Title of article
Bench-scale pertraction of iodine using a bulk liquid membrane system Original Research Article
Author/Authors
Betsabe Nabieyan، نويسنده , , Ali Kargari، نويسنده , , Tahereh Kaghazchi، نويسنده , , Alireza Mahmoudian، نويسنده , , Mansoureh Soleimani، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2007
Pages
10
From page
167
To page
176
Abstract
The transport of iodine through a bulk liquid membrane containing kerosene as solvent and alkaline sodium sulfite solution as receiving phase in a bench scale system was studied. It was found that the pH of feed solution has a major effect on the extraction rate. On the other hand, the concentration of the receiving phase has an important role on the stripping efficiency. Using proper conditions for extraction and stripping, the system is able to extract 82.5% of iodine present in the feed solution within 8.5 hours and 98.83% within 28.5 hours. At the same time, the stripping efficiencies are 71.8% and 85.12% at 8.5 and 28.5 hours, respectively.
Keywords
Iodine , Bulk liquid membrane , Extraction , Bench scale , Pertraction , Stripping
Journal title
Desalination
Serial Year
2007
Journal title
Desalination
Record number
1111070
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