# Continuous Adsorption Modeling and Fixed Bed Column Studies: Adsorption of Tannery Wastewater Pollutants Using Beach Sand

Authors: Ghita El Mouhri; Mohammed Merzouki; Hajar Belhassan; Youssef Miyah; Halima Amakdouf; Rabea Elmountassir; Anissa Lahrichi
Journal: Journal of Chemistry
 (2020)

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## Abstract

This study deals with the removal of residual pollutants from tanning wastewater by continuous adsorption mechanism, using local sand as a low-cost adsorbent. The possibility of pretreating a complex tannery effluent heavily loaded with a natural material such as sand is significant. The characterization of the adsorbent before and after continuous adsorption was performed by X-ray diffraction, Fourier transform infrared spectroscopy, and scanning electron microscopy. Column studies were also carried out to evaluate the performance of the adsorbent and the efficiency of column adsorption. The adsorption kinetic rate seems to be strongly influenced by certain parameters such as the particle size of the material used, the withdrawal rate of the influent and the height of the adsorbent bed, and optimized parameters were found to be 63μm, 15 ml·min−1, and 7 cm, respectively, and the color removal has achieved maximum values which vary between 95 and 100%. The results suggest that sand can be used as an economical adsorbent for the removal of color from the wastewater of the tanning industries.


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## Body

## 1. Introduction

Industrial tanning is one of the most important sectors in Morocco’s economy [1]. Consequently, the consumption of huge quantities of water during all leather processing operations and the discharge of untreated effluents leads to very serious problems, particularly on water quality and human health, and makes it one of the main polluters that influence the ecological balance negatively [2–5].Both scientists and health authorities have spent the effort considered in pollution clean-up and prevention [3, 5, 6]. Many types of treatment systems have been considered to eliminate heavy metal contamination in the environment [7–9], including ion exchange, flocculation, coagulation, chemical oxidation, chemical precipitation, ozonation, membrane filtration, electrochemical filtration, and activated carbon adsorption [10–15]. However, the main limiting factors against the use of these processes are high operational costs, low disposal efficiency, generation of toxic byproducts and sludge, and difficulty of implementation and time [11, 16].Among the different processes for purifying effluents loaded with heavy metals, adsorption, which involves fixing the pollutant load at the interface through physical or chemical bonds, offers better performance and fewer problems compared with other advanced processes [17, 18]. Adsorption also offers an economical solution by developing sorbents with a much lower cost [18–22].In this study, the use of continuous adsorption was chosen for the treatment of larger volumes and to remove as many pollutants as possible from the tannery effluent. Preliminary experimental studies were conducted to understand the general mechanism of adsorption, the different characteristics and limitations in column design. Adsorption was designed in continuous mode by percolating effluents through fixed bed columns with detailed kinetic modeling to evaluate the variation in some operating parameters such as granulometry, adsorbent bed height, and influent withdrawal rate.


## 2. Materials and Methods

### 2.1. Materials

The effluent from the tannery’s activity was collected from an industrial unit located in the Dokkarat district of Fez and stored at a temperature of 4°C until use. The adsorbent material used is sand from a Moroccan beach, and this adsorbent has undergone several rinses with ultrapure water until the removal of residues and neutralization of the pH. It is then dried in an oven overnight at 80°C for total removal of water, ground, and sieved to obtain a fraction in the range of 63–80μm in diameter [3, 18, 23]. The physicochemical characteristics of the tannery effluent are shown in Table 1.Table 1
Physicochemical characteristics of real tannery wastewater.
Parameter
Values
pH
6,25
Temperature (°C)
25
Electrical conductivity (μs·cm−1)
10900
COD (mg·L−1)
11800
BOD5 (mg·L−1)
1200
Total chromium (mg·L−1)
32,2
Color
Dark blue


### 2.2. Instrumental Analysis

The granulometric curve of the sand and the simple percentages (%) of each granular fraction were established using a vibrating sieve shaker (RETSCH AS 200) [24], and the crystalline structure of the sand powder was analyzed by X-ray diffractometry (Diffractometer X’Pert PRO); the Fourier transform infrared spectroscopy was carried out to study the particular types of chemical bonds and groups existing in the sample, and morphological analysis of the sand before and after saturation by effluent components was performed by scanning electron microscope, equipped with an X-ray energy dispersion spectrometer (EDX).


