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。     

生物法同时脱硫脱硝试验研究

采用轻质陶粒生物滴滤塔处理摸拟燃煤烟气中二氧化硫和氮氧化物的试验研究，探讨生物法同时脱硫脱硝的影响因素及生物降解宏观动力学。研究结果表明，生物法能有效同时去除烟气中的二氧化硫和氮氧化物，烟气同时脱硫脱硝效率分别可达99.9%和88.9%。为获得最佳烟气同时脱硫脱硝效果，二氧化硫和氮氧化物进气负荷应分别＜140 g/（m³·h）和20 g/（m³·h），循环液pH=7～8，空床停留时间为30.28 s，喷淋密度为8.81 L/（m³·h）。     

以焦炭为填料的生物滴滤塔处理含挥发性脂肪酸臭气

在以焦炭为填料的生物滴滤塔对挥发性脂肪酸臭气的处理研究中考察了空床停留时间、臭气浓度、体积负荷以及进气温度等参数对净化效果的影响。结果表明，空床停留时间较长时对臭气降解有利。在停留时间超过97 s时，能实现完全降解；此外，净化率随臭气浓度和体积负荷的不断增加呈先增加后降低的趋势。当臭气浓度为24.29 mg/m³即臭气的体积负荷为3 g/（m³·h）时，去除率约为96%；当臭气浓度增至1 345.74 mg/m³即体积负荷增至18 g/（m³·h），去除率达100%；然而，当臭气浓度增至4 934.38 mg/m³即体积负荷增至66 g/（m³·h）时，去除率降至73.1%。另外，进气温度对净化率也有一定程度影响。当进气温度较低时，净化效率相对较高。     

一种包埋微生物复合填料的制备及性能评价简

采用包埋法制备出一种复合生物填料，测其各项理化性质，并以NO_x模拟废气验证其脱硝性能。填料主要由碳酸钙、牛粪堆肥腐殖质、菌剂载体、水泥、轻质珍珠岩、立体网状纤维及脱硝功能微生物等复合而成，粒径12 mm×20 mm，自然堆积密度（471±0.8）kg/m³，持水量（49±1.3）%，比表面积3.91 m²/g，平均机械强度（427.3±0.2）N，pH为10.5±0.2。填料能长期在潮湿环境中保持良好的粘结强度，并具有营养缓释及pH缓冲能力。包埋脱硝功能微生物复合填料中初期微生物数量5.3 ×10⁵ CFU/g，运行60 d后微生物数量达到8.6×10⁸ CFU/g，闲置停运30 d微生物有所减少，但重启后净化效率基本不变。当进气负荷低于1 878 mg/（m³·h），气体停留时间为14.47 s时，BF₁的去除率高达93.15%。     

基于甘蔗渣的生物过滤器长期运行研究

用甘蔗渣和蘑菇堆肥作为生物过滤器的填料,去除空气中的甲苯。生物过滤器长期连续运行,在无营养液和pH缓冲剂加入的条件下,研究了生物过滤器中填料含水量和pH的变化以及甲苯去除效率的变化规律,并对填料中的微生物菌属进行了初步鉴定。运行6个月后,填料含水量从56%降到约20%,pH从7.4降至4.5。生物过滤器可以保持4个月的...     

焦化废水深度处理试验研究

采用BC法＋复合过滤技术工艺对焦化废水生化出水进行深度处理试验。结果表明，在SE混凝剂投药量为30 mg/L、BC池停留时间为1.5 h、复合过滤器水力负荷为2.4 m³/（m²·h）的条件下，当深度处理进水水质为COD＝196.1 mg/L、色度＝120倍、NH₃-N＝35.1 mg/L时，其去除率分别为74.7%、86.7%和69.7%，出水可达回用水要求。     

