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Byproduct Recovery from Reclaimed Water Reverse Osmosis Concentrate Using Lime and Soda‐Ash Treatment
Author(s) -
Mohammadesmaeili Farah,
Badr Mostafa Kabiri,
Abbaszadegan Morteza,
Fox Peter
Publication year - 2010
Publication title -
water environment research
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.356
H-Index - 73
eISSN - 1554-7531
pISSN - 1061-4303
DOI - 10.2175/106143009x12487095236919
Subject(s) - reverse osmosis , lime , chemistry , magnesium , calcium carbonate , calcium hydroxide , fouling , pulp and paper industry , precipitation , materials science , metallurgy , membrane , biochemistry , physics , organic chemistry , meteorology , engineering
Lime and soda‐ash softening of reclaimed water reverse osmosis concentrates as a pretreatment step for concentration by seawater reverse osmosis was the focus of this study. The objectives were removal of the potential fouling minerals of calcium, magnesium, and silica by selective precipitation, while producing byproducts with potential resale value. Three different bench‐scale lime‐soda processes were evaluated. The traditional method produced low‐quality magnesium hydroxide [Mg(OH) 2 ] and calcium carbonate (CaCO 3 ) byproducts. A modified process with pre‐acidification to eliminate carbonate removed 98 to 99% of calcium and magnesium and produced CaCO 3 that was >94% pure. To prevent the contamination of byproducts with calcium sulfate (CaSO 4 ) in high‐sulfate concentrates, a CaSO 4 crystallization step was added successfully to the modified process to precipitate CaSO 4 before Mg(OH) 2 precipitation and produce gypsum that was 92% pure. The modified lime‐soda process also removed 94 to 97% silica, 72 to 77% barium, and 95 to 96% strontium, which are known as reverse osmosis membrane foulants.