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1.
以北京市阿苏卫垃圾填埋场中晚期渗滤液为研究对象,通过正交实验的方法分析了改性土、原土、明矾、改性土加明矾等的用量及搅拌速度、搅拌时间、静置时间等因素对垃圾渗滤液CODcr去除率的影响。通过对改性土、原土、明矾处理垃圾渗滤液的机理进行分析后,将改性土、原土分别用来处理垃圾渗滤液中可溶性物质中的疏水性物质和亲水性物质,并结合明矾的絮凝作用组合处理垃圾渗滤液。处理后垃圾渗滤液CODcr值从4700mg/L明显下降到839mg/L,CODcr去除率为82.15%,BOD5从700mg/L下降到263mg/L,BOD5去除率为62.43%。有机改性膨润土、明矾、原土组合处理是一种有效的处理垃圾渗滤液方法。  相似文献   

2.
通过3个对比反应柱研究了厌氧渗滤液循环中垃圾的破碎和压实对垃圾降解的影响。实验结果显示：在填埋垃圾量和渗滤液循环量相同的条件下，经过60d的厌氧渗滤液循环，对比垃圾柱的出水CODcr浓度为1333．2mg／L，而破碎垃圾柱和压实垃圾柱出水的CODcr浓度分别为582．4mg／L和2112．4mg／L。在厌氧渗滤液循环中，对垃圾进行破碎处理能够加速垃圾的降解，降低垃圾填埋场对地下水的危害；而对垃圾填埋体的压实不利于垃圾的降解，从而增加了垃圾填埋场污染地下水的风险。  相似文献   

3.
垃圾渗滤液治理一直是城市生活垃圾卫生填埋场的难题。能否利用矿物-微生物交互作用提高垃圾渗滤液有机污染物厌氧转化的效率是值得研究的问题。本文设置4组厌氧生物反应器(分别为只添加褐铁矿或者白云石、同时添加褐铁矿和白云石以及不添加矿物的空白组),考察添加褐铁矿、白云石对垃圾渗滤液厌氧消化的影响。实验结果表明,厌氧生化反应12 d时,添加了褐铁矿和白云石的反应器中COD去除率均达到80%以上,而空白对照组COD去除率仅为50%;4组反应器中溶液pH值变化表明,矿物的存在提高了溶液的pH值0.5左右;4组反应器中氨氮含量变化不大,也没有表现出明显差异。研究认为褐铁矿或白云石矿物在垃圾渗滤液中有机物的厌氧消化过程中起到了重要促进作用。研究结果为提高垃圾渗滤液厌氧处理效率提供了一个可供参考的方法。  相似文献   

4.
采用多阶段水解 -好氧串联工艺处理高浓度玉米淀粉废水。试验结果表明 :①废水经多阶段水解 -好氧工艺的水解段H1后 ,废水的 ρ(BOD5) /ρ(CODCr)从 0 .90提高到 0 .95 ;废水经水解段H2 后 ,废水的 ρ(BOD5) /ρ(CODCr)从 0 .81提高到 0 .97,说明水解段具有提高废水可生化性的功能。②在总水力停留时间 (HRT)为 6 0h、进水pH为 5 .9～ 6 .0 8和进水 ρ(CODCr)、ρ(BOD5)、ρ(NH+ 4)平均分别为 82 0 5mg/L、7395mg/L、16 0 .0mg/L的情况下 ,CODCr、BOD5和NH+ 4去除率分别达97.7%、99.1%和 88.1% ,出水水质达到或接近国家污水排放二级标准 (GB8978- 96 )。③各处理单元对CODCr、NH+ 4去除效果各不相同。  相似文献   

5.
针对传统水解酸化和好氧氧化处理工艺存在的问题,对水解酸化工艺及好氧氧化处理工艺进行了改进;并针对东北制药集团制药废水水质特征,设计开发了预处理 复合水解酸化 复合好氧氧化的生物处理技术。工程设计规模为30000 m3/d,两年的运行结果表明,此工艺运行稳定,耐冲击负荷能力强。当平均进水浓度COD为3600 mg/L、BOD5为1000 mg/L、SS为450 mg/L时,平均出水浓度COD≤300mg/L、BOD5≤100 mg/L、SS≤50 mg/L,达到了国家城市排水三级标准医药企业污水排放标准(COD300mg/L)。  相似文献   

