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21.
中温(35±1)℃条件下,采用上流式厌氧污泥床(upflowanaerobicsludgebed,简称UASB)反应器处理了含蒽醌类-活性艳蓝(c.I.ReactiveBlue5,简称K—GR)或偶氮类-活性艳红(C.I.ReactiveRed20,简称KD-8B;C.I.ReactiveRed2,简称X-3B)模拟染料废水,重点研究了回流比对染料脱色率和COD去除率的影响,在最佳回流比的条件下,探讨HRT(hydraulicretentiontime)对脱色的影响和不同结构染料的脱色效果,并初步分析了脱色机理。结果表明,适宜的回流比有利于提高系统的脱色率;控制回流比和HRT分别为2和24h,当模拟废水中染料的浓度为100mg/L时,COD去除率和脱色率分别为90%~96%和85%~92%;蒽醌和偶氮类染料的脱色是通过偶氮键和葸醌共轭结构的断裂来实现的。 相似文献
22.
To gain more insight into the interactions between anaerobic bacteria and reactor performances (chemical oxygen demand-COD, 2,4 dichlorophenol-2,4 DCP removals, volatile fatty acid-VFA, and methane gas productions) and how they depended on operational conditions the microbial variations in the anaerobic granular sludge from an upflow anaerobic sludge blanket (UASB) reactor treating 2,4 DCP was studied. The study was composed of two parts. In the first part, the numbers of methanogens and acedogens in the anaerobic granular sludge were counted at different COD removal efficiencies. The relationships between the numbers of methanogens, the methane gas production and VFA production were investigated. The COD removal efficiencies increased to 74% from 30% while the number of total acedogens decreased to 10 from 30 cfu ml(-1). The number of total methanogens and acedogens varied between 11 x 10(3) and 10 x 10(9)MPN g(-1) and 10 and 30 cfu ml(-1) as the 2,4 DCP removal efficiencies were obtained between 60% and 99%, respectively. It was seen that, as the number of total acedogens decreased, the COD removal efficiencies increased. However, the number of total methanogens increased as the COD removal efficiencies increased. Correlations between the bacterial number and with the removal efficiencies obtained in different operational conditions were investigated. From the results presented in this paper a high correlation between the number of bacteria, COD removals, methane gas percentage, 2,4 DCP removals and VFA was observed. In the second part, methanogen bacteria in the anaerobic granular sludge were identified. Microbial observations and biochemical tests were applied to identify the anaerobic microorganisms from the anaerobic granular sludge. In the reactor treating 2,4 DCP, Methanobacterium bryantii, Methanobacterium formicicum, Methanobrevibacter smithii, Methanococcus voltae, Methanosarcina mazei, Methanosarcina acetivorans, Methanogenium bourgense and Methanospirillum hungatei were identified. 相似文献
23.
Biological sulfate removal from acrylic fiber manufacturing wastewater using a two-stage UASB reactor 总被引:2,自引:0,他引:2
A two-stage UASB reactor was employed to remove sulfate from acrylic fiber manufacturing wastewater. Mesophilic operation (35±0.5℃) was performed with hydraulic retention time (HRT) varied between 28 and 40 hr. Mixed liquor suspended solids (MLSS) in the reactor was maintained about 8000 mg/L. The results indicated that sulfate removal was enhanced with increasing the ratio of COD/SO42-. At low COD/SO42-, the growth of the sulfate-reducing bacteria (SRB) was carbon-limited. The optimal sulfate removal efficiencies were 75% when the HRT was no less than 38 hr. Sulfidogenesis mainly happened in the sulfate-reducing stage, while methanogenesis in the methane-producing stage. Microbes in sulfate-reducing stage performed granulation better than that in methane-producing stage. Higher extracellular polymeric substances (EPS) content in sulfate-reducing stage helped to adhere and connect the flocculent sludge particles together. SRB accounted for about 31% both in sulfate-reducing stage and methane-producing stage at COD/SO42- ratio of 0.5, while it dropped dramatically from 34% in sulfate-reducing stage to 10% in methane-producing stage corresponding to the COD/SO42- ratio of 4.7. SRB and MPA were predominant in sulfate-reducing stage and methane-producing stage respectively. 相似文献
24.
Nearly 91% of organic pollutants in Hong Kong leachate could be effectively removed by the UASB(upflow anaerobic sludge blanket)process followed by the fenton coagulation.The COD(chemical oxygen demand)of leachate was lowered from an average of 5620 mg/L to 1910 mg/L after the UASB treatment at 37℃,and was further lowered to 513 mg/L after fenton coagulation.The remaining refractory residues could be further removed by plotochemical oxidation with the addition of H2O2.The BOD/COD ratio was greatly increased from 0.062 to 0.142,indicating the biodegradability of organic residues was improved.The photochemical oxidation for the fenton-coagulation supernatant was most effective at pH3-4,with the addition of 800 mg/L of H2O2,and UV radiation time of 30 minutes.The final effluent contained only 148 mg/L of COD,21 mg/L of BOD(biochemical oxygen demand)and 56 mg/L of TOC (total organic carbon). 相似文献
25.
用二相UASB反应器处理碱法草浆黑液,酸化相为8.87L的普通升流式反应器,甲烷相为28.75L的UASB反应器,系统温度35±1℃。结果表明:当酸化相进水COD5513 ̄955mg/L,SO4^2-8370 ̄1041mg/L,pH值为5.5时,二相系统COD去除率为76.18%。 相似文献
26.
27.
因畜禽废水除了含有大量的有机物,还含有一定量的氨基酸,因此,研究利用UASB处理畜禽废水,在不同环境条件和工况条件下对氨化率的影响,结果表明:氨化菌适应的pH值范围较宽,在6.5—8.0范围均可以较好的生存,其中以7.0为最佳;温度与氨化率基本成正相关关系,从经济等多种角度考虑,中温阶段38%为最适宜;氨化率随进水浓度的增加而增加;进水有机负荷越大,氨化率越小。 相似文献
28.
29.
UASB反应器处理精制棉废水的试验研究 总被引:3,自引:1,他引:2
采用颗粒污泥接种UASB厌氧反应器处理精制棉生产废水,对其可生化性及能降解程度进行研究。通过近1个月的运行可知:在进水CODCr质量浓度为5000—6000mg/L,HRT为24h,容积负荷在4.5~6.2kg/(m3·d)的范围时,有机污染物的去除率稳定保持在70%~80%的范围内,并且运行稳定。 相似文献
30.