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411.
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413.
研究构建了2个容积为1.1 L的好氧活性污泥反应器(即1号和2号反应器)1,号反应器每天直接通加低剂量臭氧(投加量为0.01 g O3/g TSS),不加臭氧的2号反应器作为对照平行运行,均采用每天换一次人工污水的充/排式操作。运行71 d的结果表明2,个反应器对人工污水COD的处理效果基本相同。反应器运行40 d后1,号反应器的污泥浓度比2号反应器的污泥浓度低1 400~1 700 mg/L并可稳定在8 200 mg/L,污泥减量化效果明显。低剂量臭氧的直接通加明显降低了胞内ATP浓度,并影响了微生物的抗氧化活性,2号反应器的平均超氧化物歧化酶和过氧化氢酶酶活比1号反应器分别高了24.3%和9.5%。PCR-DGGE对两反应器微生物种群的分析结果表明:Uncultured gammaproteobacteria bacteri-um、Nannocystis exedens和Uncultured actinobacterium为1号反应器的主要种群;而2号反应器的主要种群为Uncultured bacte-rium和Uncultured gammaproteobacteria bacterium。 相似文献
414.
垂直流人工湿地水力学特性研究 总被引:6,自引:2,他引:4
通过示踪剂实验从停留时间分布(RTD)曲线及其统计特征值等方面对垂直流人工湿地的水力学特性进行了定性和定量的分析。研究表明水流在垂直流人工湿地中的流动是一种非理想的不均匀流动,存在一定的死区和水流的扩散;垂直流人工湿地较大的死区率与其表面布水的不均匀性有关,这也可能是其死区率大于表流人工湿地的最主要的原因。实验还表明,进水流量对垂直流人工湿地停留时间分布影响较大,随着进水流量的增加,平均停留时间减小,但标准平均停留时间增大,死区率减小;当进水流量为15L/h(水力负荷为620mm/d)时,水流在湿地中的散度最大,水流更接近全混流,不利于污染物的降解。 相似文献
415.
油田回注水中优势硫酸盐还原菌的分离鉴定与生理特性研究 总被引:2,自引:0,他引:2
从胜利油田回注水中筛选得到一株硫酸盐还原菌,命名为zsz1209。经过16SrDNA序列分析,鉴定zsz1209为梭菌属(Clostridium)。实验研究了zsz109的生理特性,并对通过调节环境pH来抑制菌株zsz1209生长繁殖的可行性进行了探讨。实验结果表明:菌株zsz1209的理想碳源为乙酸钠,在30~60℃之间可较好地生长;SOi浓度低至50mg/L时,生长未受到明显抑制。当培养环境pH高至8.5~9.0或低至3.5~4.0时,检测菌株zsz1209对SO4^2-和碳源(COD)的利用情况,发现zsz1209的生长受到明显抑制,结果表明利用改变环境pH来抑制微生物对油田的腐蚀具有可行性。 相似文献
416.
Comparison of semi-aerobic and anaerobic degradation of refuse with recirculation after leachate treatment by aged refuse bioreactor 总被引:2,自引:0,他引:2
Two fresh refuse bioreactors (F1 and F2) were operated under semi-aerobic and anaerobic conditions, respectively. The leachate from the bioreactors F1 and F2 was introduced into the aged refuse bioreactors (A1 and A2), and the effluent from A1 and A2 was subsequently recirculated into F1 and F2, respectively. The effect of the semi-aerobic recirculation process on refuse degradation was investigated, comparing it with that of the anaerobic recirculation process. Results indicate that the semi-aerobic recirculation process can increase the accumulated net production of leachate and promote evaporation. The accumulated net production of refuse in F1 is 320 mL/kg and that of F2 is 248 mL/kg, with leachate reduction amounting to 315 and 244 mL/kg refuse, respectively. The leachate quantity reduction of semi-aerobic and anaerobic leachate recirculation process accounted for 98.4% and 98.3% of the accumulated net production of leachate, respectively. The semi-aerobic leachate recirculation process can improve the biodegradation of organic matter from fresh refuse and the reduction rate of the pollutant concentration in leachate. This should shorten considerably the time required to meet the discharge standard and the time of stabilization of the refuse as observed in the anaerobic recirculation process. It was predicted that the COD concentration of leachate from the anaerobic recirculation process would reach 1000 mg/L in the anaerobic recirculation process after 2.2 years, as for semi-aerobic leachate recirculation process it is about 100 days. Compared with anaerobic recirculation process, the semi-aerobic recirculation process is more effective on NH3-N transformation and TN removal. The NH3-N and TN concentration of F1 is far below those of F2 at the end of our experiment. Refuse settlement in the semi-aerobic recirculation process was faster than that in the anaerobic recirculation process. At the end of the experiment, refuse settlement ratios in the semi-aerobic and anaerobic bioreactors were 33.5% and 18%, respectively. 相似文献
417.
