Kato K, Murotani N, Matsufuji H, Saitoh M, Tashiro Y
Research & Development Division, Sanki Engineering Co., Ltd., 1742-7, Shimotsuruma, Yamato-shi, Kanagawa, 242-0001, Japan.
Environ Technol. 2006 May;27(5):501-10. doi: 10.1080/09593332808618660.
We describe a process for the recovery of phosphorus from excess sludge in a sewage treatment plant that currently uses polyaluminium chloride for chemical phosphorus removal. Instead, we employed alkaline dissolution of excess sludge with calcium phosphate precipitation to recover phosphorus from sewage. The recovery ratio for phosphorus from sewage using the phosphorus recovery system is approximately 50%. In addition, the amount of excess sludge in the phosphorus recovery system is approximately half that of conventional chemical phosphorus removal. Alkaline dissolution of excess sludge resulted in dissolution of aluminium into the supernatant. Furthermore, since dissolved aluminium can be reused as a coagulant, the phosphorus recovery system could be used to economize coagulant consumption. Operation and maintenance costs of the phosphorus recovery system are 25.9 U.S. cents per 1 m3 of sewage compared to 32.0 U.S. cents per 1 m3 of sewage for conventional chemical phosphorus removal, representing a decrease of 20% in the operation and maintenance costs.
我们描述了一种从污水处理厂的剩余污泥中回收磷的工艺,该厂目前使用聚合氯化铝进行化学除磷。相反,我们采用了用磷酸钙沉淀对剩余污泥进行碱性溶解的方法,以从污水中回收磷。使用该磷回收系统从污水中回收磷的回收率约为50%。此外,磷回收系统中剩余污泥的量约为传统化学除磷的一半。对剩余污泥进行碱性溶解导致铝溶解到上清液中。此外,由于溶解的铝可以作为混凝剂重新使用,因此磷回收系统可用于节省混凝剂消耗。磷回收系统的运行和维护成本为每立方米污水25.9美分,而传统化学除磷为每立方米污水32.0美分,运行和维护成本降低了20%。