Climate change significantly disrupts the global water cycle, impacting rainfall and social and economic development in countries like Morocco. This has led to the need for alternative solutions like desalinating sea and brackish water. However, the efficiency of water pre-treatment operations depends on the characteristics of the raw water to be treated and affects the overall system's performance in terms of water quality and cost. The final objective of this study is to design a solar-powered brackish pre-treatment technique before desalination for remote rural populations. The primary task is to select the most suitable geographical area in Morocco for sampling and analysis of water characteristics and their compliance with drinking water standards. The results help identify the most appropriate provinces for our case according to certain selection criteria (distance, annual solar radiation, rural population, access to drinking water) and analyse the water's characteristics and compliance with national or international drinking water health standards. This provides a solid foundation for the next stages of desalination method development.

  • Classify potential provinces for sampling brackish water.

  • Analyse physico-chemical characteristics of water samples.

  • Identify whether the mineral content of samples complies with national and international health standards regarding drinking water.

  • Propose a technique for pre-treatment of brackish water before the desalination unit according to the characteristics of the water and the reality of remote rural populations.

Water is an essential element for human activities, and it is used for domestic, agricultural, and industrial purposes. The existing water on the earth is about 332.5 million cubic miles, but 96% is salty and only 2.5% is fresh (Gleick 1993). Faced with the demographic and economic development that humanity has experienced, this resource is becoming increasingly scarce; around 40% of the world's population, which is predicted to increase to 60% by 2025, currently has severe water shortages (Ibrahim et al. 2017). Thus, the endowment of water resources in the world went from 9,317 m3/capita/year in 1980 to 5,500 m3/capita/year in 2020 (Official website of the world bank).

Morocco, in particular, suffers from water stress. In fact, the endowment of water resources in Morocco has decreased from 2,560 m3/capita/year in 1960 to 632 m3/capita/year in 2020. In addition, Morocco will have a deficit of nearly 2.3 billion m3/year by 2030 (Report by the Directorate of Financial 2020). Faced with this situation, the desalination of sea water and brackish water is among the solutions that have gained popularity in recent decades in several countries around the world (Jones et al. 2019). This technique remains a good alternative to conventional water supply (surface water, groundwater).

A major issue still remains to be resolved, that of access to water for rural populations in the most remote areas. In this sense the use of small desalination units based on renewable energy remains one of the most widespread solutions (Chafidz et al. 2016; Yoon et al. 2022). Their development requires, in particular, work in the field to locate sampling areas of the water to be desalinated and the analysis of these physio-chemical characteristics. This analysis constitutes an important step in characterizing water and then subsequently developing the appropriate pre-treatment methods (Maazouzi et al. 2013).

In this perspective, we will propose a brackish water pre-treatment method before desalination to serve the rural populations in Morocco who are suffering from lack of water. Considering the performance of this technique in terms of water quality (Hafez et al. 2009) and the importance of taking water characteristics into account before designing and validating the various techniques to be used, the choice of the deployment area for the desalination and analysis of water test samples reveals a crucial importance to be able to identify the populations to target, the analyses to prepare, and consequently the characteristics of the raw water that should be expected throughout the project (Gourai et al. 2015).

Through this study, we were able to identify potential provinces and prioritized based on predefined criteria to optimize sampling locations and install brackish water pre-treatment units before desalination. Starting with analysing brackish water samples, we focus on mineral content and physico-chemical characteristics, crucial for validating pre-treatment techniques before desalination. This aids in proposing a pilot model for pre-treatment techniques later on.

Criteria for study area selection

The objective of this section is to determine the provinces in which samples will be taken to analyse brackish water and to be able to subsequently adapt the water pre-treatment processes. This is done first through the identification of the selection criteria by the research group: the geographical proximity to the greater Casablanca area, the accessibility of the population to drinking water, the number of the targeted rural population, and the solar energy potential of the area.

To determine the target area, we decided to choose among the provinces of Morocco. For logistical and financial reasons, it was also decided to eliminate provinces with a distance of more than 200 km from Casablanca (National portal 2023). The potential provinces are then presented subsequently (Figure 1).

Before proceeding to the stage of choosing specific provinces by setting the importance of each criterion, it is wise to detail the information on each criterion and the method of evaluation.
Figure 1

Geographical map of Morocco with the different provinces.

Figure 1

Geographical map of Morocco with the different provinces.

Close modal

Geographical proximity of the Great Casablanca

We included this criterion because of the financial costs of travel and the costs necessary to carry out the sampling. To control the financial aspects of the project, a maximum distance of 200 km from Casablanca was set (Table 1).

Number of rural population by province

The number of rural populations in the study area is an important criterion as the project targets the largest possible rural population to ensure the impact of our solution will reach the maximum number of rural populations. Below is the number of rural populations in the provinces concerned. The data are taken from the general census established by the HCP (High Commission for Planning) in 2014 (HCP official website) (Table 2).

Population's access rate to drinking water

This accessibility rate measures the percentage of the population connected to the national drinking water network. It is of crucial importance since it designates a population that is open to solutions to guarantee their access to drinking water. The data from the HCP (High Commission for Planning 2014) (HCP official website) are collected. Figure 2 shows this rate at the provinces concerned.
Figure 2

Rate of rural population per province without access to water.

