produce unit of desalinated water, p c o n v is the amount of electricity required for extracting and transferring unit of water from conventional water supplies, and p p m p is the required electricity for pumping unit of water from the desalination facility to the reservoir.

Appendix A.1.2. Separated System

The water sector’s electricity demand is assumed to be constant for the separated system, which is obtained from Equation (A13).
p w ( t , y ) = [ D e s s h a r e ( y ) × ( p p m p + p d e s ) + ( 1 D e s s h a r e ( y ) ) × p c o n v ] × w d ( d , y ) × 1 24

Appendix A.2. Energy Module

In the proposed model, the hourly wind power generation is obtained from Equation (A14) [81]
p w i n d ( t , y ) = C a p w i n d ( y ) v ( t ) 3
where p w i n d is the wind electricity generation in each hour, C a p w i n d describes the capacity of wind supply, and v is the normalized hourly wind speed (normalized based on maximum wind speed throughout each year 0     ν 3     1 ).
The hourly electricity production from photovoltaic panels follows Equation (A15) [82].
p p v ( t , y ) = C a p p v ( y ) I ( t )
which p p v depicts the solar electricity production, C a p p v is the capacity of the solar electricity supply, and I is the normalized hourly solar irradiation (normalized based on the maximum solar radiation throughout the year 0 I ( t ) 1 ).
As a result, the hourly renewable electricity generation is calculated as (A16).
p R E ( t , y ) = p p v ( t , y ) + p w i n d ( t , y )
where p R E is the hourly renewable energy generation.
Equation (A17) ensures to meet the yearly target share of renewable energy generation of the total electricity demand.
t p R E ( t , y ) = R E s h a r e ( y ) × t [ p d ( t , y ) ]
where R E s h a r e depicts the yearly target share of variable renewable energy generation and p d ( t , y ) describes the hourly electricity demand.
Equation (A18) guarantees the balance to meet hourly electricity demand.
p d ( t , y ) + p w ( t , y ) = p g r i d ( t , y ) + p R E ( t , y )
where p g r i d is the absolute value of hourly electricity exchange with the electric grid. p g r i d includes both negative (selling electricity to the grid) and positive values (purchasing electricity from the grid).
The objective function is to minimize the electricity exchange with the national grid, which is explained as:
Min t , y | p g r i d ( t , y ) |
For the integrated system, the capacity of solar supply, wind supply and desalination facilities, hourly water extraction from the conventional water supplies, hourly water production of each desalination facility, hourly pumped water from the desalination unit’s reservoir to the water reservoir (only for the integrated system with centralized water sector), and hourly electricity exchange with the national grid are the variables of the optimization problem. For the separated system, the capacity of solar supply, wind supply, and hourly electricity exchange with the national grid are considered as the variables of the optimization problem.

Appendix B. Energy Storage Module

The energy storage module is developed to find required batteries equivalent to the operational capacity of the flexible water sector. To this aim, the share of excess renewable electricity generation of the base scenario is required to be equal to the other proposed scenarios by installing new batteries, which is imposed on the model based on Equation (A20).
if   p g r i d ( t , y ) < 0 p g r i d ( t , y ) / ( R E s h a r e ( y ) × t [ p d ( t , y ) ] ) = E x s c ( y )
where E x s c depicts the share of excess renewable electricity generation for each scenario. This excess electricity generation refers to the portion of variable renewable power production, which exceeds electric load.
Equation (A21) describes the amount of stored energy in the battery storage.
E b a t ( t , y ) = E b a t ( t 1 , y ) × e f f b a t + p c h ( t , y ) p d c h ( t , y )
where E b a t depicts the amount of hourly stored energy, which cannot exceed the capacity of the battery storage (see (A22)), p c h is the amount of hourly electricity charge of the battery storage, and p d c h shows the amount of hourly discharged energy from the battery storage.
E b a t ( t , y ) C a p b a t ( y )
To limit the hourly amount of charged or discharged electricity based on charge and discharge rate limitation of battery storage, Equation (A23) is considered in the model.
p c h ( t , y ) C a p b a t ( y ) × R b a t p d c h ( t , y ) C a p b a t ( y ) × R b a t
In Equation (A23), R b a t is the maximum charge/discharge rate of the battery storage (share of the total capacity).
Equation (A24) ensures the electricity balance to meet hourly electricity demand in this model.
p d ( t , y ) + p w ( t , y ) + p c h ( t , y ) = p g r i d ( t , y ) + p R E ( t , y ) + p d c h ( t , y )
The objective function, which is depicted in (A25), is to minimize the capacity of batteries ( C a p b a t ( y ) ) equivalent to the operational capacity of the flexible water sector.
Min y C a p b a t ( y )
The new required battery storage capacity, hourly electricity exchange with the national grid, and charge/discharge of the battery storage are the variables of this optimization problem.

