铁氧化物多孔陶粒生物滴滤塔净化硫化氢气体

采用装有凹凸棒石基铁氧化物多孔陶粒作为填料的生物滴滤塔,进行了长期实验室H2S脱臭实验。结果表明,该生物滴滤塔H2S的进气浓度低于500 mg/m3 时,循环营养液喷淋量高于1.5 L/h,气体最佳停留时间为54.9 s,去除率在95 % 以上。代谢产物以SO42-为主,转化速率在52.42 g/(m3·d)左右。该滴滤塔系统可稳定而有效运行。生物相观察表明,滴滤塔填料表面附着大量微生物,铁氧化物陶粒具有化学和生物惰性,有利于微生物的附着。     

静压箱式错流生物滴滤床去除甲苯废气的研究

根据静压箱原理设计静压箱式错流生物滴滤床,设置进气静压区进一步改善气流分布情况,气流进入后在圆柱形静压区内动压降低,气流均匀分布.以甲苯为目标污染物、陶粒为填料、恶臭假单胞菌为菌源进行实验,研究静压箱式错流生物滴滤床的挂膜启动情况及稳定运行阶段甲苯停留时间、进气浓度对甲苯去除率的影响,分析了运行后期填料层压力损失增大的...     

黑麦草根际强化微生物净化甲苯

采用在普通生物反应器上种植黑麦草的方法,研究了黑麦草根系强化微生物净化甲苯污染气体的作用,及甲苯入口浓度、填料深度、温度对反应器净化甲苯速率的影响。结果表明,在生物反应器相同的填料深度,细菌数量的水平分布为黑麦草根际区>过渡区>非根际,与相同位置的甲苯浓度分布呈负相关,说明黑麦草根系通过促进细菌的活性进而增加甲苯的降解。在相同的甲苯入口浓度下,甲苯的净化速率随着填料深度的增加而增加,在甲苯入口浓度不高于500 mg/m3条件下,相同的填料深度,反应器对甲苯的净化速率随着甲苯浓度的增加而增加。在5~35℃范围内,温度升高有助于提高微生物活性,促进微生物对甲苯的降解,且有黑麦草处理的甲苯净化速率大于同等条件下无黑麦草处理。     

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。     

生物滴滤塔净化甲苯启动性能研究

研究以甲苯为驯导物的生物滴滤塔挂膜启动阶段净化性能的变化。实验结果表明,通过控制pH和湿度得到了真菌滴滤系统,启动周期为14 d,比细菌滴滤塔长7 d;在进化性能方面,在入口负荷、浓度为80 g/(m3.h)、3 000 mg/m3的条件下获得了稳定在98%以上的去除效率;对比2种填料对启动阶段的影响,在较低负荷下(≤80 g/(m3.h))对系统的启动时间和去除效率没有显著影响。     

管式生物过滤器去除乙苯废气

生物过滤由于其良好的成本效益和环境友好性已经成为控制挥发性有机化合物(VOCs)含量和气味气体排放的常规技术。营养物质的均匀分布、生物膜和介质床内的气体流是成就一个性能优良的生物过滤器至关重要的因素。而由本实验室开发的管式生物过滤器(TBFs)已被证明具备此优势。本实验的管式生物过滤器以聚氨酯海绵作为填料,研究在不同有机负荷、气体停留时间(EBCT)、进气量和表面活性剂等条件下乙苯废气的去除效率(RE)。实验同时记录了管式生物过滤器启动阶段的表现。初期使附着在填料上的微生物暴露在浓度为40 mg/m3的乙苯废气中40 d,此时的气体停留时间为15 s,使微生物慢慢适应并逐步降解乙苯废气;然后连续地控制管式生物过滤器的入口乙苯浓度为40、80、120和160 mg/m3,以使有机负荷逐步升高。结果表明,乙苯去除效率随着有机负荷的增大而逐步减小。当气体停留时间从15 s增加到30 s和60 s,而有机负荷控制在38.60 g/(m3·h)时,乙苯废气去除效率略微增加。此外,随着进气量的增大乙苯废气的最大平均去除效率有所下降而此时的降解容量增大,这个过程中乙苯进气浓度保持不变。结果还表明,在营养液中加入聚乙二醇辛基苯基醚这种表面活性剂可以提高乙苯废气的去除效率。     