Figure 2

Rate of rural population per province without access to water.

Close modal

Solar energy potential by selected zone

To have an idea of the solar energy potential of the potential provinces, we have resorted to the solar mapping of Morocco elaborated by IRESEN (Institute of Research in Solar Energy and New Energies) (IRESEN official website). Figure 3 shows solar irradiation throughout Morocco.
Figure 3

Moroccan map of global horizontal irradiation in kWh/m2/year.

Figure 3

Moroccan map of global horizontal irradiation in kWh/m2/year.

Close modal

This mapping gives the global horizontal irradiation in kWh/m2/year of Morocco. We have selected the concerned provinces, and we have been able to summarize their respective irradiation in Table 3.

Table 1

Distances of the provinces from Casablanca

ProvinceDistance from Casablanca (km)
Sale 99 
Khémissat 183 
Skhirate Temara 92 
El Jaddida 101 
Benslimane 52 
Berrechid 36 
Sidi Bennour 165 
Settat 75 
Nouaceur 18.3 
Mediouna 14 
Mohammadia 30 
Rhamna 187 
Khouribga 124 
Fquih Ben Salah 171 
ProvinceDistance from Casablanca (km)
Sale 99 
Khémissat 183 
Skhirate Temara 92 
El Jaddida 101 
Benslimane 52 
Berrechid 36 
Sidi Bennour 165 
Settat 75 
Nouaceur 18.3 
Mediouna 14 
Mohammadia 30 
Rhamna 187 
Khouribga 124 
Fquih Ben Salah 171 
Table 2

Number of rural population by province

ProvinceRural population
Sale 66,505 
Khemissat 261,142 
Skhirate Témara 56,987 
El Jaddida 474,546 
Benslimane 119,033 
Berrechid 210,669 
Sidi Bennour 367,575 
Settat 417,357 
Nouaceur 55,166 
Mediouna 52,402 
Mohammadia 115,378 
Rhamna 211,926 
Khouribga 164,365 
Fquih Ben Salah 297,107 
ProvinceRural population
Sale 66,505 
Khemissat 261,142 
Skhirate Témara 56,987 
El Jaddida 474,546 
Benslimane 119,033 
Berrechid 210,669 
Sidi Bennour 367,575 
Settat 417,357 
Nouaceur 55,166 
Mediouna 52,402 
Mohammadia 115,378 
Rhamna 211,926 
Khouribga 164,365 
Fquih Ben Salah 297,107 
Table 3

The global horizontal irradiation in kWh/m2/year by province

ProvinceDaily horizontal solar radiation (kWh/m2/day)
Sale 5.32 
Khemissat 5.30 
Skhirate Témara 5.32 
El Jaddida 5.33 
Benslimane 5.27 
Berrechid 5.24 
Sidi Bennour 5.41 
Settat 5.37 
Nouaceur 5.4 
Médiouna 5.32 
Mohammadia 5.31 
Rhamna 5.47 
Khouribga 5.50 
Fquih Ben Salah 5.51 
ProvinceDaily horizontal solar radiation (kWh/m2/day)
Sale 5.32 
Khemissat 5.30 
Skhirate Témara 5.32 
El Jaddida 5.33 
Benslimane 5.27 
Berrechid 5.24 
Sidi Bennour 5.41 
Settat 5.37 
Nouaceur 5.4 
Médiouna 5.32 
Mohammadia 5.31 
Rhamna 5.47 
Khouribga 5.50 
Fquih Ben Salah 5.51 

The launch of sample analysis tests

Before embarking on the water quality analysis of the samples which will come from the selected provinces and for reasons of convenience, we decided to launch a test to collect and analyse some samples in the commune of Benslimane at the level of four wells with different depths in meters (P1/200 m, P2/120 m, P2/20 m, and P3/15 m). It was also decided, for comparative purposes, to include another source of brackish water in the Tissa area and a sample of seawater in EL Mansouria.

Twenty parameters were measured, five of which were carried out in the field after calibration and/or validation of the portable equipment: temperature, conductivity, pH using a multi-parameter analyser Type CONSORT – Model C535, and turbidity using a turbidity meter Type HACH-Model 2100P. Table 4 summarizes the method used and the unit of measurement for each parameter analysed.

