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Treatment of Food Industry Waste by Bench-Scale Upflow Anaerobic Sludge Blanket-Anoxic-Aerobic System

机译:台式规模厌氧污泥-厌氧-好氧系统处理食品工业废物

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An upflow anaerobic sludge blanket (UASB)-anoxic-aerobic system was used for treatment of tomato and bean processing wastewater. At various hydraulic retention times, ranging from 0.7 to 5 days, excellent removal of chemical oxygen demand (COD), biochemical oxygen demand (BOD), total suspended solids (TSS), ammonia-nitrogen (NH_4-N), and total Kjeldahl nitrogen was achieved with final effluent BOD/TSS/NH_4-N concentrations of less than 15/15/1 mg/L. Biogas yield in the UASB reactor varied from 0.33 to 0.44 m~3/kgCOD_(re,pved). The kinetics of anaerobic treatment were investigated. The yield coefficient was 0.03 gVSS/gCOD; maximum specific growth rate was 0.24 day~(-1); Monod half velocity constant was 135 mgCOD/L; and specific substrate utilization rate was 3.25 gCOD/gVSS . d. Nitrification and denitrification kinetics were studied in batch experiments, and the rates were comparable with those in the continuous flow system.
机译:上流式厌氧污泥层(UASB)-缺氧-好氧系统用于处理番茄和豆类加工废水。在各种水力停留时间(从0.7到5天)内,可以很好地去除化学需氧量(COD),生化需氧量(BOD),总悬浮固体(TSS),氨氮(NH_4-N)和凯氏氮最终出水的BOD / TSS / NH_4-N浓度小于15/15/1 mg / L时,可达到目标浓度。 UASB反应器中的沼气产量在0.33至0.44 m〜3 / kgCOD_(re,pved)之间变化。研究了厌氧处理的动力学。产率系数为0.03gVSS / gCOD。最大比生长率为0.24天〜(-1);单峰半速度常数为135 mgCOD / L;底物利用率为3.25 gCOD / gVSS。 d。分批实验研究了硝化和反硝化动力学,其速率与连续流系统中的速率相当。

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