6.
厌氧折流板反应器中酸化菌活性研究   总被引：5，自引：0，他引：5  
本实验将厌氧折流板反应器控制在水解酸化阶段,以比INT脱氢酶活性来表征反应器中各室内的酸化菌活性。探讨了各格室酸化菌活性的变化规律,并对影响各室酸化菌活性的影响因素进行了分析。结果表明,在有机负荷2.4 kgCOD/（m3·d） 条件下,反应器中各室酸化率与酸化菌比INT脱氢酶活性成相关性,一室、二室的酸化率占总酸化率的73%;同一格室内比INT脱氢酶活性中部高于底部。  相似文献   

7.
以位于北京昌平小汤山的阿苏卫垃圾卫生填埋场渗滤液为研究对象,在不同的环境条件下:酸度(pH=5~9),温度(4℃~30℃),利用片沸石、钙基膨润土去除垃圾渗滤液中有害物质的实验,以化学耗氧量(COD)、氨氮为评价指标,分别探讨片沸石、钙基膨润土的COD、氨氮去除效果与其用量、渗滤液pH、温度、振荡时间的关系。研究表明,在实验条件下,片沸石对COD的最大去除量约为31×10-3,对氨氮的最大去除量约为27×10-3;去除COD、氨氮的最佳条件分别为:片沸石用量20 g/L、pH为5、温度4℃、振荡时间100 min。在实验条件下,钙基膨润土对COD的最大去除量约为63×10-3,对氨氮的最大去除量约为14×10-3;去除COD、氨氮的最佳条件分别为:钙基膨润土用量30 g/L、pH为5、温度4℃、振荡时间100 min。根据实验结果,对片沸石、钙基膨润土去除COD、氨氮的机理主要是氢键、静电作用及离子交换作用。  相似文献   

8.
垃圾填埋场渗滤液水质复杂,危害性大,对其无害化处理尚未得到很好解决。研究发现,垃圾渗滤液中有机污染物可标识划分为亲水性和疏水性两大类物质。实验针对性采用亲水的天然膨润土处理亲水性有机物,疏水的有机膨润土处理疏水性有机物,再结合鸟粪石结晶法去除氨氮,从而获得一套处理中晚期垃圾渗滤液的经济高效的矿物法组合处理技术。采用GC-MS技术鉴定经矿物法处理后的垃圾渗滤液,亲水性和疏水性有机污染物的种类和含量都明显降低。检测进水与出水的COD、氨氮及重金属浓度这三项关键指标,垃圾渗滤液原液COD为2566 mg/L,氨氮3859 mg/L,重金属Hg为0.305 mg/L。矿物法组合处理后出水的COD为245mg/L,氨氮48 mg/L,重金属Hg未检出。矿物组合法为垃圾渗滤液的无害化处理提供了一条新的思路。  相似文献   

9.
刘静静  曾南石  徐文炘 《矿产与地质》2012,26(2):165-167,176
文章以垃圾渗滤液为研究对象,分别用铁粉、改性膨润土、活性炭及其混合物为反应介质,设计4种不同介质配比的PRB反应器进行实验研究。结果表明,PRB对垃圾渗滤液有较好的处理效果,其中,以还原铁粉、改性膨润土为介质的反应器,对氨氮的去除效率最大为97.58%,以还原铁粉、活性炭为介质的反应器对COD的去除效率为84.87%,对总磷的去除效率最大为80%。  相似文献   

10.
贝壳填料酸化反应器预处理生活污水试验   总被引：1，自引：0，他引：1  
在中国沿海一带,海产品废弃物贝壳多数进行废弃处理,成为潜在的环境隐患,对其进行废物资源化利用将是很好的选择.利用贝壳做填料,通过98 d的小试研究,考察了厌氧固定膜反应器在18～25 ℃条件下的运行效果.在水力停留时间分别为4 h、8 h和12 h的条件下,考察了反应器处于酸化段对污染物的处理效能.运行期间获得了较高的TP去除率,水力停留时间4 h、8 h和12 h对应的平均COD去除率分别为55.0%,58.0%和58.9%,平均TP去除率分别为16.90%,25.95%和27.43%.在试验条件下,贝壳释放的碱度足以调节系统的pH值,水力停留时间8 h和12 h对应的出水pH值较进水增加11.6%和16.5%.试验结果表明,贝壳是一种理想的酸化反应器微生物附着和生长载体,从技术和经济角度,水力停留时间设定为8 h较佳.  相似文献   