炭纤维载体固定床厌氧发酵启动运行效果实验

以开发高效率、抗冲击性能强的高浓度有机废水沼气发酵技术为目的，用传统的 UASB反应器作为对照，研究了以炭纤维为生物膜载体的固定床厌氧反应器的启动运行效果。反应器进口废水 COD 为 5 000 mg/L, 水力停留时间 (HRT) 由213 h 逐步缩短为35 h，进水有机容积负荷(OLR)由0.56 kg COD/ (m³·d)提到3.45 kg COD/(m³·d)。结果表明，固定床反应器厌氧发酵的效率比对照高，出水 pH 值也比对照稳定；运行到第 50 d 时，固定床厌氧反应器和对照的 COD去除率分别由第 7 d 的36.56%和33.58%上升到87.9%和62.6%；固定床厌氧反应器的容积比产气率最高为1.16 m³/(m³·d)，累计产气量为415.59 L，而对照的容积比产气率最高值仅为0.31 m³ /(m³·d)，累计产气量为 71.66 L，前者最高容积比产气率和累计产气量分别是后者的3.74倍和5.78倍。固定床厌氧反应器的启动速度、COD 去除率和产甲烷效率显著地高于对照反应器。     

固定化假单胞菌降解油烟废气的研究

将从受油烟废气污染严重的土壤中分离筛选的具有较强降解油烟能力的假单胞菌利用活性炭为填料吸附固定后制成填料床生物反应器。实验考察了进气浓度、气体流量、气体停留时间、容积负荷等对油烟去除率的影响，初步研究了生物反应器的抗冲击能力。结果表明，活性炭填料对菌体具有良好的吸附能力，当油烟进气浓度小于100 mg/L，气体流速小于8 L/h，停留时间大于30 s，容积负荷为2.6～18.9 g油烟废气/(m³·h)，生物反应器的降解效率可达到95%以上，且活性炭填料床反应器具有较强的抗冲击能力。     

BAF处理生活污水过程中同步去除H2S的试验研究

采用曝气生物滤池处理生活污水的过程中，以混和臭气的空气为气源，以掺入了陶粒和铁炭颗粒的复合填料为载体，研究了反应器的运行条件和参数，结果表明，以混合臭气的空气作为气源对污水处理过程的需氧量基本无影响。当反应器的进气量为40 L/h，进水容积负荷和进气H2S的浓度分别在0.3～1.6 kg COD/(m³·d)和0.8～2.3 mg/m³之间变化时，可以实现出气和出水中H₂S和COD分别小于0.04 mg/m³和90 mg/L，满足同时达标排放的要求。H₂S的同步去除可能是通过微生物的氧化分解和形成FeS沉淀来实现的。     

改进型升流式固体反应器处理猪粪污新工艺研究

对传统升流式固体反应器（USR）进行改进，反应器内设置专用搅拌器，搅拌器间歇开启，在保留USR各项优势的前提下，使料液与厌氧微生物接触更充分，反应温度更均匀，提高产气率，同时还解决了传统USR的“结壳”问题，提高了反应器的传质效率、甲烷产气率和COD去除效果。进料含固量在12.1%时，水利停留时间为17 d，反应器最高容积负荷达到4.9 kg COD/(m³·d)，产气速率为2.55 m³/(m³·d)，产气率达到0.359 m³/kg干猪粪。     

Backfitting Electrostatic Precipitators: Gas Velocity and Reliability Considerations

