کد مقاله کد نشریه سال انتشار مقاله انگلیسی نسخه تمام متن
6364281 1623062 2016 12 صفحه PDF دانلود رایگان
عنوان انگلیسی مقاله ISI
Compact secondary treatment train combining a lab-scale moving bed biofilm reactor and enhanced flotation processes
ترجمه فارسی عنوان
قطب درمان جامع ثانویه ترکیب یک رآکتور بیوفیلم در حال حرکت در آزمایشگاه و فرآیندهای شناور افزایش یافته است
کلمات کلیدی
رآکتور بیوفیلم تخت حرکتی، روند جداسازی نوآورانه، شناور پیشرفته هموگلوبین سبز، پلیمر سبز، فرایند با سرعت بالا،
موضوعات مرتبط
مهندسی و علوم پایه علوم زمین و سیارات فرآیندهای سطح زمین
چکیده انگلیسی


- A treatment train combining an HR-MBBR with an enhanced flotation process was studied.
- CSCOD removal efficiency increased with the MBBR HRT (inversely with OLR) up to 88%.
- An MBBR OLR of 6-10 kg COD m−3 reactor d−1 resulted in the best XCOD recovery.
- MBBR effluent solids were characterized by a bimodal volume particle size distribution.
- Enhanced flotation with green chemicals allowed to reach 10 ± 3 mg TSS/L in the MBBR effluent.

High-rate wastewater processes are receiving a renewed interest to obtain energy positive/efficient water resource recovery facilities. An innovative treatment train combining a high-rate moving bed biofilm reactor (HR-MBBR) with an enhanced flotation process was studied. The two objectives of this work were 1) to maximize the conversion of soluble organics to particulate matter in an HR-MBBR and 2) to maximize the particulate matter recovery from the HR-MBBR effluent by green chemicals to enhance biogas production by anaerobic digestion. To achieve these objectives, lab-scale MBBRs fed with synthetic soluble wastewater were operated at organic loading rates (OLRs) between 4 and 34 kg COD m−3 reactor d−1 corresponding to hydraulic retention times (HRTs) between 6 and 54 min.Colloidal and soluble chemical oxygen demand (COD) removal efficiency in the HR-MBBR increased with HRT to reach a plateau of 85% at an HRT longer than 27 min. Carrier clogging observed at an OLR higher than 16 kg COD m−3 d−1 (HRT < 13 min) resulted in about 23% loss in colloidal and soluble COD removal efficiency. Thus, the recommended parameters were between 22 and 37 min and between 6 and 10 kg COD m−3 d−1 for the HRT and the OLR, respectively, to maximize the conversion of soluble organics to particulate matter.Total suspended solids (TSS) recovery of 58-85% and 90-97% were achieved by enhanced flotation using green and unbiodegradable chemicals, respectively, corresponding to a TSS effluent concentration below 14 and 7 mg TSS/L. Among the synthetic polymers tested, a high molecular weight and low charge density cationic polyacrylamide was found to give the best results with less than 2 mg TSS/L in the clarified effluent (97% TSS recovery). Green chemicals, although performing slightly less for solids separation than unbiodegradable chemicals, achieved a mean TSS concentration of 10 ± 3 mg/L in the clarified effluent.

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ناشر
Database: Elsevier - ScienceDirect (ساینس دایرکت)
Journal: Water Research - Volume 106, 1 December 2016, Pages 571-582
نویسندگان
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