Continuous biohydrogen production from diluted molasses in an anaerobic contact reactor

An anaerobic contact reactor (ACR) system comprising a continuous flow stirred tank reactor (CSTR) with settler to decouple the hydraulic retention time (HRT) from solids retention time (SRT) was developed for fermentative hydrogen production from diluted molasses by mixed microbial cultures. The ACR was operated at various volumetric loading rates (VLRs) of 20–44 kgCOD·m⁻³·d⁻¹ with constant HRT of 6 h under mesophilic conditions of 35°C. The SRT was maintained at about 46–50 h in the system. At the initial VLR of 20 kgCOD·m⁻³·d⁻¹, the hydrogen production rate dropped from 22.6 to 1.58 L·d⁻¹ as the hydrogen was consumed by the hydrogentrophic methanogen. After increasing the VLR to 28 kgCOD·m⁻³·d⁻¹ and discharging the sludge for 6 consecutive times, the hydrogentrophic methanogens were eliminated, and the hydrogen content reached 36.4%. As the VLR was increased to 44 kgCOD·m⁻³·d⁻¹, the hydrogen production rate and hydrogen yield increased to 42.1 L·d⁻¹ and 1.40 mol H₂·molglucose-consumed-1, respectively. The results showed that a stable ethanoltype fermentation that favored hydrogen production in the reactor was thus established with the sludge loading rate (SLR) of 2.0–2.5 kgCOD·kgMLVSS⁻¹·d⁻¹. It was found that the ethanol increased more than other liquid fermentation products, and the ethanol/acetic acid (mol/mol) ratio increased from 1.27 to 2.45 when the VLR increased from 28 to 44 kgCOD·m⁻³·d⁻¹, whereas the hydrogen composition decreased from 40.4% to 36.4%. The results suggested that the anaerobic contact reactor was a promising bioprocess for fermentative hydrogen production.     

Relationships between loading rates and nitrogen removal effectiveness in subsurface flow constructed wetlands

Nitrogen removal of wetlands under 40 different inflow loadings were studied in the field during 15 months. The removal efficiency of four different sets of beds, namely the reed bed, the Zizania caduciflor bed, the mixing planting bed, and the control bed were studied. The outflow loading and total nitrogen (TN) removal rate of these beds under different inflow loadings and pollution loadings were investigated. The inflow loadings of 4 subsurface flow systems (SFS) ranged from 400 to 8000 mg·(m²·d)⁻¹, while outflow loadings were less than 7000 mg·(m²·d)⁻¹. The results showed that the inflow and outflow loading of TN removal rate in SFS presented an obvious linear relationship. The optical inflow loading to run the system was between 2000 to 4000 mg·(m²·d)⁻¹. Average removal rate was between 1062 and 2007 mg·(m²·d)⁻¹. SFS with plant had a better removal rate than the control. TN removal rates of the reed and Zizania caduciflora bed were 63% and 27% higher than the control bed, respectively. The results regarding the TN absorption of plants indicated that the absorption amount was very limited, less than 5% of the total removal. It proved that plants clearly increase TN removal rates by improving the water flow, and increasing the biomass, as well as activities of microorganisms around the roots. The research provided a perspective for understanding the TN removal mechanism and design for SFS. __________ Translated from Environmental Science, 2006, 27(2): 253–256 [译自: 环境科学]     

Influence of aeration intensity on the performance of A/O-type sequencing batch MBR system treating azo dye wastewater

