炼油废水处理生物填料的选择与优化研究

对4种填料进行了挂膜试验,选择出3种挂膜性能良好的填料.并在自行开发的固定生物床反应器中,比较了这3种填料对炼油废水处理的效果.试验结果表明,F-Ⅲ型陶粒填料挂膜速度快,是一种理想的炼油废水处理生物填料.在炼油废水COD平均不大于700 mg/L,酚含量平均不大于100 mg/L,处理2 h的条件下,COD和酚的平均降解率分别可达68.5%和90.4%,COD的负荷及降解速率分别可达5.98 kg COD/m3·d和3.89 kg COD/m3·d.     

改性聚丙烯填料水处理性能试验研究

采用化学氧化-铁离子覆盖技术对普通聚丙烯填料进行改性,并对改性前后的填料进行生物亲水性、表面特性、临界表面张力以及模拟污水的生物挂膜等特性研究。结果发现,改性填料的亲水性和表面粗糙度大大提高,临界表面张力变大,表面电性为正,在生物膜法水处理中,其挂膜速度提高了46.7%,终期氨氮去除率提高了8.84%。可见改性填料与普通填料相比,其水处理性能较好。     

自然通风生物滴滤池的填料挂膜特性研究

研究了自然通风生物滴滤池内浮石、聚氨酯两种填料的挂膜特性,考察不同工况下的污水净化规律。结果表明,浮石填料在生物滴滤池内的挂膜效果更好,挂膜成功后对COD、NH+4-N均有较好的去除效果,去除率大都分别达到70%～85%、60%～80%,且小粒径浮石比大粒径浮石的去除效果更佳。聚氨酯填料在第9天挂膜成功,大粒径聚氨酯填料对COD的去除效果略好于小粒径聚氨酯填料,挂膜成功后两者对COD的去除率均可以达到60%～80%,而对NH+4-N的去除效果较差,去除率仅达到10%～40%。浮石填料生物滴滤池对TN、TP的去除率较好,当水力负荷为0.85m3/(m2·d)时,TN、TP去除率分别为45.58%、38.44%,而聚氨酯填料生物滴滤池对TN、TP的去除率较差。浮石在挂膜生物量上占优势,聚氨酯的孔径较大,污水流经时停留时间较短,使得微生物不易附着其上。     

硝化型曝气生物滤池的挂膜与启动

近年来,曝气生物滤池广泛应用于污水硝化过程中,硝化型曝气生物滤池应运而生。采用快速排泥挂膜法和自然挂膜法相结合的复合挂膜法,考察了进水是否含有机物对硝化型曝气生物滤池挂膜的影响。在19℃、HRT=55 min、出水DO=8 mg/L、进水NH4+-N约为50 mg/L的条件下,两滤池挂膜启动时间差异较大,进水不含有机物的1#滤池挂膜成功仅需18 d,当其运行稳定时NH4+-N的去除率达到100%;而进水含有机物的2#滤池挂膜成功需24 d,当其运行稳定时,COD和NH4+-N去除率分别为84.6%和91.2%。此结果表明,与含有机物的实际生活污水相比,采用不含有机物的模拟生活污水启动硝化型曝气生物滤池挂膜启动时间可缩短6 d,这主要是由于异氧菌产率系数比硝化菌大。     

错流式生物滴滤床净化甲苯废气

采用焦化厂污泥为菌源驯化甲苯降解菌,接种错流式生物滴滤床,净化含甲苯废气。研究了生物滴滤床的挂膜启动和长期运行情况,填料和营养液对滴滤床去除能力的影响,并对长期运行的压降进行了观察分析。反应器挂膜启动需要6 d时间,稳定运行的平均去除效率为95％,单位体积最大去除负荷为251 g/(m³·h)。结果表明,采用错流式生物滴滤床可以有效去除甲苯废气;以比表面积大的生物陶粒作为填料以及定期适量更换营养液,均有助于提高生物滴滤床的去除能力;错流式生物滴滤床具有压降小、气液分布均匀的特点。     

核桃壳-陶粒填料曝气生物滤池去除氨氮的研究

对核桃壳-陶粒填料曝气生物滤池(BAF)的挂膜启动和处理效果进行了研究,同时考察不同的水力负荷、气水比、填料层高度对污染物去除效果的影响。结果表明:微生物在核桃壳-陶粒填料上成功挂膜仅需21d,运行稳定后核桃壳-陶粒填料BAF的COD、氨氮去除率分别稳定在92.0%、88.3%左右;在水力负荷为0.06~0.08m3/(m2·h)、气水比为9∶1(体积比)的条件下,核桃壳-陶粒填料BAF处理效果较好且较稳定,氨氮和COD去除率可达70%以上;填料层0~15cm段为核桃壳-陶粒填料BAF去除COD的高效段,15~30cm段为去除氨氮的高效段。     

