کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
1274559 1497549 2012 8 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Effect of hydraulic retention time on hydrogen production and chemical oxygen demand removal from tapioca wastewater using anaerobic mixed cultures in anaerobic baffled reactor (ABR)
موضوعات مرتبط
مهندسی و علوم پایه شیمی الکتروشیمی
پیش نمایش صفحه اول مقاله
Effect of hydraulic retention time on hydrogen production and chemical oxygen demand removal from tapioca wastewater using anaerobic mixed cultures in anaerobic baffled reactor (ABR)
چکیده انگلیسی

This study evaluated hydrogen production and chemical oxygen demand removal (COD removal) from tapioca wastewater using anaerobic mixed cultures in anaerobic baffled reactor (ABR). The ABR was conducted based on the optimum condition obtained from the batch experiment, i.e. 2.25 g/L of FeSO4 and initial pH of 9.0. The effects of the varying hydraulic retention times (HRT: 24, 18, 12, 6 and 3 h) on hydrogen production and COD removal in a continuous ABR were operated at room temperature (32.3 ± 1.5 °C). Hydrogen production rate (HPR) increased with a reduction in HRT i.e. from 164.45 ± 4.14 mL H2/L.d (24 h HRT) to 883.19 ± 7.89 mL H2/L.d (6 h HRT) then decreased to 748.54 ± 13.84 mL H2/L.d (3 h HRT). COD removal increased with reduction in HRT i.e. from 14.02 ± 0.58% (24 h HRT) to 29.30 ± 0.84% (6 h HRT) then decreased to 21.97 ± 0.94% (3 h HRT). HRT of 6 h was the optimum condition for ABR operation as indicated.


► HPR and COD removal from tapioca wastewater using ABR were studied.
► ABR was conducted on optimum condition, i.e. 2.25 g/L of FeSO4 and initial pH of 9.0.
► ABR operation at room temperature (32.3 ± 1.5 °C) with HRT of 24, 18, 12, 6 and 3 h.
► HRT of 6 h was the optimum condition for ABR operation.
► HPR of 883.19 ± 7.89 mL H2/L.d and COD removal of 29.30 ± 0.84% were achieved.

ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: International Journal of Hydrogen Energy - Volume 37, Issue 20, October 2012, Pages 15503–15510
نویسندگان
, , ,