Table 4

Methods for analysing physico-chemical components

ParameterAnalysis methodUnit
Conductivity Conductivity meter Type CONSORT – Model C535 μs/cm 
Turbidity Turbidimeter Type HACH-Model 2100P NTU 
pH CONSORT pH meter – Model C535 From 0 to 14 
Temperature Mercury thermometer/multi-parameter analyser Type CONSORT – Model C535 °C 
Alcalimetric Title Titrimetry with 0.1 N hydrochloric acid and phenophthalein meq/L 
Full Alkalinity Title Titrimetry with 0.1 N hydrochloric acid and methyl orange mg/L 
Hydrotimetric Title Complexometric titration with 0.02 M EDTA and eriochromic black T meq/L 
Calcic hardness Complexometric titration with 0.02 M EDTA and HSN mg/L 
Magnesium Deducted by the difference between total hardness and calcium mg/L 
Chlorides Determination using mercuric nitrate in the presence of an indicator: diphenylcarbazone mg/L 
Nitrates Sodium salicylate mg/L 
Nitrites Zamballi reagent method mg/L 
Ammonium Sodium phenol nitroprusside and chlorine solution mg/L 
Sulfates Precipitation of barium sulphates in a hydrochloric medium mg/L 
Potassium Flame spectrophotometry mg/L 
Sodium Flame spectrophotometry mg/L 
ParameterAnalysis methodUnit
Conductivity Conductivity meter Type CONSORT – Model C535 μs/cm 
Turbidity Turbidimeter Type HACH-Model 2100P NTU 
pH CONSORT pH meter – Model C535 From 0 to 14 
Temperature Mercury thermometer/multi-parameter analyser Type CONSORT – Model C535 °C 
Alcalimetric Title Titrimetry with 0.1 N hydrochloric acid and phenophthalein meq/L 
Full Alkalinity Title Titrimetry with 0.1 N hydrochloric acid and methyl orange mg/L 
Hydrotimetric Title Complexometric titration with 0.02 M EDTA and eriochromic black T meq/L 
Calcic hardness Complexometric titration with 0.02 M EDTA and HSN mg/L 
Magnesium Deducted by the difference between total hardness and calcium mg/L 
Chlorides Determination using mercuric nitrate in the presence of an indicator: diphenylcarbazone mg/L 
Nitrates Sodium salicylate mg/L 
Nitrites Zamballi reagent method mg/L 
Ammonium Sodium phenol nitroprusside and chlorine solution mg/L 
Sulfates Precipitation of barium sulphates in a hydrochloric medium mg/L 
Potassium Flame spectrophotometry mg/L 
Sodium Flame spectrophotometry mg/L 

For nitrogenous elements, water samples are fixed with concentrated sulphuric acid in a 500-mL polyethylene bottle and with concentrated nitric acid for Na+ and K+ cations in a 250-mL polyethylene bottle. The other unfixed parameters were sampled in a 1 L polyethylene bottle. The bottles of water taken, in accordance with Moroccan standard 03.7.059 (Moroccan standard 2020), are labelled and then sent to the laboratory in a cool box at a low temperature of ±4 °C, accompanied by a card bearing all the necessary information, in particular the origin, date, and time of sampling. Water samples are taken, transported, and stored in accordance with the protocol of national drinking water office (commonly called ONEP) quality control laboratory and standard norms (ONEP 2007; ONEP 2008).

The methods used in the Laboratory of Natural Resources and Environment (LNRE) of the Polydisciplinary Faculty of Taza (FPT) are as follows: volumetry for bicarbonates, chlorides (Cl), calcium, and magnesium (Ca2+ and Mg2+); molecular absorption spectrophotometry for sulphates, nitrates, nitrites, ammonium ions, and orthophosphates; and flame spectrophotometry for sodium and potassium (ABOUZAID and DUCHESNE 1984; Rodier 2009).

Study area selection

To summarize the results of each province by criteria, Table 5 represents an overview of the main statistics of our case study.

Table 5

Descriptive statistics of study criteria

ProvinceDistance from Casablanca (km)Rural population(%) of rural households without access to waterDaily horizontal solar radiation (kWh/m2/day)
Average 96.24 205,011.29 70.44 5.36 
Standard deviation 62.12 141,365.76 23.36 0.084 
ProvinceDistance from Casablanca (km)Rural population(%) of rural households without access to waterDaily horizontal solar radiation (kWh/m2/day)
Average 96.24 205,011.29 70.44 5.36 
Standard deviation 62.12 141,365.76 23.36 0.084 

To show once again the deviation of each province value from the global variation of each criterion, we used the normalization technique to allow aggregation of criteria with numerical and comparable data.

In our case, we aim to select the provinces that have the best possible combination to minimize the distance to Casablanca and maximize the other criteria.

To do this and considering the different scales we have, we will normalize the data using the Min-Max Scaler, which has the following mathematical Equation (1) (Izonin et al. 2022):
(1)

Table 6 summarizes the calculation of the normalized values. For the criterion of the distance, the formula of the Min-Max Scaler will be preceded by 1 minus the value found by the formula to show the punishing aspect to have a big value for the distance. For the rest, we write directly the result calculated only by the formula, and the final score for each province will be the sum of its normalized values for all criteria.

