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BBFR-IVCW工艺对微污染水体的脱氮效果
引用本文:孔令为,贺 锋,徐 栋,张 义,吴振斌.BBFR-IVCW工艺对微污染水体的脱氮效果[J].环境科学研究,2014,27(7):711-718.
作者姓名:孔令为  贺 锋  徐 栋  张 义  吴振斌
作者单位:1.中国科学院水生生物研究所, 湖北 武汉 430072 ;浙江省环境保护科学设计研究院, 浙江 杭州 310007
基金项目:国家水体污染控制与治理科技重大专项(2012ZX07101-00705);国家自然科学基金项目(51178452);国家科技支撑计划项目(2012BAJ21B03-04)
摘    要:以BBFR(biomass bio-film reactor, 生物质生物膜反应器)和IVCW(integrated vertical-flow constructed wetland,复合垂直流人工湿地)构成小试系统,由改性水草塘、生态塘和IVCW构建中试系统,对高碳低氮水的脱氮效果及其影响因素进行了研究. 结果表明,小试系统中CW2(2#湿地)出水ρ(TN)低于CW1(1#湿地);中试系统对TN的去除率为52.49%,出水达到GB 3838—2002《地表水环境质量标准》Ⅳ级标准. C/N〔ρ(CODCr)/ρ(TN)〕对BBFR中TN去除率的影响较大,但对NO3--N去除率的影响并不明显. 从经济成本和反硝化效果来看,小试系统最优C/N为4.9,中试系统最优C/N为4.8. C/N为2.8时,CW1对NO3--N的去除率为71.88%±15.70%,与C/N>2.8时相比,差异显著(F3,6=21,P<0.05);C/N为4.1时,CW2对NO3--N的去除率为92.83%±11.26%,与其他C/N下NO3--N去除率的差异显著(F3,6=4.34,P<0.05). 小试系统中BBFR对CODCr的去除贡献率高于TN,但各单元作为一个有机整体优势互补,共同保证系统出水水质. 

关 键 词:生物质生物膜反应器(BBFR)    复合垂直流人工湿地(IVCW)    反硝化脱氮
收稿时间:2013/10/15 0:00:00
修稿时间:2014/3/12 0:00:00

Study of Nitrogen Removal from Lightly Polluted Water Treated with BBFR-IVCW Process
KONG Ling-wei,HE Feng,XU Dong,ZHANG Yi and WU Zhen-bin.Study of Nitrogen Removal from Lightly Polluted Water Treated with BBFR-IVCW Process[J].Research of Environmental Sciences,2014,27(7):711-718.
Authors:KONG Ling-wei  HE Feng  XU Dong  ZHANG Yi and WU Zhen-bin
Institution:1.Institute of Hydrobiology, Chinese Academy of Sciences, Wuhan 430072, China ;Environmental Research and Design Institute of Zhejiang Province, Hangzhou 310007, China2.Institute of Hydrobiology, Chinese Academy of Sciences, Wuhan 430072, China
Abstract:Following social and economic development and population growth, water pollution is getting more severe and becoming a worldwide problem. Currently, there are many techniques for the removal of nitrate pollution from water bodies; however, large-scale engineering applications are still at the preliminary stages. The biomass bio-film reactor (BBFR) and the integrated vertical-flow constructed wetland (IVCW) were combined in a small experiment to treat high nitrogen-low carbon lightly polluted surface water. A pilot system was proposed, and its performance was investigated. The results of the small experiment showed that the mean effluent TN concentration of CW2 (#2 wetland system), which met the Class Ⅳ surface water environmental quality standards, was lower than that of CW1. The average TN removal of the pilot experiment reached 52.49%. The ration of C/N greatly influenced the TN removal of the BBFR system, but did not obviously influence the removal of nitrate. Considering the economic cost of additional carbon and the system denitrification effect, the optimal C/N ratio in this experiment was 4.9, though the C/N of the pilot experiment was 4.8. The CW1 achieved its highest NO3--N removal rate (71.88%±15.70%) under the condition of C/N=2.8, which was significantly different from the removal rates when C/N>2.8 (F3,6=21, P<0.05). For C/N=4.1, the NO3--N removal rate of CW2 was 92.83%±11.26%, which was significantly different than results with other C/N ratios (F3,6=4.34, P<0.05). In the small experiment, BBFR had a higher contribution to the combined system in terms of removing CODCr as compared to TN. The removal of TN in the pilot experiment showed that each unit which had an integrated system had complementary advantages, maintaining the effluent quality. 
Keywords:BBFR  IVCW  denitrification
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