Liu X Sun L Yuan D Yin L Chen J Liu Y Liu C Liang Y Lin F 《Environmental science and pollution research international》2011,18(8):1324-1332
Background and purpose
More and more coal-fired power plants equipped with seawater flue gas desulfurization systems have been built in coastal areas. They release large amount of mercury (Hg)-containing waste seawater into the adjacent seas. However, very limited impact studies have been carried out. Our research targeted the distribution of Hg in the seawater, sediment, biota, and atmosphere, and its environmental transportation. 相似文献418.
Coastal land subsidence is a serious problem in Taiwan. Starting in 1995, the goal of the “Land Subsidence Prevention and
Treatment Implementation Program” is to restructure the aquaculture industry to reduce groundwater consumption and reduce
coastal land subsidence problems. However, this goal has not been met. This study aims to determine the reasons for its failure
through a literature review and an analysis of questionnaires of stakeholders taken over a 5-year period, and design a new
program to resolve these problems. The study was conducted in 2005–2009. According to the literature, over-pumping of groundwater
around densely concentrated coastal fish ponds is the primary cause of coastal land subsidence. However, the key measure of
the program was to establish aquaculture districts primarily in subsiding coastal areas, which failed to reduce land subsidence.
In addition, the program did not consider reductions in agricultural and industrial groundwater use. Results of the questionnaire
survey were in accord with the literature review results. This paper proposes to establish a “Fish Farming Abandonment Program”
offering compensation payments and job training to fish farmers who leave the aquaculture business, thus reducing the amount
of coastal land devoted to fish farming, decreasing groundwater consumption, and halting further coastal subsidence. In addition,
the proposal also suggests adjustments to the structure of the agriculture industry. The results of this study can serve as
a reference for governments of Taiwan and other countries. 相似文献
419.
Sorption of pyrene on black carbons (BCs) obtained by heating sawdust at two temperatures (400 and 700 °C, denoted as 400BC and 700BC, respectively), as well as on modified BCs (via oxidation, oximation, and hydrolysis) was studied to investigate the role of BC structural characteristics in sorption of hydrophobic organic compounds. Pyrene was bound strongly by 700BC and 400BC, with organic carbon normalized distribution coefficients (Koc) of 105.04-105.86 and 104.65-105.16, respectively, at equilibrium pyrene concentrations of 10-100 μg L−1. Both chemical composition and pore distribution of the two BCs changed after modifications, which led to changes in their sorption characteristics for pyrene. After modifications, the linearity of pyrene sorption isotherm increased for 700BC but decreased for 400BC. For 700BC, both oxidation and oximation reduced pyrene sorption, with Koc decreasing by 69.1-73.7% and 18.7-33.9%, respectively, whereas hydrolysis did not exert a significant influence. For 400BC, oxidation and hydrolysis reduced Koc by 2.28-25.9% and 29.2-33.9%, respectively, while oximation increased Koc. In most cases, the change in sorption capacity could be explained by the changes in C content and type, polarity, surface area, and micropore volume of the BCs; however, the role of conformation (the accessibility to sorption sites) could not be ignored. 相似文献
420.
对炼油废水处理场现有工艺进行流程优化,将MBR装置调整在接触氧化池之后运行.优化流程后氨氮平均去除率可从近于0提高至71.70%;COD平均去除率可从50.00%提高至72.00%.通过对工艺流程的对比,分析了现有工艺氨氮质量浓度难以降低的原因,指出废水中存在的某些污染物对硝化细菌起到抑制作用,减少了反应器中硝化细菌的... 相似文献