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1.
Multi-stage ponds-wetlands ecosystem for effective wastewater treatment   总被引:2,自引:0,他引:2  
INTRODUCTION Pond systems are commonly employed formunicipal sewage purification, especially in devel-oping countries, due to its cost-effectiveness andhigh potential of removing different pollutants. Un-fortunately, algae would bloom in the ponds andcause secondary pollution of the following stream.To tackle this problem, several methods combiningboth ponds and filtering system had been tried(Christian et al., 2003). Dongying multi-stageponds-wetlands ecosystem was designed embodyi…  相似文献   

2.
根据酱菜废水的水质特点,采用两级SBR处理酱菜废水,对其处理效能进行了研究。结果表明:室内温度维持在17~22℃,进水有机物浓度在3000mg/L,DO为4.2mg/L,反应器运行工况为进水0.5h—曝气8h—沉淀1h—滗水0.5h—待机2小时的条件下,二级SBB反应器对BOD、COD、TN、NH4+-N、TP的去除率分别达到98.3%、97.5%、88.7%、97.1%、52.4%。  相似文献   

3.
1 Introduction ? The biological aerated filter technique has developed rapidly since 1980s, and is widely used in municipal sewage treatment. It has been used in the primary and secondary treatment processes due to its desirable economical efficiency and …  相似文献   

4.
题目:改良型多介质土壤渗滤系统对甲鱼养殖废水的净化效果研究
  目的:通过向多介质土壤渗滤系统(MSL)的土壤层添加污泥,研究改进后的系统对工厂化甲鱼养殖废水的处理效果,分析系统内微生物群落的变化,以期部分揭示其可能的作用机理。
  创新点:工厂化甲鱼养殖废水排放量日益增大,且水体氨氮含量较高。目前市场上缺乏针对甲鱼养殖废水的处理技术,MSL系统对该废水的处理也未有报道。本文在 MSL 系统的基础上进行改良,并将其应用于甲鱼养殖废水处理上,提出一套有效的甲鱼养殖废水处理技术,并对 MSL 系统内微生物群落结构进行了分析。
  方法:向4套MSL小试装置中分别添加0%、5%、10%和20%污泥,研究其对工厂化甲鱼养殖废水的净化效果。试验中水质指标测定均按国家标准方法进行,系统内微生物群落结构采用聚合酶链反应-变性梯度凝胶电泳(PCR-DGGE)法测定。
  结论:MSL系统可有效地处理工厂化甲鱼养殖废水,向系统中添加20%污泥后处理效果更佳。添加20%污泥的系统内具有较高的硝化类细菌多样性和都较多的生物量。  相似文献   

5.
在处理制革废水中常用SBR工艺,试验探讨了不同HRT、进水pH、COD负荷、NH3-N浓度、活性污泥浓度的运行参数,研究SBR工艺处理制革废水的最优运行参数.结果表明:SBR反应器在进水COD为1500~2000mg/L、NH3-N为150~250mg/L、pH为7.5、运行污泥浓度在3.0g/L左右、曝气时间为18h时COD去除率能达到95%左右,NH3-N去除率达到97%左右,其出水能够达到一级出水标准.  相似文献   

6.
采用“加压气浮+水解酸化+SBR”工艺处理制药厂废水,处理量为3000m^3/d,CODcr、BOD5、SS去除率分别为97.2%、99.3%和98%。出水均达到国家污水综合排放一级标准。  相似文献   

7.
为探索EM菌在淡水水质净化处理中的作用,以不同的EM菌液浓度(VEM/V污水为0‰、0.1‰、0.5‰、1‰、5‰)在有氧通风、常温条件下处理天心湖水样,通过测定湖水样处理前后的pH、SS、色度、COD和氨氨水平变化,评价EM菌对淡水水质的处理效果,研究结果表明:浓度为0.1‰的EM菌液处理对天心湖水的COD去除效果最佳;浓度为1‰的EM菌液对天心湖水的氨氮去除效果最佳;浓度为5‰的EM菌液处理使湖水COD、氨氮水平升高,水质反而受到污染.通过选择EM浓度、处理时间、处理温度三个影响因素,按L9(34)正交表进行正交实验,结果表明EM处理天心湖水的最佳工艺条件是:处理时间7d、处理温度30℃、EM浓度0.2‰,对COD的去除率达到36.52%;按上述正交实验最佳工艺条件进行验证实验,结果表明,对天心湖水中COD的去除率可达到35.47%,对生活污水处理COD去除率可达41.18%.本实验可为进一步研究EM在水质处理上的应用提供参考.  相似文献   