Table 6

Values of the different normalized criterion values and scores by province

ProvinceDistance from Casablanca (km)Rural population(%) of rural households without access to waterDaily horizontal solar radiation (kWh/m2/day)Total score
Sale 0.51 0.03 0.94 0.30 1.78 
Khemissat 0.02 0.49 0.77 0.22 1.51 
Skhirate Témara 0.55 0.01 0.52 0.30 1.38 
El Jaddida 0.50 1.00 0.76 0.33 2.59 
Benslimane 0.78 0.16 0.86 0.11 1.91 
Berrechid 0.87 0.37 1.00 0.00 2.25 
Sidi Bennour 0.13 0.75 0.63 0.63 2.13 
Settat 0.65 0.86 0.98 0.48 2.97 
Nouaceur 0.98 0.01 0.15 0.59 1.72 
Mediouna 1.00 0.00 0.00 0.30 1.30 
Mohammadia 0.91 0.15 0.25 0.26 1.57 
Rhamna 0.00 0.38 0.41 0.85 1.64 
Khouribga 0.36 0.27 0.90 0.96 2.50 
Fquih Ben Salah 0.09 0.58 0.03 1.00 1.71 
ProvinceDistance from Casablanca (km)Rural population(%) of rural households without access to waterDaily horizontal solar radiation (kWh/m2/day)Total score
Sale 0.51 0.03 0.94 0.30 1.78 
Khemissat 0.02 0.49 0.77 0.22 1.51 
Skhirate Témara 0.55 0.01 0.52 0.30 1.38 
El Jaddida 0.50 1.00 0.76 0.33 2.59 
Benslimane 0.78 0.16 0.86 0.11 1.91 
Berrechid 0.87 0.37 1.00 0.00 2.25 
Sidi Bennour 0.13 0.75 0.63 0.63 2.13 
Settat 0.65 0.86 0.98 0.48 2.97 
Nouaceur 0.98 0.01 0.15 0.59 1.72 
Mediouna 1.00 0.00 0.00 0.30 1.30 
Mohammadia 0.91 0.15 0.25 0.26 1.57 
Rhamna 0.00 0.38 0.41 0.85 1.64 
Khouribga 0.36 0.27 0.90 0.96 2.50 
Fquih Ben Salah 0.09 0.58 0.03 1.00 1.71 

We note after the calculations made above that we can select the main provinces that have the highest scores (the top 6) to carry out several samples in each province. According to our study, these are the following provinces: Settat, El Jaddida, Khouribga, Berrechid, Sidi Bennour, and Benslimane.

Analysis of the mineral load and the physico-chemical characteristics of the test samples

Analysis of the mineral load of the test water samples

Following the experimental protocol established in the material and method section, we were able to calculate the concentration of several elements that represent the mineral load of each sample from different sources. For visualization purposes, we have summarized the results in graphs. Figure 4 shows a summary of the mineral load of the four brackish water sampling points.
Figure 4

Mineral load for the four brackish water samples.

Figure 4

Mineral load for the four brackish water samples.

Close modal

From these figures, we can extract the following observations:

  • For the sample from P1/200 m, the elements Cl and Na+ represent 73.31% with 2,128 and 1,686 mg/L, while represents 9.95% (518 mg/L) and represents 3.13% (163 mg/L), exceeding World Health Organization (WHO) thresholds and recommendations of 200 mg/L, 200, 250, and 50 mg/L, respectively (Diouf et al. 2022). The elements responsible for the hardness of the water (Mg2+ and Ca2+) represent 5.09% and 7.07%, respectively, with a concentration of 265 and 368 mg/L, exceeding WHO thresholds ranging from [50–150 mg/L] to [75–200 mg/L], while the rest of the elements are less than 1.42%.

  • For the sample from P2/120 m, the elements Cl and Na+ represent 71.47% with 3,692 and 2,646 mg/L, while represents 9.73% (863 mg/L) and represents 2.51% (223 mg/L), exceeding WHO thresholds and recommendations already mentioned earlier. The elements responsible for the hardness of the water (Mg2+ and Ca2+) represent 7.96% and 7.21%, respectively, with a concentration of 706 and 640 mg/L, exceeding WHO thresholds ranging from [50 mg/L–150 mg/L] to [75 mg/L–200 mg/L], while the rest of the elements are less than 1.1%.

  • For the sample from P2/20 m, the elements Cl and Na+ represent 61.83% with 989 and 789 mg/L, while represents 12.48% (359 mg/L) and represents 10.05% (289 mg/L), exceeding WHO thresholds and recommendations already mentioned. The elements responsible for the hardness of the water (Mg2+ and Ca2+) represent 7.34 and 7.23%, respectively, with a concentration of 211.2 and 208 mg/L, exceeding WHO thresholds and recommendations already mentioned, while the rest of the elements are less than 1.03%.

  • For the sample from P3/15 m, the elements Cl and Na+ represent 43.71% with 823 and 667 mg/L, while represents 39.37% (1,342 mg/L) and represents 5.05% (172 mg/L), exceeding WHO thresholds and recommendations already mentioned. The elements responsible for the hardness of the water (Mg2+ and Ca2+) represent 6.25 and 4.69%, respectively, with a concentration of 213.1 and 160 mg/L, exceeding WHO threshold ranging from [50–150 mg/L] for Mg2+, while the rest of the elements are less than 0.89%.

The concentrations of the different components as well as their variations in relation to the depth of the wells can be justified by taking into account the location of the sampling zone and the following elements:

According to Bear et al. (1999), high ratios of Ca enrichment (>1) could be regarded as saltwater intrusion. After calculating this ratio, we can see that it varies between 0.75 and 1.38 (P1/200 m: 1.38, P2/120 m: 0.91, P2/20 m: 0.98, P3/15 m: 0.75). We can also see that this rate generally increases with depth, which gives an indication of possible marine intrusion in the deep layers of the ground.

For comparison purposes, it was decided to take another sample of brackish water away from the first sampling area and a sample of seawater close to the main sampling area. Their mineral loadings are summarized in Figure 5.
Figure 5

Mineral load of samples from Tissa and seawater used for comparative purposes.