Among the numerous parameters affecting the membrane bioreactor (MBR) performance, the aeration intensity is one of the most important factors. In the present investigation, an anoxic/aerobic-type (A/O-type) sequencing batch MBR system, added anoxic process as a pretreatment to improve the biodegradability of azo dye wastewater, was investigated under different aeration intensities and the impact of the aeration intensity on effluent quantity, sludge properties, extracellular polymeric substances (EPS) amount generated as well as the change of permeation flux were examined. Neither lower nor higher aeration intensities could improve A/O-type sequencing batch MBR performances. The results showed 0.15 m³·h⁻¹ aeration intensity was promising for treatment of azo dye wastewater under the conditions examined. Under this aeration intensity, chemical oxygen demand (COD), ammonium nitrogen and color removal as well as membrane flux amounted to 97.8%, 96.5%, 98.7% and 6.21 L·m⁻²·h⁻¹, respectively. The effluent quality, with 25.0 mg·L⁻¹COD, 0.84 mg·L⁻¹ ammonium nitrogen and 8 chroma, could directly meet the reuse standard in China. In the meantime, the sludge relative hydrophobicity, the bound EPS, soluble EPS and EPS amounts contained in the membrane fouling layer were 70.3%, 52.0 mg·g⁻¹VSS, 38.8 mg·g⁻¹VSS and 90.8 mg·g⁻¹VSS, respectively, which showed close relationships to both pollutant removals and membrane flux.     

Dilution sampling and analysis of particulate matter in biomass-derived syngas

Thermochemical biomass gasification, followed by conversion of the produced syngas to fuels and electrical power, is a promising energy alternative. Real-world characterization of particulate matter (PM) and other contaminants in the syngas is important to minimize damage and ensure efficient operation of the engines it powers and the fuels created from it. A dilution sampling system is demonstrated to quantify PM in syngas generated from two gasification plants utilizing different biomass feedstocks: a BioMax?15 Biopower System that uses raw and torrefied woodchips as feedstocks, and an integrated biorefinery (IBR) that uses rice hulls and woodchips as feedstocks. PM_2.5 mass concentrations in syngas from the IBR downstream of the purification system were 12.8–13.7 μg·m⁻³, which were significantly lower than the maximum level for catalyst protection (500 μg·m⁻³) and were 2–3 orders of magnitude lower than those in BioMax?15 syngas (2247–4835 μg·m⁻³). Ultrafine particle number concentration and PM_2.5 chemical constituents were also much lower in the IBR syngas than in the BioMax?15. The dilution sampling system enabled reliable measurements over a wide range of concentrations: the use of high sensitivity instruments allowed measurement at very low concentrations (∼1 μg·m⁻³), while the flexibility of dilution minimized sampling problems that are commonly encountered due to high levels of tars in raw syngas (∼1 g·m⁻³).     

Magnetic properties of the microorganism Candidatus Magnetoglobus multicellularis

Magnetotactic microorganisms use the interaction of internal biomineralized nanoparticles with the geomagnetic field to orientate. The movement of the magnetotactic multicellular prokaryote Candidatus Magnetoglobus multicellularis under an applied magnetic field was observed. A method using digital image processing techniques was used to track the organism trajectory to simultaneously obtain its body radius, velocity, U-turn diameter, and the reorientation time. The magnetic moment was calculated using a self-consistent method. The distribution of magnetic moments and radii present two well-characterized peaks at (9 ± 2) × 10⁻¹⁵ and (20 ± 3) × 10⁻¹⁵ A m² and (3.6 ± 0.1) and (4.3 ± 0.1) μm, respectively. For the first time, simultaneous determination of the distribution of the organism radii and magnetic moment was obtained from the U-turn method by a new digital imaging processing. The bimodal distributions support an organism reproduction process model based on electron microscopy observations. These results corroborate the prokaryote multicellular hypothesis for Candidatus M. multicellularis.     

