共查询到18条相似文献,搜索用时 109 毫秒
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研究了二段式接触氧化工艺处理城市生活垃圾填埋渗滤液的强化预处理单元溶解氧变化对单元运行效果的影响。监测了0.2mg/L,0.4mg/L,0.6mg/L,0.8mg/L,1.0mg/L五个DO水平下,COD、NH3-N在0~30h内降解状况,降解曲线在较低的DO条件下,高效段较短,而DO越高,高效段越长。同时,对不同DO水平下C/N随时间的变化也进行了检测,为达到不同的C/N水平提供了工况选择上的参考。分析了降解曲线的特征及其工程应用的价值,提出了常规条件下该单元较优的溶解氧工况水平。 相似文献
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微生物对石油烃类的降解机理 总被引:5,自引:1,他引:4
文章分析了生物降解需要的条件、环境因素对石油烃微生物降解的影响,石油烃类的有氧降解机理、有氧降解方式,石油烃类的厌氧降解机理、厌氧降解过程中某些无机含氧化合物作受氢体的递氢过程,石油烃类化合物微生物降解难易程度,提出了以后应进一步重视原油的生物降解应用于我国微生物采油的研究。 相似文献
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城市污水处理厂剩余污泥中温厌氧消化处理研究 总被引:4,自引:0,他引:4
应用污水处理厂剩余污泥开展污泥中温厌氧消化实验,对一系列影响污泥厌氧消化反应的因素进行了考察。实验结果表明:由于污泥C/N值较低,单独消化非常困难,有机物分解率比较低,分解速度慢,气体发生量少。在35℃时,污泥投配率为7.5%~10%,基质的去除率可达到35.54%。37.62%,去除单位基质的产甲烷量为O.265~O.274m^3/kgCOD。 相似文献
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石油污染生物修复技术研究 总被引:2,自引:0,他引:2
本文概述了影响石油污染物生物降解修复处理的多种因素,对石油污染生物处理技术的发展进行了展望。其中主要影响因素包括:菌种的影响,菌种在不同的环境中和对不同碳链长度的碳氢化合物表现出不同的降解效率;石油物质本身物理化学特性的影响,如石油物质在水体或土壤中的浓度以及石油的粘度、沸点、折射率等特性;生存环境条件的影响,在接种入高效率的降解菌或利用土著微生物进行降解时,降解率受到生存环境中各种条件的影响,如表面活性剂、光照条件、吸附剂的利用、营养盐、共代谢底物、氧气、温度、盐度等。 相似文献
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缺氧反应时间对反硝化除磷系统脱氮除磷效果的影响 总被引:4,自引:0,他引:4
反硝化除磷工艺具有节省碳源、曝气量以及污泥产量低等优点,因而在处理城市生活污水中具有显著优势。反硝化除磷效能主要在缺氧阶段完成。缺氧时间直接影响系统的脱氮除磷效率。本实验以SBR反应器在厌氧/缺氧/好氧条件下富含的反硝化聚磷菌(DPAOs)为研究对象,通过调节不同的缺氧反应时间(150 min,210 min和270 min),考察缺氧反应时间冲击对下一周期代谢的影响和长期对整个反硝化除磷系统的影响。冲击实验发现:缺氧时间的改变基本不影响下一周期挥发性脂肪酸(VFAs)的吸收以及硝氮去除。在长期缺氧反应时间不同的系统中,当缺氧时间分别为150 min、210 min和270 min时,除磷效率分别是-10.4%、62.5%、73.6%,脱氮率均达到100%。当缺氧反应时间从150 min延长到270 min时,微生物体内聚羟基脂肪酸酯(PHAs)水平和聚磷(poly-P)水平以及释磷量都升高。实验表明,缺氧时间的适当延长利于提高除磷效率。 相似文献
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田晶 《中国环境管理干部学院学报》2010,20(5):68-72
通过考察Cu2+、Cd2+对渤海海岸带沉积物中甲氰菊酯、氯氰菊酯和溴氰菊酯的缺氧生物降解的影响,发现:外加Cu2+和Cd2+均对渤海海岸带沉积物中甲氰菊酯、氯氰菊酯和溴氰菊酯的缺氧生物降解有抑制作用,且随着外加金属离子浓度的增大,抑制作用更为明显。与Cu2+相比较,Cd2+对渤海沉积物中拟除虫菊酯缺氧生物降解的抑制作用更大,这跟Cu、Cd在渤海海岸带沉积物中的存在形态和对生物的毒性不同有密切的关系。 相似文献
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A study was conducted to examine N and P removal by a laboratory-scale extended aeration treatment system employing oxidation-reduction potential (ORP) controlled aeration. The system was provided with a 90-L aeration tank. When ORP controlled aeration was applied, the aeration tank was divided into three zones, namely the ORP zone (45 L), the anaerobic zone (27 L) and the aerobic zone (18 L). An external anoxic selector of 3.8 L in volume was also added. An ORP set point of 70 mV was used for the ORP zone. The extended aeration treatment system operating without the ORP controlled aeration was used as the control.COD removal (97%) was not affected, but both N and P removal were enhanced significantly in the ORP reactor. Total N removal efficiency was increased from 49.1% (control) to 83.5%. Almost all P was captured (99%), leaving an average of 0.09 mg L−1 P in the effluent. The ORP reactor yielded a sludge P content of 3.1%, compared to only 1.8% for the control. This indicated luxury P uptake in ORP reactor. Very significant P release and denitrification were found in the anoxic selector. Fairly good simultaneous nitrification and denitrification had occurred in the ORP zone. However, P release was very limited in the anoxic zone. However, anoxic P uptake and nitrification were found in this zone.Low F/M bulking was observed in both the control and ORP operation before the installation of a selector. Bacterial Type 0041 was identified as the predominant bulking organism. For the Control, an aerobic selector cured the bulking problem in one sludge age while an anoxic selector fixed up the problem during the ORP operation. 相似文献
