Desalination of Water Using ZVI (Fe0)

Water

David D. J. Antia¹ 

[1] DCA Consultants Ltd., Haughend, Bridge of Earn Road, Dunning, Perthshire PH2 9BX, UK; E-Mail

关键词: desalination;    zero valent metal;    Eh;    pH;    electrical conductivity (EC);    Fe⁰;    Al⁰;    Cu⁰;    FeOOH;   

DOI  :  10.3390/w7073671

来源: mdpi

【 摘 要 】

Batch treatment of water (0.2 to 240 L) using Fe⁰ (44,000–77,000 nm) in a diffusion environment operated (at −8 to 25 °C) using: (a) no external energy; (b) pressurized (<0.1 MPa) air; (c) pressurized (<0.1 MPa) acidic gas (CO₂); (d) pressurized (<0.1 MPa) anoxic gas (N₂); (e) pressurized (<0.1 MPa) anoxic, acidic, reducing gas (H₂ + CO + CO₂ + CH₄ + N₂), reduces the salinity of water. Desalination costs increase with increasing NaCl removal. The cost of reducing water salinity from: (i) 2.65 to 1.55 g·L⁻¹ (over 1–24 h) is $0.002–$0.026 m⁻³; (ii) 38.6 to 0.55 g·L⁻¹ (over 210 days) is $67.6–$187.2 m⁻³. Desalination is accompanied by the removal, from the water, of one or more of: nitrate, chloride, fluoride, sulphate, phosphate, As, B, Ba, Ca, Cd, Co, Cu, Fe, Mg, Mn, Na, Ni, P, S, Si, Sr, Zn. The rate of desalination is enhanced by increasing temperatures and increasing HCO₃⁻/CO₃²⁻ concentrations. The rate of desalination decreases with increasing SO₄²⁻ removal under acidic, or pH neutral, operating conditions.

【 授权许可】

CC BY   
© 2015 by the authors; licensee MDPI, Basel, Switzerland.