废水处理用聚乙烯生物填料表面改性与表征研究

采用化学氧化-铁离子覆盖和化学氧化-表面接枝2种方法对聚乙烯生物填料进行表面改性,并使用接触角、扫描电镜及X射线光电子能谱等手段对改性前后的填料表面进行表征,同时还考察其在废水处理中的挂膜速度和处理效果。结果表明,2种改性方法都能使填料表面形成腐蚀坑而增加了表面粗糙度,并引入基团使填料表面呈正电性,使得填料的亲水性与生物亲和性增强,有利于微生物的粘附。2种改性方法可将挂膜时间分别缩短37.5%和60%,挂膜量分别提高54.8%和76.1%,COD的去除率也分别提高10.63%和8.64%。     

填料-生物转盘处理有机模拟污水

针对传统生物转盘启动慢、挂膜性能差、水力停留时间长等缺点,采用英国某生物技术公司研制的新型填料复合式生物转盘处理有机模拟污水,考察水力停留时间、转盘转速、有机负荷等因素对工艺运行效果的影响。结果表明,新型生物转盘启动快,微生物相变化明显,微生物量大,挂膜效率高;抗负荷冲击能力强,有机负荷大幅度变化对其影响较小;二级转笼处有机负荷相对较低,溶解氧高,微生物的种类、数量均比一级转笼多;该转盘处理有机模拟污水的最优水力停留时间为1.5 h,最佳转速为12.4 r/min,较传统生物转盘污水处理量大,且污水COD去除率高达97%,大大降低运行能耗,出水水质达到城镇污水处理厂污染物排放标准(GB18918-2002)中的一级A标准。     

低湿密度竹炭悬浮生物载体在移动床生物膜反应器中的应用

以普通竹炭为原料,采用氢氧化钾活化法改性制备低湿密度竹炭,扫描电镜(SEM)、比表面积和孔径分析(BET-BJH)和傅立叶变换红外光谱(FT-IR)等表征结果表明改性后的竹炭总孔容增多,湿密度降低。将低湿密度竹炭作为悬浮生物载体应用到移动床生物膜反应器(MBBR)中,用以处理模拟生活污水,研究不同影响因素下,对COD、氨氮、TN和TP的去除效果,探索最佳运行工艺。结果表明,低湿密度竹炭悬浮生物载体流化状态好,去除效果较好。对于进水COD质量浓度为200mg/L的模拟生活污水,适宜的MBBR工艺条件为气水比100∶1(体积比)、竹炭填充率15%、水力停留时间4h,处理后出水COD、氨氮、TN和TP去除率分别为83%、77%、48%、57%。     

改性HDPE填料的制备及对MBBR脱氮除磷效果的强化

为解决传统填料亲水性差、挂膜速度慢等问题,对高密度聚乙烯(HDPE)填料进行亲水改性并改善填料的挂膜性能及在移动床生物膜反应器(MBBR)中的应用效果,用浸涂的方式将纳米SiO2、聚乙烯醇(PVA)、聚多巴胺(PDA)等材料涂覆在HDPE填料表面,对改性后填料进行接触角、 SEM、 FT-IR和XPS表征以及MBBR挂膜启动实验,研究化学需氧量(COD)、氨氮(NH3-N)、总氮(TN)、总磷(TP)的去除效果以及对填料挂膜时间、生物膜量、蛋白质和多糖含量的影响。结果表明：改性后,填料接触角由94.82°降至60.1°,填料亲水性明显增强;填料表面出现褶皱,粗糙度增加;上述材料成功负载在填料表面并引入了亲水基团且未改变填料基本结构;填料挂膜时间由25 d提前至16 d,挂膜时间提前了9 d, COD、 NH₃-N、 TN、 TP去除率分别达到94.9%、95.4%、83.5%、71.6%,与改性前比分别提高了9.3%、6.7%、13.7%、11.5%;填料的生物膜量是改性前的1.57倍,从27.35 mg·g^-1提高到42.87 mg·g     

Evaluation of kapok (Ceiba pentandra (L.) Gaertn.) as a natural hollow hydrophobic-oleophilic fibrous sorbent for oil spill cleanup