11.
Continuous upflow anaerobic sludge blanket reactor performs more favorably at the higher organic loading rate than other anaerobic treatment. The treatment of municipal landfill leachate of Shiraz??s city investigated using continuous flow anaerobic reactor and subsequently aerated lagoon. Landfill leachate has chemical oxygen demand of 45,000?C90,000?mg/L and ammonia nitrogen at 1,000?C2,500 and heavy metals that can impact biological treatments. Capacity of anaerobic and aerobic reactors is 10 and 20?L that operated at detention time of 2 and 4?days, respectively. Organic loading rate of upflow anaerobic sludge blanket is between 0.5?C20?g chemical oxygen demand/L/day. Chemical oxygen demand removal efficiencies are between 57?C87, 35?C70 and 66?C94% in the anaerobic, aerobic and whole system, respectively. As the entry, leachate organic loading rate increased from 1 to 20?g/L/day, the chemical oxygen demand removal efficiency reached a maximum of 71% and 84% in the anaerobic reactor and whole system, respectively, at high organic loading rate. Ammonium removal efficiency was about 54% after the aerobic stage.  相似文献   

12.
In this research, physical, chemical and biological treatability of Tehran solid waste leachate was studied. Results indicate that the amount of COD for the fresh raw leachate of Tehran is equal to 66,608 mg/l. The leachate is transferred to an equalization tank for storage and pH control process. After neutralization, leachate is introduced to an up flow and down flow anaerobic reactor. The effluent of anaerobic reactor is conducted to a sequencing batch reactor. Sequence batch reactor (SBR) effluent was pumped in to sand and activated carbon filters, after chemical coagulation and clarification. Results showed that anaerobic reactor with detention time of 3 days had a 35% COD removal and increasing the detention time to 4.5 days would improve the COD removal to 45%. Nutrient adjustment with phosphorus and nitrogen increased the initial 23% efficiency of sequence batch reactor to 44%. The effluent COD of SBR reactor was 21,309 mg/l. Recycling of aerobic reactor effluent with incoming feed to anaerobic reactor reduced the anaerobic reactor influent COD to 20,000 mg/l and this caused 53% and 57% COD removal in the anaerobic and aerobic effluent, respectively. The total systems COD performance increased to 80% and SBR effluent COD eventually reduced to 4,000 mg/l. Coagulation, flocculation and sedimentation processes were practiced to make the 4,000 mg/l effluent COD comply with environmental standards of Iran. The optimum coagulant found to be ferric chloride with the dosage of 50 mg/l at pH of 12, which reduced 10% of COD to an amount of 3,676 mg/l. The effluent was stored in a tank and then pumped in to pressure sand filter and afterwards to activated carbon filter. The COD removal was three and 90% for sand and activated carbon filters, respectively. The total process reduced the remaining COD to 36 mg/l, which is in compliance with environmental standards of Iran.  相似文献   

13.
Performance of moving bed biofilm reactor system for a real hospital wastewater (HW) was experimented, modelled, and optimized using response surface methodology. Prior to conducting laboratory tests, design of the experiments was evaluated to minimize any prediction error. Statistical analyses demonstrated the models’ validity and adequacy for anticipation of the removal of BOD and COD by the process. The models predictions (with desirability of 0.98) were found to be in very good agreement with confirmative experiments results. The results indicated that under convenient operating conditions of the studied variables (packing rate 70%, HRT 24 h, and MLSS 3000 mg/L), the removal efficiencies for BOD and COD were 97.8 and 95.6%, respectively. Moreover, kinetics of the biological process showed that removal of organic matters for the tested wastewater adheres to modified Stover–Kincannon model with a correlation coefficient of 0.998. Ratio of BOD to COD of 0.6 (optimal range for biological treatment normally is >0.5) suggests acceptable efficiency of the reactor for decomposing organic load. A high overall efficiency of the process and fulfilling the related standards make this system an appropriate option for treating HDW.  相似文献   

