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本文初步研究了用SBBR法处理垃圾渗滤液的处理效果。在驯养结束后的20个连续运行周期里,控制曝气量为250 L/h,温度为27℃,有机负荷为0.4 Kg(BOD5)/m3.d。当系统进水CODCr,NH3-N分别为810 mg/L和93 mg/L时,系统出水CODCr,NH3-N分别为160 mg/L和28 mg/L,运行结果表明:该系统在此条件下可以稳定运行。在此基础上,维持有机负荷和温度不变,在曝气量为150 L/h,200 L/h,250 L/h时分别测定不同进水水质时CODCr,氨氮的去除率。实验结果表明:当气量为250 L/h时,CODCr的去除率随进水CODCr浓度的升高而升高;当进水CODCr为790 mg/L时,CODCr的去除率随气量的升高而升高,去除率为65.78%~79.68%,并且在1小时以后有较高的去除率。稳定运行8小时之后,去除率较接近各自的最高去除率。当气量为250 L/h时,氨氮的去除率随进水氨氮浓度的升高而降低;当进水氨氮较低时(低于50 mg/L),氨氮的去除率随曝气量的升高而升高,去除率为62.07%~97.69%。 相似文献
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复合式厌氧反应器处理生活污水运行特性研究 总被引:2,自引:1,他引:2
本文对复合式折流板厌氧反应器处理生活污水的运行特性进行了研究,并作了灵敏度分析。结果表明:HABR反应器因其特殊的结构而具有很好的耐冲击负荷能力及很好的去除效果;当进水的CODCr在300mg/L左右,温度在16 3~30 5℃时,水力停留时间采用6h,容积负荷为1 2kgCOD/m3·d左右,COD去除率可保持在70%以上,出水CODCr可小于100mg/L,出水SS浓度在27~64mg/L之间;各操作参数对HABR反应器CODCr去除率的影响有显著性不同;HRT是系统运行过程中需严格控制的关键因素。 相似文献
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《中国环境管理干部学院学报》2017,(3)
以江苏铜山区3个行政村生活垃圾为对象,设计了厌氧垃圾生物反应器,研究了农村生活垃圾在反应器中的变化情况。研究表明:潘塘村和姜楼村生活垃圾中含有大量的水分和蛋白质,促进了厌氧微生物的生长繁殖和甲烷产气发生,使渗滤液p H值迅速上升,30周pH达到最高点8.24和8.33。初期反应器中BOD浓度,3个行政村都呈上升趋势,16周左右达到最大值,30周后赵店村、潘塘村、姜楼村3个行政村渗滤液中BOD浓度分别下降到26 101 mg/L、16 121 mg/L、20 105 mg/L。 相似文献
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水解酸化-两级接触氧化工艺在啤酒废水处理中的应用 总被引:1,自引:0,他引:1
潘俊艳 《中国环境管理干部学院学报》2013,(4):61-63,91
啤酒废水具有有机物含量高、悬浮物浓度高、温度高、 pH 值变化大及可生化性较好等特点,生化处理成为国内外啤酒废水处理的主要工艺。公司采用“水解酸化-两级生物接触氧化”工艺对啤酒废水进行处理,运行结果表明,废水pH在8~9, SS、 CODCr、 NH3-N平均浓度分别为710 mg/L、1910 mg/L、49 mg/L时,处理后出水pH在6.5~8.5, SS、 CODCr、NH3-N平均浓度分别为52 mg/L、70 mg/L、11 mg/L, SS、 CODCr、 NH3-N平均去除率分别为93%、96%、77%,满足啤酒废水排放标准的要求。该工艺对废水具有较好的适应性。 相似文献
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针对海洋溢油污染问题,采用实验室筛选的海洋溢油降解菌HJ01和HJ02开展海洋溢油微生物降解优化研究,采用单因素实验和多因素正交实验进行降解率测定。结果表明,单因素实验条件下,当pH值为7、培养温度35℃、石油初始浓度7 500mg/L、NaCl含量20 000mg/L时,HJ01和HJ02对海洋溢油的降解效果最佳。正交实验条件下,HJ01在pH值为7、培养温度35℃、石油初始浓度7 500mg/L、NaCl含量10 000mg/L时降解效果最佳;HJ02在pH值为7、培养温度30℃、石油初始浓度11 000 mg/L、NaCl含量10 000mg/L时降解效果最佳。 相似文献
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采用垂直流人工湿地模拟装置对新疆油田外排含盐稠油废水进行了处理。实验表明:对于进水CODCr为402~406mg/L,盐度5701~5712mg/L,石油类40.62mg/L的含盐稠油废水,该系统的出水指标为CODCr35~38mg/L,盐度1535~1542mg/L,湿地系统对CODCr和盐分的去除率达到91%和73%;当水力停留时间为11d以上,出水石油类<5mg/L,处理后出水CODCr、石油类达到《污水综合排放标准》(GB8978-1996)的一级标准。 相似文献
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G. N. Demirer 《International Journal of Green Energy》2016,13(13):1320-1324
Pistachio processing wastes create significant waste management problems unless properly managed. However, there are not well-established methods to manage the waste generated during the processing of pistachios. Anaerobic digestion can be an attractive option not only for the management of pistachio processing wastes but also producing renewable energy in the form of biogas. This study investigated anaerobic digestibility and biogas production potential of pistachio de-hulling waste from wet de-hulling process. Best to our knowledge, this is the first report on biogas production from pistachio de-hulling waste. The results indicated that (1) anaerobic digestion of pistachio de-hulling wastewater, solid waste, and their mixtures in different ratios is possible with varying levels of performance; (2) 1 L of de-hulling wastewater (chemical oxygen demand concentration of 30 g/L) produced 0.7 L of methane; (3) 1 L of de-hulling wastewater and 20 g of pistachio de-hulling solid waste produced 1.25 L of methane; and (4) 1 g of de-hulling solid waste produced 62.6 mL of methane (or 134 mL of biogas). 