Nader
Rezaei
a,
Nancy
Diaz-Elsayed
a,
Shima
Mohebbi
b,
Xiongfei
Xie
c and
Qiong
Zhang
*a
aDepartment of Civil and Environmental Engineering, University of South Florida, 4202 E. Fowler Avenue, Tampa, FL 33620, USA. E-mail: qiongzhang@usf.edu
bSchool of Industrial and Systems Engineering, University of Oklahoma, 202 W. Boyd St, Norman, OK 73019, USA
cCity of Lakeland Water Utilities Department, 501 East Lemon Street, Lakeland, Florida 33801, USA
First published on 15th November 2018
Water shortage and water contamination necessitate adopting a reverse logistics and a closed-loop supply chain approach, which is the process of moving wastewater from its typical final destination back to the water supply chain with different levels of treatment for reuse. Hence, the incorporation of sustainability concepts through life cycle assessments for selecting reclaimed water applications considering reverse logistics and closed-loop systems is receiving more attention. However, no prior studies have evaluated the trade-off between the reclaimed water quality and corresponding costs, environmental impacts and social benefits for different types of water reuse. The aim of this study is therefore to design possible scenarios for water reuse based on water reuse guidelines and evaluate the different types of end use based on the three dimensions of sustainability (i.e., economic, environmental and social aspects) simultaneously. The different reuse types considered include unrestricted urban reuse, agricultural reuse, indirect potable reuse (IPR), direct potable reuse (DPR), distributed unrestricted urban reuse, as well as some degree of decentralization of treatment plants for distributed unrestricted urban reuse. The trade-off investigation and decision-making framework are demonstrated in a case study and a regret-based model is adopted as the support tool for multi-criteria decision-making. This study revealed that although increasing the degree of treatment for water reuse increases the implementation and operation and maintenance (O&M) costs of the design, it increases the value of resource recovery significantly, such that it can offset the capital and O&M costs associated with the treatment and distribution for DPR. Improving the reclaimed water quality also reduces the environmental footprint (eutrophication) to almost 50% for DPR compared to the other reuse scenarios. This study revealed that the distance between the water reclamation facility and the end use plays a significant role in economic and environmental (carbon footprint) indicators.
Water impactUsing the proposed multi-criteria analysis framework, sustainability of different alternatives for water reuse were evaluated through a holistic sustainability perspective that accounted for environmental, economic, and social dimensions. This study provides stakeholders with a decision-making support tool in reverse logistics application in water systems and formation of closed-loop water supply chains, as an alternative to withdrawals from natural water resources. |
Supply chain network design is receiving growing attention for solving production and demand problems in a variety of research fields.7 Traditional supply chain designs rely primarily on forward networks to manufacture products using raw materials. The reverse logistics network, also known as a backward or recovery network, is the process of returning used products to the collection and repair centers in order to be remanufactured and become qualified for reuse. The same notion can be applied to water production: wastewater can be diverted back to decentralized, satellite, or centralized wastewater treatment systems such that it is treated to a water quality level that permits water reclamation (see Fig. 1). A study conducted by Fleischmann et al. (2001) analyzed the impacts of product recovery on logistics networks.8 They showed that the product recovery impacts such as economic benefits, environmentally conscious customers and regulations, are context-dependent and require an individually comprehensive approach for redesigning any type of industrial production activity in an integral way.
