厌氧消化
废物管理
环境科学
制浆造纸工业
废水
流出物
污水处理
无氧运动
热水解
化学
污水污泥处理
毯子
活性污泥
过程(计算)
分数(化学)
污泥膨胀
混合液悬浮物
环境工程
好氧消化
发电
发酵
无氧呼吸
沼气
废物处理
水解
生态足迹
碳足迹
火力发电站
作者
Xiao Xu,Thomas Dockhorn
标识
DOI:10.1016/j.biortech.2025.133564
摘要
• Thermal alkaline process as posttreatment is recommended rather than pretreatment. • Electricity balance can be improved by 344.7–472.3 kWh/t TS with DS posttreatment. • DS posttreatment can achieve a profit of 29.9–171.3 US$/t TS. • CO 2eq. emission can be further reduced by 149.8 ± 42 kg/t TS with DS posttreatment. • Results are transferable across the 5 WWTPs studied. To determine whether wastewater treatment plants (WWTPs) should use the thermal hydrolysis process (THP) or the thermal alkaline process (TAP) as sludge pretreatment or posttreatment methods, this study was conducted on five WWTPs implementing THP/TAP under seven different scenarios. The evaluation focused on impacts on energy, economic, and CO 2eq. balances compared to conventional anaerobic sludge digestion. In this study, THP/TAP as a posttreatment method yielded better results in energy, economic, and CO 2eq. balances than pretreatment. TAP of digested sludge (DS) at pH 9 achieved the highest net electricity generation of 344.7–472.3 kWh/t total solids (TS). An economic profit of 29.9–171-3 US$/tTS can be obtained from digesting the liquid fraction of THP-treated DS, and in this scenario, CO 2eq . emissions can be further reduced by 149.8 ± 42 kg/tTS. However, additional space is required for the construction of a digester or an upflow anaerobic sludge blanket in the DS posttreatment.
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