Abstract

The kinetic behavior of the toluene biofiltration process was investigated in this research. Toluene was used as a model compound for less water-soluble gas pollutants. The limiting factor in the overall toluene biofiltration process was determined by analyzing the effectiveness factor of the biofilm along the biofilter. Experiments were conducted in three laboratory-scale biofilters packed with mixtures of chaff/compost, D.E. (diatomaceous earth)/compost and GAC (granular activated carbon)/compost, respectively. A mathematical model previously proposed was verified in this study as being applicable to these biofilters packed with different filter materials. Both the experimental and theoretical results confirmed that the biodegradation rate along the biofilter followed the zero order, fractional order to first order kinetics as toluene concentration decreased. Moreover, at higher toluene concentration, biodegradation rate and mass flux of toluene were lower near the bottom of the biofilter due to substrate inhibition. Analysis of the effectiveness factor indicated that biofiltration of a less soluble compound such as toluene should not be operated at high gas flow rates (low gas residence times) due to the mass transfer limitation of such a system. At an approximate constant inlet toluene concentration of 0.9 g/m³, the toluene removal efficiency in these three biofilters would drop below 90% when the gas residence time decreased to 2.5, 2.5, and 2.0 min, respectively.     

Effect of temperature and dissolved oxygen on the growth kinetics of Pseudomonas putida F1 growing on benzene and toluene

Batch experiments were conducted to determine the effect of temperature and dissolved oxygen concentration on the rates of growth and substrate (benzene and toluene) degradation by the toluene degrading strain, Pseudomonas putida F1. Over a range of temperature from 15 to 35 degrees C the maximum specific growth rate followed the Topiwala-Sinclair relationship when either benzene or toluene served as the sole carbon and energy source. Oxygen limited growth followed Monod saturation kinetics with the specific growth rate given as a function of the dissolved oxygen concentration. The oxygen half-saturation coefficient was found to be approximately 1 mg/l regardless of whether benzene or toluene was the substrate. Similar experiments with Burkholderia (Ralstonia) pickettii PKO1 for grown on toluene revealed an oxygen half-saturation coefficient of 0.7 mg/l.     

Degradation characteristics of toluene,benzene, ethylbenzene,and xylene by Stenotrophomonas maltophilia T3-c

Stenotrophomonas maltophilia T3-c, isolated from a biofilter for the removal of benzene, toluene, ethylbenzene, and xylene (BTEX), could grow in a mineral salt medium containing toluene, benzene, or ethylbenzene as the sole source of carbon. The effect of environmental factors such as initial toluene mass, medium pH, and temperature on the degradation rate of toluene was investigated. The cosubstrate interactions in the BTEX mixture by the isolate were also studied. Within the range of initial toluene mass (from 23 to 70 pmol), an increased substrate concentration increased the specific degradation of toluene by S. maltophilia T3-c. The toluene degradation activity of S. maltophilia T3-c could be maintained at a broad pH range from 5 to 8. The rates at 20 and 40 degrees C were 43 and 83%, respectively, of the rate at 30 degrees C. The specific degradation rates of toluene, benzene, and ethylbenzene by strain T3-c were 2.38, 4.25, and 2.06 micromol/g-DCW/hr. While xylene could not be utilized as a growth substrate by S. maltophilia T3-c, the presence of toluene resulted in the cometabolic degradation of xylene. The specific degradation rate of toluene was increased by the presence of benzene, ethylbenzene, or xylene in binary mixtures. The presence of toluene or xylene in binary mixtures with benzene increased the specific degradation rate of benzene. The presence of ethylbenzene in binary mixtures with benzene inhibited benzene degradation. The presence of more than three kinds of substrates inhibited the specific degradation rate of benzene. All BTEX mixtures, except tri-mixtures of benzene, ethylbenzene, and xylene or mixtures of all four substrates, had little effect on the degradation of ethylbenzene by S. maltophilia T3-c. The utilization preference of the substrates by S. maltophilia T3-c was as follows: ethylbenzene was degraded fastest, followed by toluene and benzene. However, the specific degradation rates of substrates, in order, were benzene, toluene, and ethylbenzene.     