Figure 5

Mineral load of samples from Tissa and seawater used for comparative purposes.

Close modal

From Figure 5, we can extract the following observations:

  • For the Tissa sample, the elements Cl and Na+ represent 76.32% with 1,420 and 1,076 mg/L, respectively, while represents 12.17% (398 mg/L) and represents 4.34% (142 mg/L), exceeding WHO thresholds and recommendations already mentioned. The elements responsible for the hardness of the water (Mg2+ and Ca2+) represent 3.31 and 2.78%, respectively, with a concentration of 108.5 and 91.2 mg/L, while the rest of the elements are less than 1.04%.

  • For the seawater sample, orders of magnitude of concentrations vary greatly compared to brackish water samples. The elements Cl and Na+ represent 85.40% with 20,620 and 10,089 mg/L, while represents 8.17% (2,940 mg/L) and represents 0.6% (219 mg/L), exceeding WHO thresholds and recommendations already mentioned. The elements responsible for the hardness of the water (Mg2+ and Ca2+) represent 3.97 and 1.11% respectively, with a concentration of 1,430 and 400 mg/L, exceeding WHO thresholds and recommendations already mentioned. The rest of the elements are less than 0.8%.

Analysis of the physico-chemical characteristics of the test samples

The analysis of the physico-chemical characteristics of the samples mainly concerned measurements of conductivity, turbidity, salinity, and pH. The details of the measurements are described in Figure 6.
Figure 6

Summary of the physico-chemical characteristics of the samples.

Figure 6

Summary of the physico-chemical characteristics of the samples.

Close modal
Figure 7

Basic diagram of an electrocoagulation unit.

Figure 7

Basic diagram of an electrocoagulation unit.

Close modal

The main information that can be drawn from the figure is as follows:

  • For conductivity, all the samples are above the WHO threshold of 1 mS/cm or that recommended by the Moroccan standard of 2.7 mS/cm (Moroccan standard 2020). It is clear that the conductivity of the seawater sample is very high because of its high dissolved salt content, whereas that of the brackish water samples is relatively low compared with seawater. According to the samples we have, the relationship between conductivity and well depth is not trivial and depends very much on the specific characteristics of the sampling site. It is the same case for salinity which exceeds the desirable threshold for drinking water of <1 g/L

  • For turbidity, which measures the opacity of the water due to the presence of suspended particles, all the samples were below the threshold recommended by the Moroccan standard, which is the limit value of 5 NTU (Moroccan standard 2020). The pH measurement is also compliant between 6.5 and 8.5.

Proposal of the brackish water pre-treatment technique

Selection of the pre-treatment technique

To validate the choice of our pre-treatment technique, we went through a set of pre-treatment techniques, and we were able to characterize them in terms of application and performance using the existing literature. Table 7 summarizes our relevant results.

Table 7

An overview of brackish water pre-treatment techniques

TechniqueApplicationsPerformance
Coagulation-flocculation Elimination of colloids and suspended particles responsible for turbidity (Cherif et al. 2016; Poirier et al. 2023 
DAF Elimination of suspended solids/heavy metals (Yuan et al. 2008, Opedal et al. 2011 
Adsorption Elimination of organic matter (Shen et al. 2023 
Electrocoagulation 
  • - Elimination of colloids, elimination of organic matter, and reduction of total dissolved solids and hardness (Poirier et al. 2023)

 
 
Microfiltration (MF)/ultrafiltration (UF)/nanofiltration (NF) 
  • - Do not allow particles that have a size larger than the pores of MF (0.1–10 μm)

  • - Eliminate suspended particles, bacteria, and colloids

  • - Do not allow particles that have a size larger than the pores of UF (10 nm to 1 μm) and eliminate macromolecules and viruses.

  • - Do not allow particles that are larger than the NF pores (a few nm) and eliminate macromolecules and divalent ions (En CHIMIE G. D. D. 2019)

 
 
TechniqueApplicationsPerformance
Coagulation-flocculation Elimination of colloids and suspended particles responsible for turbidity (Cherif et al. 2016; Poirier et al. 2023 
DAF Elimination of suspended solids/heavy metals (Yuan et al. 2008, Opedal et al. 2011 
Adsorption Elimination of organic matter (Shen et al. 2023 
Electrocoagulation 
  • - Elimination of colloids, elimination of organic matter, and reduction of total dissolved solids and hardness (Poirier et al. 2023)

 
 
Microfiltration (MF)/ultrafiltration (UF)/nanofiltration (NF) 
  • - Do not allow particles that have a size larger than the pores of MF (0.1–10 μm)

  • - Eliminate suspended particles, bacteria, and colloids

  • - Do not allow particles that have a size larger than the pores of UF (10 nm to 1 μm) and eliminate macromolecules and viruses.

  • - Do not allow particles that are larger than the NF pores (a few nm) and eliminate macromolecules and divalent ions (En CHIMIE G. D. D. 2019)

 
 

From Table 7, we can see that the electrocoagulation (EC) technique is the pre-treatment technique which has more advantages whether in terms of pollutant elimination (Hardness, Turbidity) or even lower energy consumption. In addition, the suitability of the technique for our project given that it uses electricity which will be supplied by solar energy will contribute to reducing the carbon footprint of our technique. In addition, this technique is more compact and requires less human intervention which is not the case for other techniques which require the addition of chemicals.

