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
Link To Document :
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