Characteristics of photocatalytic oxidation of toluene, benzene, and their mixture

The investigation of the photocatalytic oxidation (PCO) of multicomponent volatile organic compounds (VOCs) is very important to the application of PCO technology, because there is seldom a single VOC component in indoor air. In this paper, the characteristics of binary indoor VOCs, toluene and benzene, were experimentally studied using a mass transfer based method that we developed. The concentration ranges for toluene and benzene were 4.48-27.4 mg/m3 and 1.82-4.08 mg/m3, respectively. We found the following: (1) the PCO of each individual contaminant studied obeys the unimolecular form of the Langmuir-Hinshelwood (L-H) rate form; (2) the PCO of the binary contaminants follow the competitive adsorption L-H rate form; (3) the reaction-coefficient for PCO of individual contaminants differs from that in the competitive adsorption L-H rate form; and (4) the component impact factor of A to B, put forward in this paper, is a useful parameter describing the influence of A on the reaction coefficient of B, and it was found that the impact factor of toluene (a chemically active component) on benzene (a chemically stable component) is high, and the impact factor of benzene on toluene is low.     

Effects of Air-Fuel Ratio on Composition of Hydrocarbon Exhaust from Toluene,Toluene-n Heptane Mixture and Isooctane

This study describes the variations in the chemical composition of the exhaust at various air-fuel ratios when toluene, toluene-n-heptane mixture, and isooctane are used as fuels in a Labeco single cylinder engine. The exhaust products from toluene are divided into three groups: those which decrease as the equivalence ratio is increased: toluene, benzene, methane, and dimethylacetylene; those which increase with increasing equivalence ratio: benzaldehyde, and products which exhibit a maximum at an equivalence ratio of 1, then decrease: acetylene, ethyl acetylene, ethyl benzene, and styrene. Combustion of the mixture of 25 volume percent n-heptane in toluene reveals interesting information, compared to emissions from pure toluene: concentrations of ethyl benzene, styrene, and dimethylacetylene surprisingly are increased by factors of 1.9, 1.9, and 2.1 respectively, probably because reactive radicals derived from heptane interact with toluene to form unsaturated molecules. Ethyl acetylene, benzene, and benzaldehyde remained unchanged but the fractional mole concentration of unreacted toluene decreased. These results show that fuels rich in aromatics may produce less unsaturates than when diluted with aliphatic fuels. For isooctane fuel, methane, and isooctane in the exhaust decrease as the equivalence ratio is increased, while isobutylene, propylene, ethylene, and propadiene concentrations exhibit maxima at an equivalence ratio of 1.     

Ammonia emissions from the composting of different organic wastes. Dependency on process temperature

Ammonia emissions were quantified for the laboratory-scale composting of three typical organic wastes with medium nitrogen content: organic fraction of municipal solid wastes, raw sludge and anaerobically digested sludge; and the composting of two wastes with high nitrogen content: animal by-products from slaughterhouses and partially hydrolysed hair from the leather industry. All the wastes were mixed with the proper amount of bulking agent. Ammonia emitted in the composting of the five wastes investigated revealed a strong dependence on temperature, with a distinct pattern found in ammonia emissions for each waste in the thermophilic first stage of composting (exponential increase of ammonia emitted when increasing temperature) than that of the mesophilic final stage (linear increase of ammonia emissions when increasing temperature). As composting needs high temperatures to ensure the sanitisation of compost and ammonia emissions are one of the main environmental impacts associated to composting and responsible for obtaining compost with a low agronomical quality, it is proposed that sanitisation is conducted after the first stage in large-scale composting facilities by a proper temperature control. CAPSULE: Ammonia emission pattern and correlation with process temperature are presented for the composting process of different organic wastes.     