Development of the pre-treatment pilot model

Presentation of the technique

EC is a technique that has been used to treat many types of water, and this is especially the case for wastewater from different types of industrial or even domestic wastewater, groundwater, brackish water, and many other applications for the elimination of particular pollutants. Several possibilities exist for the design of EC, but in general, the basic scheme of EC is the following (Figure 7).

Simplified pilot model
Energy consumption of the EC unit: To assemble the EC unit with solar energy, particularly photovoltaic panels, it is essential to understand the operational cost and in particular the energy cost of this technique to be able to dimension our energy needs. The simplified operational cost calculation model which covers EC's electricity requirement. The operational cost of EC includes the cost linked to direct electricity consumption as well as the cost of the electrodes which will be consumed during the reaction (Geraldino et al. 2015). The mathematical equation which summarizes it is as follows:
(3)
where α is the cost of energy and β is the cost of the electrode.
(4)
where ith U is the electric tension (V), I is the current (A), t is time (h), and V is the volume (m3)
(5)
where I is the current (A), t is the time (s), M is the molar mass (g), F is the Faraday constant, and z is the number of electrons.

Illustrative case study: In advancing the proposal for the simplified pilot model, it is imperative to establish operational hypotheses for the numerical application of this illustrative case study.

  • - For the energy requirements of the unit:

    • • We admit an objective to produce potable water sufficient for a family, estimated at V = 20 L/day.

    • • In addition, we presume that the maximum pollutant removal efficiency has been experimentally validated for a specific set of factors influencing EC (detailed in Section 3.3.2.1). In our context, we consider U = 20 V, I = 3A, and t = 1 h as the parameters for this experimentation. In this case, the necessary electrical energy will be calculated according to Equation (4) as follows: Energy required = (20 × 3 × 1)/(0.02) = 3,000 W h/m3.day.

  • - Calculation of the size of the photovoltaic generator:

The calculation of the dimensions of the photovoltaic panels takes into account the initial energy requirement as well as factors linked to weather conditions and solar radiation of the area concerned by the installation (Soro et al. 2018). In this case, we will have the following calculation relations:
(6)
where K is the coefficient of meteorological uncertainty, generally [0.55, 0.65] and most often 0.65.
(7)
where power is represented in Watts peak and IR represents the irradiation in kWh/m2 per day. According to Table 5, the average value of IR = 5.36 kWh/m2/day. In our case, energy produced = 4,615 W h/m3.day and power consumed = 861 Wpeak.
Subsequently, the number of photovoltaic panels must be chosen by browsing a set of commercial products following the following equation:
(8)

For a PHOTOWATT panel from the PX1650 DE range with a power of 165 Wpeak, we will have N = 6.

  • - Simplified diagram of the pilot model:

We admit that our pilot model works without the direct use of energy from the solar panel without the need for a charge controller, and in addition, we will work with a parallel configuration for the panels since this will increase the current (given its importance for the reaction) without increasing the tension. The diagram of our simplified model is shown in Figure 8.
Figure 8

Wiring of the simplified pilot model.

Figure 8

Wiring of the simplified pilot model.

Close modal

This study focused on identifying candidate provinces in Morocco by considering various criteria, including distance, rural population, rates of non-access to drinking water, and solar irradiation. The selected areas were subject to brackish water sample collection to comprehensively understand their characteristics, essential for designing effective pre-treatment processes for water pre-treatment before desalination prototype. Analysing test samples revealed insights into mineral loads and physico-chemical characteristics, shedding light on the impact of soil location and human activities. Moreover, depth played a role in the presence of certain elements, such as and . Notably, the elements contributing to water hardness exceeded drinking water standards, necessitating further exploration of appropriate pre-treatment techniques through a simplified pilot model. This is what was done by a simplified EC pilot model.

We are grateful to the host laboratory LARILE (Laboratory of Advanced Research in Industrial and Logistic and Engineering), especially the OSIL team (Optimization of Industrial and Logistics Systems), LIEME (Laboratory of Electrochemistry Engineering, Modeling and Environment) and Laboratory of Natural Resources and Environment (LNRE) of the Polydisciplinary Faculty of Taza (FPT) for their support and help. This work was established within the framework of a joint research project between CNRST (National Center for Scientific and Technical Research) in Morocco and FRQ (Québec Research Funds) in Quebec.

All relevant data are included in the paper or its Supplementary Information.

The authors declare there is no conflict.