Oil sorption capacity and hydrophobic-oleophilic characteristics of an agricultural product, kapok (Ceiba pentandra), was thoroughly examined. The kapok fiber has a hollow structure with large lumen. Its performance was compared with that of a polypropylene (PP), a widely used commercial oil sorbent for oil spill cleanup. The oils investigated were diesel, hydraulic oil (AWS46), and engine oil (HD40). Reusability of the kapok after application to various oils was also evaluated. Both loose (at its natural state) and densely packed kapok assemblies were examined. Sorption capacities of the packed kapok assemblies were very much dependent on their packing densities. At 0.02gcm(-3), its oil sorption capacities were 36, 43 and 45gg(-1) for diesel, ASW46 and HD40, respectively. The values decreased to 7.9, 8.1 and 8.6gg(-1) at 0.09gcm(-3). Its sorption capacities for the three oils were significantly higher than those of PP. When the oil-saturated kapok assemblies were allowed to drain, they exhibited high oil retention ability, with less than 8% of the absorbed diesel and HD40, and 12% of the absorbed AWS46 lost even after 1h of dripping. When applied on oil-over-water baths, the kapok exhibited high selectivity for the oils over the water; almost all oils spilled could be removed with the kapok, leaving an invisible oil slick on water. After the 4th cycle of reuse, the reused kapok assembly only lost 30% of its virgin sorption capacity if packed at 0.02gcm(-3), and the loss in sorption capacity was much less at higher packing densities. The hydrophobic-oleophilic characteristics of the kapok fiber could be attributed to its waxy surface, while its large lumen contributed to its excellent oil absorbency and retention capacity.     

聚丙烯基改性纤维固相萃取水中的苯酚

通过高能电子束辐照的方法,在聚丙烯（PP）纤维基体上分别接枝长链丙烯酸十八酯（SA）和亲水性丙烯酸-β-羟乙酯（HEA）2种单体,并将该纤维作为固相萃取填料,用于固相萃取（SPE）水中的痕量苯酚。研究了SPE过程中上样速度、洗脱溶剂、洗脱体积以及洗脱速度等因素对纤维萃取效果的影响。结果表明,改性纤维对痕量苯酚的富集倍数达95~145倍,回收率达到90%~98%,甲醇对纤维有良好的再生效果,纤维重复使用6次以内时,吸附性能无明显变化。     

Leaching of terbumeton and terbumeton-desethyl from mini-columns packed with soil aggregates in laboratory conditions

Leaching of terbumeton (TER) and terbumeton-desethyl (TED) from mini-columns packed with natural soil aggregates was investigated. Five soil samples from the Champagne area (France) with different physicochemical parameters were used. The soil samples were hand-packed into a 50 mm column in laboratory conditions. An aqueous solution of TER or TED was percolated through the column and collected effluents were analyzed for TER or TED using HPLC-DAD. The leaching experiments showed that TER and TED were moderately mobile. TED was more mobile than TER, possibly because of its higher polarity. The proportion of organic matter affected the mobility of TER and TED through soil columns (r=0.971) and leaching was lowest for soil having the highest organic matter content (5.9%). TER and TED were not significantly influenced by leaching solution composition (deionized water or CaCl(2) solution), but were strongly affected by soil packing. Packing resulted in less rapid release of compounds suggesting that unpacking may have contributed to preferential pathways through the soil columns. Increasing contact time between TER and soils before leaching decreased the mobility of TER and increased its persistence in soils. Indeed, 76% of TER was released when leaching started after a 15 h contact time whereas it was down to 26% after an aging treatment of 360 h. A proportion of TER (from 8% to 32%) and TED (from 8% to 17%) remained in soil. Associated to its high stability in soils this could in part account for a very slow transfer over the years towards the groundwater.     

A System for Control of Aluminum Chloride Fumes

During primary aluminum processing the molten aluminum is periodically fluxed with chlorine to separate impurities from the metal. The gaseous effluent from the chlorination process contains submicron particulates and gaseous vapors which produce a dense, white plume. The plume is acidic with hydrogen chloride and chlorine vapors, which cause a variety of corrosion problems. Since the stack discharge temperature can range as low as 200°F-and aluminum chloride sublimates at about 360°F, blockage of ductwork can also occur. For effective removal of both the particulates and chloride gases in the effluent, a sodium hydroxide solution is recommended. However, such a scrubbing liquor produces a flocculent precipitate. Therefore, a nonplugging type of scrubber is required. The solution UOP advanced was a “mobile packing” type of scrubber, utilizing a bed of polypropylene spheres in random, turbulent motion. The motion of the packing prevents plugging. The paper describes the design for such a system, describing the optimum use of ductwork, scrubber placement, gas saturation, and recirculation equipment. Instrumentation requirements, both minimum and optimum are discussed.     