生物滴滤法净化低浓度磷化氢及其微生物群落分析

采用生物滴滤法净化低浓度磷化氢气体,探讨填料种类、进气量、氧浓度、进气磷化氢浓度等因素对净化过程的影响。复合填料能促进气态磷化氢的吸附,但微生物对磷化氢的净化起决定性作用。进气负荷高于300 mL·min~(-1)(空间速度为8.2 h~(-1))时,滴滤塔内磷化氢去除率下降明显;进气中氧含量不足时,生物氧化进程受到抑制,磷化氢净化效果变差。在进气流量200 mL·min~(-1)、氧体积分数8.2%、磷化氢入口浓度20 mg·m~(-3)条件下,磷化氢脱除率可高达76.8%,定期废弃的吸收液中总磷含量均低于1.0 mg·L~(-1)。生物滴滤塔内具有较高的微生物种群多样性,细菌以变形菌门(Proteobacteria)最为丰富,主要的细菌种属有:鞘氨醇单胞菌(Sphingomonas)、甲醇杆菌(Methylobacterium)、嗜甲基菌(Methylophilus)及伯克氏菌(Burkholderia)。     

生物滴滤塔净化苯乙烯废气的实验研究

采用生物滴滤(BTF)系统对含苯乙烯的有机废气进行了生物净化实验并研究该系统VOCs生物降解性能。实验表明,苯乙烯进气浓度低于20 mg/m3时BTF去除效率可达92%以上,出口苯乙烯浓度低于1.6 mg/m3,达到GB14554-1993中规定的排放标准;该BTF装置对苯乙烯的去除负荷在2.0 g/(m3.h)左右;系统稳定运行时循环液COD、浊度和pH等都保持稳定,无脱落生物膜积累现象;生物滴滤塔系统适宜的气液比为300;系统总压降约100 Pa,鲍尔环填料和聚氨酯发泡填料混合装填方式可以降低系统压降并有利于微生物挂膜。     

酸性洗涤塔-生物滤塔-生物曝气池组合工艺处理恶臭气体NH3和H2S

采用酸性洗涤塔、生物滤塔和生物曝气池的组合工艺处理NH3、H2S恶臭混合气体,研究表明,该组合工艺对NH3和H2S有很好的去除效果,在进气流量为35 L/min,喷淋量45 L/h时,NH3进气浓度50.15~525.4 mg/m3,H2S进气浓度10.23~110.36 mg/m3时,NH3单一进气去除率稳定在99%以上,H2S单一进气去除率90%以上。混合进气后,NH3去除率几乎为100%,H2S的去除率提高至98%以上。在一定的浓度范围内,NH3和H2S之间的相互作用对两者的去除效果没有明显的影响,而且起到了相互促进降解的作用。同时,进气流量和填料层高度都会影响NH3、H2S的去除率。系统对进气容积负荷变化的缓冲能力强,在偶尔超负荷条件下运行并不能使系统崩溃,并且微生物对高负荷逐渐表现出适应性。大部分溶于水的氨由生物曝气池去除,去除率达到96.9%。     

微包埋恶臭假单胞菌复合填料制备及性能评价

填料是废气生物净化系统的核心组件,对净化性能有直接影响。以聚乙烯醇、海藻酸钠、腐熟植物纤维等为辅料,采用微包埋法制备出一种包埋恶臭假单胞菌复合填料,并将其装填于生物过滤塔中评价其对甲苯的净化性能。结果表明,制备的复合填料性能稳定、启动速度快、适宜微生物生长,对甲苯有较好的净化效果。生物过滤塔在空床停留时间47 s、进气负荷不高于42.00 g·(m3·h)-1的条件下,去除率可达90%以上。系统停运3 d和7 d,重新启动1 h后,去除率即可恢复至80%以上。动力学研究显示,与Michaelis-Menten模型相比,Haldane模型对使用该复合填料的生物净化过程拟合度较高。制备的复合填料理化性能好,对甲苯具有较高的净化效果,具有一定的应用前景。     