### 2.3. Adsorption Studies in a Continuous System

The treatment of the tannery effluent was carried out with an experimental system made of a glass column, with a dimension of 3 cm in inner diameter and 50 cm in height. The sand bed was packed into the column and wetted with ultrapure water to release the trapped air between the particles. Tannery wastewater was continuously supplied through the column using a peristaltic pump. Every 10 minutes, the treated influent was collected, and the optimal parameters were selected using a spectrophotometer (UV-Visible BioSpec-mini) at a maximum wavelength (λmax) of 400 nm Figure 1.Figure 1
Experimental device.


#### 2.3.1. Effect of Sand Granulometry

To evaluate the effect of particle size, five sand fractions were varied at different diameters: 63, 125, 200, 315, and 400μm. These granular fractions were filled into separate columns to form compacted beds with a height of 5 cm. The withdrawal flow rate has been set at 15 ml·min−1.


#### 2.3.2. Effect of the Withdrawal Rate

To choose the most appropriate withdrawal rate for the treatment of tannery effluent, we opted for a grain size of 63μm in diameter, a compacted bed of 3 cm in height, and adjusted the withdrawal rates of the influents to values of 15, 65, 115, and 170 ml·min−1.


#### 2.3.3. Effect of the Adsorbent Bed Height

After the determination of the two parameters: grain size and flow rate, the effect of filter bed height on the rate of discolouration was studied to determine which one provides better continuous adsorption. And, for this, the sand beds were varied according to different masses, namely, 20.2, 36, and 50 g, and the heights of the sand beds were measured at 3, 5, and 7 cm, respectively.


## 2.1. Materials

The effluent from the tannery’s activity was collected from an industrial unit located in the Dokkarat district of Fez and stored at a temperature of 4°C until use. The adsorbent material used is sand from a Moroccan beach, and this adsorbent has undergone several rinses with ultrapure water until the removal of residues and neutralization of the pH. It is then dried in an oven overnight at 80°C for total removal of water, ground, and sieved to obtain a fraction in the range of 63–80μm in diameter [3, 18, 23]. The physicochemical characteristics of the tannery effluent are shown in Table 1.Table 1
Physicochemical characteristics of real tannery wastewater.
Parameter
Values
pH
6,25
Temperature (°C)
25
Electrical conductivity (μs·cm−1)
10900
COD (mg·L−1)
11800
BOD5 (mg·L−1)
1200
Total chromium (mg·L−1)
32,2
Color
Dark blue


## 2.2. Instrumental Analysis

The granulometric curve of the sand and the simple percentages (%) of each granular fraction were established using a vibrating sieve shaker (RETSCH AS 200) [24], and the crystalline structure of the sand powder was analyzed by X-ray diffractometry (Diffractometer X’Pert PRO); the Fourier transform infrared spectroscopy was carried out to study the particular types of chemical bonds and groups existing in the sample, and morphological analysis of the sand before and after saturation by effluent components was performed by scanning electron microscope, equipped with an X-ray energy dispersion spectrometer (EDX).


## 2.3. Adsorption Studies in a Continuous System

The treatment of the tannery effluent was carried out with an experimental system made of a glass column, with a dimension of 3 cm in inner diameter and 50 cm in height. The sand bed was packed into the column and wetted with ultrapure water to release the trapped air between the particles. Tannery wastewater was continuously supplied through the column using a peristaltic pump. Every 10 minutes, the treated influent was collected, and the optimal parameters were selected using a spectrophotometer (UV-Visible BioSpec-mini) at a maximum wavelength (λmax) of 400 nm Figure 1.Figure 1
Experimental device.


### 2.3.1. Effect of Sand Granulometry

To evaluate the effect of particle size, five sand fractions were varied at different diameters: 63, 125, 200, 315, and 400μm. These granular fractions were filled into separate columns to form compacted beds with a height of 5 cm. The withdrawal flow rate has been set at 15 ml·min−1.


### 2.3.2. Effect of the Withdrawal Rate

To choose the most appropriate withdrawal rate for the treatment of tannery effluent, we opted for a grain size of 63μm in diameter, a compacted bed of 3 cm in height, and adjusted the withdrawal rates of the influents to values of 15, 65, 115, and 170 ml·min−1.