Comparison of the effect of biodiesel-diesel and ethanol-diesel on the gaseous emission of a direct-injection diesel engine

Experiments were conducted on a 4-cylinder direct-injection diesel engine using ultralow sulfur diesel blended with biodiesel and ethanol to investigate the gaseous emissions of the engine under five engine loads at the maximum torque engine speed of 1800 rev min^?1. Four biodiesel blended fuels and four ethanol blended fuels with oxygen concentrations of 2%, 4%, 6% and 8% were used. With the increase of oxygen content in the blended fuels, the brake thermal efficiency improves slightly.For the diesel-biodiesel fuels, the brake specific HC and CO emissions decrease while the brake specific NO_x and NO₂ emissions increase. The emissions of formaldehyde, 1,3-butadiene, toluene, xylene and overall BTX (benzene, toluene, xylene) in general decrease, however, acetaldehyde and benzene emissions increase. For the diesel-ethanol fuels, the brake specific HC and CO emissions increase significantly at low engine load, NO_x emission decreases at low engine load but increases at high engine load. The emissions of benzene and BTX vary with engine load and ethanol content. Similar to the biodiesel-diesel fuels, the formaldehyde, 1,3-butadiene, toluene and xylene emissions decrease while the acetaldehyde and NO₂ emissions increase. Despite having the same oxygen contents in the blended fuels, there are significant differences in the gaseous emissions between the biodiesel-diesel blends and the ethanol-diesel blends.     

Effect of bulking agents on maturity and gaseous emissions during kitchen waste composting

This study investigated the effect of bulking agents on the maturity and gaseous emissions of composting kitchen waste. Three different bulking agents (cornstalks, sawdust, and spent mushroom substrate) were used to compost kitchen waste under aerobic conditions in 60-L reactors for a 28-d period. A control treatment was also studied using kitchen waste without a bulking agent. During the experiment, maturity indexes such as temperature, pH value, C/N ratio, and germination index were determined, and continuous measurements of leachate and gaseous emissions (CH₄, N₂O, and NH₃) were taken. The results showed that all of the composts with bulking agents reached the required maturity standard, and the addition of spent mushroom substrate gave the highest maturity (C/N ratio decreased from 23 to 16 and germination index increased from 53% to 111%). The bulking agents also reduced leachate production and CH₄ and N₂O emissions, but had little impact on NH₃ emissions. Composting with sawdust as a bulking agent was found to emit less total greenhouse gas (33 kg CO₂-eq t⁻¹ dry matter) than the other treatments.     

污泥含炭吸附剂对挥发性有机废气吸附实验研究

研究了污泥含炭吸附剂对挥发性有机污染物的吸附特性。结果表明,污泥含炭吸附剂对苯系物的吸附为典型的物理吸附,其吸附甲苯等温线的类型系优惠型吸附等温线,表明具有良好的吸附能力;在吸附反应温度为20℃,气体流量为500 mL/m in(停留时间为0.424 s),甲苯浓度为2 700 mg/m3时,甲苯的饱和吸附容量为150.0 mg/g;同时,研究表明污泥含炭吸附剂对苯系物的饱和吸附容量和吸附强弱次序为二甲苯甲苯苯。结果表明污泥含炭吸附剂适合对中低浓度有机废气的吸附净化。     

Characterization of compost biofiltration media.

The effect of compost quality on performance of biofiltration media was investigated. Three types of compost media were characterized in terms of their key properties, including pH, total organic carbon (TOC) and nitrogen, moisture content, oxygen uptake rates and heterotrophic and fungal plate counts. Laboratory-scale biofilter columns were each filled with a different compost medium mixed with buffer and a bulking agent. The columns were operated with a volatile organic compound (VOC) mixture consisting of ethyl alcohol, butyraldehyde, ethyl acetate, and 1,1-diethoxybutane and subjected to various operating conditions. After 13 months, the columns were sampled and post-characterization of the media was performed. A mixture of biosolids/horse manure compost, which had a high initial microbial activity, had the shortest acclimation period. Best overall performance, however, was observed with yard waste compost, which was the most stable medium. Media hydrophobicity was a key factor in long-term performance. Significant changes in compost structure, moisture content, pH, volatile solids, oxygen uptake rates, and microbial population densities were observed over the course of the study. Analyses of organic nitrogen content showed that significant amounts of nitrogen were not depleted from the media.