以能量方法研究紫外辐射在大气中的传输

2004年9月～2006年10月,在华北地区4个站点开展了太阳辐射、气象参数等综合观测,得到了紫外辐射UV、总辐射Q等的变化特征.水汽和散射因子对于UV/Q和UV有明显影响.建立了实际天气UV小时累计值(时累)的经验模式,得到了较好的计算结果.水汽因子对于UV在大气中的传输有一定的作用,应给予重视.计算表明,华北地区受水汽因子衰减到达地面的UV以及占地面UV的比例分别为15.00W.m-2和37.45%,受散射因子衰减到达地面的UV以及占地面UV的比例分别为23.89W.m-2和62.55%.华北地区受水汽因子和散射因子影响损失于大气中的UV分别为19.30、35.31W.m-2,这一能量损失表现出明显的季节变化和地区差异.敏感性实验表明,地表UV对于水汽和散射因子的变化有不同的响应,UV对散射因子的变化比对水汽因子的变化更敏感.水汽因子与UV之间的关系与水密切相关,水汽项的真正含义是大气中各种物质成分(气、液、固态)对于UV的直接吸收和间接利用(通过化学和光化学反应,包括均相和非均相过程)的总和.利用经验模式计算了大气顶的UV,计算误差为+7.83%.未来研究中应重视和考虑消耗于大气且与水汽有关的这部分能量.以能量观点分析实测资料并研究大气中的物理化学过程是一种行之有效的方法.     

Copper and zinc interaction on water clearance and tissue metal distribution in the freshwater mussel, Cristaria plicata, under laboratory conditions

Copper and zinc interaction on clearance from water and distribution in different tissues was investigated for the freshwater mussel, Cristaria plicata, under laboratory conditions. Clearance rate of Cu or Zn from water was highly dependent on exposure concentration. Interaction effect was most evident at 300 μg·L⁻¹ Cu exposure and depressed the Zn clearance rate significantly (p<0.05). However, the presence of 100 μg·L⁻¹ and 300 μg·L⁻¹ Zn hardly affected the Cu clearance rate. The 300 μg·L⁻¹ Cu presence enhanced Cu accumulation in each tissue most significantly (p<0.01), but caused Zn content to decrease in the gills by 62% (p<0.05), viscera by 49% (p<0.05) and foot by 31% (p<0.05), and increase in the mantle by 97% (p<0.05) and the muscles by 243% (p<0.05) for different Zn exposure treatments. The response of metal accumulation in various tissues of the test mussels indicated that Zn transferred from the gills, viscera and foot to the mantle and muscles might be one of the important characteristics of the Zn regulatory mechanism by leading to a narrow range of Zn concentration in the different tissues.     

Nitrifying population dynamics in a redox stratified membrane biofilm reactor (RSMBR) for treating ammonium-rich wastewater

Nitrogen removal performance and nitrifying population dynamics were investigated in a redox stratified membrane biofilm reactor (RSMBR) under oxygen limited condition to treat ammonium-rich wastewater. When the NHt₄⁺-N loading rate increased from 11.1±1.0 to 37:2 ± 3:2 gNHt₄⁺-N·m⁻²·d⁻¹, the nitrogen removal in the RSMBR system increased from 18.0±9.6 mgN·d⁻¹ to 128.9±61.7 mgN·d⁻¹. Shortcut nitrogen removal was achieved with nitrite accumulation of about 22:3 ± 5:3 mgNO₂⁻-N·L⁻¹. Confocal micrographs showed the stratified distributions of nitrifiers and denitrifiers in the membrane aerated biofilms (MABs) at day 120, i.e., ammonia and nitrite oxidizing bacteria (AOB and NOB) were dominant in the region adjacent to the membrane, while heterotrophic bacteria propagated at the top of the biofilm. Real-time qPCR results showed that the abundance of amoA gene was two orders of magnitude higher than the abundance of nxrA gene in the MABs. However, the nxrA gene was always detected during the operation time, which indicates the difficulty of complete washout of NOB in MABs. The growth of heterotrophic bacteria compromised the dominance of nitrifiers in biofilm communities, but it enhanced the denitrification performance of the RSMBR system. Applying a high ammonia loading together with oxygen limitation was found to be an effective way to start nitrite accumulation in MABs, but other approaches were needed to sustain or improve the extent of nitritation in nitrogen conversion in MABs.     