Appendix C. Learning Curve

Equation (A26) describes the two-factor learning curve in detail [55].
C n e w ( y ) = C i n i t i a l × ( P r d n e w ( y ) P r d i n i t i a l ) α × ( K n e w ( y ) K S ) β
where C n e w depicts the unit cost, C i n i t i a l is the initial unit cost, P r d i n i t i a l is the initial cumulative production, P r d n e w describes the historical cumulative production, which is described in Equation (A27) [72], α is the learning-by-doing elasticity, K S shows the knowledge stock, K n e w depicts the historical cumulative investment on R&D, which is obtained from Equation (A28) [55], and β is the learning-by-searching elasticity.
P r d n e w ( y ) = Y = 0 y Pr d ( Y )
where Pr d describes the yearly new production and Pr d ( 0 ) refers to the production in the starting year of applying the technology.
K n e w ( y ) = Y = 0 y K ( Y )
Based on this learning curve, the technology cost decreases by increasing the cumulative production as well as investment in research and development (R&D). In the two-factor learning curve, learning-by-doing (LDR) and learning-by-searching (LSR) illustrate this decreasing technology cost, denoting the percentage of variation in cost as a result of doubling the cumulative production and R&D investment, respectively. The LDR is calculated as 1 2 α and the LSR is obtained as 1 2 β .
Due to a lack of data, a new approach is developed to estimate the learning-by-searching ratio of the two-factor learning curve and the average R&D budget using particle swarm optimization coded into MATLAB R2019b.
To validate this approach, the results for the United States residential photovoltaic [83] and the United States wind supply [84] are compared with the IEA R&D budget database [64] and other studies [55]. For residential photovoltaic using 17-year data from 2000 to 2016 for the US, with a time delay of one year for investment on R&D, the estimated learning-by-doing ratio is 9.5%, and the learning-by-searching ratio is 18.8% with a goodness of fit (R2) of 94.0%. For the United States residential photovoltaic, using real data from 2009 to 2016, a study [60] reached 94.9% for a goodness of fit (R2). The real yearly average investment on R&D in the United States residential photovoltaic [64] is 0.128 $Billion (2018 United States dollars) based on the IEA R&D budget database, and the estimated average by the proposed PSO (particle swarm optimization) approach in this study is 0.124 $Billion (2018 United States dollars).
For wind technology, using data from 2009 to 2018 for the US, with a time delay of three years for investment on R&D, the estimated LDR is 17.1%, and the LSR is 38.7% with a goodness of fit (R2) of 92.2%. For the United States wind technology, using real data from 2009 to 2016, a study [60] reached 97.4% for a goodness of fit (R2). The real yearly average investment on R&D in the United States wind industry [64] is 0.059 $Billion (2018 United States dollars) based on the IEA R&D budget database, and the estimated average by the proposed (particle swarm optimization) PSO approach in this study is 0.056 $Billion (2018 United States dollars).
Based on the literature [60], the decay factor for invested R&D on wind and photovoltaic technologies is between 2.5% and 10.5%. By considering this decay factor, the proposed approach is considered suitable to apply in this study. The parameters of two-factor learning curves for the levelized cost of desalinated water and levelized cost of utility-scale wind and photovoltaic electricity are estimated using the proposed approach.
Due to a lack of data for the levelized cost of wind and photovoltaic energy in the Middle East, 81 projects have been examined to estimate the LCOE, which are summarized in Table A1 and Table A2. The levelized cost of energy is obtained from study [81] as:
y = 0 L f 1 I n ( y ) + O M ( y ) + F ( y ) ( 1 + d r ) y t = 1 n C a p ( y ) × C f ( y ) × 8760
where I n describes the investment expenditures in each year, O M depicts the operations and maintenance expenditures in year y, F is the fixed expenditures in year y, d r is the discount rate, L f shows the lifetime of the technology, C a p is the installed capacity of the technology in each year, and C f is the capacity factor of the supply technology in each year.
The capital investment costs, fixed and variable costs, and the average capacity factor (see Table A3) of utility-scale wind and photovoltaic electricity supplies have been obtained using overall variable renewable electricity production of the countries [85,86,87] in the Middle East and the examined projects in Table A1 and Table A2. The capacity of wind and photovoltaic resources from 2000 to 2018 in the Middle East is shown in Figure A1.
