摘要
在悬浮污泥系统中,当PH、温度适宜,碳源无限制时,反硝化速率和耗碳速率动力学呈零级反应,当以挥以性脂肪酸(VFA)为碳源时,异化反硝化的耗碳量接近于1.07mgVFAC/mgNO^-3-N。用于同化作用的碳仅占投加碳的一小部分,随着进水C/N的提高,污泥产率(YN)增加,用于同化作用的碳耗亦增加,出水氧化态氮降低。在PH7.5,温度25℃,污泥产率0.72mgVSS/mgNO^-3-N时。
In the suspended sludge system, when pH, temperatuer were suitable and carbon source was not limited, the denitrification and C uptake rate followed a zero-order reaction. When VFA was used for carbon source, consumed carbon quantity for denitrfication was closed to 1.07mg VFA-C/mg NO3--N. The carbon quantity for assimilation occupied part of carbon source added. As rising of influent C/N, the sludge yield (YN) grow up, this part of carbon consumption increased and the effluent oxidized nitrogen decreased. Under pH 7.5, temperature 25℃, sludge yield 0.72 mgVSS/mg NO3--N, the influent VFA-C/NO3--N suitable value was 1.43 for complete denitrification.
出处
《华东师范大学学报(自然科学版)》
CAS
CSCD
1995年第2期70-76,共7页
Journal of East China Normal University(Natural Science)
关键词
生物反硝化
污泥
挥发性脂肪酸
碳氮比
biological denitrification
suspended sludge
volatile fatty acids (VFA) C/N ratio
nitrate