### 2.3.3. Effect of the Adsorbent Bed Height

After the determination of the two parameters: grain size and flow rate, the effect of filter bed height on the rate of discolouration was studied to determine which one provides better continuous adsorption. And, for this, the sand beds were varied according to different masses, namely, 20.2, 36, and 50 g, and the heights of the sand beds were measured at 3, 5, and 7 cm, respectively.


## 2.3.1. Effect of Sand Granulometry

To evaluate the effect of particle size, five sand fractions were varied at different diameters: 63, 125, 200, 315, and 400μm. These granular fractions were filled into separate columns to form compacted beds with a height of 5 cm. The withdrawal flow rate has been set at 15 ml·min−1.


## 2.3.2. Effect of the Withdrawal Rate

To choose the most appropriate withdrawal rate for the treatment of tannery effluent, we opted for a grain size of 63μm in diameter, a compacted bed of 3 cm in height, and adjusted the withdrawal rates of the influents to values of 15, 65, 115, and 170 ml·min−1.


## 2.3.3. Effect of the Adsorbent Bed Height

After the determination of the two parameters: grain size and flow rate, the effect of filter bed height on the rate of discolouration was studied to determine which one provides better continuous adsorption. And, for this, the sand beds were varied according to different masses, namely, 20.2, 36, and 50 g, and the heights of the sand beds were measured at 3, 5, and 7 cm, respectively.


## 3. Results and Discussion

### 3.1. Particle Size Curve of Sand

The descriptive percentages of the granulometric analyses are illustrated in Figure2; the figure shows the allocation of 7 fractions for the granulometric distribution of sand, and the preponderant size which predominates is 200 μm with a percentage of 61.5%. This size is less than 500 μm, which gives it the class of fine sands.Figure 2
Granulometric curve of the sand used.


### 3.2. X-Ray Diffraction

The crystalline composition of the sand particles before and after adsorption is shown in Figure3. The X-ray diffractograms of the sand before and after adsorption shows almost the same appearance and reveal the existence of several characteristic peaks of quartz and calcite [25, 26]. For unsaturated sand, these two elements have a codominance indicated by the major peaks corresponding to the position 2θ, 27.7° and 29.7°, respectively [27–31]. Whereas for saturated sand, quartz predominates over calcite with the appearance of two unidentified peaks at 2θ, 43.41° and 51.08°, which can be attributed to the effluent components of the tannery.Figure 3
Diffractometric analysis of (a) natural sand and (b) loaded sand.
(a)
(b)


### 3.3. Infrared Spectroscopy Analysis

Figure4 and Table 2 present the main functional groups of the specific elements of natural sand and the possible modifications after the adsorption process. On one hand, the examination of these results show no change in the basic structure of Lowded Sand (LS) particles and this allows us to say that adsorption is done by physical interaction forces [25]. On other hand, the maximum intensities have decreased slightly; this may be related to an energy variation due to the bonds established with the pollutants in the effluent, and a small shift has been observed in the position of the adsorption bands, which probably justifies the feasibility of adsorption [18].Figure 4
Infrared spectrum of natural sand (NS) and loaded sand (LS).Table 2
Sand infrared bands and their assignments.
Natural sand position (cm−1)
Loaded sand position (cm−1)
Assignments
Reference
3419.60
3427.62
OH group stretch vibration
[18, 32, 33]
2922.88
2924.36
C–H asymmetrical stretching vibrations
[25, 32, 34]
2519.05
2518.98
C–H asymmetrical stretching vibration
[25]
1797.17
1796.91
Typical vibration of the OH stretching group
[3]
—
1620.91
OH group stretch vibration
[18]
1450.90
1452.76
CO3 stretching of calcite
[3, 35]
1082.85
1083.32
Valence vibration of the Si–O–Si bond
[18, 23, 32]
874.56
874.60
CO3 stretching of calcite
[35]
779.91
780.64
O–Si–O stretching
[25]
712.48
712.55
O–Si–O stretching
[25]
469.17
469.92
Valence vibration of the Si–O–Si bond
[25]These results also confirm the existence of the bonds characterizing calcite and quartz previously revealed by diffractometric analysis.


