کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
221630 464263 2016 11 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Evaluation of operating parameters with respect to charge loading on the removal efficiency of arsenic from potable water by electrocoagulation
ترجمه فارسی عنوان
ارزیابی پارامترهای عملگرا با توجه به بارگذاری شارژ در راندمان حذف آرسنیک از آب آشامیدنی توسط الکتروکواگولاسیون
کلمات کلیدی
الکترو کلاژن؛ آرسنیک؛ بارگذاری شارژ؛ هزینه های عملیاتی
موضوعات مرتبط
مهندسی و علوم پایه مهندسی شیمی مهندسی شیمی (عمومی)
چکیده انگلیسی


• Removal efficiency of arsenic from potable water was conducted in the batch EC reactor using Fe electrodes.
• The process was able to remove more than 95% of arsenic from arsenic contaminated potable water.
• The operating cost at the optimum operating conditions was 0.00075 €/m3.
• The removal process followed the pseudo second-order kinetics.

Charge loading is the most important parameter for controlling the reaction rate within electrocoagulation process (EC) which determines the coagulant production rate, and it may also serve as a design parameter for the process. In the present study, arsenic removal from potable water by a batch EC process using iron plate electrodes was investigated with respect to charge loading and effects of operating parameters such as current density, operating time, initial arsenic concentration, ratio of electrode surface area over volume (S/V), and electrode connection mode on removal efficiency of arsenic were evaluated. The results showed that arsenic concentration of 150 μg/L in monopolar series (MP-S) electrode connection mode during the EC process decreased the arsenic concentration to less than 6 μg/L corresponding to removal efficiency of 95.1% (under the limit set by the World Health Organization) at current density of 2.5 A/m2, charge loading of 50 C/L, S/V of 10 m2/m3 (ratio of electrode surface area over volume), EC time of 7.5 min. Arsenic removed capacity and charge dosage rate at the optimum operating conditions were 2.8 μg As removed/C and 4.00 C/L/min. The adsorption of arsenic over electrochemically produced hydroxides and metal oxide complexes followed pseudo second-order adsorption model (r2 > 0.94). Operating costs were affected with current density, electrode connection mode, S/V and initial concentration of arsenic from potable water. The operating cost at MP-S connection mode was calculated as 0.00075 €/m3 at 150 μg/L, 0.05 A, 7.5 min and 30 C/L.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Journal of Environmental Chemical Engineering - Volume 4, Issue 2, June 2016, Pages 1484–1494
نویسندگان
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