Solley D, Armstrong M
Brisbane Water, GPO Box 1434, Brisbane, Australia 4001.
Water Sci Technol. 2003;47(11):157-63.
A phased approach has been adopted for upgrading the Luggage Point WWTP for nitrogen removal. Luggage Point WWTP (900,000 EP) is the largest plant operated by Brisbane Water. Management actions recommended by the South East Queensland Wastewater Management Strategy require the effluent total nitrogen levels to be reduced to less than 5 mg/L (50th percentile) by 2005. Luggage Point WWTP originally featured primary settling and a completely nitrifying activated sludge process. Effluent total nitrogen levels from the plant averaged 27 mg/L. Characteristics of the wastewater are highly variable, with primary settled wastewater having a COD/BOD5 ratio averaging 2.5, a TKN/COD ratio averaging 0.12 and effluent non-ammonia TKN averaging 1.8 mg/L (but up to 5 mg/L). The upgrade presented a substantial challenge, due to the limited available substrate for denitrification, a significant level of unbiodegradeable nitrogen and the low existing bioreactor HRT. The phased upgrading strategy was adopted to overcome these challenges most effectively and at low cost. The first stage of the upgrade included modifications to the existing plant infrastructure, without constructing new tankage. The existing bioreactors have been retrofitted using a five stage Bardenpho nutrient removal process, incorporating significant flexibility. The first phase upgrade has been commissioned and preliminary results indicate that the effluent total nitrogen has been reduced below the required first phase target of 8 mg/L. This represents a reduction of 3 tonnes of nitrogen per day entering Moreton Bay. The process is also operating with good stability and with excellent sludge settleability. The first phase of the upgrade will be completed for 25M AUS dollars, which represents a low cost of 28 dollars per equivalent person. Further upgrade works are likely to include separate treatment of the digested sludge dewatering centrate and advanced control of the biological process. The upgrade of Luggage Pt WWTP has shown that low effluent nitrogen can be achieved at low cost, through optimum utilisation of existing assets and a phased approach to modifications.
已采用分阶段方法对拉格比角污水处理厂进行升级,以实现脱氮。拉格比角污水处理厂(服务人口90万)是布里斯班水务运营的最大工厂。昆士兰东南部废水管理战略建议的管理行动要求到2005年将出水总氮水平降至5毫克/升以下(第50百分位数)。拉格比角污水处理厂最初的特点是一级沉淀和完全硝化活性污泥工艺。该厂出水总氮水平平均为27毫克/升。废水特性变化很大,一级沉淀后的废水化学需氧量/五日生化需氧量(COD/BOD5)平均为2.5,总凯氏氮/化学需氧量(TKN/COD)平均为0.12,出水非氨总凯氏氮平均为1.8毫克/升(但最高可达5毫克/升)。由于反硝化可用底物有限、不可生物降解氮含量高以及现有生物反应器水力停留时间短,升级带来了巨大挑战。采用分阶段升级战略以最有效且低成本地克服这些挑战。升级的第一阶段包括对现有工厂基础设施进行改造,无需建造新的罐体。现有生物反应器已采用五阶段巴登甫脱氮工艺进行改造,具有很大的灵活性。第一阶段升级已投入使用,初步结果表明出水总氮已降至第一阶段要求的8毫克/升目标以下。这意味着每天进入莫顿湾的氮减少了3吨。该工艺运行稳定,污泥沉降性能良好。升级的第一阶段将耗资2500万澳元完成,相当于每人28澳元的低成本。进一步的升级工作可能包括对消化污泥脱水浓缩液进行单独处理以及对生物过程进行先进控制。拉格比角污水处理厂的升级表明,通过优化现有资产利用和分阶段改造方法,可以低成本实现低出水氮排放。