### 3.4. Scanning Electron Microscopy Coupled with the EDX

The SEM results coupled with the EDX of the sand before and after saturation as well as the mass percentages of each element are shown in Figure5 and Table 3. The internal microstructure of unmodified sands shows a rough, irregular, and proportionally porous and cracked appearance with the presence of some luminous and relatively ordered aggregations, that probably indicate the existence of quartz crystals previously detected by the DRX analysis [18, 36]. This mineralogical composition allows the interchanges of substances with adjacent cells and thus makes the adsorption mechanism possible (Figure 5(a)).Figure 5
Morphological examination of natural sand (a, b) and loaded sand (c, d) by SEM-EDX.Table 3
Percentage of elements found by X-ray energy dispersion EDX in natural and loaded sand.
Elements
Natural sand (NS)
Loaded sand (LS)
C
26.34
32.05
O
46.18
18.12
N
—
34.55
Na
3.42
1.45
Mg
0.94
0.45
Si
8.66
5.36
S
—
0.40
Cl
—
0.43
K
0.54
0.37
Ca
12.63
5.98
Cr
—
0.27
Fe
1.3
0.58
Total
100
100Microstructural analysis reveals significant changes in the surface morphology of the sand after adsorption of the effluent. We notice the formation of a dense and compact matrix with a decrease in the degree of porosity and luminosity, and this can be explained by the adsorption of the molecules contained in the treated solute on the sand cracks and pores (Figure5(b)) [18].The chemical analysis by EDX proves the validity of spectral analysis with regard to the chemical composition of the sand used and shows that it consists mainly of C, O, Ca, and Si. The results also indicate the appearance of certain elements involved in the chemical composition of tannery effluent such as nitrogen, sulfur, chlorine, and chromium. The mass percentage of some elements such as O, Mg, Si, Fe, and Na decreased slightly after adsorption; this leads us to suppose that they were involved in the adsorption process of the effluent components Table3 and Figure 5.


### 3.5. Column Experiments

#### 3.5.1. Effect of Sand Grain Size on Effluent Discolouration

Figure6 shows the tannery effluent discolouration kinetics that have been studied for the different grain sizes of sand powder from 63 μm to 400 μm.Figure 6
Effect of sand grain size on the discolouration rate.The results show that the highest rate of discolouration is represented by the preponderant size of 63μm, and discolouration decreases with the increase in the diameter of the sand particles. The graphical presentation also shows that the fading rate is optimal and provides total fading of 100% for the 63 μm grain size, while the fading rate does not exceed 82% for the 400 μm grain size. The discolouration rates for the 125 μm, 200 μm, and 315 μm particle sizes are 97.2%, 94.4%, and 93.61%, respectively. As a conclusion, it can be said that the particle size is an important factor, which affects the adsorption capacity, and the fixation of the organic matter on the surface of the adsorbent material is generally more important when the grain size of the material is small [37].The studies of Sakr et al. conducted on the adsorption of methylene blue on cactus found similar results to those of our study with regard to the effect of particle size, and the highest percentages of adsorption were obtained using a size of 0.04 mm of cactus [38]. And, according to Guiza and Bagane who have worked with bentonite for the adsorption of Congo Red; an increase in particle diameter leads to a decrease in the transfer rate of the material [39].


#### 3.5.2. Effect of Flow Rate on Effluent Discolouration

The experimental results shown in Figure7 show that the discolouration capacity of the tannery effluent by sand is proportionally inverse to the withdrawal rate.Figure 7
Effect of the withdrawal rate on the discolouration rate.The rate of discolouration is maximum with a value of 95.6% for low flow which is equal to 15 ml·min−1 and minimum with a value of 90.4% for flow increased to 170 ml·min−1. From the results, it can be seen that the increase in the withdrawal rate causes a decrease in the residence time of the effluent molecules in the column. Thus, the exchange speed decreases, resulting in a loss of adsorption efficiency. Experimentally, the increase in flow rate causes a rapid saturation of the filter bed, and this is due to the increase in the exchange speed.Research carried out by Biswas and Mishra has also found that an increase in the withdrawal rate reduces the adsorbent-adsorbate contact time [40]. And, according to Sathvika et al., low flows increase the adsorption efficiency and increase the contact time between chromium VI solution and the biosorbent used [41].


