不同COD浓度下低基质厌氧氨氧化的启动特征

采用厌氧序批式反应器(ASBR)处理NH4+-N和NO2--N浓度分别为(25. 00±0. 40) mg·L~(-1)和(33. 00±0. 60) mg·L~(-1)的模拟废水,在温度为30℃时,投加乙酸钠控制COD浓度分别为5. 00、15. 00、30. 00和50. 00 mg·L~(-1),研究对厌氧氨氧化启动的影响.结果表明:①4种COD浓度下分别经过74、94、106和129 d均能成功启动厌氧氨氧化. COD浓度为15. 00 mg·L~(-1)和30. 00 mg·L~(-1)时,反应器脱氮性能较好,稳定运行后,平均出水NH4+-N浓度分别为1. 98 mg·L~(-1)和1. 89 mg·L~(-1),平均出水NO2--N浓度低于0. 62 mg·L~(-1),平均出水TN浓度分别为2. 37、2. 28 mg·L~(-1);②启动过程中反硝化对脱氮的平均贡献率逐渐降低至4. 78%、9. 59%、10. 21%和36. 50%,厌氧氨氧化对脱氮的平均贡献率逐渐上升至95. 22%、90. 41%、89. 79%和63. 50%;③厌氧氨氧化活性分别在第44、76、86和114 d时超过反硝化活性,最后分别达到0. 700、0. 690、0. 670和0. 510mg·(g·h)~(-1),反硝化活性分别为0. 110、0. 130、0. 240和0. 410 mg·(g·h)~(-1).该研究结果可为厌氧氨氧化技术在实际工程中的应用提供参考.     

国务院安委办通报陕西西安“9·10”脚手架坠落事故

2011年9月19日,国务院安全生产委员会办公室发布了《关于陕西省西安市玄武路凯玄大厦工地“9·10”重大附着式脚手架坠落事故情况的通报》,以有效防范和遏制重特大事故的发生。     

正压式呼吸保护装备的选择与应用

正压式空气呼吸器(以下简称空呼)以其稳定的工作状态,简便易操作的设计,广泛的应用在化工行业、消防部队等单位。正压式空气呼吸器这个大家族当中,针对不同的环境设计出了不同类型的产品,一般可分为以下     

分离浮罩式沼气池在车八岭国家级自然保护区的实践与探索

在农村生态建设中,沼气在减少自然资源的消耗和发展农业经济等方面都具有重要作用,深受群众的欢迎。分离浮罩式沼气池性能优越,克服了固定水压式沼气池许多缺点,具有良好的社会、经济和生态效益。本文介绍了分离浮罩式沼气池在车八岭国家级自然保护区的实践与探索经验,对沼气在保护区及其他地方的推广具有重要的借鉴意义。     

飞机地面积/除冰环境模拟与试验研究

飞机地面积冰是飞机进入冬季安全飞行的重要隐患,很多飞行事故都是因为没有清除飞机表面的积冰而造成的。基于对飞机地面积/除冰的真实环境的分析,在低温湿热试验箱中模拟积/除冰时的大气条件,对机翼积/除冰进行试验研究。通过改变环境温度、除冰液温度、流量、浓度等影响因素,利用光纤式结冰传感器得到不同环境条件下,除冰液参数对除冰过程的影响数据,并对这些数据进行了分析。试验结果表明该装置能有效地模拟飞机地面积/除冰过程,数据分析显示飞机地面结冰过程主要受外界环境温度,湿度(空气的水含量)的影响;对飞机地面除冰来说,除冰液温度参数是除冰效果达到最佳的关键因素。     

改性活性氧化铝除磷性能的试验

为提高活性氧化铝对废水中磷的去除效果,以硫酸铝为改性剂,采用浸渍法对其进行改性;测定了改性前后活性氧化铝的比表面积及孔容孔径;考察了吸附时间、pH、废水初始浓度、改性剂投加量等因素对去除废水中磷的影响;探讨了改性活性氧化铝对磷的吸附机理.结果表明,改性后活性氧化铝的比表面积为398.364 m2/g,提高了14.22%...     