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Xinfeng Wang Chao He Gang Li Panpan Li Quanguo Zhang Baoming Li 《International Journal of Green Energy》2015,12(10):1018-1024
In order to obtain the characteristics of anaerobic fermentation with different parts of corn stalks at low concentrations, air-dried corn stalks stem bark (SB), stem pith (SP), leaves (L), and corn stalks (CS) were, respectively, mixed with cow dung to perform fermentation at the temperature of 35 oC and carbon-to-nitrogen ratio (C/N) of 25. Mixed with cow dung compost, the fermentation broths were adjusted to a neutral pH value. Along with the enhancing of the total solid (TS) content of SB, SP, L, and CS fermentation broths, both of the daily biogas yields and methane contents increased under the same fermentation condition, except for Sample TS 6% of L. The optimal TS content of SB, SP, L, and CS broth is 8%, 5%, 10%, and 8%, separately. In 35 days, the highest methane yield of SB, SP, L, and CS broth was 125.0 mL/(volatile solid) VS g, 115.3 mL/VS g, 109.7 mL/VS g, and 80.0 mL/VS g, respectively, and the potential of methane transformation production of broth ranks as: SB> L> SP> CS. Daily methane producing rate of SB, SP, and L broth are faster than that of CS. It is necessary to separate the corn stalks into different parts to ferment because the optimal fermentation concentrations for the different parts are different. Additionally, the Gompertz equation was also adopted to simulate the anaerobic digestion process of different materials. The Gompertz equation fitting parameters show that the biodegradation (from easy to difficult) was: L < SP < SB < CS. 相似文献
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Effect of sequentially combining methanol and acetic acid on the performance of biological nitrogen and phosphorus removal 总被引:1,自引:0,他引:1
A sequentially combined carbon (SCC) source using methanol and acetic acid was investigated for biological nitrogen and phosphorus removal in a wastewater treatment process consisting of an anoxic zone, an oxic zone and a final settling tank. The anoxic zone was divided into two separate anoxic zones to feed methanol in the first anoxic zone and acetic acid in the second anoxic zone. Methanol and acetic acid, each as the sole carbon source, were also tested for comparison. The use of SCC was superior in nitrogen removal with all combined COD ratios of methanol/acetic acid tested, yielding 95.8-97% efficiency (less than 1 mg N/l in the final effluent). The highest phosphorus removal of above 92% (final effluent concentration of 0.12 mg P/l) was achieved when only acetic acid was used at a quantity equivalent to 50 mg COD/l. However, when SCC was used, the acetic acid dosage of 50 mg COD/l could be reduced down to 20 mg COD/l when 30 mg COD/l was replaced by methanol; this resulted in a final effluent phosphorus concentration of 0.6 mg P/l. Additional benefits of SCC included the excellent sludge settling properties compared to the use of methanol or acetic acid alone. 相似文献
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Anaerobic ammonium oxidation by Nitrosomonas spp. and anammox bacteria in a sequencing batch reactor 总被引:2,自引:0,他引:2
Lek Noophan P Sripiboon S Damrongsri M Munakata-Marr J 《Journal of environmental management》2009,90(2):967-972