New and Improved Procedures for Gas Sampling and Analysis in the National Air Sampling Network

The NASN sampler for the collection of gaseous pollutants has been modified to increase its versatility and efficiency. Oxides of nitrogen are collected in bubblers employing a 70-100 μ frit with a collection efficiency of approximately 50% depending upon the frit porosity. Included in the sampler is a bubbler for the collection of aldehydes in which the aldehyde-MBTH complex is stable at least two weeks. This inert bubbler, which is constructed of polypropylene and Teflon, makes it possible for samples to be collected over the network and analyzed at a central laboratory. In addition, gaseous ammonia is collected in 0.1N H₂SO₄. This collecting system has an efficiency of greater than 85%. Low-level samples are analyzed automatically employing Nesslerization, whereas high-level samples from source emissions may be collected in indicating boric acid and titrated with 0.02N H₂SO₄. The sampler will accommodate either 50 or 100 ml polypropylene collecting tubes.     

气水比对曝气生物活性炭处理原水的影响

针对从臭氧-活性炭工艺中开发出来的预臭氧-曝气生物活性炭,在不同气水比工况下进行实验,分析了不同气水比对曝气生物活性炭处理微污染原水的影响与作用。结果表明:在滤速为8～12 m/h,空床接触时间为11.5～15.4 min,装填密度为510 g/L条件下,不同气水比对去除氨氮的影响大于对CODMn的影响。气水比为0.3∶1时,对氨氮浓度为1.65～2.10 mg/L范围的进水平均去除率为81.9%,亚硝酸盐氮平均积累率为1.4%,CODMn去除率为70.6%。当气水比逐渐增加时,氨氮平均去除率有所提高,亚硝酸盐氮积累率则有所下降,对较低浓度的CODMn影响不大。     

羧甲基壳聚糖的制备及絮凝性能探讨

制备了具有水溶性、无毒羧甲基壳聚糖（以下简称NOCC），将其作为絮凝剂与聚丙烯酰胺（PAM）一道处理生活污水，通过测定其沉降时间，沉降絮体高度，沉降速度，沉降后溶液透光率等参数，表征了其絮凝能力，提出了普遍认为聚丙烯酰胺处理一般污水具有良好絮凝能力的不同看法，为壳聚糖的开发利用做了有益的探索。     

高效生物滴滤床净化含二甲苯废气的实验研究

通过摇床实验筛选出一株二甲苯降解菌．将该菌种接种于生物滴滤床中,研究其净化含二甲苯废气的效果。实验结果表明,纯菌种的生物滴滤床的净化效果比混合菌种生物滴滤床有显著提高。当气体停留时间在28．3～84．8s变化时,系统的净化效率变化不大;当气体停留时间缩短到17．0s时,滤床的净化效率随人口浓度有较大变化。在实验范围内,喷淋液的流量对滤床的净化效果几乎没有影响。滤床填料中生物量分布呈递减趋势。     

Changes in air saturation and air-water interfacial area during surfactant-enhanced air sparging in saturated sand

Reduction in the surface tension of groundwater, prior to air sparging for removal of volatile organic contaminant from aquifer, can greatly enhance the air content and the extent of influence when air sparging is implemented. However, detailed information on the functional relationship between water saturation, air-water contact area induced by air sparging and the surface tension of water has not been available. In this study, the influence of adding water-soluble anionic surfactant (sodium dodecyl benzene sulfonate) into groundwater before air sparging on the air-water interfacial area and water saturation was investigated using a laboratory-scale sand packed column. It was found that water saturation decreases with decreasing surface tension of water until it reaches a point where this trend is reversed so that water saturation increases with further decrease in the surface tension. The lowest water saturation of 0.58 was achieved at a surface tension of 45.4 dyn/cm, which is considered as the optimum surface tension for maximum de-saturation for the initially water-saturated sand used in this study. The air-water contact area generated in the sand column due to air sparging was measured using a gaseous interfacial tracer, n-decane, and was found to monotonically increase with decreasing water saturation. The results of this study provide useful design information for surfactant-enhanced air sparging removal of volatile contaminants from aquifers.