#### 3.5.3. Effect of Filter Bed Height on Effluent Discolouration

Figure8 shows the effect of sand bed height on the rate of effluent discolouration. The results show that the total adsorption capacity increases with increasing bed height. The 3 cm and 5 cm beds have discolouration rates of 95.4% and 97.4%, respectively. The maximum fading rate is given by the 7 cm bed with a percentage that is close to 100%. From these results, it can be deduced that the height of the bed through which the effluent passes is one of the parameters that influence the performance of continuous adsorption and the operation of the column. The amount of adsorbent material used affects significantly the residence time, discolouration rate and volume of the treated effluent. The contact time becomes shorter as the height of the adsorbent bed decreases. This indicates that the bed with the minimum height of 3 cm is saturating faster. Whereas increasing the height of the adsorbent to 7 cm slows down the rate of solute-solid exchange and thus increases the residence time and improves the availability of active adsorption sites, which quantitatively and qualitatively promotes the retention of pollutants present in the tannery effluent [42].Figure 8
Effect of the sand bed height on the discolouration rate.Similar results were found by Lim and Aris who showed that the adsorption of CD(II) and Pb(II) is higher for the longest bed of the dead limestone skeletons and which is 2.20 cm equivalent of 40 g [8]. In another study conducted by (Tsai et al.), the results showed that the increase in the height of the activated carbon bed leads to a decrease in the concentration of Pb (II), Cu (II), and Ni (II) in the influent [43].


#### 3.5.4. Visual Appearance of the Raw Effluent and the Adsorbates

The visual appearance and reduction of the coloration of the raw effluent from the tannery (A0, B0, and C0) according to the different effects are shown in Figure9. These results show that the adsorbates (A1, A2, A3, and A4) have a slight coloration compared with the raw effluent A0, and this coloration decreases as the size of the sand grains decreases until an almost colourless influent is obtained (A5) (Figure 9(a)). The visual aspect of the adsorbates obtained at different flow rates (B1, B2, and B3) also show increasing discolouration with the decrease in the withdrawal rate Figure 9(b). For the effect of the height of the adsorbent bed, we notice that, from a dark blue effluent C0, we obtain translucent adsorbates with a slightly yellowish coloration for C1, while C3 and C4 have practically the same aspect as indicated by the graphical data (Figure 9(c)).Figure 9
Visual appearance of the raw effluent and the adsorbates obtained according to the different effects.
(a)
(b)
(c)


## 3.1. Particle Size Curve of Sand

The descriptive percentages of the granulometric analyses are illustrated in Figure2; the figure shows the allocation of 7 fractions for the granulometric distribution of sand, and the preponderant size which predominates is 200 μm with a percentage of 61.5%. This size is less than 500 μm, which gives it the class of fine sands.Figure 2
Granulometric curve of the sand used.


## 3.2. X-Ray Diffraction

The crystalline composition of the sand particles before and after adsorption is shown in Figure3. The X-ray diffractograms of the sand before and after adsorption shows almost the same appearance and reveal the existence of several characteristic peaks of quartz and calcite [25, 26]. For unsaturated sand, these two elements have a codominance indicated by the major peaks corresponding to the position 2θ, 27.7° and 29.7°, respectively [27–31]. Whereas for saturated sand, quartz predominates over calcite with the appearance of two unidentified peaks at 2θ, 43.41° and 51.08°, which can be attributed to the effluent components of the tannery.Figure 3
Diffractometric analysis of (a) natural sand and (b) loaded sand.
(a)
(b)


## 3.3. Infrared Spectroscopy Analysis

Figure4 and Table 2 present the main functional groups of the specific elements of natural sand and the possible modifications after the adsorption process. On one hand, the examination of these results show no change in the basic structure of Lowded Sand (LS) particles and this allows us to say that adsorption is done by physical interaction forces [25]. On other hand, the maximum intensities have decreased slightly; this may be related to an energy variation due to the bonds established with the pollutants in the effluent, and a small shift has been observed in the position of the adsorption bands, which probably justifies the feasibility of adsorption [18].Figure 4
Infrared spectrum of natural sand (NS) and loaded sand (LS).Table 2
Sand infrared bands and their assignments.
Natural sand position (cm−1)
Loaded sand position (cm−1)
Assignments
Reference
3419.60
3427.62
OH group stretch vibration
[18, 32, 33]
2922.88
2924.36
C–H asymmetrical stretching vibrations
[25, 32, 34]
2519.05
2518.98
C–H asymmetrical stretching vibration
[25]
1797.17
1796.91
Typical vibration of the OH stretching group
[3]
—
1620.91
OH group stretch vibration
[18]
1450.90
1452.76
CO3 stretching of calcite
[3, 35]
1082.85
1083.32
Valence vibration of the Si–O–Si bond
[18, 23, 32]
874.56
874.60
CO3 stretching of calcite
[35]
779.91
780.64
O–Si–O stretching
[25]
712.48
712.55
O–Si–O stretching
[25]
469.17
469.92
Valence vibration of the Si–O–Si bond
[25]These results also confirm the existence of the bonds characterizing calcite and quartz previously revealed by diffractometric analysis.


