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活性炭厌氧流化床反应器处理高浓度含酚废水 总被引:3,自引:0,他引:3
活性炭厌氧流化床反应器处理高浓度含酚废水连续试验的结果表明,本反应器能充分地发挥活性炭对酚的吸附性能和微生物对酚的降解能力,为生物厌氧发酵过程创造良好的基础和环境条件。在这两方面的综合作用下,先用活性炭把酚吸附,再经微生物作用转化为甲烷。甲烷的实际产率与理论产率基本一致,进出CODcr物料达到平衡,有机基质得到较好的降解,去除率高达94%以上,发酵效率相当高。含酚量从952毫克/升降到0.5毫克/升以下。连续运行384天,无需排泥,活性炭保持较强活性。回收的甲烷气有一定经济价值。 相似文献
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以海藻酸钠为固定化载体材料,以氯化钙作为交联剂,将高效降解油脂菌--解脂耶氏酵母(Yarrowia tipolyt-ica)包埋制备成固定化微生物小球,用以处理油脂废水,考察了最佳处理条件.结果表明,解脂耶氏酵母经固定化包埋后处理色拉油废水的最适条件为:温度25~35℃、pH 4~8、摇床转速100~200 r/min,处理初始油浓度在2 000 mg/L,包埋菌浓度6.65×106个/mL,包埋量为4 mL/150 L.与悬浮状态相比,固定化微生物温度适应范围增大、热适应性增强、pH值往酸性方向偏移.将固定化解脂耶氏酵母投入YPD液体培养基内驯化30 h再处理色拉油废水,结果显示:驯化后的固定化微生物在同样条件下对色拉油的降解率达到82%,比未驯化状态高20%,且驯化后的机械强度、稳定性和重复使用性都有明显改善. 相似文献
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降酚菌株的固定化细胞处理含酚废水的性能研究 总被引:2,自引:0,他引:2
用海藻酸钠作为载体将一株降酚菌株进行固定化包埋。利用正交实验确定了该菌株固定化细胞制备的最优条件。研究表明,该降酚菌株的固定化细胞对苯酚的降解能力和耐受能力均大于游离细胞。降酚菌株固定化细胞降解苯酚的最适温度范围是30~35℃,最适pH值范围为6~8。该菌株的固定化细胞对废水中的COD也具有良好的降解效果。 相似文献
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降酚菌株的固定化细胞处理含酚废水的性能研究 总被引:1,自引:0,他引:1
用海藻酸钠作为载体将一株降酚菌株进行固定化包埋.利用正交实验确定了该菌株固定化细胞制备的最优条件.研究表明,该降酚菌株的固定化细胞对苯酚的降解能力和耐受能力均大于游离细胞.降酚菌株固定化细胞降解苯酚的最适温度范围是30~35℃,最适pH值范围为6~8.该菌株的固定化细胞对废水中的COD也具有良好的降解效果. 相似文献
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蒽的高效降解菌的固定化小球的制备及其降解特性 总被引:1,自引:0,他引:1
旨在利用固定化高效降解菌小球去除水中蒽,充分发挥累托石的吸附和生物降解的协同作用,以累托石、聚乙烯醇(PVA)、海藻酸钠(SA)作为固定化载体材料,硼酸和氯化钙作为交联剂,将蒽的高效降解菌包埋制备固定化微生物小球.考察了累托石用量、PVA投加量、海藻酸钠用量、氯化钙用量、微生物包埋量和交联时间等因素对微生物小球活性的影响,通过正交实验确定了微生物小球的最佳制备条件.结果表明,制备固定化微生物小球的最佳条件为:累托石2.5%,PVA 12%,SA 0.3%,CaCl24%,交联时间28 h,微生物包埋量10%.对40 mgJ/L的蒽溶液,游离微生物在50 h后开始发挥明显的降解作用,经过68 h蒽的去除率达到35.65%;而固定化微生物小球经过9 h即可使蒽的去除率达到81.8%,23 h后葸的去除率可达100%.固定化微生物小球对水中蒽的去除机理与吸附-降解工艺的机理类似,即固定化微生物小球类似于一个一体化的微型反应器,经过迟滞期后,在该反应器内同时发生吸附和降解作用. 相似文献
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真菌在含酚废水处理中的应用 总被引:3,自引:0,他引:3
含酚废水是一种典型的难降解有机废水,成分复杂,毒性较强,对环境污染严重.利用真菌处理含酚废水是一种新兴环境生物技术,逐渐成为了国内外环境工作者关注的焦点.概述了真菌降解酚类物质的研究现状和降解的主要机理及途径,介绍了真菌固定化技术在酚类废水治理的进展,并提出了真菌技术治理含酚废水的研究发展方向. 相似文献
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对四级三相式生物流化床分段进水工艺脱氮效能进行了研究。通过改变进水C/N比、水力停留时间(HRT)和污泥回流比,考察了系统的脱氮效能,并与流化床A/O工艺脱氮效能进行对比。出水氨氮均小于1 mg/L,去除率保持在97%以上,TN去除率最高可达90%,出水水质均能够保证达标。在相同水质和运行条件下,将四级三相式生物流化床分段进水工艺与流化床A/O工艺进行对比,前者从脱氮效能和节约能源方面均表现出较强的优势。四级三相式生物流化床分段进水工艺无需外加碳源和内回流系统,是一种低碳节能的污水脱氮新工艺。 相似文献
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Performance of three-phase three-dimensional electrode reactor for the reduction of COD in simulated wastewater-containing phenol 总被引:18,自引:0,他引:18
The removal of chemical oxygen demand (COD) from wastewater-containing phenol was investigated using three-phase three-dimensional electrode reactor. Special attention was paid to experimentally probe the performance of the reactor in COD removal in the process of repeated batch runs. The experimental results showed that the reactor could remove COD from phenol-containing wastewater much more efficiently than both granulated activated carbon (GAC) adsorption bed and conventional three-dimensional electrode. For 200th batch run, the three-phase three-dimensional electrode reactor with an airflow of 5 l min(-1) and a cell voltage of 30 V could remove 1350 ppm COD from the wastewater in 30 min while