生物过滤塔处理实验室废气

研究了生物过滤塔处理实验室排放的模拟混合废气,考察了反应器对苯、甲苯、二甲苯、乙醇、丙酮、乙酸乙酯和甲烷等废气的去除效果。运行结果表明,在设备稳定运行期间,进气中总挥发性有机物(TVOCs)的浓度为124～380 mg/m3,而出气浓度在10～40 mg/m3,去除效率保持在85%以上。实验室废气中的多种污染物在生物过滤塔中去除机理不同,亲水性污染物的去除效率高于疏水性污染物。通过系统关停后重启,污染物的去除效果在第2天就能恢复,这为生物过滤塔处理实验室废气过程的停运检修或者系统闲置提供了可行性。     

超声波预处理对污泥好氧/缺氧消化的效果

为评价超声波预处理对城市污泥好氧/缺氧消化效果的影响,将超声波-好氧/缺氧消化工艺与传统的好氧/缺氧消化工艺进行了对比研究。结果表明,经25 d消化处理,引进超声波后的好氧/缺氧消化效果显著提高,污泥的VSS去除率达到51.98%,高于传统好氧/缺氧消化的42.98%。2种工艺消化的污泥TCOD以及污泥上清液中的SCOD、TP和NH3-N的变化趋势相似;而经超声波-好氧/缺氧消化的污泥上清液中硝态氮和亚硝态氮浓度较传统好氧/缺氧的高,说明经超声波处理后的污泥中的硝化细菌的活性增强,硝化反应加快。     

Isolates identification and characteristics of microorganisms in biotrickling filter and biofilter system treating H2S and NH3

A combination system of biotrickling filter （BTF） and biofilter （BF）, adopting surfactant-modified clinoptilolite and surfactant- modified wood chip as the media respectively, was applied to treat H2S and NH3 simultaneously. The identification and sole carbon sources utilization patterns of isolates in the combination system were studied by Biolog system. The isolates were identified as Bacillus sphaericus, Geobacillus themoglucosidasius （55℃） and Micrococcus luteus （ATCC 9341） in BTF, and Aspergillus sydowii （Bainier ＆ Sartory） Thom＆ Church in BE Among 95 substrate classes supplied by Biolog system, the carboxylic acids and methyl esters had the highest utilization extent for the four species, followed by the amino acids and peptides. The descending sequence of carbon sources utilization capability of isolates was A. sydowii （52.6%）, M. luteus （39.5%）, B. sphaericus （21.6%）, and G. thermoglucosidasius （17.7%）.     

模拟城市污水在厌氧、缺氧以及好氧反应器中的毒性削减研究

采用发光细菌法测定城市污水毒性,并研究了模拟城市污水分别在厌氧、缺氧、好氧条件下的毒性削减情况.试验采用人工配水,其中添加了甲苯、邻二甲苯、对二甲苯、吲哚、吡啶、环己酮、苯丙酸7种有毒有机物.并用GC-MS检测上述有机物在不同生物处理过程中的降解情况及出水有机物的变化情况.结果表明,模拟城市污水经厌氧生物处理后毒性增大(HRT≤10h);缺氧生物处理对模拟城市污水的毒性略有削减;而好氧生物处理对模拟城市污水的毒性削减能力较强,效果明显.     

折流式水解反应器处理印染废水水温影响研究

在水温为5℃、9.7℃、14.9℃、19.7℃、23.5℃和31.1℃6种温度的条件下,应用折流式水解反应器对印染废水进行水解试验研究.结果表明,提高水温可增大COD、色度及UVA254的去除效率,相应的ORP值变小,pH值升高,水解程度加深.水温5℃时,水解效果较差;水温在10～23.5℃内,水解效果相对较好,31.1℃水解效果最好,研究结果能为工程应用提供一定的参考.     