Fig. 1 Conventional reverse logistics compared to its application for integrated wastewater management. |
One primary challenge in realizing such a closed-loop water system can be the lack of a planning and design framework to evaluate and identify the most sustainable application for reclaimed water. During the last decade, the emerging challenges in water systems such as water shortage, increasing water demand, and water pollution, have motivated researchers to evaluate and improve the sustainability of water systems by focusing on water reclamation and reuse. There have also been several life cycle assessment (LCA) studies, as a standard method,9,10 in recent decades to determine the impacts resulting from water treatment, water distribution, and/or wastewater treatment for reclaimed water use. In combination or parallel with LCA, multi-criteria analysis has been widely used to evaluate the available alternatives according to a defined set of measurable criteria.11 These approaches are broadly used to help decision-makers choose the most appropriate solutions in achieving particular goals according to the evaluation criteria. However, lack of environmental dimensions in the evaluation criteria for decision-making has led to tremendous problems in the past century (e.g., fog, acid rain, and red tide), necessitating a transition in allocation of the evaluation criteria for decision-making. The transition needs to provide the insights with respect to economic, environmental, and social impacts, amongst which trade-offs may arise, to be supported by the decision-makers in both private and public sectors. In addition, decision-makers may have to deal with unknowns and uncertainties, which are characteristics of investing in new designs and models.12 The bottom line is that the criteria (definition and quantification algorithm) and assessment method (data collection and visualization pattern) are highly influenced by the decision-making framework, which is selected initially based on the case-specific parameters and the study's goal.13 Amores et al. (2013) evaluated the environmental impacts of reclaimed water use for non-potable purposes such as irrigation in Spain.14 They showed that this scenario reduces the freshwater consumption due to net water savings, but it didn't make a significant improvement to the environmental impacts due to the additional resources required for tertiary treatment. Pasqualino et al. (2011) studied the environmental profile of four wastewater treatment plants for different water reuse scenarios and revealed that using the reclaimed water for potable purposes not only preserves freshwater resources, but also results in higher environmental impacts due to the additional required treatment processes.15 Muñoz et al. (2009) designed four bench-scale treatment systems to evaluate the environmental impacts of wastewater treatment for reuse via irrigation.16 The results showed that wastewater reuse for irrigation with any of the studied tertiary treatment systems had lower ecotoxicity impacts than those without tertiary treatment. Meneses et al. (2010) used LCA methods to evaluate the environmental advantages and disadvantages of reclaimed water use for non-potable applications.17 The results showed that replacing desalinated water with reclaimed water for non-potable purposes is beneficial when there is a scarcity of freshwater.
Other studies analyzed the environmental impacts of urban water systems that mainly focus on treatment technologies.18–20 These studies revealed that as the degree of treatment increases, the cost and the negative environmental impacts associated with the treatment increases, although they offset a portion of the freshwater needed. There are also a few studies that apply multi-criteria analysis in the design and evaluation of water systems. Ren and Liang (2017) developed a group multi-attribute decision analysis (MADA), with economic, environmental, and society-politic evaluation criteria, to assess the sustainability of four treatment processes for water reclamation in China.21 The developed MADA analysis consisted of: 1) determining the relative performances of the treatment processes regarding the evaluation criteria (extreme poor, very poor, poor, medium poor, fair, medium good, good, very good, and extreme good); 2) weights determination for the evaluation criteria; 3) establishing the aggregated decision-making matrix; and 4) determining the priority sequences of the alternatives and comparing their relative priorities. The results revealed that with the selected weighting strategy, anaerobic single-ditch oxidation obtained the best score among the treatment technologies; however, the selection was highly dependent on the weighting strategy. Benedetti et al. (2010) developed a Monte Carlo simulation and multi-criteria analysis to achieve the optimal configuration in the operation phase of a wastewater treatment plant in Belgium.22 The evaluation criteria consisted of effluent quality (weighted sum of contaminants load in the effluent), the portion of the time during which the effluent fails to meet the water quality limit, and costs (capital, operation, and maintenance). The proposed framework was based on the optimization of impact categories in the defined evaluation criteria. The results revealed a significant improvement in terms of economic (total costs and operation costs) and environmental (total nitrogen) impact assessments. They also showed that the anoxic fraction of the reactor volume and the volume of the primary clarifier played a significant role in system's performance. Flores-Alsina et al. (2008) also developed a multi-criteria analysis to evaluate the operational configuration of six wastewater treatment plants under uncertainty, using a Monte Carlo simulation.23 The evaluation criteria consisted of environmental, economic, legal, and technical aspects. The evaluation procedure consisted of the normalization of the systems' performance (best = 1; worst = 0), weighting of the evaluation criteria, and summation of the weighted normalized factors to obtain the final score for each treatment alternative. The results revealed that the selected configuration showed a relatively better performance in almost all of the selected impact categories, and helped reduce the risk of system failure. Nonetheless, no prior studies evaluated treatment requirements and different types of water reuse applications in a holistic (i.e., economic, environmental and social) sustainability assessment. Therefore, the goal of this study is to evaluate the trade-off between reclaimed water quality and corresponding costs, environmental impacts and social benefits for different types of water reuse applications. This trade-off analysis paired with a regret-based model can help decision-makers identify the degree of treatment needed to produce reclaimed water as well as the type of reuse applications to initiate.
