上向流曝气生物滤池反冲洗实验研究

为进一步探讨水头损失、反冲洗条件及反冲洗效果之间的关系,在前期理论分析的基础上,对天然斜发沸石、页岩陶粒和石灰岩碎石填料等3座曝气生物滤池的水洗、气洗和水漂洗等基本反冲洗过程进行了优化研究,考察了反冲洗后滤池水头损失的恢复情况以及反冲洗对处理效能的影响。结果表明,反冲洗后初滤出水的COD和SS稍有增加,但很快就在2 h...     

沸石曝气生物滤池去除氨氮性能及生物学特征分析

天然沸石具有较大的孔隙率和比表面积,对氨氮有较强的选择性离子交换能力.运用天然沸石曝气生物滤池处理城市污水厂二级生化出水,结果表明,曝气生物滤池有良好的去除效果.在气水比为3∶1,水力负荷为1 m/h,温度＞20℃情况下,沸石曝气生物滤池对城市污水厂二级生化出水COD去除率为12.7%,NH3-N去除率为96.6%;试验系统沿程微生物活性和微生物量呈现逐渐下降趋势,而单位生物量的生物活性沿程分布则与此相反;曝气生物滤池对水中污染物的去除主要集中在底部进水端部分,当水流达到距进水端上方105 cm时,曝气生物滤池对水中NH3-N的去除率已达86.8%(占氨氮总去除率的90%),COD的去除率为13.3%(占COD总去除率的67%).     

沸石曝气生物滤池去除氨氮性能及生物学特征分析

天然沸石具有较大的孔隙率和比表面积，对氨氮有较强的选择性离子交换能力。运用天然沸石曝气生物滤池处理城市污水厂二级生化出水，结果表明，曝气生物滤池有良好的去除效果。在气水比为3：1，水力负荷为1m／h，温度＞20℃情况下，沸石曝气生物滤池对城市污水厂二级生化出水COD去除率为12．7％，NH3-N去除率为96．6％；试验系统沿程微生物活性和微生物量呈现逐渐下降趋势，而单位生物量的生物活性沿程分布则与此相反；曝气生物滤池对水中污染物的去除主要集中在底部进水端部分，当水流达到距进水端上方105cm时，曝气生物滤池对水中NH3-N的去除率已达86．8％（占氨氮总去除率的90％），COD的去除率为13．3％（占COD总去除率的67％）。     

2种曝气生物滤池的启动比较分析

分别采用陶粒和沸石作为曝气生物滤池的填料,在相同运行参数下进行曝气生物滤池启动对比研究,分析挂膜过程中COD、NH4+-N和浊度的去除效果。试验结果表明,在平均气温为30℃的条件下,2种曝气生物滤池都能很快完成启动挂膜,陶粒曝气生物滤池所需时间为12d,沸石曝气生物滤池所需时间为15d;陶粒曝气生物滤池具有更好的COD去除效果,沸石曝气生物滤池具有更好的NH4+-N去除效果;2个滤池对浊度都能够达到95%左右的去除率。     

改进型曝气生物滤池的生物量和生物活性

改进型曝气生物滤池为下向流中部曝气法,采用进水水力负荷为1.63 m/d,气水比为10∶1,温度25～30℃,气水联合反冲与局部反冲相结合的方式,利用重量法及脂磷法对曝气生物滤池内的生物量和生物活性进行了研究分析。结果表明:生物滤池沿程生物量逐渐减少,进水口及曝气口附近生物量生长密集,生物膜沿程好氧速率(OUR)逐渐减少,滤层深度90 cm处最低,出水端OUR值反弹升高;生物TTC-脱氢酶活性沿水流方向逐渐减低,滤层深度90 cm处附近反弹增加。     

滤料粒径对给水曝气生物滤池运行稳定性的影响

利用给水曝气生物滤池(UBAF)处理刘屋洲水源水,考察了不同陶粒粒径对氨氮、高锰酸盐指数的去除效果以及水头损失变化的影响。结果表明,陶粒3～5 mm的UBAF对氨氮、高锰酸盐指数的去除效果较高,但是其水头损失较大,且反冲洗前后水头损失变化偏大,不利于UBAF稳定运行。陶粒6～10 mm的UBAF运行状况良好,氨氮的去除率为73.8%,高锰酸盐指数的去除率为18.6%,滤池24 h过滤水头损失<0.4 m,反冲洗前后过滤水头损失变化量<5 cm。其出水氨氮和高锰酸盐指数均达到《生活饮用水卫生标准》(GB5749-2006),滤池的水头损失小,反冲洗前后也变化甚微。进一步的实验表明陶粒破碎会导致滤料粒径级配变化,使得水头损失增加。     