The Middle East in this study refers to these countries: Islamic Republic of Iran, Iraq, Israel, Jordan, Kuwait Bahrain, Palestine, Turkey, Egypt, Syrian Arab Republic, Lebanon, Oman, Qatar, Kingdom of Saudi Arabia, United Arab Emirates, Yemen.
Table A1. List utility-scale wind projects for obtaining LCOE.
Table A1. List utility-scale wind projects for obtaining LCOE.
ProjectCapacity in MWInvestment M$ 2018LCOE ($/MWh)Year
Bahçe Wind Farm135230.31107.82010
Sayalar Wind Power Plant2332.9373.82011
Samurlu Wind Power Plant3049.4577.82011
Kozbeyli Wind Power Plant29.947.9777.02011
Usak Wind Power Plant5462.1469.12012
Sadilli Wind Power Plant38.554.7568.82012
Karadere Wind Power Plant1529.7577.72012
Edincik Wind Power Plant3052.4374.02012
Günaydın Wind Power Plant12.518.7570.12012
Geres Wind Power Plant27.538.15667.82013
Söke Wind Power Plant4557.7966.12013
Salman Wind Power Plant27.539.4368.52013
Mocha Wind Park Project60155.2287.52013
Geres Wind Power Plant27.537.5760.92014
Bozyaka Wind Power Plant4.88.6466.12014
Ova Wind Power Plant1824.0960.52014
Edincik Ii Wind Power Plant26.436.0160.92014
Pitane Wind Power Plant4.89.1069.22014
Tafila Wind Farm117304.0680.12014
Amasya Wind Power Plant4276.7764.42015
Bozyaka Wind Power Plant12.58.6646.52015
Umurlar Ext Power Plant26.435.8152.62016
Soma Wind Power Plant3036.5550.82016
Edincik Iii Wind Power Plant2126.2051.22016
Incesu Wind Power Plant1420.8554.42016
Çakıl Wind Power Plant31.5550.5354.52017
Çamseki Plant (Extension)42.339.9845.62017
Alibey Adası Wind Power Plant3036.6449.32017
Gulf Of El Zayt Farm, El Zayt200348.3056.42017
Egypt - Development Project250409.7755.02018
Lekela Egypt Power Boo S.A.E25233930.12018
Yahşelli Wind Power Plant2031.430.12018
Table A2. List of large-scale PV projects for obtaining LCOE.
Table A2. List of large-scale PV projects for obtaining LCOE.
ProjectCapacity in MWInvestment M$ 2018LCOE ($/MWh)Year
Belectric And Solel Boneh10-169.02013
Talmei Bilu Solar Power Plant2148.39256.42013
Falcon Ma An For Solar Energy1050179.82014
Shamsuna Power Company Llc.1021171.92014
Zahrat Al-Salam For Energy1031200.22014
Al-Zanbaq For Energy Generation Psc1031200.22014
Al-Ward Al-Joury For Energy Generation PSC4031200.22014
Ketura Solar Facility20083.7139.32015
Mohammed Bin Rashid Almaktoum Solar Park Phase II10345.38130.72015
Maan Development Area1031.78164.82015
Martifer Solar52.527.55154.82015
First Solar28.3158.92161.22015
Scatec Solar Asa4350.3131.92015
Sunedison12.9105.94148.02015
Zaatari Syrian Refugee Camp5015.69110.12016
Al Sharika Al Mahaliya Li Aamal Al Miya Wa Al Taka Al Shamsia Psc8572115.22016
Akfen Solar Power Project17.9100109.22016
Soho Solar PV Power Plant20025.46114.82016
Mohammed Bin Rashid Al Maktoum Solar Park II29.68327.82119.72016
Hipot Solar PV Power Plant50038.07111.62016
MGES Power200261.5694.32016
Baynouna Solar Energy Company Psc66.6266.35103.12017
Alsafawi For Green Energy PSC5.8143578.12017
İven Solar PV Power Plant17.9887.8496.12017
Caba Solar PV Power Plant723.7795.52017
Stars Solar PV Power Plant48.94611.56102.82017
Met-Gün Solar PV Power Plant34.556.4991.82017
Çiftay Solar PV Power Plant10.347.4896.72017
Başarı Solar PV Power Plant35.913.6595.62017
Zen Solar PV Power Plant15.2557.37101.62017
Aktaş Solar PV Power Plant10.5919.4094.42017
Zigana Solar PV Power Plant8.1515.2398.12017
Koyuncu Nevşehir Solar PV Power Plant9509.6292.42017
Mohammed Bin Rashid Al Maktoum Park1177962.9688.82017
Noor Abu Dhabi Solar PV Plant in Sweihan100891.2583.12017
Pdo Amin PV Plant100100.0080.82018
Askar Landfill9.98-49.22018
Mt Dogal Solar PV Power Plant9.9518.9398.82018
Omicron Engil Solar PV Power Plant9.918.4597.92018
Me - Se Solar PV Power Plant9.9816.4694.12018
Yaysun Solar PV Power Plant12.21999.02018
Sunfarming Eurasia Asset Enerji Yat5001686.22018
Ibri PV Plant9.95500.0080.82018
Omicron Ercis Solar PV Power Plant9.9517.4755.42019
Iota Solar PV Power Plant9.9517.9155.42019
Psi Engil Solar PV Power Plant2617.8055.42019
Cingilli Solar PV Power Plant (Licensed)-38.3555.42019
Sakaka Project200300.0023.42019
Al-Muwaqqar Solar Energy Project10253.8355.42019
Table A3. Average capacity factor and LCOE of wind and PV electricity resources in the Middle East.
Table A3. Average capacity factor and LCOE of wind and PV electricity resources in the Middle East.
YearWind CF Photovoltaic CFWind LCOE ($/MWh)Photovoltaic LCOE ($/MWh)
20000.190.17--
2001-0.17--
20020.210.21--
2003-0.17--
20040.230.16--
20050.230.19--
20060.200.15--
20070.170.21--
20080.250.19--
20090.180.16--
20100.260.20107.8-
20110.310.1776.2-
20120.290.1772.7-
20130.280.2072.5212.7
20140.290.2066.3190.5
20150.290.1955.4147.2
20160.340.2052.2110.7
20170.340.2151.594.2
20180.370.2342.585.8
2019-0.23-50.1

