School of Civil and Environmental Engineering, Georgia Institute of Technology, Atlanta, GA, 30332-0512, USA.
School of Civil and Environmental Engineering, Georgia Institute of Technology, Atlanta, GA, 30332-0512, USA.
Water Res. 2015 Dec 15;87:432-45. doi: 10.1016/j.watres.2015.04.031. Epub 2015 May 5.
A bench-scale investigation was conducted to select external organic wastes and mixing ratios for co-digestion with municipal sludge at the F. Wayne Hill Water Resources Center (FWHWRC), Gwinnett County, GA, USA to support a combined heat and power (CHP) project. External wastes were chosen and used subject to two constraints: a) digester retention time no lower than 15 d; and b) total biogas (methane) production not to exceed a specific target level based on air permit constraints on CO2 emissions. Primary sludge (PS), thickened waste activated sludge (TWAS) and digested sludge collected at the FWHWRC, industrial liquid waste obtained from a chewing gum manufacturing plant (GW) and dewatered fat-oil-grease (FOG) were used. All sludge and waste samples were characterized and their ultimate digestibility was assessed at 35 °C. The ultimate COD to methane conversion of PS, TWAS, municipal sludge (PS + TWAS; 40:60 w/w TS basis), GW and FOG was 49.2, 35.2, 40.3, 72.7, and 81.1%, respectively. Co-digestion of municipal sludge with GW, FOG or both, was evaluated using four bench-scale, mesophilic (35 °C) digesters. Biogas production increased significantly and additional degradation of the municipal sludge between 1.1 and 30.7% was observed. Biogas and methane production was very close to the target levels necessary to close the energy deficit at the FWHWRC. Co-digestion resulted in an effluent quality similar to that of the control digester fed only with the municipal sludge, indicating that co-digestion had no adverse effects. Study results prove that high methane production is achievable with the addition of concentrated external organic wastes to municipal digesters, at acceptable higher digester organic loadings and lower retention times, allowing the effective implementation of CHP programs at municipal wastewater treatment plants, with significant cost savings.
在美国佐治亚州格温内特县 F. 韦恩·希尔水资源中心(FWHWRC)进行了一项中试规模的研究,以选择外部有机废物并确定混合比例,用于与城市污泥共消化,以支持热电联产(CHP)项目。选择外部废物并使用受到两个限制:a)消化器停留时间不低于 15 d;b)总沼气(甲烷)产量不超过根据空气许可对 CO2 排放的限制的特定目标水平。使用 FWHWRC 收集的初沉污泥(PS)、浓缩剩余活性污泥(TWAS)和消化污泥、从口香糖制造厂获得的工业液体废物(GW)和脱水脂肪油渣(FOG)。对所有污泥和废物样品进行了特性分析,并在 35°C 下评估了其最终消化率。PS、TWAS、城市污泥(PS+TWAS;以 TS 为基础的 40:60 w/w)、GW 和 FOG 的最终 COD 到甲烷的转化率分别为 49.2、35.2、40.3、72.7 和 81.1%。使用四个中试规模的中温(35°C)消化器评估了城市污泥与 GW、FOG 或两者的共消化。沼气产量显著增加,观察到城市污泥的额外降解为 1.1%至 30.7%。沼气和甲烷的产量非常接近 FWHWRC 弥补能源赤字所需的目标水平。共消化导致的出水质量与仅用城市污泥进料的对照消化器相似,表明共消化没有不利影响。研究结果证明,通过向城市消化器中添加浓缩的外部有机废物,可以实现高甲烷产量,同时接受更高的消化器有机负荷和更低的停留时间,从而可以在污水处理厂有效实施 CHP 计划,并节省大量成本。