2种曝气生物滤池深度处理含CMC模拟退浆废水

采用陶粒滤料和活性炭滤料的2组曝气生物滤池(BAF)处理含CMC模拟退浆废水,在水力负荷0.071 m3·(m2·h)-1、水力停留时间24 h条件下,分析曝气生物滤池对COD、CMC和浊度去除效果和曝气强度对滤池运行的影响,研究滤柱高度方向污染物去除规律以及和微生物量、微生物活性间的关系。研究结果表明,随着气水比的增大,生物滤池对COD、CMC的去除效率增大,强烈的曝气作用会引起出水浊度增大。在气水比为4∶1的条件下,2组生物滤池对COD和CMC的平均去除率分别约为72%和65%、67%和62%。曝气生物滤池对COD、CMC、浊度的主要去除区域分别位于滤柱1.5、1.3和1.1 m高度以下区域。陶粒滤柱相对活性炭滤柱微生物量略高,两组滤池单位滤料微生物量和微生物脱氢酶活性沿滤柱高度方向变化趋势相似。两组滤池对CMC的去除主要依靠吸附作用,生物降解部分仅占CMC总去除率的34.7%和26.1%。     

曝气生物滤池处理生活污水研究

研究了上向流式曝气生物滤池反应器对生活污水COD和NH3-N的启动性能.结果表明,在启动期间,COD和NH3-N的最佳去除率分别达到了94.8%和93.2%;稳定运行期间,在气水比为3:1的条件下,曝气生物滤池对COD和NH3-N的平均去除率分别为95.9%和93.7%;沿程COD和NH3-N的去除率随着滤层高度的增加...     

复合沸石滤料的制备及其性能测试

以活化后的天然斜发沸石为主要原料,添加粘合剂、成孔剂等制备出孔隙率高、比表面积大的球型复合沸石滤料。通过正交实验得到最优工艺组合条件为ω沸石粉∶ω粘合剂∶ω成孔剂=55%∶35%∶10%,活化温度为150℃,活化时间为3 h。制备的成品堆积密度为674 kg/m3,筒压强度为4.32 MPa,显气孔率59.02%。较陶粒相比,该滤料用于曝气生物滤池在挂膜启动与稳定运行阶段,均具有较高的氨氮去除效果,且挂膜微生物量高,更适宜作为曝气生物滤池的载体。     

臭氧曝气沸石生物滤池处理硝基苯废水

利用臭氧曝气沸石生物滤池处理硝基苯废水,了解了该方法对废水中的硝基苯、氮和磷的去除效果,考察了水力停留时间的变化对污染物去除效果的影响。臭氧曝气沸石生物滤池与空气曝气沸石生物滤池相比,臭氧曝气生物滤池对硝基苯、COD、氨氮的去除效果优于空气曝气沸石生物滤池,对总磷的去除效果与空气曝气沸石生物滤池差别不大。当臭氧曝气沸石生物滤池的HRT=4 h、臭氧浓度为126 mg/L时,对初始浓度为100 mg/L的硝基苯污水去除率接近99%。在相同条件下,空气曝气沸石生物滤池对硝基苯的去除率仅为59%。在HRT=4 h、臭氧浓度为126 mg/L时,臭氧曝气沸石生物滤池与空气曝气沸石生物滤池对COD的去除率为94%和83%,对NH+4-N的去除率为64%和59%,对TP的去除率为42%和45%。     

Microbial fouling of a reverse osmosis municipal water treatment system

Microbial fouling of a municipal water treatment system using reverse osmosis was investigated. From a combination of growth and molecular assays, it was discovered that the prefilter unit concentrated and facilitated microbial growth, and such growth led to microbial fouling of the reverse osmosis unit. Few cells were observed in the prefilter influent, but substantial microbial contamination was observed in the prefilter effluent, and this correlated with increasing headloss across the prefilter. The effluent caused microbial fouling of the leading elements of the reverse osmosis unit, as determined by reduced permeate flow, analysis of the elements, and assays of the membrane foulant. Both the introduction of microorganisms to the reverse osmosis unit from the prefilter unit and headloss across the prefilter could be effectively controlled through cleansing of the prefilter housing unit with sulfuric acid. Such treatments must be performed at appropriate intervals to prevent subsequent microbial growth in the prefilter unit.     

