工业水处理
工業水處理
공업수처리
INDUSTRIAL WATER TREATMENT
2015年
5期
23-26
,共4页
李桂淑%李广%李晶%韩相奎
李桂淑%李廣%李晶%韓相奎
리계숙%리엄%리정%한상규
上清液%碳源%反硝化速率
上清液%碳源%反硝化速率
상청액%탄원%반초화속솔
supernatant%carbon source%denitrification rate
研究了将经乙醇型发酵后剩余污泥上清液作为反硝化外加碳源的可行性,并进行了上清液、甲醇和生活污水作为外加碳源的对比试验。结果表明,在相同的试验条件下,采用上清液和生活污水作为反硝化碳源时,系统反硝化过程中NO3--N的降解过程分为三个阶段,而以甲醇作为碳源时,NO3--N的降解过程为两个阶段;对比试验还发现,采用上清液代替甲醇作为反硝化系统的外加碳源,可在保持高反硝化速率的同时降低运行成本。
研究瞭將經乙醇型髮酵後剩餘汙泥上清液作為反硝化外加碳源的可行性,併進行瞭上清液、甲醇和生活汙水作為外加碳源的對比試驗。結果錶明,在相同的試驗條件下,採用上清液和生活汙水作為反硝化碳源時,繫統反硝化過程中NO3--N的降解過程分為三箇階段,而以甲醇作為碳源時,NO3--N的降解過程為兩箇階段;對比試驗還髮現,採用上清液代替甲醇作為反硝化繫統的外加碳源,可在保持高反硝化速率的同時降低運行成本。
연구료장경을순형발효후잉여오니상청액작위반초화외가탄원적가행성,병진행료상청액、갑순화생활오수작위외가탄원적대비시험。결과표명,재상동적시험조건하,채용상청액화생활오수작위반초화탄원시,계통반초화과정중NO3--N적강해과정분위삼개계단,이이갑순작위탄원시,NO3--N적강해과정위량개계단;대비시험환발현,채용상청액대체갑순작위반초화계통적외가탄원,가재보지고반초화속솔적동시강저운행성본。
Research on the feasibility of using residual sludge supernatant fluid after ethanol type fermentation as an additive carbon source for denitrification has been studied. In addition ,contrast tests on the denitrifying characteris-tics of supernatant,methanol and domestic sewage as additive carbon sources has been accomplished.. The results show that under the same experimental conditions ,when supernatant and domestic sewage are used as denitrification carbon sources,the degradation process of NO3--N in the process of system denitrification is divided into three stages,while methanol is used as the carbon source,the degradation process of NO3--N is divided into two stages. It is also found in the contrast tests that using supernatant fluid,instead of methanol, as the additive carbon source in the process of system denitrification ,high denitrification rate can be maintained ,while low operation cost reduced.