The city's sewer collection system covers approximately 40000 square miles of service area and encompasses 50 miles of forced sewer and 300 miles of gravity mains. The system is being used to convey raw wastewater to two wastewater treatment plants.26 The Glendale wastewater treatment plant (WWTP) is the larger treatment facility with a design capacity of 13.7 mgd located in the southern part of the city and the Northside plant is the smaller plant with a design capacity of 8 mgd, covering the northern part of Lakeland.24 Both wastewater treatment plants consist of primary treatment and secondary treatment (conventional activated sludge [CAS]) followed by disinfection (chlorination). The City of Lakeland's current reclaimed water infrastructure provides 5.11 mgd of reclaimed water to the McIntosh power generation facility where the water is used as cooling make-up water. The other portion of treated wastewater effluent receives further treatment in the Lakeland artificial wetlands. From there, the water is pumped by the TECO power generation plant.
Although Lakeland's water system is suitable for present-day water demand and treatment requirements, the City of Lakeland is undergoing rapid growth in the southwest and northeast regions of the service area, which makes it challenging to satisfy future water demand. The amount of water that the City of Lakeland can withdraw from the Floridian aquifer has been limited to an annual average daily demand (AADD) of 35.03 mgd and a monthly average maximum of 42.04 mgd. The city's water use permit is issued by SWFWMD and is valid through December 16, 2028.24 Since the service area and the population in the City of Lakeland are growing quickly, it has been predicted that in 2026 the city will have a population of approximately 242000 and a water demand projection of 35.03 mgd. Based on the city's existing permit and current water system capacity, meeting the water demand will be challenging in a few years (see Fig. S2 in ESI†). Different types of water reuse options, which can satisfy the future water demand projection, were designed, evaluated and compared based on economic and environmental criteria. Ultimately, a decision-making tool that can be used by stakeholders to evaluate the trade-offs between water reuse types, degree of treatment and sustainability constraints was also introduced. The effluent from the Glendale water reclamation facility and Lakeland's artificial wetland were considered for reuse scenarios, or as the influent for the additional treatment, when needed. The effluent water quality reports were obtained from the facilities, which were reported based on an annual average basis (2017). More information regarding the water quality and water quality requirements (reuse standards) used for the design of additional treatments can be found in the ESI† (Table S1).
First, the best location for implementation of each reuse scenario was identified based on various considerations such as available land with the minimum distance from the reclaimed water production's location, land price in the City of Lakeland, the stakeholders and the city officials' preferences and the US EPA guidelines (e.g., requirement for the minimum water travel distance between injection point and extraction wells for IPR). The different locations were evaluated and discussed during several meetings with the city officials and also based upon the US EPA guidelines. In fact, the potential locations for reuse were fairly restricted. For reuse scenarios 1 and 2, the golf courses and strawberry farmlands already existed in the city, and for DPR, the water treatment plant (between the two existing plants), which had available design capacity to receive the reclaimed water, was selected. For IPR, the nearest location for injection of reclaimed water, based on the minimum water travel distance required by EPA, was chosen. In the next step, considering the amount of available reclaimed water for each scenario, reclaimed water quality at different points of generation and the quality requirements, the best facility for providing the water needed for each reuse design was selected. The effluent water quality in each facility (e.g., Glendale WWTP, Glendale pond, and artificial wetland) was compared to the water quality requirements for each reuse scenario and the facility that required fewer (additional) treatment processes, was selected. The major pipelines were designed (i.e., diameter and length) to convey the reclaimed water from the source of generation to the reuse scenario's location; they accounted for the required water flow rate and the expected water velocity. For the minor pipelines, the same approach was adopted and the junctions and fittings were selected based on the space limitations (where needed).