不同挂膜方式生物滴滤塔处理含H2S恶臭气体

采用菌剂挂膜,活性污泥挂膜和自然挂膜3种不同方式形成生物滴滤塔,考察挂膜方式对生物滴滤塔去除H2s恶臭气体的影响。结果表明,当进气H2S浓度为5mg／m3时,菌剂挂膜、活性污泥挂膜、自然挂膜形成的生物滴滤塔出气H2s浓度分别为15．7～17．4、11．6～14．8和15．0～15．9μg／m3;塔内压降分别为3—4mm水柱、6mm水柱和4—5mm水柱;喷淋后滤出液中硫酸根的浓度分别为14、22和17mg／L,硫的转化率分别为45％、60％和50％。当进气H2S浓度增大至7mg／m3时,3个塔经过7d的调整后,均能达到稳定状态,稳定后3个塔中出气H2s浓度和压降基本没变,喷淋后滤出液中硫酸根浓度依次增大至25、31和30mg／L左右。采用活性污泥挂膜形成的生物滴滤塔处理H2s的能力比菌剂挂膜和自然挂膜的高。     

Feasibility of soil dust source apportionment by the pyrolysis-gas chromatography/mass spectrometry method

This study tested the feasibility of using pyrolysis (Py)-gas chromatography (GC)/mass spectrometry (MS) to obtain organic chemical species data suitable for source apportionment modeling of soil-derived coarse particulate matter (PM10) dust on ambient filters. A laboratory resuspension apparatus was used with known soils to generate simulated receptor filter samples loaded with approximately 0.4 mg of PM10 dust, which is within the range of mass loading on ambient filters. Py-GC/MS at 740 degrees C generated five times more resolvable compounds than were obtained with thermal desorption GC/MS at 315 degrees C. The identified compounds were consistent with literature from Py experiments using larger samples of bulk soils. A subset of 91 organic species out of the 178 identified Py products was used as input to CMB8 software in a demonstration of source apportionment using laboratory-generated mixtures simulating ambient filter samples. The 178 quantified organic species obtained by Py of soil samples is an improvement compared with the 38 organic species obtained by thermal desorption of soils and the four functionally defined organic fractions reported by thermal/ optical reflectance. Significant differences in the concentration of specific species were seen between samples from different sites, both geographically distant and close, using analysis of variance and cluster analysis. This feasibility study showed that Py-GC/MS can generate useful source profile data for receptor modeling and justifies continued method development.     

SARA Title III,Section 313 —Looking Ahead

This study performed a workplace evaluation of emission control using available air sampling filters and characterized the emitted particles captured in filters. Characterized particles were contained in the exhaust gas released from carbon nanotube (CNT) synthesis using chemical vapor deposition (CVD). Emitted nanoparticles were collected on grids to be analyzed using transmission electron microscopy (TEM). CNT clusters in the exhaust gas were collected on filters for investigation. Three types of filters, including Nalgene surfactant-free cellulose acetate (SFCA), Pall A/E glass fiber, and Whatman QMA quartz filters, were evaluated as emission control measures, and particles deposited in the filters were characterized using scanning transmission electron microscopy (STEM) to further understand the nature of particles emitted from this CNT production. STEM analysis for collected particles on filters found that particles deposited on filter fibers had a similar morphology on all three filters, that is, hydrophobic agglomerates forming circular beaded clusters on hydrophilic filter fibers on the collecting side of the filter. CNT agglomerates were found trapped underneath the filter surface. The particle agglomerates consisted mostly of elemental carbon regardless of the shapes. Most particles were trapped in filters and no particles were found in the exhaust downstream from A/E and quartz filters, while a few nanometer-sized and submicrometer-sized individual particles and filament agglomerates were found downstream from the SFCA filter. The number concentration of particles with diameters from 5 nm to 20 µm was measured while collecting particles on grids at the exhaust piping. Total number concentration was reduced from an average of 88,500 to 700 particle/cm³ for the lowest found for all filters used. Overall, the quartz filter showed the most consistent and highest particle reduction control, and exhaust particles containing nanotubes were successfully collected and trapped inside this filter.