工业废水为主的城市污水A/O工艺启动研究

文章研究了以工业废水为主的城市污水A/O处理工艺的启动。结果表明,水解酸化池的酸性出水经过曝气池氧化后,pH值基本稳定在7.41左右。随进水中工业废水比例的增加,水解酸化池的COD去除率明显下降,但曝气池的出水质量仍较好。氨氮的去除率起初下降,接着逐渐提升并趋于稳定,但总氮的去除率一直呈上升趋势。色度随工业废水比例的增加而增大,但出水色度一直维持在较好的水平。     

污泥缺氧好氧消化的减量研究

实验主要进行缺氧好氧工艺在不同运行条件下消化效果的研究;在常温和中温下,与传统污泥好氧消化处理的效果对比,并进行pH等控制参数的统计规律分析,提出优化处理工艺条件,也为污泥缺氧好氧消化工艺的设计、运行管理和进一步研究提供可靠的理论依据。     

缺氧条件下含氮杂环化合物吲哚和吡啶的共代谢研究

以含氮杂环化合物吲哚和吡啶为研究对象,在传统的缺氧反硝化机理研究基础上,通过向配制废水中加入硝酸盐氮,研究吡啶和吲哚在缺氧条件下的共代谢作用.结果表明,吡啶和吲哚缺氧共代谢的最佳碳氮比为8.4～8.9之间.硝酸还原酶适宜作用的环境条件为:温度28℃,pH值7.0～7.5.吡啶的加入有利于硝酸还原酶活性的提高,吡啶对吲哚的缺氧降解有协同作用.在最佳碳氮比条件下,当吲哚起始浓度为150mg/L,吲哚和吡啶的浓度比例为1～10之间时,吲哚的降解符合零级动力学规律,反应过程中亚硝酸盐氮基本没有积累.当吡啶和吲哚的浓度比小于0.25时,随着吡啶浓度比例的提高,硝酸还原酶活性及吲哚降解速率的增长较快;当吡啶和吲哚的浓度比大于0.25时,硝酸还原酶活性及吲哚降解速率的增长变得比较缓慢.     

Nitrous oxide gas removal by using compost-based biofilter medium

This paper is aimed at introducing our research result in the efficiency in removing nitrous oxide gas (N2O) by using compost as a medium filter,which is actually a kind of manure derived from cow faeces at Kukusan Kelurahan farm containg wood chips and some other microorganisms.Practically speaking,N2O is a major greenhouse gas,whose continuous presence in the atmosphere is expected to last over a 100 years and produce its radiative warming effect just next to CO2.In spite of its rather small concentration in the atmosphere,it is the Number Four largest greenhouse gas contributor to the overall global warming,behind carbon dioxide,methane and water vapour.The biofiltration experiments we have conducted to explore its removing rate of N2O from flue gas help us to find various operating factors in the biofilter system.So far as we know,N2O gas has been fed from the top of the column.It was flowing through the column when it is made to get circulated with a peristaltic pump for 6 hours.The data obtained in our paper prove to be in conformity with the Langmuir adsorption model.The highest N2O gas removing efficiency can be made to be as high as 70.22% at the highest biofilter length of 50 cm with the gas flowing rate of 200 mL/min.The results of this research have finally been modeled by the Langmuir adsorption isotherm formula with its K value obtained being 16.949 L/mol.     

Economical assessment of the design,construction and operation of open-bed biofilters for waste gas treatment

A protocol was developed with the purpose of assessing the main costs implied in the set-up, operation and maintenance of a waste gas-treating conventional biofilter. The main operating parameters considered in the protocol were the empty bed residence time and the gas flow rate. A wide variety of investment and operating costs were considered. In order to check its reliability, the protocol was applied to a number of scenarios, with biofilter volumes ranging from 8.3 to 4000 m³. Results show that total annualized costs were between 20?000 and 220?000 €/year and directly dependent, among other factors, on the size of the system. Total investment and operating costs for average-size compost biofilters were around 60?000 € and 20?000 €/year, respectively, which are concordant with actual costs. Also, a sensitivity analysis was performed in order to assess the relative influence of a series of selected costs. Results prove that operating costs are those that influence the total annual costs to a higher extent. Also, packing material replacement costs contribute significantly to the total yearly costs in biofilters with a volume higher than 800 m³. Among operating costs, the electricity consumption is the main influencing factor in biofilters with a gas flow rate above 50?000 m³/h, while labor costs are critical at lower gas flow rates. In addition, the use of a variety of packing materials commonly employed in biofiltration was assessed. According to the results obtained, special attention should be paid to the packing material selected, as it is the main parameter influencing the medium replacement costs, and one of the main factors affecting investment costs.