ABOUZAID and DUCHESNE
1984
Water Quality Control Department (Water Sampling and Analysis Manual)
.
ONEP, Rabat
.
AlJaberi
F. Y.
2022
Desalination of groundwater by electrocoagulation using a novel design of electrodes
.
Chemical Engineering and Processing-Process Intensification
174
,
108864
.
Arevalo
J.
,
Sandin
R.
,
Kennedy
M. D.
,
Salinas Rodriguez
S. G.
,
Rogalla
F.
&
Monsalvo
V. M.
2018
Membrane-based pretreatment to mitigate variations in desalination plants
.
Water Science and Technology
77
(
12
),
2858
2866
.
Auliya
V. R.
,
Marsono
B. D.
,
Yuniarto
A.
&
Nurhayati
E.
2021
Brackish water treatment for small community by using membrane technology
. In:
IOP Conference Series: Earth and Environmental Science
(Vol. 896, No. 1, p. 012073)
.
IOP Publishing
.
Bear
J.
,
Cheng
A. H. D.
,
Sorek
S.
,
Ouazar
D.
&
Herrera
I.
(Eds.).
1999
Seawater Intrusion in Coastal Aquifers: Concepts, Methods and Practices
Vol. 14
.
Springer Science & Business Media, Dordrecht
.
Chafidz
A.
,
Kerme
E. D.
,
Wazeer
I.
,
Khalid
Y.
,
Ajbar
A.
&
Al-Zahrani
S. M.
2016
Design and fabrication of a portable and hybrid solar-powered membrane distillation system
.
Journal of Cleaner Production
133
,
631
647
.
https://doi.org/10.1016/j.jclepro.2016.05.127
.
Cheng
W.
,
Liu
C.
,
Tong
T.
,
Epsztein
R.
,
Sun
M.
,
Verduzco
R.
,
Ma
J.
&
Elimelech
M.
2018
Selective removal of divalent cations by polyelectrolyte multilayer nanofiltration membrane: Role of polyelectrolyte charge, ion size, and ionic strength
.
Journal of Membrane Science
559
,
98
106
.
Cherif
L.
,
Chiboub Fellah
A.
,
Chiboub Fellah
F. Z.
,
Boulefred
S.
&
Benadda
L.
2016
The effect of suspended matter concentration on the coagulation–flocculation and decantation process for low brackish water C (NaCl) = 3 g/L
.
Desalination and Water Treatment
57
(
13
),
6106
6115
.
Diouf
O. C.
,
Weihermüller
L.
,
Diedhiou
M.
,
Beltoungou
E. Y. T. B.
,
Dieng
N. M.
,
Faye
S. C.
,
Vereecken
H.
&
Faye
S.
2022
Groundwater geochemistry and saltwater intrusion in the Dakar coastal area, Senegal
.
Journal of Geoscience and Environment Protection
10
(
12
),
45
64
.
https://doi.org/10.4236/gep.2022.1012004
.
Egboka
B. C. E.
1984
Nitrate contamination of shallow groundwaters in Ontario, Canada
.
Science of the Total Environment
35
(
1
),
53
70
.
https://doi.org/10.1016/0048-9697(84)90368-1
.
En CHIMIE, G. D. D.
2019
Valorisation des ressources hydriques et production de l'eau purifiée par les procédés membranaires
.
Doctoral dissertation
,
KU
,
Leuven
.
Garcia-Segura
S.
,
Eiband
M. M. S.
,
de Melo
J. V.
&
Martínez-Huitle
C. A.
2017
Electrocoagulation and advanced electrocoagulation processes: A general review about the fundamentals, emerging applications and its association with other technologies
.
Journal of Electroanalytical Chemistry
801
,
267
299
.
Geraldino
H. C. L.
,
Simionato
J. I.
,
de Souza Freitas
T. K. F.
,
Garcia
J. C.
,
de Carvalho Júnior
O.
&
Correr
C. J.
2015
Efficiency and operating cost of electrocoagulation system applied to the treatment of dairy industry wastewater. Acta Scientiarum
.
Technology
37
(
3
),
401
408
.
Gleick
P.
1993
Water in Crisis: A Guide to the World's Fresh Water Resources
.
Oxford University Press
,
New York
.
Gourai
K.
,
Allam
K.
,
El Bouari
A.
,
Belhorma
B.
,
Bih
L.
&
Cherai
N.
2015
AQUASOLAR-macro project: Brackish water desalination by coupling solar energy with reverse osmosis and membrane distillation process
.
Journal of Materials and Environmental Science
6
(
12
),
3524
3529
.
Hafez
A.
,
Khedr
M.
,
El-Katib
K.
&
Gadallah
H.
2009
Pilot scale investigation of low pressure nanofiltration and reverse osmosis membrane techniques for the treatment of El-Salaam canal water, Sinai, Egypt
.
Desalination and Water Treatment
8
(
1–3
),
279
285
.
doi: 10.5004/dwt.2009.789
.
Hakizimana
J. N.
,
Gourich
B.
,
Chafi
M.
,
Stiriba
Y.
,
Vial
C.
,
Drogui
P.
&
Naja
J.
2017
Electrocoagulation process in water treatment: A review of electrocoagulation modeling approaches
.
Desalination
404
,
1
21
.
Ibrahim
A. G.
,
Rashad
A. M.
&
Dincer
I.
2017
Exergoeconomic analysis for cost optimization of a solar distillation system
.
Solar Energy
151
,
22
32
.
http://dx.doi.org/10.1016/j.solener.2017.05.020
.
Izonin
I.
,
Tkachenko
R.
,
Shakhovska
N.
,
Ilchyshyn