Implications: As concern for the toxicity of engineered nanoparticles grows, there is a need to characterize emission from carbon nanotube synthesis processes and to investigate methods to prevent their environmental release. At this time, the particles emitted from synthesis were not well characterized when collected on filters, and limited information was available about filter performance to such emission. This field study used readily available sampling filters to collect nanoparticles from the exhaust gas of a carbon nanotube furnace. New agglomerates were found on filters from such emitted particles, and the performance of using the filters studied was encouraging in terms of capturing emissions from carbon nanotube synthesis.     

Feasibility of Soil Dust Source Apportionment by the Pyrolysis-Gas Chromatography/Mass Spectrometry Method

Abstract

This study tested the feasibility of using pyrolysis (Py)-gas chromatography (GC)/mass spectrometry (MS) to obtain organic chemical species data suitable for source apportionment modeling of soil-derived coarse particulate matter (PM₁₀) dust on ambient filters. A laboratory resuspension apparatus was used with known soils to generate simulated receptor filter samples loaded with ～0.4 mg of PM₁₀ dust, which is within the range of mass loading on ambient filters. Py-GC/MS at 740 °C generated five times more resolvable compounds than were obtained with thermal desorption GC/MS at 315 °C. The identified compounds were consistent with literature from Py experiments using larger samples of bulk soils. A subset of 91 organic species out of the 178 identified Py products was used as input to CMB8 software in a demonstration of source apportionment using laboratory-generated mixtures simulating ambient filter samples. The 178 quantified organic species obtained by Py of soil samples is an improvement compared with the 38 organic species obtained by thermal desorption of soils and the four functionally defined organic fractions reported by thermal/optical reflectance. Significant differences in the concentration of specific species were seen between samples from different sites, both geographically distant and close, using analysis of variance and cluster analysis. This feasibility study showed that Py-GC/MS can generate useful source profile data for receptor modeling and justifies continued method development.     

Adsorption and desorption of selected VOCs in dust collected on air filters

Adsorption and desorption properties of the dust accumulated on air filters were examined by using a small-scale test apparatus with model compounds. The dust samples were loaded with the model compounds either by adsorption from a constant concentration in air flow or by direct injection into the dust. Desorption was measured at three different relative humidities of air (4–5%, 40–50%, 70–80%). Results indicated that constant relative humidity (RH) of air did not affect the rate of desorption in the test conditions. However, an increase in humidity substantially increased desorption of the model compounds. Similar results were obtained when experiments were conducted using dirty filters without added model compounds. In addition, emission products from clean and dusty filter materials were analyzed at two temperatures (50°C and 100°C) by using an automatic thermodesorption device. The main compounds released were carboxylic acids, aldehydes and terpenes. The emission profiles were similar for the pre-filters and main filters, but the emissions were higher from pre-filters than from the main filters. This result is consistent with the earlier findings of higher odor emissions from pre-filters.     

Economic implications of fine-pore diffuser aging.

Aerobic biological treatment, such as the activated sludge process, is commonly used for municipal wastewater treatment. Fine-pore diffusers have virtually replaced coarse-bubble diffusers in such operations, but most of the plant's energy expenditure is still consumed by aeration. Therefore, the performance of diffusers will critically affect plant economics. This paper analyzes and quantifies the consequences of aging processes on fine-pore diffusers. Datasets from 94 field measurements were analyzed and showed a clear pattern of performance decline with time in operation. Efficiency declines rapidly during the first 24 months of operation when the rate of decline decreases and efficiency stabilizes at a low value. For example, cost analysis scenarios were performed using the measured rate of decline in diffuser performance. The analyses include loss of transfer efficiency and elevated headloss, which both increase operating cost. Cleaning the diffusers within 12 months of operation is generally economically favorable, restores efficiency, and reduces power overhead. Periodic cleaning prolongs the economically viable lifespan for the aeration system.     