## 3.4. Scanning Electron Microscopy Coupled with the EDX

The SEM results coupled with the EDX of the sand before and after saturation as well as the mass percentages of each element are shown in Figure5 and Table 3. The internal microstructure of unmodified sands shows a rough, irregular, and proportionally porous and cracked appearance with the presence of some luminous and relatively ordered aggregations, that probably indicate the existence of quartz crystals previously detected by the DRX analysis [18, 36]. This mineralogical composition allows the interchanges of substances with adjacent cells and thus makes the adsorption mechanism possible (Figure 5(a)).Figure 5
Morphological examination of natural sand (a, b) and loaded sand (c, d) by SEM-EDX.Table 3
Percentage of elements found by X-ray energy dispersion EDX in natural and loaded sand.
Elements
Natural sand (NS)
Loaded sand (LS)
C
26.34
32.05
O
46.18
18.12
N
—
34.55
Na
3.42
1.45
Mg
0.94
0.45
Si
8.66
5.36
S
—
0.40
Cl
—
0.43
K
0.54
0.37
Ca
12.63
5.98
Cr
—
0.27
Fe
1.3
0.58
Total
100
100Microstructural analysis reveals significant changes in the surface morphology of the sand after adsorption of the effluent. We notice the formation of a dense and compact matrix with a decrease in the degree of porosity and luminosity, and this can be explained by the adsorption of the molecules contained in the treated solute on the sand cracks and pores (Figure5(b)) [18].The chemical analysis by EDX proves the validity of spectral analysis with regard to the chemical composition of the sand used and shows that it consists mainly of C, O, Ca, and Si. The results also indicate the appearance of certain elements involved in the chemical composition of tannery effluent such as nitrogen, sulfur, chlorine, and chromium. The mass percentage of some elements such as O, Mg, Si, Fe, and Na decreased slightly after adsorption; this leads us to suppose that they were involved in the adsorption process of the effluent components Table3 and Figure 5.


## 3.5. Column Experiments

### 3.5.1. Effect of Sand Grain Size on Effluent Discolouration

Figure6 shows the tannery effluent discolouration kinetics that have been studied for the different grain sizes of sand powder from 63 μm to 400 μm.Figure 6
Effect of sand grain size on the discolouration rate.The results show that the highest rate of discolouration is represented by the preponderant size of 63μm, and discolouration decreases with the increase in the diameter of the sand particles. The graphical presentation also shows that the fading rate is optimal and provides total fading of 100% for the 63 μm grain size, while the fading rate does not exceed 82% for the 400 μm grain size. The discolouration rates for the 125 μm, 200 μm, and 315 μm particle sizes are 97.2%, 94.4%, and 93.61%, respectively. As a conclusion, it can be said that the particle size is an important factor, which affects the adsorption capacity, and the fixation of the organic matter on the surface of the adsorbent material is generally more important when the grain size of the material is small [37].The studies of Sakr et al. conducted on the adsorption of methylene blue on cactus found similar results to those of our study with regard to the effect of particle size, and the highest percentages of adsorption were obtained using a size of 0.04 mm of cactus [38]. And, according to Guiza and Bagane who have worked with bentonite for the adsorption of Congo Red; an increase in particle diameter leads to a decrease in the transfer rate of the material [39].