Appendix D. Location of Rural Districts

The name and location of 19 rural districts in Jask county, which are selected in this study, are summarized in Table A4.
Table A4. List of rural locations selected as the case study.
Table A4. List of rural locations selected as the case study.
Name of Rural DistrictPopulation [59]Households [59]Link of Location [57]
Bahl1755426https://www.google.com/maps/place/Bahl,+Hormozgan+Province,+Iran/@25.6905931,57.8505706,16z/data=!3m1!4b1!4m5!3m4!1s0x3ef245334b39178d:0xbcdfde949993da52!8m2!3d25.6921894!4d57.8509418
Jāsk-e-kohne1202288https://www.google.com/maps/place/J%C4%81sk-e-kohne,+Hormozgan+Province,+Iran/@25.7422102,57.7639997,15z/data=!3m1!4b1!4m5!3m4!1s0x3ef24eda7e4c933b:0x39806870cdc083c1!8m2!3d25.7411497!4d57.7714829
Koeek786210https://www.google.com/maps/place/Koeek,+Hormozgan+Province,+Iran/@25.7583282,57.6670104,11z/data=!4m5!3m4!1s0x3ef249017572c2df:0x42d897398e4154ba!8m2!3d25.7942639!4d57.778575
Gazdan1258317https://www.google.com/maps/place/Gazdan,+Hormozgan+Province,+Iran/@25.7694311,57.7917444,16z/data=!3m1!4b1!4m5!3m4!1s0x3ef248cf39072dff:0xc39d472d0a032940!8m2!3d25.766858!4d57.7962176
Zaminlashkari464131https://www.google.com/maps/place/Zaminlashkari,+Hormozgan+Province,+Iran/@25.7484823,57.7553738,16z/data=!3m1!4b1!4m5!3m4!1s0x3ef24eca56ac286b:0x799bae564cc8787c!8m2!3d25.7472196!4d57.7587182
Bahmadi505133https://www.google.com/maps/place/Bahmadi,+Hormozgan+Province,+Iran/@25.7871894,57.5510557,11.79z/data=!4m5!3m4!1s0x3ef23541f3128313:0x9ddef543c32eaa32!8m2!3d25.8285336!4d57.6644487
Negar711181https://www.google.com/maps/place/Negar-e-p%C4%81yin,+Hormozgan+Province,+Iran/@25.8007038,57.4989623,11.79z/data=!4m5!3m4!1s0x3ef3cae3da854af5:0x47584c97d37659c!8m2!3d25.8385738!4d57.6148668
Gangan50996https://www.google.com/maps/place/Gang%C4%81n,+Hormozgan+Province,+Iran/@25.8542635,57.3436244,11.83z/data=!4m5!3m4!1s0x3ef3cf59b0851fb7:0x125e05cd1f4c4417!8m2!3d25.8631558!4d57.4606046
Bunji-ye Maski748176https://www.google.com/maps/place/Bunji-ye+Maski,+Hormozgan+Province,+Iran/@25.8960276,57.2979087,14z/data=!3m1!4b1!4m5!3m4!1s0x3ef3dd2d6ca6c17f:0x22f178da9751952a!8m2!3d25.8960291!4d57.3154183