A sequencing batch reactor (SBR) was inoculated with mixed nitrifying bacteria from an anoxic tank at the conventional activated sludge wastewater treatment plant in Nongkhaem, Bangkok, Thailand. This enriched nitrifying culture was maintained under anaerobic conditions using ammonium (NH(4)(+)) as an electron donor and nitrite (NO(2)(-)) as an electron acceptor. Autotrophic ammonium oxidizing bacteria survived under these conditions. The enrichment period for anammox culture was over 100 days. Both ammonium and nitrite conversion rates were proportional to the biomass of ammonium oxidizing bacteria; rates were 0.08 g N/gV SS/d and 0.05 g N/g VSS/d for ammonium and nitrite, respectively, in a culture maintained for 3 months at 42 mg N/L ammonium. The nitrogen transformation rate at a ratio of NH(4)(+)-N to NO(2)(-)-N of 1:1.38 was faster, and effluent nitrogen levels were lower, than at ratios of 1:0.671, 1:2.18, and 1:3.05. Fluorescent in situ hybridization (FISH) was used to identify specific autotrophic ammonium oxidizing bacteria (Nitrosomonas spp., Candidatus Brocadia anammoxidans, and Candidatus Kuenenia stuttgartiensis). The ammonium oxidizing culture maintained at 42 mg N/L ammonium was enriched for Nitrosomonas spp. (30%) over Candidati B. anammoxidans and K. stuttgartiensis (2.1%) while the culture maintained at 210 mg N/L ammonium was dominated by Candidati B. anammoxidans and K. stuttgartiensis (85.6%). The specific nitrogen removal rate of anammox bacteria (0.6 g N/g anammox VSS/d) was significantly higher than that of ammonium oxidizing bacteria (0.4 g N/g Nitrosomonas VSS/d). Anammox bacteria removed up to 979 mg N/L/d of total nitrogen (ammonium:nitrite concentrations, 397:582 mg N/L). These results suggest significant promise of this approach for application to wastewater with high nitrogen but low carbon content, such as that found in Bangkok. 相似文献
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Improvement of fruit and vegetable waste anaerobic digestion performance and stability with co-substrates addition 总被引:1,自引:0,他引:1
The effect of fish waste (FW), abattoir wastewater (AW) and waste activated sludge (WAS) addition as co-substrates on the fruit and vegetable waste (FVW) anaerobic digestion performance was investigated under mesophilic conditions using four anaerobic sequencing batch reactors (ASBR) with the aim of finding the better co-substrate for the enhanced performance of co-digestion. The reactors were operated at an organic loading rate of 2.46–2.51 g volatile solids (VS) l−1 d−1, of which approximately 90% were from FVW, and a hydraulic retention time of 10 days. It was observed that AW and WAS additions with a ratio of 10% VS enhanced biogas yield by 51.5% and 43.8% and total volatile solids removal by 10% and 11.7%, respectively. However FW addition led to improvement of the process stability, as indicated by the low VFAs/Alkalinity ratio of 0.28, and permitted anaerobic digestion of FVW without chemical alkali addition. Despite a considerable decrease in the C/N ratio from 34.2 to 27.6, the addition of FW slightly improved the gas production yield (8.1%) compared to anaerobic digestion of FVW alone. A C/N ratio between 22 and 25 seemed to be better for anaerobic co-digestion of FVW with its co-substrates. The most significant factor for enhanced FVW digestion performance was the improved organic nitrogen content provided by the additional wastes. Consequently, the occurrence of an imbalance between the different groups of anaerobic bacteria which may take place in unstable anaerobic digestion of FVW could be prevented. 相似文献