### 3.5.2. Effect of Flow Rate on Effluent Discolouration

The experimental results shown in Figure7 show that the discolouration capacity of the tannery effluent by sand is proportionally inverse to the withdrawal rate.Figure 7
Effect of the withdrawal rate on the discolouration rate.The rate of discolouration is maximum with a value of 95.6% for low flow which is equal to 15 ml·min−1 and minimum with a value of 90.4% for flow increased to 170 ml·min−1. From the results, it can be seen that the increase in the withdrawal rate causes a decrease in the residence time of the effluent molecules in the column. Thus, the exchange speed decreases, resulting in a loss of adsorption efficiency. Experimentally, the increase in flow rate causes a rapid saturation of the filter bed, and this is due to the increase in the exchange speed.Research carried out by Biswas and Mishra has also found that an increase in the withdrawal rate reduces the adsorbent-adsorbate contact time [40]. And, according to Sathvika et al., low flows increase the adsorption efficiency and increase the contact time between chromium VI solution and the biosorbent used [41].


### 3.5.3. Effect of Filter Bed Height on Effluent Discolouration

Figure8 shows the effect of sand bed height on the rate of effluent discolouration. The results show that the total adsorption capacity increases with increasing bed height. The 3 cm and 5 cm beds have discolouration rates of 95.4% and 97.4%, respectively. The maximum fading rate is given by the 7 cm bed with a percentage that is close to 100%. From these results, it can be deduced that the height of the bed through which the effluent passes is one of the parameters that influence the performance of continuous adsorption and the operation of the column. The amount of adsorbent material used affects significantly the residence time, discolouration rate and volume of the treated effluent. The contact time becomes shorter as the height of the adsorbent bed decreases. This indicates that the bed with the minimum height of 3 cm is saturating faster. Whereas increasing the height of the adsorbent to 7 cm slows down the rate of solute-solid exchange and thus increases the residence time and improves the availability of active adsorption sites, which quantitatively and qualitatively promotes the retention of pollutants present in the tannery effluent [42].Figure 8
Effect of the sand bed height on the discolouration rate.Similar results were found by Lim and Aris who showed that the adsorption of CD(II) and Pb(II) is higher for the longest bed of the dead limestone skeletons and which is 2.20 cm equivalent of 40 g [8]. In another study conducted by (Tsai et al.), the results showed that the increase in the height of the activated carbon bed leads to a decrease in the concentration of Pb (II), Cu (II), and Ni (II) in the influent [43].


### 3.5.4. Visual Appearance of the Raw Effluent and the Adsorbates

The visual appearance and reduction of the coloration of the raw effluent from the tannery (A0, B0, and C0) according to the different effects are shown in Figure9. These results show that the adsorbates (A1, A2, A3, and A4) have a slight coloration compared with the raw effluent A0, and this coloration decreases as the size of the sand grains decreases until an almost colourless influent is obtained (A5) (Figure 9(a)). The visual aspect of the adsorbates obtained at different flow rates (B1, B2, and B3) also show increasing discolouration with the decrease in the withdrawal rate Figure 9(b). For the effect of the height of the adsorbent bed, we notice that, from a dark blue effluent C0, we obtain translucent adsorbates with a slightly yellowish coloration for C1, while C3 and C4 have practically the same aspect as indicated by the graphical data (Figure 9(c)).Figure 9
Visual appearance of the raw effluent and the adsorbates obtained according to the different effects.
(a)
(b)
(c)


## 3.5.1. Effect of Sand Grain Size on Effluent Discolouration

Figure6 shows the tannery effluent discolouration kinetics that have been studied for the different grain sizes of sand powder from 63 μm to 400 μm.Figure 6
Effect of sand grain size on the discolouration rate.The results show that the highest rate of discolouration is represented by the preponderant size of 63μm, and discolouration decreases with the increase in the diameter of the sand particles. The graphical presentation also shows that the fading rate is optimal and provides total fading of 100% for the 63 μm grain size, while the fading rate does not exceed 82% for the 400 μm grain size. The discolouration rates for the 125 μm, 200 μm, and 315 μm particle sizes are 97.2%, 94.4%, and 93.61%, respectively. As a conclusion, it can be said that the particle size is an important factor, which affects the adsorption capacity, and the fixation of the organic matter on the surface of the adsorbent material is generally more important when the grain size of the material is small [37].The studies of Sakr et al. conducted on the adsorption of methylene blue on cactus found similar results to those of our study with regard to the effect of particle size, and the highest percentages of adsorption were obtained using a size of 0.04 mm of cactus [38]. And, according to Guiza and Bagane who have worked with bentonite for the adsorption of Congo Red; an increase in particle diameter leads to a decrease in the transfer rate of the material [39].


