LIANJie,ZHUOYang,YANGPei-zhen,et al.Start-up of UASB for Treating Thermal Hydrolyzed Filtrate of Excess Sludge with High Solid Content[J].China Water & Wastewater,2023,39(5):114-120.
UASB处理高含固污泥热水解滤液启动特性
- Title:
- Start-up of UASB for Treating Thermal Hydrolyzed Filtrate of Excess Sludge with High Solid Content
- Keywords:
- UASB; exces sludge with high solid content; thermal hydrolyzed filtrate; organic loading rate
- 摘要:
- 针对高含固剩余污泥热水解滤液采用UASB处理的启动特性,开展连续运行试验(HRT为26~7.8 d)并分析启动过程中有机物去除率、甲烷产量的变化。结果表明,COD去除率及甲烷产率随着有机负荷的提升而增加,当HRT为7.8 d时COD去除率可达(65.92±2.44)%。相比于COD去除率,系统启动过程中更应关注甲烷产量的变化。当HRT为7.8 d时,出水氨氮浓度及pH分别为(2 532.37±129.93) mg/L、8.02±0.28。负荷提升过程中,应更注重氨抑制风险。由于沼气产量及进水量较低,系统启动初期可采用间歇进水并增设内回流的方式增加UASB内的上升流速。
- Abstract:
- To investigate the start-up characteristics of UASB for treating thermal hydrolyzed filtrate of excess sludge with high solid content, a continuous running test (HRT ranging from 26 days to 7.8 days) was carried out and the changes of organic matter removal rate and methane yield during the start-up process were analyzed. The COD removal rate and methane yield rate increased with the organic loading rate. When the HRT was 7.8 days, the COD removal rate reached (65.92±2.44)%. Compared with COD removal rate, more attention should be paid to the change of methane yield during system start-up. When the HRT was 7.8 days, the effluent ammonia nitrogen and pH were (2 532.37±129.93) mg/L and 8.02±0.28, respectively. In the process of load increase, more attention should be paid to the risk of ammonia inhibition. Due to the low biogas yield and influent volume, intermittent feeding and internal reflux can be adopted to increase the up-flow velocity in UASB at the initial start-up stage.
相似文献/References:
[1]王新,刘海玉,刘莉.微电解+Fenton+UASB+A/O+砂滤处理青霉素废水[J].中国给水排水,2018,34(20):92.
WANG Xin,LIU Hai yu,LIU Li.Treatment of Semi-synthetic Penicillin Wastewater by Microelectrolysis,Fenton, UASB, A/O and Sand Filtration Process[J].China Water & Wastewater,2018,34(5):92.
[2]涂保华,黄鑫,张晟,等.Fenton/生化组合工艺降解农药中间体废水苯系物[J].中国给水排水,2018,34(20):96.
TU Bao hua,HUANG Xin,ZHANG Sheng,et al.Degradation of Benzene Series in Pesticide Intermediates Wastewater by Fenton Oxidation/Biochemical Process[J].China Water & Wastewater,2018,34(5):96.
[3]邓觅,余郭龙,杨二奎,等.微电解+UASB+两级A/O+絮凝工艺处理医药废水[J].中国给水排水,2020,36(24):155.
DENG Mi,YU Guo-long,YANG Er-kui,et al.Pharmaceutical Production Wastewater Treatment by Micro-electrolysis, UASB, Two-stage A/O and Flocculation[J].China Water & Wastewater,2020,36(5):155.
[4]马晓伟,安浩东,朱乐辉,等.废塑料造粒洗气废水处理工程实例[J].中国给水排水,2021,37(2):90.
MA Xiao-wei,AN Hao-dong,ZHU Le-hui,et al.Project Case of Gas Washing Wastewater Treatment of Waste Plastic Granulation[J].China Water & Wastewater,2021,37(5):90.
[5]高波,张磊,郭修智.UASB+A/O+MBR+两级RO处理垃圾焚烧发电厂渗滤液[J].中国给水排水,2021,37(4):67.
GAO Bo,ZHANG Lei,GUO Xiu-zhi.Process of UASB+A/O+MBR+Two-stage RO for the Treatment of Leachate from Waste Incineration Power Plant[J].China Water & Wastewater,2021,37(5):67.
[6]张勇,胡群林,徐广松,等.蜂巢石对UASB反应器启动性能的影响[J].中国给水排水,2021,37(21):75.
ZHANG Yong,HU Qun-lin,XU Guang-song,et al.Effect of Pumice on Start-up of Upflow Anaerobic Sludge Blanket[J].China Water & Wastewater,2021,37(5):75.
[7]李长海,张雅潇,普建国,等.生物法+膜法工艺处理垃圾焚烧电厂渗滤液[J].中国给水排水,2022,38(2):104.
LI Chang?hai,ZHANG Ya?xiao,PU Jian?guo,et al.Treatment of Leachate from Waste Incineration Power Plant by Biological and Membrane Process[J].China Water & Wastewater,2022,38(5):104.