Biofiltration of gasoline vapor by compost media

Gasoline vapor was treated using a compost biofilter operated in upflow mode over 4 months. The gas velocity was 6 m/h, yielding an empty bed retention time (EBRT) of 10 min. Benzene, toluene, ethylbenzene and xylene (BTEX) and total petroleum hydrocarbon (TPH) removal efficiencies remained fairly stable approximately 15 days after biofilter start-up. The average removal efficiencies of TPH and BTEX were 80 and 85%, respectively, during 4 months of stable operation. Biodegradation portions of the treated TPH and BTEX were 60 and 64%, respectively. When the influent concentration of TPH was less than 7800 mg TPH/m3, approximately 50% of TPH in the gas stream was removed in the lower half of the biofilter. When the influent concentration of BTEX was less than 720 mg BTEX/m3, over 75% of BTEX in the gas stream was removed in the lower half of the biofilter. Benzene removal efficiency was the lowest among BTEX. A pressure drop could not be detected over a 1-m bed height at a gas velocity of 6 m/h after approximately 4 months of operation. Results demonstrated that BTEX in gasoline vapor could be treated effectively using a compost biofilter.     

Treatment of N,N-dimethylacetamide waste gas by a trickle-bed air biofilter.

The system performance of a trickle-bed air biofilter (TBAB) for treating N,N-dimethylacetamide (DMAC) waste gas was investigated under different gas flow rates and influent concentrations. In the pseudo-steady-state conditions, the DMAC elimination capacity increased but the removal efficiency decreased as the influent loading increased. More than 90% and 80% DMAC removal efficiencies are achieved for influent loadings below 20.2 and 34.5 g DMAC/m3/h, respectively. The TBAB appears to be an effective treatment process for controlling DMAC emission with low-to-medium loadings and the effectiveness could be maintained over a long-period operation.     

Treatment of 1,3-Butadiene in an Air Stream by a Biotrickling Filter and a Biofilter

ABSTRACT

This paper presents results obtained from a performance study on the biotreatment of 1,3-butadiene in an air stream using a reactor that consisted of a two-stage, in-series biotrickling filter connected with a three-stage, in-series biofilter. Slags and pig manure-based media were used as packing materials for the biotrickling filter and the biofilter, respectively. Experimental results indicated that, for the biotrickling filter portion, the butadiene elimination capacities were below 5 g/m³/hr for loadings of less than 25 g/m³/hr, and the butadiene removal efficiency was only around 17%. For the biofilter portion, the elimination capacities ranged from 10 to 107 g/m³/hr for loadings of less than 148 g/m³/hr. The average butadiene removal efficiency was 75–84% for superficial gas velocities of 53–142 m/hr and a loading range of 10–120 g/m³/hr. The elimination capacity approached a maximum of 108 g/m³/hr for a loading of 150 g/m³/hr. The elimination rates of butadiene in both the biotrickling filter and biofilter were mass-transfer controlled for influent butadiene concentrations below about 600 ppm for superficial gas velocities of 29–142 m/hr. The elimination capacity was significantly higher in the biofilter than in the biotrickling filter. This discrepancy may be attributed to the higher mass-transfer coefficient and gas-solid interfacial area offered for transferring the gaseous butadiene in the biofilter.     

Microbial degradation of livestock-generated ammonia using biofilters at typical ambient temperatures

The purpose of this research was to neutralize livestock-generated ammonia by using biofilters packed with inexpensive inorganic and organic packing material combined with multicultural microbial load at typical ambient temperatures. Peat and inorganic supporting materials were used as biofiltration matrix packed in a perfusion column through which gas was transfused. Results show the ammonia removal significantly fell in between 99 and 100% when ammonia concentration of 200 ppmv was used at different gas flow rates ranged from 0.030 to 0.060 m3 h(-1) at a fluctuating room temperature of 27.5 +/- 4.5 C (Mean +/- SD). Under these conditions, the emission concentration of ammonia that is liberated after biofiltration is less than 1 ppmv (0.707 mg m(-3)) over the period of our study, suggesting the usage of low-cost biofiltration systems for long-term function is effective at wider ranges of temperature fluctuations. The maximum (100%) ammonia removal efficiency was obtained in this biofilter was having an elimination capacity of 2.217 g m(-3) h(-1). This biofilter had high nitrification efficiencies and hence controlled ammonia levels with the reduced backpressure. The response of this biofilter to shut down and start up operation showed that the biofilm has a superior stability.     