8.
采用"内循环厌氧反应器-缺氧/好氧工艺"处理维生素生产废水.试验结果表明:系统处理效率高,维护管理方便,处理后的水水质稳定,COD=108 mg·L-1,BOD5=23 mg·L-1,ρ(SS)=42 mg·L-1,ρ(NH3-N)=12 mg·L-1,pH=7.1,达到《发酵类制药工业水污染物排放标准》(GB21903-2008)要求。  相似文献   

9.
通过对晋城市巴公污水处理厂工艺改进前后两年同期运行数据的对比发现:COD去除率比较稳定,但在问一水温奈件下,技改后的C01)去除率略高于技改前;技改后NH3-N去除率2009年前半年有一定提高,后半年效果不明显,但出水总氯浓度有所降低;污泥负荷不稳定,相同污泥负荷条件下,技改后的NH3-N去除率高于技改前基于对主要影响因子的分析,建议在厌氧段前增设缓冲池稳定进水水质,提高碳氛比,在曝气池前加加热池、用废弃蒸汽或电加热等手段增强保温等措施、  相似文献   

10.
本文在以复合式膜生物反应器系统为基础,以模拟城市污水为处理对象。通过运行条件优化研究,综合脱氮除磷效果及经济因素,将复合区水力停留时间控制在7h左右。此时系统总去除率为:CODcr≧96.28%、NH3-N≧97.54%、TN≧74.87%、TP≧74.34%,出水可以稳定保证在CODcr≦14.35mg/L、NH3-N≦0.74mg/L、TN≦9.02mg/L、TP≦1.05mg/L。效果较好。  相似文献   

11.
SBR法处理模拟印染废水的实验研究   总被引:1,自引:0,他引:1  
采用实验室规模的序批式活性污泥曝气反应器(SBR)工艺处理模拟的印染废水.通过实验分析了不同曝气时间、进水浓度、静沉时间与SBR处理效果之间的关系,确定了SBR法处理中低浓度的印染废水的最佳运行参数.实验结果表明,在SBR的曝气时间为8h,沉淀时间为1h的条件下,且废水进水pH值为7.5~8.6,COD—cr为8901080mg/L、氨氮为13~20mg/L、色度为350倍左右时,该工艺对CODcr、氨氮、色度等均有很好的去除效果,经处理的印染废水COD、氨氮、色度去除率分别为50%~70%、40%~67%、20%.该法具有投资少、运行费用低、操作简单的特点.  相似文献   

12.
以沙溪河县段主要污染无SS、DO、CPDma、BOD5、NH3-N、NO2-N、NO3-N、挥发C4H5-OH、总硬度为参评因子采用Daniel的趋势实验,分析沙溪河县段近7年各期水质的变化趋势、结果表明除总硬度外其它主要污染物均有不同趋势的下降.  相似文献   

13.
为了快速培养出能同时去除生活污水中化学需氧量(COD)和氮的微氧颗粒污泥,采用膨胀颗粒污泥床(EGSB)反应器接种污水处理厂剩余污泥,研究了微氧颗粒污泥的培养过程以及稳定运行条件下供氧量对处理效果和污泥性能的影响。结果表明,水力停留时间(HRT)为6h,微氧颗粒污泥的成功培养仅需1个月;供氧速率在2.83.2gO2/d,COD,NH3-N和总氮(TN)的去除率最高分别可达91%,85%和81%,脱氮速率达1.7gN/d,出水水质最佳;成熟的微氧颗粒污泥粒径集中在0.453.2gO2/d,COD,NH3-N和总氮(TN)的去除率最高分别可达91%,85%和81%,脱氮速率达1.7gN/d,出水水质最佳;成熟的微氧颗粒污泥粒径集中在0.452mm,当供氧速率低于2.3gO2/d时,颗粒污泥结构致密,供氧速率在2.32mm,当供氧速率低于2.3gO2/d时,颗粒污泥结构致密,供氧速率在2.33.2gO2/d时,污泥性能稳定,供氧速率增加到3.2gO2/d时,污泥沉降性能下降,并出现颗粒解体和丝状菌生长优势。  相似文献   

14.
The feasibility and performance of nitrogen removal from municipal sewage were investigated through the completely autotrophic nitrogen removal over nitrite (CANON) process in a continuous reactor. CANON process was successfully started up with the transformation of nitrogen into gas by mass-balance analysis. For the synthetic waste-water (up to 480 mg NH4+-N/(L·d)), removal rates of the ammonia nitrogen and total nitrogen (TN) were about 80% and 55%, respectively, at 1.25 h hydraulic retention time (HRT). For the secondary effluent of municipal sewage, the effluent concentrations of NH4+-N and TN were below 5 mg/L and 9 mg/L, respectively. It is in accordance with the water quality standard for scenic environment with the reuse of urban recycling water (GB/T 18921-2002).  相似文献   