Gattan-e Olya1123271https://www.google.com/maps/place/Gattan-e+Olya,+Hormozgan+Province,+Iran/@25.9936337,57.2757001,11.88z/data=!4m5!3m4!1s0x3ef3de3d57d9b5f7:0xfa9800a611b82b84!8m2!3d25.9924426!4d57.2937363
Gazi689158https://www.google.com/maps/place/Gazi,+Hormozgan+Province,+Iran/@26.0719969,57.2147293,14z/data=!3m1!4b1!4m5!3m4!1s0x3ef15f06250a5fcb:0x1debd5ced9d9e613!8m2!3d26.0719984!4d57.2322389
Gavan-e Pain991235https://www.google.com/maps/place/26%C2%B005'31.0%22N+57%C2%B016'43.0%22E/@26.0922704,57.294239,10.96z/data=!4m5!3m4!1s0x0:0x0!8m2!3d26.091944!4d57.278611?hl=en
Karti736191https://www.google.com/maps/place/Karti,+Hormozgan+Province,+Iran/@25.4438073,58.8945826,10.83z/data=!4m5!3m4!1s0x3eed201474dd91e3:0x3604e51b3390f5d5!8m2!3d25.4589232!4d59.0867475
Gati466122https://www.google.com/maps/place/25%C2%B035'48.3%22N+58%C2%B057'18.3%22E/@25.596758,58.955089,11z/data=!4m5!3m4!1s0x0:0x0!8m2!3d25.596758!4d58.955089?hl=fa
Pyveshk1220349https://www.google.com/maps/place/Pyveshk,+Hormozgan+Province,+Iran/@25.55363,58.8967607,14z/data=!3m1!4b1!4m5!3m4!1s0x3eed1084afeaabbd:0xba1cfd33f0e42fc0!8m2!3d25.5551815!4d58.9120326
Vanak486126https://www.google.com/maps/place/Vanak,+Hormozgan+Province,+Iran/@25.5372237,58.8738763,17z/data=!3m1!4b1!4m13!1m7!3m6!1s0x3eed1084afeaabbd:0xba1cfd33f0e42fc0!2sPyveshk,+Hormozgan+Province,+Iran!3b1!8m2!3d25.5551815!4d58.9120326!3m4!1s0x3eed10e3416e1997:0x81243b597e74c6f2!8m2!3d25.536638!4d58.8755018
Lirdaf1734451https://www.google.com/maps/place/Lirdaf,+Hormozgan+Province,+Iran/@25.6407523,58.8608408,16z/data=!3m1!4b1!4m5!3m4!1s0x3eed0ef9bb94f749:0x5fd6f536fdd98172!8m2!3d25.6400557!4d58.8661929
Sourgalm44796https://www.google.com/maps/place/Sourgalm,+Hormozgan+Province,+Iran/@25.6336313,58.0429605,11.83z/data=!4m13!1m7!3m6!1s0x0:0x0!2zMjXCsDQyJzA4LjAiTiA1OcKwMTEnMjguMCJF!3b1!8m2!3d25.702222!4d59.191111!3m4!1s0x3ef2639faffc5071:0x9c61b7e42e113f9e!8m2!3d25.656382!4d58.142395?hl=en
Gouhert1025264https://www.google.com/maps/place/Gouhert,+Hormozgan+Province,+Iran/@25.6304412,58.8011349,16z/data=!3m1!4b1!4m13!1m7!3m6!1s0x0:0x0!2zMjXCsDM5JzA1LjAiTiA1OMKwNDknMjYuMCJF!3b1!8m2!3d25.651389!4d58.823889!3m4!1s0x3eed0c49d0625f91:0x8c9b1145fa7ca564!8m2!3d25.6305382!4d58.8032055?hl=en
Total 16,8554221