闽南地区低温下复合填料强化生物滤柱除臭及微生物分析

通过搭建复合填料-生物滤柱反应装置,在厦门冬季低温环境下开展复合填料（蜂窝煤渣、活性炭、蜂窝沸石和陶粒）强化生物滤柱除臭研究,分析了除臭微生物群落组成特性。复合填料-生物滤柱装置在启动运行15 d时其COD去除率达到85%以上且保持稳定,对H₂S和NH₃的最大去除率可分别达到91.77%和82.53%,表明挂膜成功。菌群分析结果表明：以H₂S、NH₃等臭气喷淋液为基质的生物滤柱驯化挂膜过程会降低微生物的丰度和多样性;菌属Thiothrix、Ferruginibacter、Burkholderiaceae、Tahibacter、Dinghuibacter、Cloacibacterium和Kosakonia是除臭过程的优势功能微生物和臭气成分降解的贡献者。本研究阐明了复合填料生物膜内功能菌属对H₂S、NH₃等臭气喷淋液有机质的生物降解/转化机制,并进行了物料平衡分析;复合填料-生物滤柱装置对H₂S与NH₃的平均去除率分别达到90.77%和72.53%,具有良好的生物除臭效果与运行稳定性。本研究可为南方低温季节的污水臭气治理提供技术参考和理论支撑。     

Optimizing nutrient supply in a rotatory-switching biofilter for toluene vapor treatment

The influence of nutrient conditions on the degradation of toluene vapor in a rotatory-switching biofilter (RSB) was investigated. The biofilter consists of four segments connected in series, each with a packing layer made of polyvinyl formal. The influent airstreams including toluene vapors were passed through segments 1-3 as up-flow with a toluene concentration of 0.9-1.2 g m(-3) and with an empty-bed retention time of 26-52 sec. Nutrient solutions were fed to all packed segments once a day by means of immersion. The nutrient solution was used repeatedly and replenished by the addition of (NH4)2SO4. The result at 155 days showed nitrogen depletion was particularly obvious and the lack of nitrogen affected toluene removal. By adding 161 g of nitrogen solution per volumetric cubic meter of reactor, toluene removal efficiency was immediately increased to greater than 99%. With long-term biofilter operation, 21%-32% of ammonium was utilized for nitrification because of the growth of nitrifying bacteria such as Nitrosomonas sp. Based on the carbon-nitrogen balance, the daily nitrogen demand for toluene removal was estimated 2.1 g day(-1) at a toluene load of 70 g m(-3) hr(-1).     

Performance of an immobilized cell biofilter for ammonia removal from contaminated air stream

The performance of a lab scale biofilter packed with biomedia, encapsulated by sodium alginate and polyvinyl alcohol was used for treating ammonia (NH(3)) gas at different loading rates. The metabolic end products during NH(3) oxidation were NH(4)(+), NO(3)(-) and NO(2)(-). It is noteworthy to mention that the immobilized cell biofilter required no separate acclimatization period and showed high removal efficiencies during the start of continuous experiments. The removal efficiency was nearly 100% when ammonia loading was 4.5gm(-3)h(-1) and the maximum elimination capacity achieved in this study was 5.5gNH(3)m(-3)h(-1) at a loading rate of 7.5gm(-3)h(-1). Shock loading studies were carried out to ascertain the response of the immobilized cells to fluctuations in inlet concentration and flow rate. The inlet loading rates were varied between 0.05 and 6gNH(3)m(-3)h(-1) during this phase of operation. The biofilter responded effectively to these shock loading conditions and recovered rapidly within 4-8h. Pressure drop values were consistently less and insignificant. The results from this study indicated that this immobilized cell biofilter could be considered as a potential option to treat NH(3) under steady and transient state operation.     

IC厌氧反应器处理垃圾渗滤液

在(35±1)℃条件下,采用IC厌氧反应器对天津大港垃圾焚烧厂垃圾渗滤液进行处理,研究了COD的去除效果、容积负荷、沼气产量和污泥的颗粒化,分析了循环比、上升流速对反应器的影响.结果表明,厌氧反应器经60 d的启动运行后,达到300 m3/d的设计水量,进水容积负荷达到17.7 kg COD/(m3·d),水力停留时间3.7 d,COD去除率高于80%,出水挥发酸(VFA)低于1 500 mg/L,平均每去除1 kg COD 产沼气0.42 m3,适宜的上升流速和循环比为2.0~5.0 m/h、8:1~20:1.启动结束后,厌氧消化污泥明显出现颗粒化,颗粒污泥的沉降速度达到了67.5~96.0 m/h,0.3~1.0 mm的颗粒污泥量占有74%.