低碳源污水厂中ECOSUNIDE工艺的碳源利用分析  

Use of Carbon Source in ECOSUNIDE Process in Low-carbon Municipal Sewage Treatment Plant

作　　者：李若谷[1] 张雁秋[1] 孙艳[1] 丁毅[1] 

机构地区：[1]中国矿业大学环境与测绘学院,江苏徐州221008

出　　处：《中国给水排水》2013年第13期97-100,共4页China Water & Wastewater

基　　金：中国矿业大学科技基金资助项目(OP080268)

摘　　要：针对城市污水处理厂在低碳源条件下的实际运行情况,分析了ECOSUNIDE工艺中碳源的分布及利用情况,指出水中慢速降解有机物(X S)经好氧水解产生的易降解有机物(S S)是参与反硝化过程的主要碳源。根据简化的ASM1模型,对X S水解和异养菌衰减产生的S S进行了数值计算,在BOD5=80 mg/L、NH3-N=30 mg/L、TP=4 mg/L、X S=90 mg/L的进水条件下,异养菌衰减和50%进水中的X S好氧水解产生的S S用于反硝化即可基本满足脱氮除磷所需的碳源,而其中及时利用X S水解产生的S S是反硝化的关键。For the operation of low-carbon wastewater treatment plants, the distribution and use of carbon source in ECOSUNIDE process was analyzed. The main carbon source used in denitrification is the readily biodegradable substrate （Ss ） from the slowly biodegradable substrate （Xs） hydrolysis. Based on the ASM1 model, the amount of Ss from hydrolysis of Xs and heterotrophic bacteria decay was calculated. The results showed that if the Ss from hydrolysis of 50% Xs and heterotrophic bacteria decay could be used in denitrification under the conditions of 80 mg/L BODs, 30 mg/L NH3 - N, 4 mg/L TP and 90 mg/L Xs, the demand for carbon source required for nitrogen and phosphorus removal could be met. The Ss from hydrolysis of Xs was the key for denitrification.

关 键 词：ECOSUNIDE工艺 碳源 慢速降解有机物 易降解有机物 反硝化 

分 类 号：X703[环境科学与工程—环境工程]