Appendix E. Renewable-Powered Desalination Technologies

Table A5. List of the reference studies to outline the development state of renewable-powered desalination technologies.
Table A5. List of the reference studies to outline the development state of renewable-powered desalination technologies.
TechnologySize (m3/day)Cost ($/m3)Year Ref.
PV RO1–2503.6–33.02017[88]
PV RO4001.5–3.42015[89]
PV RO<1006.5–15.62013[90]
PV RO-12.5–16.82017[91]
PV RO<10011.7–15.62017[92]
Wind RO 80-2017[91]
Wind RO2400–33600.7–2.02017[88]
Wind RO-1.8–5.42015[89]
Wind RO50–20001.9–9.02013[90]
Wind RO50–20002.0–5.22017[92]
Solar thermal MED20-2017[91]
Solar thermal MED> 50002.4–2.82017[88]
Solar thermal MED>50002.5–3.02017[91]
Solar thermal MED>50002.0–2.52017[92]
Solar thermal MED-1.0–7.32015[89]
Solar still0.01–0.21.3–6.52017[88,93]
Solar still<1.2-2019[94]
Solar still<1.01.3–6.52013[90]
PV ED<1.05.8–16.02017[88]
PV ED<1.01.2–12.62017[91]
PV ED0.001–0.20.2–13.02015[95]
Geothermal MED200-2017[91]
Geothermal MED19201.72017[88]
Geothermal MED802.0–2.82013[90]
Geothermal MED50–1000-2017[92]
Geothermal MED 3.8–5.72018[96]
Geothermal MED14401.72019[97]
Solar HDH0.005–1.23.0–7.02016[98]
Solar HDH-8.6–9.72017[88]
Solar HDH-2.8–7.02017[91]
Solar HDH0.001–0.12.6–6.52017[92]
Solar thermal MSF-1.0–5.02017[88]
Solar thermal MSF0.2–10-2011[99]
Solar thermal MSF1–10-2019[100]
Solar MD 0.002–0.110.5–19.52017[88]
Solar MD0.002–0.110.5–19.52013[90]
Wind/MVC < 100 5.2–7.82017[88]
Wind/MVC<1005.2–7.82013[90]
Wind MVC<1005.6–8.42017[91]
Ocean-based RO1000–30000.7–1.22017[92]
Ocean-based RO500–18000.9–1.02014[101]
Wind ED72–192-2011[102]
Wind ED-2.0–3.52018[96]
Geothermal MD17132018[103]
Geothermal MD20,0000.52018[96]
Geothermal HDH31.22005[104]
Geothermal HDH-1.22007[105]
Geothermal HDH-1.22019[97]
Geothermal HDH-1.22016[106]

