易腐有机垃圾单级高固体厌氧消化实验研究

在中温(35～37℃)条件下,对连续式单级高固体厌氧消化反应器处理易腐有机垃圾进行了试验研究,连续试验时间达半年以上.结果表明,系统稳定运行时,在进料TS为24.79%、VS为23.06%的情况下,单位体积反应器产气效率最高达到3.69L/(L·d),易腐有机垃圾的产气能力(以VS计)为746.33 L/kg,有机负荷(以VS计)达到4.94 kg/(m3·d),水力停留时间47 d,此时期处理效果理想;试验启动之初易发生酸化,其抑制情况严重,出现0产气,经碱性溶液调节后情况得到较好解决;反应进行至80 d后产气速率降至最高速率的一半以下,推断是氨氮浓度超过2000mg/L而产生氨氮抑制,经过投加化学药剂和调节进料C/N抑制情况得到缓解.

Research on Single Phase High Solid Anaerobic Digestion of Organic Fraction of Municipal Solid Wastes

Under mesophilic condition (35 degrees C), a bench-scale experiment based on high solid anaerobic digestion process was conducted in a fed-batch single phase reactor to treat the OFMSW. The experiment has lasted for more than half a year and significant results were obtained. At the start-up stage, acidification occurred and showed large inhibition to gas production and the gas production rate once dropped to 0. After pH conditioning, the system has recovered and began to stably running. In this period, gas production rate reached 746.33 L/kg volatile solids (VS) 3.69 L/(L x d)] when the total solids (TS) content of the feeding waste was 24.79% and the VS content was 23.06%. The organic loading rate and hydraulic retention time(HRT) was 4.94 kg/(m3 x d) and 47 d respectively. However, with time went by, accumulated ammonia exceeded its limited value, which is deduced as 2000 mg/L, and the gas production rate dropped below half of the maximum value. By adding chemicals to diminish the amount of ammonia and adjusting the C/N of the feeding, inhibition was relaxed and gas production rate increased gradually.