14.
A pilot scale study was set up to investigate the principle design parameters of up flow anaerobic sludge blanket (UASB) reactors for treating wastewater of small communities in the tropical regions of Iran. A steel pipe with a diameter of 600 mm and a height of 3.6 m was used as the reactor in which a digestion and a 3-phase separator element had a volume of 0.848 and 0.17 m3 respectively. During this study, which lasted for 203 days, two distinct phases were carried out according to the ambient temperature. The temperature of the wastewater entering the reactor was naturally ranged from 22 to 26 °C and no heat exchanger was used. The hydraulic retention times including 2, 4, 6, 8, and 10 hours with various loading rates of 0.95 to 5.70 kg COD/m3/day for colder period and from 1.35 to 6.40 kg COD/m3/day for warmer period were examined. On the basis of the results the optimal hydraulic retention time for warmer period with a 2.20 kg COD/m3/day organic loading rate was 6 hours which BOD5, COD and TSS removal efficiency were 71, 63 and 65 percent respectively. During the colder period the removal ratio of BOD5, COD and TSS with an optimal hydraulic retention time of 8 hours and organic loading rate of 1.22 kg COD/m3/day were 54, 46 and 53 percent respectively.  相似文献   

15.
This study focuses on treatment of landfill leachate in column experiments by immobilized Trametes versicolor on polyurethane foam, collected from Nonthaburi landfill site, Thailand. In this study, glucose was used as a co-substrate. The effect of biomass growth on color removal was observed by immobilizing fungi on polyurethane foam. The same immobilized fungi were used for four cycles of 5 days each to find the reuse of fungi. Leachate was diluted to see the effect of organic loading on color removal. At optimum pH of 4 and in 20 days with 3 g/L of glucose, the fungi could decolorize 78 % and 63 % for 5-times dilution and concentrated leachate, respectively, using immobilized fungi after 4 days initial growth. Fungi could also reduce biological oxygen demand and chemical oxygen demand of 52 % and 42 % (with initial biological oxygen demand and chemical oxygen demand of 48,900 and 96,512 mg/L), respectively, with glucose 3 g/L in concentrate leachate and with 4 days initial immobilization of fungi on polyurethane foam. About 1–6% higher color removal was observed on day 20 with 15 days fungi immobilization initially as compared to 4 days immobilization. Higher removal efficiency was observed for the same leachate after dilution due to reduction in organic loading. Addition of co-substrate enhances significantly removal of color, biological oxygen demand and chemical oxygen demand. Chemical oxygen demand removal reached to 0.6 mg/mg of biomass with the co-substrate. Therefore, white rot fungi can be considered as potentially useful microorganisms in landfill leachate treatment.  相似文献   

16.
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17.
There is an urgent need for characterization of leachate arising from waste disposal to ensure a corresponding effective leachate management policy. Field and laboratory studies have been carried out to investigate the impact of municipal landfill leachate on the underlying groundwater at a site in West Malaysia. The solid waste was disposed of directly onto an unprotected natural soil formation. This situation was made worse by the shallow water table. The hydrochemical composition of groundwater in the vicinity of the site (background) is a dilute mixed cation, bicarbonate water. The high ionic balance error of ~13.5% reveals that the groundwater body underneath the site was a highly contaminated leachate rather than contaminated groundwater. Elevated concentration of chloride (355.48 mg/L), nitrate (10.40 mg/L as NO3), nitrite (14.59 mg/L), ammoniacal-N (11.61 mg/L), sodium (227.56 mg/L), iron (0.97 mg/L), and lead (0.32 mg/L) measured downgradient indicate that the contamination plume has migrated further away from the site. In most cases, the concentration of these contamination indicators, together with the ranges of sodium percentage (66.3–89.9%) and sodium adsorption ratio (10.1–19.7%), were found to be considerably higher than the limit values of safe water for both domestic and irrigation purposes, respectively.  相似文献   

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