کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
7717776 1497476 2014 10 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Overcoming propionic acid inhibition of hydrogen fermentation by temperature shift strategy
ترجمه فارسی عنوان
غلبه بر مهار غلظت پروتئین اسید فرآیند هیدروژن توسط استراتژی تغییر دما
کلمات کلیدی
فاضلاب آشامیدنی، بیفیدوباکتریوم، رآکتور مخزن مداوم، سلنوموناس، تغییر دما،
موضوعات مرتبط
مهندسی و علوم پایه شیمی الکتروشیمی
چکیده انگلیسی
A novel temperature shift strategy has been proposed to overcome an inhibition on hydrogen fermentation of beverage industry wastewater (BW) due to the accumulation of propionic acid (HPr) during continuous reactor operation. The continuous performance at constant pH 5.5, temperature 37 °C and hydraulic retention time (HRT) 8 h with BW concentration of 20 g/Lhexose-equivalent in a stirred tank reactor (2 L) showed an accumulation of HPr to 2.36 g/L leading to a drop in hydrogen production rate (HPR) from 10 to 8.5 L L−1 d−1. To overcome the HPr inhibition, a temperature shift (from 37 °C) to 45 °C for 8 h was applied. This significantly improved the inhibited HPR and HY to 13.6 L L−1 d−1 and 1.68 mol-H2 mol−1 hexose, respectively, with a simultaneous reduction in the HPr concentration to 0.7 g/L. Microbial community analysis based on PCR-DGGE after temperature shift revealed the non-dominance of Selenomonas lacticifex and Bifidobacterium catenulatum (involved in HPr formation), and dominance of hydrogen producing bacteria namely Clostridium butyricum, Clostridium perfringenes, Clostridium acetobutylicum, and Ethanoligenens harbinense. This study demonstrated that temperature shift strategy could overcome the HPr inhibition and significantly improve the hydrogen fermentation of an industrial wastewater.
ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: International Journal of Hydrogen Energy - Volume 39, Issue 33, 11 November 2014, Pages 19232-19241
نویسندگان
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