## 3.5.2. Effect of Flow Rate on Effluent Discolouration

The experimental results shown in Figure7 show that the discolouration capacity of the tannery effluent by sand is proportionally inverse to the withdrawal rate.Figure 7
Effect of the withdrawal rate on the discolouration rate.The rate of discolouration is maximum with a value of 95.6% for low flow which is equal to 15 ml·min−1 and minimum with a value of 90.4% for flow increased to 170 ml·min−1. From the results, it can be seen that the increase in the withdrawal rate causes a decrease in the residence time of the effluent molecules in the column. Thus, the exchange speed decreases, resulting in a loss of adsorption efficiency. Experimentally, the increase in flow rate causes a rapid saturation of the filter bed, and this is due to the increase in the exchange speed.Research carried out by Biswas and Mishra has also found that an increase in the withdrawal rate reduces the adsorbent-adsorbate contact time [40]. And, according to Sathvika et al., low flows increase the adsorption efficiency and increase the contact time between chromium VI solution and the biosorbent used [41].


## 3.5.3. Effect of Filter Bed Height on Effluent Discolouration

Figure8 shows the effect of sand bed height on the rate of effluent discolouration. The results show that the total adsorption capacity increases with increasing bed height. The 3 cm and 5 cm beds have discolouration rates of 95.4% and 97.4%, respectively. The maximum fading rate is given by the 7 cm bed with a percentage that is close to 100%. From these results, it can be deduced that the height of the bed through which the effluent passes is one of the parameters that influence the performance of continuous adsorption and the operation of the column. The amount of adsorbent material used affects significantly the residence time, discolouration rate and volume of the treated effluent. The contact time becomes shorter as the height of the adsorbent bed decreases. This indicates that the bed with the minimum height of 3 cm is saturating faster. Whereas increasing the height of the adsorbent to 7 cm slows down the rate of solute-solid exchange and thus increases the residence time and improves the availability of active adsorption sites, which quantitatively and qualitatively promotes the retention of pollutants present in the tannery effluent [42].Figure 8
Effect of the sand bed height on the discolouration rate.Similar results were found by Lim and Aris who showed that the adsorption of CD(II) and Pb(II) is higher for the longest bed of the dead limestone skeletons and which is 2.20 cm equivalent of 40 g [8]. In another study conducted by (Tsai et al.), the results showed that the increase in the height of the activated carbon bed leads to a decrease in the concentration of Pb (II), Cu (II), and Ni (II) in the influent [43].


## 3.5.4. Visual Appearance of the Raw Effluent and the Adsorbates

The visual appearance and reduction of the coloration of the raw effluent from the tannery (A0, B0, and C0) according to the different effects are shown in Figure9. These results show that the adsorbates (A1, A2, A3, and A4) have a slight coloration compared with the raw effluent A0, and this coloration decreases as the size of the sand grains decreases until an almost colourless influent is obtained (A5) (Figure 9(a)). The visual aspect of the adsorbates obtained at different flow rates (B1, B2, and B3) also show increasing discolouration with the decrease in the withdrawal rate Figure 9(b). For the effect of the height of the adsorbent bed, we notice that, from a dark blue effluent C0, we obtain translucent adsorbates with a slightly yellowish coloration for C1, while C3 and C4 have practically the same aspect as indicated by the graphical data (Figure 9(c)).Figure 9
Visual appearance of the raw effluent and the adsorbates obtained according to the different effects.
(a)
(b)
(c)


## 4. Conclusion

The treatment of effluent from tanning activity by a biological process appears to be difficult, as it is highly loaded with heavy metals and has a toxic environment for microbial biomasses. This study proved the effectiveness of marine sands in cleaning up industrial tanning water and removing micropollutants as a pretreatment step. Experimental tests show that the discolouration rate is optimal and close to 100% for the sand grain size of 63μm. The rate of discolouration is maximum with a value of 95.6% for the low flow rate which is equal to 15 ml·min−1. The maximum fading rate is given by the 7 cm sand bed with a value of 98.7%.The characterization of the sand by the different FTIR, SEM, and X-RD techniques has revealed modifications in the surface as well as the crystalline and chemical structure of the sand after adsorption which means the retention of effluent pollutants through pores and cracks in marine sand.



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*Source: 7613484-2020-01-24.xml*