Abstract
Forward osmosis (FO) is a membrane technology which has attracted attention for water treatment and desalination. However, selecting an appropriate draw solute is vital to optimize its performance. This study seeks the efficiency of aluminum sulfate as an alternative draw solute in FO desalination with a cellulose triacetate (CTA) membrane. The effects of operating parameters on the performance of the FO were studied such as feed and draw temperatures, concentrations and flow. The experiments revealed that the permeate flux was improved by monitoring draw temperature, with a maximum of 2.5 L/m2 h was obtained at 53 °C. Also, the permeate flux was found to decrease with feed concentration. A maximum permeate flux of 2 L/m2 h was obtained at a draw flow rate of 35 L/h and draw concentration of 1 mol/L. On the other hand, using deionized water as feed solution yielded a reverse aluminum sulfate flux of 1.46 g/m2 h. The plots of the experimental and the modeling water flux displayed analogous trends in all tests, but the results showed a large deviation which was attributed to reverse solute flux, internal polarization concentration (ICP), external polarization concentration (ECP) and membrane fouling. Precipitation reaction using calcium hydroxide served to recover product water from the diluted draw solution. This operation was carried out via a precipitation reaction of aluminum sulfate with calcium hydroxide to eliminate the soluble chemicals like insoluble aluminum hydroxide and calcium sulfate. Eventually, aluminum sulfate draw solution was recovered by the reaction of aluminum hydroxide with sulfuric acid.
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Abbreviations
- ϕ:
-
Osmotic coefficient
- νa :
-
Number of anions in the electrolyte formula
- νc :
-
Number of cations in the electrolyte formula
- Za :
-
Charges of the anion
- Zc :
-
Charges of the cation
- m:
-
Overall molality of the electrolyte (mol/kg)
- Cac :
-
Third virial coefficient
- C:
-
Solution concentration (mg/L)
- M:
-
Molar mass of aluminum sulfate (kg/mol)
- ρ:
-
Draw solution density (kg/m3)
- Cϕ :
-
Pitzer parameter
- β(0)ac , β(1)ac :
-
Second virial coefficients
- α, b:
-
Model parameters
- I:
-
Ionic strength
- Aϕ :
-
Debye–Hückel constant
- ma :
-
Respective molality values of the anion (mol/kg)
- mb :
-
Respective molality values of the cation (mol/kg)
- NA :
-
Avogadro number
- \( \uprho_{{{\text{H}}_{2} {\text{O}}}} \) :
-
Density of water (kg/m3)
- e:
-
Electronic charge
- T:
-
Absolute temperature (K)
- ε:
-
Water dielectric constant
- k:
-
Boltzmann’s constant
- π:
-
Osmotic pressure (Pa)
- R:
-
Universal gas constant (J/mol/K)
- ρ:
-
Density of aluminum sulfate draw solution (kg/m3)
- w:
-
Mass fraction
- \( \bar{\nu } \) :
-
Partial molar volume (m3/kg)
- Jw :
-
Water flux (L/m2 h, LMH)
- ΔV:
-
The change in volume of feed solution (L)
- Δt:
-
Time interval for the volume change of ΔV (h)
- S:
-
Active membrane surface area (m2)
- A:
-
Membrane water permeability coefficient (m/s/Pa)
- πD :
-
Osmotic pressure of the draw solution (Pa)
- πF :
-
Osmotic pressure of the feed solution (Pa)
- Js :
-
Reverse salt flux (g/m2 h, gMH)
- C0 :
-
Initial feed concentrations (g/L)
- Cf :
-
Final feed concentrations (g/L)
- V0 :
-
Initial volume of the feed solution (L)
- Vf :
-
Final volume of the feed solution (L)
- σ0 :
-
Initial conductivity of the feed solution (S/m)
- σf :
-
Final conductivity of the feed solution (S/m)
- λ:
-
Molar electrical conductivity of the feed solution (S m2/mol)
- C0 :
-
Initial aluminum feed concentration (mol/m3)
- Cf :
-
Final aluminum feed concentration (mol/m3)
- CP:
-
Concentration polarization
- ICP:
-
Internal concentration polarisation
- ECP:
-
External concentration polarisation
- FS:
-
Feed solution
- DS:
-
Draw solution
- FO:
-
Forward osmosis
- CTA:
-
Cellulose triacetate membrane
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Maouia, D.B., Boubakri, A., Hafiane, A. et al. Aluminum Sulfate as an Innovative Draw Solute for Forward Osmosis Desalination. Chemistry Africa 3, 141–152 (2020). https://doi.org/10.1007/s42250-019-00092-9
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DOI: https://doi.org/10.1007/s42250-019-00092-9