To calculate the pumping power required for each scenario (major and minor pumps), the Darcy–Weisbach pressure and head loss equation was used. To obtain the Reynolds number, Darcy's friction factor, skin friction coefficients and pressure drops for pipe fittings, the Moody diagram and Fundamentals of Engineering Reference Handbook were used.30,31 For the selection of the pumps, pipeline materials, pipeline fittings and the other equipment needed for designing each scenario, the process equipment cost estimation manual32 and the McMaster-CARR website and manuals were used. For the calculation of the pipelines' length needed for reuse scenarios 5, 6, and 7, which require extensive pipelines for unrestricted decentralized urban reuse, as well as for the energy requirements for reclaimed water distribution, Bentley WaterGEMS CONNECT Software Edition [10.00.00.50] was used. The GIS data and the water network and sewer system files were obtained from the City of Lakeland's Water Utilities Department.
The first reuse scenario (unrestricted urban reuse) evaluated the use of reclaimed water for the irrigation of golf courses. With a total of 1103 golf courses and 524 golf communities, golf in the state of Florida is a critical industry contributing to the state economy.33 On average, irrigation of each golf course in Florida requires 0.26 mgd of water.28 In this scenario, 2.83 mgd of reclaimed water was taken from the Glendale WWTP's pond and conveyed to 10 different golf courses around the City of Lakeland using 12-3/4′′ O.D. pipelines with a total length of 30.26 miles. Since the water quality of Glendale WWTP's effluent met the requirement for the irrigation of golf courses, no additional treatment was needed.
Scenario 2 considered agricultural water reuse for irrigating strawberries – one of Florida's major food crops. Four major pipelines (12-3/4′′ O.D.) conveyed 4.6 mgd to 170 acres of farmland over a total length of 18406 ft. No additional wastewater treatment was required for this scenario34 and drip irrigation was assumed for dispersal.
For scenario 3 (IPR), 2.83 mgd of reclaimed water was taken from the artificial wetlands and was injected into two 750 ft injection wells (1.5 mgd capacity each). Ultraviolet (UV) disinfection was added to the treatment train to meet the total number of fecal coliforms requirement,35,36 and the reclaimed water was conveyed over 11.68 miles by a major pipeline (24′′ O.D.) from the wetlands to the injection site.
In direct potable reuse, reclaimed water serves as the influent for water treatment plants. Although this type of reuse is rare, it has been receiving more attention during the last decade. Regulations and guidelines for this type of reuse are non-existent in the U.S.; however, drinking water quality standards are recommended.27 For scenario 4, the reclaimed water was conveyed 7.98 miles by a major pipeline (24′′ O.D.) from the artificial wetlands to the T. B. Williams water treatment facility, which had the available capacity to receive the extra influent. Additional filtration and disinfection processes were added to the treatment train to satisfy drinking water quality guidelines (see Table 1 and Fig. S7 in the ESI†). Figures showing the location and pipeline required to implement each scenario can be found in the ESI† (see Fig. S3–S6, and S8).
Description | Recommended treatment | Additional treatment required | Pipeline required | Pumping requirement | Energy consumption by additional treatment | Nitrogen and phosphorus concentration in the effluent | |
---|---|---|---|---|---|---|---|
Scenario 1 | Urban reuse | Secondary treatment-filtration–disinfection | — | 30.26 mi | 48000 kW h per day | 0 kW h per day | 15.01 (mg TN/l) |
12-3/4′′ O.D. | 5.7 (mg TP/l) | ||||||
Scenario 2 | Agricultural reuse | Secondary treatment-filtration–disinfection | — | 3.49 mi | 16000 kW h per day | 0 kW h per day | 15.01 (mg TN/l) |
12-3/4′′ O.D. | |||||||
5.7 (mg TP/l) | |||||||
Scenario 3 | Indirect potable reuse | Secondary treatment-filtration–disinfection-multiple barriers for pathogen and organics removal (advanced) | UV disinfection | 11.68 mi | 32486 kW h per day | 298 kW h per day | 1.54 (mg TN/l) |
24′′ O.D. | 4.1 (mg TP/l) | ||||||
Scenario 4 | Direct potable reuse | No defined standard | Ultra-filtration-UV/H2O2-additional chlorination | 7.98 mi | 31937 kW h per day | 2678 kW h per day | 1.0 (mg TN/l) |
24′′ O.D. | |||||||
4.1 (mg TP/l) | |||||||
Scenario 5 | Distributed urban reuse | Secondary treatment-filtration–disinfection | — | 569.17 mi | 35635 kW h per day | 0 kW h per day | 15.01 (mg TN/l) |
Varying diameter | 5.7 (mg TP/l) | ||||||
Scenario 6 | Centralized treatment for distributed urban reuse | Secondary treatment-filtration–disinfection | 1 medium-scale CAS system | 569.17 mi | 35635 kW h per day | 5818 kW h per day | 15.01 (mg TN/l) |
Varying diameter | |||||||
5.7 (mg TP/l) | |||||||
Scenario 7 | Decentralized treatment for distributed urban reuse | Secondary treatment-filtration–disinfection | 5 medium-scale CAS systems | 569.17 mi | 19599 kW h per day | 7263 kW h per day | 15.01 (mg TN/l) |
Varying diameter | |||||||
5.7 (mg TP/l) |
In reuse scenario 5, a total of 2.83 mgd of treated wastewater from Glendale WWTP was distributed using an extensive “purple” pipeline for non-potable urban reuse purposes such as backyard irrigation, landscaping, and carwashes.