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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Sanphoti N Towprayoon S Chaiprasert P Nopharatana A 《Journal of environmental management》2006,81(1):27-35
In order to increase methane production efficiency, leachate recirculation is applied in landfills to increase moisture content and circulate organic matter back into the landfill cell. In the case of tropical landfills, where high temperature and evaporation occurs, leachate recirculation may not be enough to maintain the moisture content, therefore supplemental water addition into the cell is an option that could help stabilize moisture levels as well as stimulate biological activity. The objectives of this study were to determine the effects of leachate recirculation and supplemental water addition on municipal solid waste decomposition and methane production in three anaerobic digestion reactors. Anaerobic digestion with leachate recirculation and supplemental water addition showed the highest performance in terms of cumulative methane production and the stabilization period time required. It produced an accumulated methane production of 54.87 l/kg dry weight of MSW at an average rate of 0.58 l/kg dry weight/d and reached the stabilization phase on day 180. The leachate recirculation reactor provided 17.04 l/kg dry weight at a rate of 0.14l/kg dry weight/d and reached the stabilization phase on day 290. The control reactor provided 9.02 l/kg dry weight at a rate of 0.10 l/kg dry weight/d, and reached the stabilization phase on day 270. Increasing the organic loading rate (OLR) after the waste had reached the stabilization phase made it possible to increase the methane content of the gas, the methane production rate, and the COD removal. Comparison of the reactors' efficiencies at maximum OLR (5 kgCOD/m(3)/d) in terms of the methane production rate showed that the reactor using leachate recirculation with supplemental water addition still gave the highest performance (1.56 l/kg dry weight/d), whereas the leachate recirculation reactor and the control reactor provided 0.69 l/kg dry weight/d and 0.43 l/kg dry weight/d, respectively. However, when considering methane composition (average 63.09%) and COD removal (average 90.60%), slight differences were found among these three reactors. 相似文献
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根据大港油田12井综合废水的污染特征,提出了"混凝-内电解-H2O2氧化"三步处理的方法。实验结果表明:三步法处理后可以使原水的CODcr从4930mg/L降低到128mg/L,去除率达到97%。处理后水质达到国家《污水综合排放标准》(GB8978-1996)二级标准要求。 相似文献