conventional three-dimensional electrode reactor with a same cell voltage and GAC adsorption bed with a same airflow only could remove 610 and 1000 ppm, respectively, at the same reaction duration. Although it was found that COD removal decreased with increasing repeated batch runs in our experimental range, due to adsorption saturation of GAC and electrode passivation, the extent of decrease for the three-phase three-dimensional electrode is much less than those for conventional three-dimensional electrodes and GAC adsorption beds. The passivated reactor could be partly re-activated by electrolysis in the presence of MnO2. 相似文献
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针对焦化废水中的有毒污染物会对敏感易受干扰的硝化细菌产生不利影响从而破坏硝化过程稳定性的现象,采用A/O1/H/O2工艺处理焦化废水的实际工程为研究对象,根据工程运行的水质监测数据分析,发现几种主要污染物的浓度变化会对二级好氧段的硝化过程产生抑制影响。序批式毒性抑制实验结果表明,苯酚、硫氰化物和喹啉对硝化过程具有毒性抑制作用,半抑制浓度EC50分别为34.26、278.5和73.24 mg/L。当二级好氧工艺段运行正常时(C/N约4.3/1,pH8~8.5,DO 4~4.5 mg/L),出水氨氮浓度可低于5 mg/L,是由于焦化废水经厌氧/好氧/水解工艺后毒物浓度大幅下降,毒性得到削减,表明焦化废水生物处理A/O1/H/O2组合流化床工艺具有较强抵抗毒物抑制并实现高效的硝化作用。 相似文献
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Amruta Shet Vidya Shetty K 《Environmental science and pollution research international》2016,23(20):20055-20064
Ag@TiO2 nanoparticles were synthesized by one pot synthesis method with postcalcination. These nanoparticles were tested for their photocatalytic efficacies in degradation of phenol both in free and immobilized forms under UV light irradiation through batch experiments. Ag@TiO2 nanoparticles were found to be the effective photocatalysts for degradation of phenol. The effects of factors such as pH, initial phenol concentration, and catalyst loading on phenol degradation were evaluated, and these factors were found to influence the process efficiency. The optimum values of these factors were determined to maximize the phenol degradation. The efficacy of the nanoparticles immobilized on cellulose acetate film was inferior to that of free nanoparticles in UV photocatalysis due to light penetration problem and diffusional limitations. The performance of fluidized bed photocatalytic reactor operated under batch with recycle mode was evaluated for UV photocatalysis with immobilized Ag@TiO2 nanoparticles. In the fluidized bed reactor, the percentage degradation of phenol was found to increase with the increase in catalyst loading. 相似文献
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S. Karthikeyan G. Sekaran V. K. Gupta 《Environmental science and pollution research international》2013,20(7):4790-4806
Nanoporous activated carbon prepared from rice husk through precarbonisation at 400 °C and phosphoric acid activation at 800 °C was used as fluidized bed in Fenton oxidation of the o, p and m-cresols in aqueous solution. The efficiencies of homogeneous Fenton oxidation, fluidized Fenton oxidation and aerobic biological oxidation systems for the removal of o, p and m-cresols in aqueous solution have been compared. The kinetic constants and the thermodynamic parameters for the homogeneous Fenton, heterogeneous Fenton and aerobic biological oxidations of o, p and m-cresols in synthetic wastewater were determined. The degradation of cresols in synthetic wastewater was confirmed using FT-IR, 1H-NMR and UV–visible spectroscopy. 相似文献