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Figure 1. The status of renewable-powered desalination technologies.
Figure 1. The status of renewable-powered desalination technologies.
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Figure 2. (a) Centralized water sector (base and C_RO scenarios). (b) Decentralized water sector (D_RO and D_MED scenarios).
Figure 2. (a) Centralized water sector (base and C_RO scenarios). (b) Decentralized water sector (D_RO and D_MED scenarios).
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Figure 3. The proposed model for an energy system with variable renewable resources (VRE) and water supply with desalination.
Figure 3. The proposed model for an energy system with variable renewable resources (VRE) and water supply with desalination.
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Figure 4. Iran’s main drainage basins (adapted from Iran Water Statistical Yearbook 2011-2012 [56]) and the county of study [57].
Figure 4. Iran’s main drainage basins (adapted from Iran Water Statistical Yearbook 2011-2012 [56]) and the county of study [57].
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Figure 5. Share of photovoltaic (PV) in the total VRE electricity production.
Figure 5. Share of photovoltaic (PV) in the total VRE electricity production.
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Figure 6. Share of wind in the total VRE electricity production.
Figure 6. Share of wind in the total VRE electricity production.
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Figure 7. Share of self-consumption from VRE electricity production and amount of excess renewable electricity generation.
Figure 7. Share of self-consumption from VRE electricity production and amount of excess renewable electricity generation.
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Figure 8. Water sector’s electricity consumption and share of total electricity demand.
Figure 8. Water sector’s electricity consumption and share of total electricity demand.
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Figure 9. Capacity and cost of the battery unit to reach the same VRE self-consumption for: (a) C_RO scenario; (b) D_RO scenario; (c) D_MED scenario. (d) The required total capacity of batteries in each year.
Figure 9. Capacity and cost of the battery unit to reach the same VRE self-consumption for: (a) C_RO scenario; (b) D_RO scenario; (c) D_MED scenario. (d) The required total capacity of batteries in each year.
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Figure 10. Learning-curve model fitting of photovoltaic (PV) investment cost.
Figure 10. Learning-curve model fitting of photovoltaic (PV) investment cost.
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Figure 11. Learning-curve model fitting of wind-power investment-cost reduction.
Figure 11. Learning-curve model fitting of wind-power investment-cost reduction.
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Figure 12. Learning-curve model fitting of the desalination industry investment cost: (a) Reverse osmosis (RO) technology; (b) multi-effect desalination (MED) technology.
Figure 12. Learning-curve model fitting of the desalination industry investment cost: (a) Reverse osmosis (RO) technology; (b) multi-effect desalination (MED) technology.
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Figure 13. Share of lifetime VRE electricity production from the saved budgets out of the total VRE electricity production of the base scenario and required budget. Share of lifetime RO water production from the saved budgets out of the total RO production of the base scenario and required budget.
Figure 13. Share of lifetime VRE electricity production from the saved budgets out of the total VRE electricity production of the base scenario and required budget. Share of lifetime RO water production from the saved budgets out of the total RO production of the base scenario and required budget.
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Figure 14. Reduction in greenhouse gas (GHG) emissions for each scenario.
Figure 14. Reduction in greenhouse gas (GHG) emissions for each scenario.
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Figure 15. Sensitivity analysis on the share of R&D from the saved budgets for the share and budget of VRE power production for: (a) The C_RO scenario; (b) the D_RO scenario; (c) the D_MED scenario.
Figure 15. Sensitivity analysis on the share of R&D from the saved budgets for the share and budget of VRE power production for: (a) The C_RO scenario; (b) the D_RO scenario; (c) the D_MED scenario.
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Figure 16. Sensitivity analysis on the share of R&D from the saved budgets for share and budget of desalination water production for: (a) the C_RO scenario; (b) the D_RO scenario; (c) the D_MED scenario.
Figure 16. Sensitivity analysis on the share of R&D from the saved budgets for share and budget of desalination water production for: (a) the C_RO scenario; (b) the D_RO scenario; (c) the D_MED scenario.