As it was mentioned before, the last two scenarios were designed to also evaluate the impacts of some degree of decentralization for wastewater treatment plants. In scenario 6, one centralized medium-scale WWTP with a capacity of 3.00 mgd was designed to treat 2.83 mgd of household wastewater. The reclaimed water was distributed using an extensive purple pipeline for non-potable urban reuse. In scenario 7, the City of Lakeland was divided into five different clusters and five decentralized medium-scale WWTPs with a capacity of 0.7 mgd were designed to treat 2.83 mgd of household wastewaters in total (see Fig. S9 in the ESI†). The reclaimed water was distributed using an extensive purple pipeline, again for non-potable urban reuse. Construction data from existing and decommissioned WWTPs in the City of Lakeland were used to model the centralized as well as the five decentralized plants. Details about this and other scenarios (e.g., the location of the WWTPs, pipelines, etc.) can be found in the ESI† (Tables S3–S9).
Fig. 3 shows the overview of the scenarios considered in the study and the summary of information related to each scenario can be seen in Table 1.
In order to combine capital and O&M costs for all the scenarios, annualized specific net present value (ASNPV) was calculated.38 First, the net present value (NPV) was calculated, which consisted of the present value of capital and O&M expenditures. The O&M expenses (CO&M) for each year (n = 1, 2, 3, …, 33) were converted to present values (PV) and the annualized specific net present value (ASNPV) was calculated using eqn (1) for an average interest rate, i, of 5%, lifespan, Tp, of 33 years, and demand (Pt) at time t for each component. More details about the cost calculations can be found in the ESI† (eqn S1–S4 and Table S17).
(1) |
Carbon footprint (CFP) is an abstract environmental sustainability indicator (ESI) to globally characterize the impact on climate change.40 It is an estimate of total greenhouse gas (GHG) emissions from a defined activity over a specific time frame or over the product/project's life cycle, typically expressed as carbon dioxide equivalents (CO2-eq.). Carbon footprint is highly influenced by the electricity consumption of the processes.43 Since previous LCA studies have revealed that CFP in water and wastewater industries is dominated by the electricity consumption during the processes,44,45 electricity consumption by the pumps and processes was selected to calculate CFP for this case. In this study, greenhouse gas equivalencies for electricity consumption were calculated based on eGRID data.46 Electricity consumption data were collected from the individual treatment plants in the City of Lakeland. Additionally, the pumping electricity was estimated based on the types of pumps assumed for each scenario and engineering handbooks.31
Water eutrophication (EU) refers to the nutrient enrichment (nitrogen and phosphorus) of aquatic environments and is becoming one of the biggest challenges in aquatic environmental protection around the world.47 Since the degree of eutrophication is largely determined by the magnitude of external nitrogen (N) and phosphorus (P) loads,48 the concentration of those elements in the final reclaimed water was considered for this environmental indicator expressed as PO4-equivalent. Depending on the level of treatment and the source of reclaimed water used for each scenario, the concentration of these two elements and the corresponding environmental impacts varied for each design. Moreover, for urban reuse (golf course irrigation), agricultural reuse (strawberry irrigation) and distributed unrestricted urban reuse (e.g., lawn irrigation), since nutrient uptake by the plants offsets a portion of eutrophication potential of the reclaimed water, it was included in the calculation of the eutrophication potential associated with these reuse scenarios. For agricultural reuse, drip irrigation was assumed for dispersal and the design of the irrigation system (plants, irrigation lands, and water requirement) for the calculation of nutrient uptake was based on the studies of strawberry production in the state of Florida.49 For calculation of nutrient uptake by golf course grass, strawberry plant and lawn irrigation, the required data was obtained from previous studies.50–52 As a rough estimation, 12%, 9% and 10% nutrient uptake from the reclaimed water for grass surface irrigation, strawberry drip irrigation and non-potable urban reuse (∼80% for lawn irrigation) was assumed, respectively. Water quality information was obtained mainly from stakeholders, the water and wastewater treatment plants' water quality data sheets, the artificial wetlands' influent and effluent water quality data and the water quality reports from the City of Lakeland.