15.
Culture of Arthrospira platensis (Spirulina platensis) in human urine was investigated to get valuable biomass. NO3-N was the proper N source, in comparison with other N source, including urea, NH4-N and NO2-N. As a result, aerobic nitrification of human urine was performed, with above 93.6% nitrification percentage finally achieved with total-N (TN) load of 46.52 mg/(L·d), in which Arthrospira platensis was successfully grown. The main compositions of the obtained biomass are close to those in Zarrouk medium. Thus, it is possible to culture Arthrospira platensis in nitrified human urine for food production within bioregenerative life support systems (BLSSs).  相似文献   

16.
以深圳市为例,采用单元分析与多元分析相结合的手段,探讨了一种基于城市水环境容量估算面源污染负荷削减率的方法在环境规划中的实际应用.计算结果表明:对于COD指标,67%~74%的面源污染负荷削减率即可满足深圳市规划后环境容量的限制;而对于NH4-N,TP和BOD5,仅依靠削减面源污染负荷则无法满足规划要求.因此,在城市水环境质量规划过程中,应针对不同流域及目标污染物种类,制定"量体裁衣"式的水环境控制策略,而非采用一成不变的措施.  相似文献   

17.
针对农村生活污水的水质特点,采用厌氧-复合人工湿地组合工艺处理农村生活污水,结果表明,厌氧池对SS的去除率为80.6%;复合人工湿地对COD、TN的去除率分别为61%和61.4%,对TP的去除率在57%~66%之间。  相似文献   

18.
This paper describes the NiiMi process designed to treat landscape water. The main aim of the research was to investigate the feasibility of NiiMi for removing organic and nutriment materials from landscape water. During the batch-scale NiiMi operation, the removal rates of color ranged from 66.7%o-80% , of turbidity from 31.7%-89.3%o, of chemical oxygen demand (COD) from 7%-36.5%, of total phosphor (TP) from 43%-84.2%, of soluble phosphate from 42.9%-100%, of total nitrogen (TN) from 4.2%-46.7%, and of NH4^+-N from 39.3%-100% at the hydraulic loading of 0.2 m^3/(m^2·d). Results showed that the removal efficiencies of COD, TP, soluble phosphate and TN decreased with the decline in the temperature. The NiiMi process had a strong shock loading ability for the removal of the organics, turbidity, TP, soluble phosphate, TN and NH4^+-N. Three sodium chloride tracer studies were conducted, labeled as TS 1, TS2, and TS3, respectively. The mean hydraulic retention times (mean HRTs) were 31 h and 28 h for TSI and TS2, respectively, indicating the occurrence of a dead zone volume of 12% and 20% for TS 1 and TS2, respectively. TS 1 and TS2 displayed the occurrence of short-circuiting in the NiiMi system. The comparison results between TS1 and TS2 were further confirmed in the values obtained for some indicators, such as volumetric efficiency (e), short-circuiting (S), hydraulic efficiency (2) and number of continuously stirred tank reactors (N).  相似文献   

19.
通过对吉水县污水处理厂的运行状况进行调研,结果表明:出水COD、NH4+-N和TN能达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级B标准.在分析氧化沟运行状况的基础上,提出了氧化沟工艺升级改造的对策.  相似文献   

20.
Evaluating the performance of a biotrickling filter for the treatment of wastewaters produced by a company manufacturing beer was the aim of this study. A pilot scale trickling filter filled with gravel was used as the experimental biofilter. Pilot scale plant experiments were made to evaluate the performance of the trickling filter aerobic and anaerobic biofilm systems for removal of chemical oxygen demand (COD) and nutrients from synthetic brewery wastewater. Performance evaluation data of the trickling filter were generated under different experimental conditions. The trickling filter had an average efficiency of (86.81±6.95)% as the hydraulic loading rate increased from 4.0 to 6.4 m3/(m2·d). Various COD concentrations were used to adjust organic loading rates from 1.5 to 4.5 kg COD/(m3·d). An average COD removal efficiency of (85.10±6.40)% was achieved in all wastewater concentrations at a hydraulic loading of 6.4 m3/(m2·d). The results lead to a design organic load of 1.5 kg COD/(m3·d) to reach an effluent COD in the range of 50–120 mg/L. As can be concluded from the results of this study, organic substances in brewery wastewater can be handled in a cost-effective and environmentally friendly manner using the gravel-filled trickling filter.  相似文献   

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