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Seaweed can be anaerobically digested for the production of energy-rich methane. However, the use of seaweed digestate as a fertilizer may be restricted because of the high heavy metal content especially cadmium. Reducing the concentration of heavy metals in the digestate will enable its use as a fertilizer. In this laboratory-scale study, the potential of seaweed and its leachate in the production of methane were evaluated in batch tests. The effect of removing the heavy metals from seaweed leachate was evaluated in both batch test and treatment in an upflow anaerobic sludge blanket (UASB) reactor. The heavy metals were removed from seaweed leachate using an imminodiacetic acid (IDA) polyacrylamide cryogel carrier. The methane yield obtained in the anaerobic digestion of seaweed was 0.12 N l CH4/g VSadded. The same methane yield was obtained when the seaweed leachate was used for methane production. The IDA-cryogel carrier was efficient in removing Cd2+, Cu2+, Ni2+ and Zn2+ ions from seaweed leachate. The removal of heavy metals in the seaweed leachate led to a decrease in the methane yield. The maximum sustainable organic loading rate (OLR) attained in the UASB reactor was 20.6 g tCOD/l/day corresponding to a hydraulic retention time (HRT) of 12 h and with a total COD removal efficiency of about 81%. Hydrolysis and treatment with IDA cryogel reduced the heavy metals content in the seaweed leachate before methane production. This study also demonstrated the suitability of the treatment of seaweed leachate in a UASB reactor. 相似文献
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为了分析0.250 mol/L与0.025 mol/L重铬酸钾法测定炼油催化剂行业高氯废水COD的适用性,进行了比对实验。结果表明:两者测定结果相差60.5~76.8 mg/L;高浓度重铬酸钾法精密性较好, RSD%≤4.8%,准确度较高,与氯气校正法测定结果基本吻合,相对误差≤6%;低浓度的重铬酸钾法精密性相对较差, RSD%≥8.1%,与氯气校正法测定结果相对误差大于40%,准确度低。在控制稀释水样Cl-浓度500~800 mg/L范围时,采用重铬酸钾法测定COD,适宜于高浓度的方法。 相似文献
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The anaerobic digestion of industrial wastes produces a biogas that is an alternative to the use of fossil fuels for energy production. At the end of this process, the stabilized biomass presents high levels of nutrients, which can be used both as biofertilizers in agriculture and for the biodegradation of contaminants in the soil through improvement of the microbiota. Thus, this study aimed to evaluate biogas production by industrial wastes and to use the biofertilizer for the bioremediation of soils previously contaminated with gasoline. The biomass (420 mL) generated approximately 10 liters (L) of methane and 3 L of other gases. Anaerobic incubation reduced total and volatile solids, as well as biochemical oxygen demand, chemical oxygen demand, and the carbon and nitrogen contents of the biomass. The bioremediation experiment showed that 15 days after contamination with gasoline, the addition of the biofertilizer improved the degradation efficiency of monoaromatic hydrocarbons; however, the degradation of polyaromatic hydrocarbons was less time efficient. So, we conclude that the anaerobic incubation of industrial wastes generates a high amount of biogas, and that biofertilizer deposition into contaminated soil does not affect the efficiency of the degradation of aromatic hydrocarbons after 30 days. Novelty or significance : Anaerobic incubation of industrial wastes generates a high calorific value gas, which can be used as an alternative source of energy. And, the resulting biomass, called biofertilizer, can be used to remediate soils contaminated with hydrocarbons. 相似文献