The complex decision-making models, such as AHP, ELECTRE, PROMETHEE, and TOPSIS, have been widely used in urban planning55–58 and they provide the ability to use both qualitative and quantitative criteria in the evaluation process. However, the potential compensation effects between lower scores on some criteria and higher scores on others, inability to identify the most preferred solution based on the defined criteria, change in the final ranking of alternatives when a new alternative is added, complexity in implementation, and time-consuming procedure are some of the disadvantages associated with these methods, which lower the popularity of them among available methods.58–60 These methods are being used mainly for strategic decisions, while a vector normalization for multi-dimensional problems is needed.61
For single dimensional problems, when there is only one network with a limited number of alternatives during the design process, WSM and regret models can be used to find the optimal alternatives based on the defined evaluation criteria. Although these methods are relatively simpler than other multi-criteria decision-making methods, they still provide a wide range of applicability, with similar results compared to methods that are more sophisticated.11,58,62 The concept of WSM is to find the closest alternative to the “best” value and the concept of regret (opportunity loss) is to make decision recommendations based on mutually exclusive strategies.63 When the dataset is not large, it would be rational to use the simpler evaluation methods such as WSM, which require less external knowledge and provide the decision-makers with better understanding of the problem and recommended solutions.55 In this study, in order to evaluate each reuse scenario and investigate the trade-offs, a regret-based model was used based on the minimax regret criterion. The minimax regret model, also known as the savage model, is an approach to decision-making under uncertainty. For instance, when the likelihood of the possible outcomes is not known with sufficient precision to use the classical expected value criteria, the regret-based model can be used as a support tool for the decision-making process.64 Moreover, when there is a discrete number of choices, such as different possible real world scenarios, the minimax regret strategy is a useful tool for risk-neutral decision-making. The minimax regret model also provides decision-makers with the ability to normalize the evaluation criteria when there is unit diversity and uncertainty in the defined criteria. This technique minimizes the risk of making the wrong decision in selecting among the possible alternatives. Although there are a variety of alternatives for decision-making and a comparison to other models can be made, it was outside of the scope of this study. In this study, a symmetric formulation was obtained for a decision-making problem stated in terms of a specific constraint to minimize (negative) or maximize (positive) impacts. If Pi,j is defined as the performance of strategy i ∈ S (reuse scenario) for indicator j ∈ F (defined criteria and constraints), the regret (Ri,j) is defined as the difference between the impact incurred and the optimum achievable,64i.e.:
(2) |
The optimum achievable is the optimum value (maximum or minimum) in each impact category across reuse alternatives. In order to make the comparison across indicators, the normalized regret scores (NR) can be calculated by:
(3) |
And the final regret score () for each scenario can be calculated by assigning weighting factors, wj, for each indicator:
(4) |
The results were reported based on individual indicators and a multi-criteria analysis; in the latter case, weighting schemes were assigned such that equal weighting was applied to each indicator (the base case), as well as weighting schemes that were cost-centered and environmentally-centered. The weighting factors for cost- and environmentally-centered results were based on stakeholder preferences, where cost-centered assigned 55% weight for the economic indicator and 15% for the other indicators and environmentally-centered assigned 35% weight for each environmental indicator and 15% for the remaining indicators.