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Figure A1. The capacity of wind and PV resources from 2000 to 2018 in the Middle East.
Figure A1. The capacity of wind and PV resources from 2000 to 2018 in the Middle East.
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Table 1. Desalination technologies.
Table 1. Desalination technologies.
Phase-Change ProcessesMembrane-Based Processes
Multi-stage flash (MSF)Reverse osmosis (RO)
Multiple effect distillation (MED)Electrodialysis (ED)
Vapor compression (VC)Membrane distillation (MD)
Freezing
Humidification/dehumidification (HDH)
Solar stills
Table 2. Renewable energy resources used for desalination purposes.
Table 2. Renewable energy resources used for desalination purposes.
Energy Sector DescriptionEnergy ResourceRef.
Model TypeDesalination TechnologySolar ElectricitySolar ThermalWind TurbineGeothermalOcean EnergyHydropowerDiesel GeneratorHydrogen
CentralizedRO [10]
RO [11]
RO [12]
RO [13]
RO, MED [14]
RO [15]
RO [16]
RO [17]
RO [18]
RO [19]
RO, MVC [20]
RO [21]
RO [22]
RO [23]
RO [24]
RO [25]
RO [26]
RO [27]
RO [28]
RO [29]
RO [30]
MSF [31]
RO [32]
RO [33]
RO [34]
RO [35]
MED [36]
MED [37]
DecentralizedRO [38]
Table 3. Transport costs of desalinated water.
Table 3. Transport costs of desalinated water.
City, CountryDistance (km)Elevation Increase (m)Transport Cost (US D/m3)
Beijing, China1351001.13
New Delhi, India10505001.90
Yemen, Sana13525002.38
Riyadh, Saudi Arabia3507501.60
Crateus, Brazil2403501.33
Mexico City, Mexico22525002.44
Zaragoza, Spain1635001.36
Mexico City, Mexico2803202.44
Table 4. Estimated future levelized cost of energy (LCOE) of renewable and levelized cost of desalinated water (LCOW) of the desalination technologies.
Table 4. Estimated future levelized cost of energy (LCOE) of renewable and levelized cost of desalinated water (LCOW) of the desalination technologies.
Year/ScenarioLCOE of Wind Electricity ($/MWh)LCOE of Solar Photovoltaic ($/MWh)Levelized cost of Desalinated Water ($/m3)
BaseC_ROD_ROD_MEDBaseC_ROD_ROD_MEDBaseC_ROD_ROD_MED
202034.734.734.734.755.255.255.255.22.462.192.192.46
202134.634.625.726.337.837.849.546.82.192.052.052.19
202234.534.525.726.234.434.439.838.91.991.941.941.99
202334.534.525.726.231.931.935.234.71.831.841.841.83
202434.434.425.626.230.030.032.231.91.701.751.751.70
202532.134.425.626.128.528.329.929.71.591.671.671.58
202632.034.325.526.027.126.828.027.81.491.601.601.48
202732.030.425.425.925.825.626.326.21.401.541.531.40
202828.230.325.225.825.024.224.724.61.331.481.471.32
202928.130.225.125.624.023.023.123.01.261.421.421.25
203027.426.924.925.523.122.121.621.61.201.371.361.18
203127.426.824.725.322.221.120.220.31.141.321.311.12
203227.326.824.625.221.420.219.019.21.091.281.271.06
203325.126.724.425.120.819.317.918.11.041.241.221.01
203425.125.324.025.020.118.517.017.21.001.201.180.97
203522.923.623.924.819.617.816.116.40.961.161.140.92
203621.123.523.724.719.217.115.315.60.921.131.110.88
203720.020.919.819.518.716.614.915.40.881.101.070.84
203819.819.919.019.318.216.114.414.80.851.071.040.80
203919.019.218.618.317.715.513.914.40.821.041.010.77
204017.818.617.517.417.315.013.514.10.791.010.980.74
Table 5. Sensitivity analysis on the share of research and development (R&D) from the saved budgets for LCOE of solar and electricity, and LCOW of desalination in 2040.
Table 5. Sensitivity analysis on the share of research and development (R&D) from the saved budgets for LCOE of solar and electricity, and LCOW of desalination in 2040.
Share of R&D (%)/ScenarioLCOE of Wind Electricity ($/MWh)LCOE of Solar Electricity ($/MWh)Levelized Cost of Desalinated Water ($/m3)
BaseC_ROD_ROD_MEDBaseC_ROD_ROD_MEDBaseC_ROD_ROD_MED
017.818.818.017.817.317.016.917.00.791.011.010.79
217.818.717.817.617.316.115.315.70.791.011.000.77
417.818.617.617.417.315.414.114.60.791.010.990.75
617.818.517.417.317.314.713.013.70.791.010.970.72
817.818.417.217.117.314.112.212.90.791.000.950.70
1017.818.417.017.017.313.611.512.20.791.000.930.68

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Ahmadi, E.; McLellan, B.; Ogata, S.; Mohammadi-Ivatloo, B.; Tezuka, T. An Integrated Planning Framework for Sustainable Water and Energy Supply. Sustainability 2020, 12, 4295. https://doi.org/10.3390/su12104295

AMA Style

Ahmadi E, McLellan B, Ogata S, Mohammadi-Ivatloo B, Tezuka T. An Integrated Planning Framework for Sustainable Water and Energy Supply. Sustainability. 2020; 12(10):4295. https://doi.org/10.3390/su12104295

Chicago/Turabian Style

Ahmadi, Esmaeil, Benjamin McLellan, Seiichi Ogata, Behnam Mohammadi-Ivatloo, and Tetsuo Tezuka. 2020. "An Integrated Planning Framework for Sustainable Water and Energy Supply" Sustainability 12, no. 10: 4295. https://doi.org/10.3390/su12104295

APA Style

Ahmadi, E., McLellan, B., Ogata, S., Mohammadi-Ivatloo, B., & Tezuka, T. (2020). An Integrated Planning Framework for Sustainable Water and Energy Supply. Sustainability, 12(10), 4295. https://doi.org/10.3390/su12104295

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