利用太阳能压缩垃圾

在不少街道上,尤其是市中心商业区的街道上,垃圾桶很快就被塞满了。如果清洁工人没有及时来收走垃圾,多余的垃圾就从垃圾桶溢出来,非常影响市容的美观。为了解决这个问题,英国研究人员开发出了一种可以压缩垃圾的太阳能垃圾桶。而且,它还是一款智能垃圾桶,在     

Biological nutrient removal by internal circulation upflow sludge blanket reactor after landfill leachate pretreatment

The removal of biological nutrient from mature landfill leachate with a high nitrogen load by an internal circulation upflow sludge blanket （ICUSB） reactor was studied. The reactor is a set of anaerobic-anoxic-aerobic （A^2/O） bioreactors, developed on the basis of an expended granular sludge blanket （EGSB）, granular sequencing batch reactor （GSBR） and intermittent cycle extended aeration system （ICEAS）. Leachate was subjected to stripping by agitation process and poly ferric sulfate coagulation as a pretreatment process, in order to reduce both ammonia toxicity to microorganisms and the organic contents. The reactor was operated under three different operating systems, consisting of recycling sludge with air （A^2/O）, recycling sludge without air （low oxygen） and a combination of both （A^2/O and low oxygen）. The lowest effluent nutrient levels were realised by the combined system of A^2/O and low oxygen, which resulted in effluent of chemical oxygen demand （COD）, NH3-N and biological oxygen demand （BOD5） concentrations of 98.20, 13.50 and 22.50 mg/L. The optimal operating conditions for the efficient removal of biological nutrient using the ICUSB reactor were examined to evaluate the influence of the parameters on its performance. The results showed that average removal efflciencies of COD and NH3- N of 96.49% and 99.39%, respectively were achieved under the condition of a hydraulic retention time of 12 hr, including 4 hr of pumping air into the reactor, with dissolved oxygen at an rate of 4 mg/L and an upflow velocity 2 m/hr. These combined processes were successfully employed and effectively decreased pollutant loading.     

Effects of idle time on biological phosphorus removal by sequencing batch reactors

Three identical sequencing batch reactors （SBRs） were operated to investigate the effects of various idle times on the biological phosphorus （P） removal. The idle times were set to 3 hr （R1）, 10 hr （R2） and 17 hr （R3）. The results showed that the idle time of a SBR had potential impact on biological phosphorus removal, especially when the influent phosphorus concentration increased. The phosphorus removal efficiencies of the R2 and R3 systems declined dramatically compared with the stable R1 system, and the Prelease and P-uptake rates of the R3 system in particular decreased dramatically. The PCR-DGGE analysis showed that uncultured Pseudomonas sp. （GQ183242.1） and β-Proteobacteria （AY823971） were the dominant phosphorus removal bacteria for the R1 and R2 systems, while uncultured γ-Proteobacteria were the dominant phosphorus removal bacteria for the R3 system. Glycogen-accumulating organisms （GAOs）, such as uncultured Sphingomonas sp. （AM889077）, were found in the R2 and R3 systems. Overall, the R1 system was the most stable and exhibited the best phosphorus removal efficiency. It was found that although the idle time can be prolonged to allow the formation of intracellular polymers when the phosphorus concentration of the influent is low, systems with a long idle time can become unstable when the influent phosphorus concentration is increased.     

混凝—淹没式曝气生物滤池组合工艺处理洗衣废水

利用混凝与淹没式曝气生物滤池相结合的处理工艺对洗衣废水进行了90d的研究。工程运行结果表明,洗衣废水经混凝后,COD平均下降52.9%,TP平均下降92.1%。混凝出水再经过曝气生物滤池进一步处理,最终出水水质为COD≤50mg/L,NH3≤2.57mg/L,TP≤0.27mg/L。