Primary and secondary treatment (CAS in this case) plays a significant role in the cost of the treatment trains and it was common among all scenarios for water reuse due to the minimum water quality requirements. Hence, the cost evaluation excluded the common processes and only included the processes that were different for different reuse scenarios. The results revealed that the implementation and operation of additional treatment processes was not a significant contributor to the economic indicator compared to the capital and O&M costs associated with the distribution of the reclaimed water (e.g., pipeline construction, reclaimed water pumping). On the other hand, as the reclaimed water quality increases, the value of resource recovery increases accordingly and the environmental impacts of water reclamation (eutrophication) decreases due to greater nutrient removal. As it can be seen in Fig. 4, although improving the reclaimed water quality from urban reuse to IPR and DPR had little impact on ASNPV (considering the costs associated with the water conveyance), it resulted in a significant increase to the VRR (173 vs. 3500 $ per MG for urban reuse and DPR, respectively). As the result also showed, increasing the degree of treatment after CAS from agricultural reuse to IPR and DPR did not increase the carbon footprint significantly, due to the low energy requirements of the additional treatment processes (i.e., ultra-filtration, UV disinfection and additional chlorination). Most of the previous studies have also shown that the operation phase in treatment process and water transfer are responsible for approximately 40% and 50% of GHG emissions associated with water systems, respectively.14,65–69 Wastewater treatment and disposal (reclaimed water quality) were also the significant contributors (∼91%) to the freshwater eutrophication potential.
As Fig. 4 also shows, distributed urban reuse (scenario 5) increased the ASNPV significantly. Distributed urban reuse for non-potable purposes (e.g., lawn irrigation and carwashes) required an extensive pipeline for distribution of the reclaimed water to the households (purple pipeline) and it increased the capital costs associated with this scenario and the ASNPV accordingly. Although distributed urban reuse had the highest ASNPV among all reuse scenarios, this type of reuse reduces the cost associated with withdrawal, treatment and distribution of water to the distributed end users (households) by replacing the potable water with the reclaimed water for non-potable purposes, to a greater level than other reuse scenarios. These considerations were outside the scope of this study since the amount of water offset was similar across scenarios. The summary of different costs associated with each scenario and more details about the capital costs, O&M costs and the value of resource recovery for reuse scenarios, can be found in the ESI† (Table S17).
The preferred scenario, with respect to the normalized regret score, changed as different individual impacts were considered. For example, agricultural reuse had the lowest normalized regret score for the economic (NR_ASNPV) and carbon footprint indicators (NR_CFP) (see Table 2), although there is only a small difference between the agricultural reuse scenario and the urban reuse, IPR and DPR scenarios in the case of the economic indicator. The lower regret scores could be attributed to the lower infrastructure requirements for water transfer pipelines and treatment (i.e., agricultural reuse, urban reuse, or IPR). Accordingly, the scenarios that required more water transfer and distribution (as was the case with distributed reuse) had a significantly higher NR_CFP. This was due to the higher consumption of pumping energy for reclaimed water distribution. Interestingly enough, however, the second most preferred option for the carbon footprint indicator (NR_CFP) was the implementation of decentralized treatment plants with distributed urban reuse (scenario 7). The savings in energy consumption from the local distribution of reclaimed water were enough to lead to significant reductions in this indicator relative to all centralized treatment options (excluding the most preferred option, agricultural reuse). Since the water distribution infrastructure and pumping energy had a significant influence on the preferred scenario, sensitivity to the distance to the end user and the type of terrain (hilly versus flat) are expected. Moreover, the better reclaimed water quality for IPR and DPR resulted in significantly lower social (NR_VRR) and environmental (NR_EU) impacts.
From Table 2, it is evident that when the weighting strategy transitioned from the base case to cost-centered, scenarios with a shorter distance between reclaimed water production and end use locations, and/or lower complexity in design implementation and treatment, obtained better final regret scores. Although increasing the distance from agricultural reuse to IPR and DPR increased the ASNPV and CFP significantly, the lower environmental impact (EU) and the higher social indicator (VRR) decreased the final regret scores (both cost- and environmentally-centered) associated with these two scenarios. Moreover, changing the weighting strategy to environmentally-centered improved the final regret score of scenarios with higher reclaimed water quality (IPR and DPR). Accordingly, DPR obtained the best cumulative regret score across the three weighting strategies. The sensitivity to the distance of the treatment plant and treatment costs for the DPR scenario will be examined further in section 3.4.
