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Development of a Modified Three-Stage Methane Production Process Using Food Wastes

机译:利用食物垃圾开发改良的三阶段甲烷生产工艺

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A modified three-stage system was developed for the rapid production of methane from food wastes. The primary stage was a semianaerobic hydroly-sis/acidogenic system, in which approx 4100 mg/L of volatile fatty acids (VFAs) was produced at a hydraulic retention time (HRT) of 2 d. The operation temperature and pH were 30°C and 5.0―5.5, respectively. The non-degraded materials were removed through a hole at the bottom of the reactor. The secondary stage was an anaerobic acidogenic system equipped with an upflow anaerobic sludge blanket (UASB) type of fermentor. VFA was accumulated up to 6100 mg/L by the addition of Clostridium butyricum to the reactor at an HRT of 2 d. The optimum temperature and pH range were 35°C and 5.0―5.5, respectively. The tertiary methanogenic stage produced CH_4 and CO_2 from the VFA in the UASB reactor. Methane content was 72% of the total gas volume, and the yield was 0.45―0.50 m~3/kg of volatile solids at an HRT of 12 d. The operation temperature and pH were 41°C and 7.6-7.9, respectively. The three-stage process exhibited an unusually high total chemical oxygen demand reduction rate up to 95%. Total nitrogen decreased to 96% and <10 mg/L of total phosphorus remained in the final effluent.
机译:开发了一种改进的三阶段系统,用于从食物垃圾中快速生产甲烷。首要阶段是半厌氧水解/产酸系统,其中在2 d的水力停留时间(HRT)下产生约4100 mg / L的挥发性脂肪酸(VFA)。操作温度和pH分别为30℃和5.0-5.5。通过反应器底部的孔除去未降解的材料。第二阶段是厌氧产酸系统,配备上流式厌氧污泥层(UASB)型发酵罐。通过在2 d的HRT下向反应器中添加丁酸梭菌,将VFA累积至6100 mg / L。最佳温度和pH范围分别为35°C和5.0-5.5。三次产甲烷阶段在UASB反应器中从VFA生成CH_4和CO_2。 HRT为12 d时,甲烷含量为总气体体积的72%,产率为0.45-0.50 m〜3 / kg挥发性固体。操作温度和pH分别为41℃和7.6-7.9。该三阶段过程显示出异常高的总化学需氧量降低率,最高可达95%。总氮减少到96%,最终出水中总磷<10 mg / L。

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