Biodegradation rates of 2-methylisoborneol (MIB) and geosmin through sand filters and in bioreactors

Taste and odour (T&O) causing compounds, in particular, 2-methylisoborneol (MIB) and geosmin, are a problem for water authorities as they are recalcitrant to conventional water treatment. In this study, biological sand filtration was shown to be an effective process for the complete removal of MIB and geosmin, with removal shown to be predominantly through biodegradation. In addition, MIB and geosmin were also effectively degraded in batch bioreactor experiments using biofilm sourced from one of the sand filters as the microbial inoculum. The biodegradation of MIB and geosmin was determined to be a pseudo-first-order reaction with rate constants ranging between 0.10 and 0.58 d⁻¹ in the bioreactor experiments. Rate constants were shown to be dependent upon the initial concentration of the microbial inoculum but not the initial concentration of MIB and geosmin when target concentrations of 200 and 50 ng l⁻¹ were used. Furthermore, rate constants were shown to increase upon re-exposure of the biofilm to both T&O compounds. Enrichment cultures with subsequent community profile analysis using 16S rRNA-directed PCR-DGGE identified four bacteria most likely involved in the biodegradation of geosmin within the sand filters and bioreactors. These included a Pseudomonas sp., Alphaproteobacterium, Sphingomonas sp. and an Acidobacteriaceae member.     

Electrostatic enhancement of collection efficiency of the fibrous filter pretreated with ionic surfactants

A study of the electrostatic enhancement of collection efficiency of filters pretreated with ionic surfactants has been carried out in controlled conditions with monodisperse aerosols. Cationic surfactant (dimethyl dioctadecylammonium bromide [DDAB]) and anionic surfactant (sodium oleate [SO]) were used to pretreat polypropylene fibrous filters as the positively and negatively charged filters, respectively. The effects of aerosol size, aerosol charge state, face velocity, aerosol type, and relative humidity (RH) were considered to elucidate their influence on the aerosol penetration. Results indicate that penetration through surfactant-pretreated filters was lower than that through untreated filters, and pretreatment of the filter with surfactant was observed not to affect the structure of the filter. The electrofieldmeter direct-measured the very clear electric field of filter when treating ionic surfactants. The results proved that pretreatment with surfactant caused filters to become charged. Comparing penetration through surfactant-pretreated filters with that through untreated filters with neutral aerosol, the penetration reduction factor of the surfactant-pretreated filters was in the range 1.3-2.2. Comparing aerosol penetration through the surfactant-pretreated filters with singly charged aerosol with that through untreated filters with uncharged aerosol indicates that the former decreases by a factor of 1.8-48.8. The surface fiber charges of the DDAB- and SO-pretreated filters were calculated to be 2.02 x 1(-10) C/m and -1.53 x 10(-1) degrees C/m. Moreover, the aerosol penetrations through the surfactant-pretreated filters increased with the face velocity. Surfactant-pretreated filters performed better against solid aerosol than against liquid aerosol. RH has no effect on aerosol penetration through the surfactant-pretreated filters. Regression equations for Coulombic and dielectrophoretic single-fiber efficiencies in terms of the dimensionless parameters could be fitted by the experimental measurements of surfactant-pretreated filters in this work.     

Chlorine residuals and haloacetic acid reduction in rapid sand filtration

It is quite rare to find biodegradation in rapid sand filtration for drinking water treatment. This might be due to frequent backwashes and low substrate levels. High chlorine concentrations may inhibit biofilm development, especially for plants with pre-chlorination. However, in tropical or subtropical regions, bioactivity on the sand surface may be quite significant due to high biofilm development—a result of year-round high temperature. The objective of this study is to explore the correlation between biodegradation and chlorine concentration in rapid sand filters, especially for the water treatment plants that practise pre-chlorination. In this study, haloacetic acid (HAA) biodegradation was found in conventional rapid sand filters practising pre-chlorination. Laboratory column studies and field investigations were conducted to explore the association between the biodegradation of HAAs and chlorine concentrations. The results showed that chlorine residual was an important factor that alters bioactivity development. A model based on filter influent and effluent chlorine was developed for determining threshold chlorine for biodegradation. From the model, a temperature independent chlorine concentration threshold (Cl_threshold) for biodegradation was estimated at 0.46-0.5 mg L⁻¹. The results imply that conventional filters with adequate control could be conducive to bioactivity, resulting in lower HAA concentrations. Optimizing biodegradable disinfection by-product removal in conventional rapid sand filter could be achieved with minor variation and a lower-than-Cl_threshold influent chlorine concentration. Bacteria isolation was also carried out, successfully identifying several HAA degraders. These degraders are very commonly seen in drinking water systems and can be speculated as the main contributor of HAA loss.