The results also revealed that the additional treatment needed after CAS results in a relatively small increase in the economic indicator due to the simplicity of the design and the low-cost treatment processes. However, the additional treatment increased the VRR significantly (enough to offset all the capital and O&M costs associated with the reuse scenarios). Currently, the major driver for implementation of DPR is severe drought due to the lack of regulations and guidelines for DPR and the social acceptance concerns. This study showed that DPR for the studied area is one of the best alternatives for supplementing water supply, based on different dimensions of sustainability.
Among different reuse scenarios, the selection of reuse location for DPR is highly restricted by the location of water treatment plants and the flexibility of reuse location is usually much higher for other reuse types. As Fig. 6 shows, if the distance between water reclamation and the water treatment plant increases by 6.17 miles, DPR will not be the best reuse scenario based on the base case regret score and IPR will become the best reuse type. Moreover, in some cases (for instance when the quality requirements for DPR are higher and/or the reclaimed water has lower quality), the treatment trains for DPR become more complex and it increases the associated cost for the additional treatment significantly. As it can be seen in Fig. 6, if the ASNPV associated with the additional treatment processes increases from 1712 $ per MG to 26809 $ per MG, IPR will be a better option than DPR. If the ASNPV of the additional treatment increases to $43869 per MG, agricultural reuse will also obtain a better base case regret score than DPR. Although a 6.17 mile increase in the distance between water reclamation and water treatment facilities is possible, a 26809 $ per MG increase in ASNPV for additional treatment doesn't seem realistic. According to the City of San Diego's report, in case of implementing an additional advanced water purification facility for IPR and DPR, consisting of membrane filtration, reverse osmosis, UV disinfection, and advanced oxidation, the ASNPV does not exceed $4010 per MG.80
Further investigations can be conducted to evaluate the influence of the degree of decentralization on water reuse options. The last two scenarios offered insight about decentralizing treatment to some extent, however, the analysis does not reflect the full spectrum of decentralization that can be considered (e.g., at the household- or building-level to large-scale WWT). Moreover, the effects of decentralization of water reuse and wastewater treatment on the economic and environmental impacts of the entire water system (e.g., including the freshwater withdrawn, water treatment and its distribution) was outside of the scope of this study.
Although most of the data used for the design of reuse scenarios was obtained from the previous construction projects in Polk County and the practical feedback from the City of Lakeland's officials, there were assumptions when the real data was missing (e.g., additional treatment for DPR). However, the conducted sensitivity analyses addressed some aspects of the uncertainty by showing robustness of the recommended solutions. An uncertainty analysis could be conducted to further address this limitation, which was outside the scope of this study.
Moreover, regulating and implementing the reuse scenarios with a higher water quality requirement (e.g., DPR) not only reduces the negative impacts of the reclaimed water on the environment but also increases the revenue from the wastewater significantly, as far as it can offset the majority of costs associated with the additional treatments. Since the energy consumption during the treatment processes plays a significant role in the carbon footprint associated with the water reuse scenarios, consideration of treatment trains with lower energy requirements for implementation helps further reduce the water reuse impacts on the future of climate change.
ANPV | Annualized net present value |
ASNPV | Annualized specific net present value |
CAS | Conventional activated sludge |
CFP | Carbon footprint |
DPR | Direct potable reuse |
EPA | Environmental Protection Agency |
EU | Eutrophication |
FDEP | Florida Department of Environmental Protection |
FV | Future value |
IPR | Indirect potable reuse |
ISO | International Organization for Standardization |
LCA | Life cycle assessment |
LCCA | Life cycle cost analysis |
N | Nitrogen |
NPV | Net present value |
O&M | Operation and maintenance |
P | Phosphorus |
PV | Present value |
SWFWMD | Southwest Florida Water Management District |
US | United States |
VRR | Value of resource recovery |
WHO | World Health Organization |
WTP | Water treatment plant |
WWTP | Wastewater treatment plant |
i | Annual discount rate |
n | Number of years for design's lifetime |
P t | Water demand |
T p | Planning horizon |
w | Weighting factor |
NR | Normalized regret score |
R | Regret score |
Final regret score |
Footnote |
† Electronic supplementary information (ESI) available. See DOI: 10.1039/c8ew00336j |
This journal is © The Royal Society of Chemistry 2019 |