B.
&
Singh
K. K.
2022
A two-step data normalization approach for improving classification accuracy in the medical diagnosis domain
.
Mathematics
10
(
11
),
1942
.
https://doi.org/10.3390/math10111942
.
Jones
E.
,
Qadir
M.
,
van Vliet
M. T.
,
Smakhtin
V.
&
Kang
S. M.
2019
The state of desalination and brine production: A global outlook
.
Science of the Total Environment
657
,
1343
1356
.
https://doi.org/10.1016/j.scitotenv.2018.12.076
.
Ju
X. T.
,
Kou
C. L.
,
Zhang
F. S.
&
Christie
P.
2006
Nitrogen balance and groundwater nitrate contamination: Comparison among three intensive cropping systems on the North China Plain
.
Environmental Pollution
143
(
1
),
117
125
.
https://doi.org/10.1016/j.envpol.2005.11.005
.
Lwimbo
Z. D.
,
Komakech
H. C.
&
Muzuka
A. N.
2019
Impacts of emerging agricultural practices on groundwater quality in Kahe catchment, Tanzania
.
Water
11
(
11
),
2263
.
https://doi.org/10.3390/w11112263
.
Maazouzi
A.
,
Kettab
A.
,
Badri
A.
,
Zahraoui
B.
&
Khalfaoui
R.
2013
Physicochemical parameters of groundwater (Foggara) and sand dune (Timimoun) Algeria
.
Desalination and Water Treatment
51
(
37–39
),
7353
7358
.
https://doi.org/10.1080/19443994.2013.791765
.
Moroccan standard on the quality of water for food use NM 03.7.001
2020
.
Moujabber
M. E.
,
Samra
B. B.
,
Darwish
T.
&
Atallah
T.
2006
Comparison of different indicators for groundwater contamination by seawater intrusion on the Lebanese coast
.
Water Resources Management
20
,
161
180
.
https://doi.org/10.1007/s11269-006-7376-4
.
ONEP
2007
Procedure for Sampling Natural, Treated and Waste Water.
Water Quality Control Department
.
ONEP
2008
Standard Operating Procedures.
Water Quality Control Department
.
Opedal
M. T.
,
Stenius
P.
,
Johansson
L.
,
Hill
J.
&
Sandberg
C.
2011
Removal of dissolved and colloidal substances in water from compressive pre-treatment of chips using dissolved air flotation. Pilot trial
.
Nordic Pulp & Paper Research Journal
26
(
4
),
364
371
.
Poirier
K.
,
Lotfi
M.
,
Garg
K.
,
Patchigolla
K.
,
Anthony
E. J.
,
Faisal
N. H.
,
Mulgundmath
V.
,
Sahith
J. K.
,
Jadhawar
P.
,
Koh
L.
,
Morosuk
T.
&
Al Mhanna
N.
2023
A comprehensive review of pre-and post-treatment approaches to achieve sustainable desalination for different water streams
.
Desalination
566,
116944
.
Report by the Directorate of Financial Studies and Forecasts
2020
Morocco in the face of climate change: situation, impacts and response policies in the water and agriculture sectors (official website of the Ministry of Finance of Morocco)
.
Rodier
J.
2009
Water Analysis – Natural Waters, Waste Water, Sea Water
, 9th edn.
Dunod
,
Paris
,
1475
p.
Rolence
C.
,
Machunda
R.
&
Njau
K.
2014
Water hardness removal by coconut shell activated carbon. East Asian Science Technology and Society an International Journal 2 (5), 97–102
.
Shutova
Y.
,
Karna
B. L.
,
Hambly
A. C.
,
Lau
B.
,
Henderson
R. K.
&
Le-Clech
P.
2016
Enhancing organic matter removal in desalination pretreatment systems by application of dissolved air flotation
.
Desalination
383
,
12
21
.
Simanjuntak
W.
,
Ginting
I.
&
Pandiangan
K. D.
2011
Removal of natural organic matter using electrocoagulation as a first step for desalination of brackish water
.
Indonesian Journal of Chemistry
11
(
1
),
103
107
.
Soro
D.
,
Yapi
M.
,
Fofana
B.
&
Yao
N. A.
2018
Dimensionnement d'une installation solaire pour la réalisation de travaux pratiques dans les lycées et collèges en zone isolée
.
Afrique Science
14
(
5
),
335
345
.
Yoon
J.
,
Kwon
H. J.
,
Kang
S.
,
Brack
E.
&
Han
J.
2022
Portable seawater desalination system for generating drinkable water in remote locations
.
Environmental Science & Technology
56
(
10
),
6733
6743
.
https://doi.org/10.1021/acs.est.1c08466
.
Yuan
X. Z.
,
Meng
Y. T.
,
Zeng
G. M.
,
Fang
Y. Y.
&
Shi
J. G.
2008
Evaluation of tea-derived biosurfactant on removing heavy metal ions from dilute wastewater by ion flotation
.
Colloids and Surfaces A: Physicochemical and Engineering Aspects
317
(
1–3
),
256
261
.
This is an Open Access article distributed under the terms of the Creative Commons Attribution Licence (CC BY 4.0), which permits copying, adaptation and redistribution, provided the original work is properly cited (http://creativecommons.org/licenses/by/4.0/).