Physical and chemical processes of wintertime secondary nitrate aerosol formation

The UCD/CIT model was modified to include a process analysis (PA) scheme for gas and particulate matter (PM) to study the formation of secondary nitrate aerosol during a stagnant wintertime air pollution episode during the California Regional PM_2.5/PM₁₀ Air Quality Study (CRPAQS) where detailed measurements of PM components are available at a few sites. Secondary nitrate is formed in the urban areas from near the ground to a few hundred meters above the surface during the day with a maximum modeled net increase rate of 4 μg·m⁻³·d⁻¹ during the study episode. The secondary nitrate formation rate in rural areas is lower due to lower NO₂. In the afternoon hours, near-surface temperature can be high enough to evaporate the particulate nitrate. In the nighttime hours, both the gas phase N₂O₅ reactions with water vapor and the N₂O₅ heterogeneous reactions with particle-bound water are important for secondary nitrate formation. The N₂O₅ reactions are most import near the surface to a few hundred meters above surface with a maximum modeled net secondary nitrate increase rate of 1 μg·m⁻³·d⁻¹ and are more significant in the rural areas where the O₃ concentrations are high at night. In general, vertical transport during the day moves the nitrate formed near the surface to higher elevations. During the stagnant days, process analysis indicates that the nitrate concentration in the upper air builds up and leads to a net downward flux of nitrate through vertical diffusion and a rapid increase of surface nitrate concentration.     

KrBr*准分子灯直接光解一甲胺气体

研究了正弦电源驱动的207 nm KrBr*准分子灯光解气相中的一甲胺(MA).考察了降解的影响因素(气体流速、初始浓度、输入功率),测定了灯的输入功率和辐射光谱.为了评价光解过程,对去除效率、能率、碳平衡和CO2的选择性这4个参数进行了研究.结果表明,去除率随着灯的输入功率升高、气体流速的降低以及气体初始浓度的升高而升高.能率与一甲胺初始浓度呈正相关性,输入功率为65.1 W时能率最高.输入功率升高,气体流速下降,碳平衡和CO2选择性都略有升高.当灯的输入功率为79.8 W,气体流速9.0 m3·h-1,初始浓度为2 897 mg·m-3,一甲胺去除率为56.8%,能率为185.6g·(kW·h)-1,相应的碳平衡和CO2选择性为16.8%和10.3%.最后,利用气质联用仪测定了一甲胺降解的产物,结合一甲胺的吸收光谱,推测了一甲胺的光解机制.     

黄土丘陵区3种典型天然草地群落土壤呼吸对模拟降雨的响应

土壤呼吸是影响陆地生态系统碳循环的关键生态学过程之一,降雨是土壤呼吸变化的重要驱动因子.为探明黄土丘陵区退耕草地群落土壤呼吸对降雨的短期响应规律,选择白羊草(Bothriochloa ischaemum)、达乌里胡枝子(Lespedeza davurica)、铁杆蒿(Artemisia gmelinii)为优势种的3种草地群落为研究对象,于2014年6月和7月,以未降雨群落为对照,对比测定了2种模拟降雨量(15 mm和50 mm)下连续8 d的土壤呼吸速率及土壤水分和土壤温度等.结果表明:2种模拟降雨量对3种草地群落土壤温度和土壤含水量均具有显著影响(p0.05).50 mm降雨下群落土壤呼吸速率增加量高于15 mm降雨.3种群落土壤呼吸对降雨的响应程度存在明显差异,其中,土壤呼吸速率峰值高低顺序为:白羊草(1.75 g·m~(-2)·h~(-1))铁杆蒿(1.69 g·m~(-2)·h~(-1))达乌里胡枝子(1.12 g·m~(-2)·h~(-1)).0~10 cm土壤含水量与土壤呼吸速率呈显著对数函数关系.3种群落土壤呼吸温度敏感性系数Q_(10)值变化范围是1.31~2.01,且月份和降雨量处理间均存在差异.研究表明,准确评估降雨格局改变背景下退耕草地生态系统碳收支需考虑群落类型的差异.     

闽江河口短叶茳芏湿地及其围垦的养虾塘CH4排放通量的比较

以闽江河口鳝鱼滩的短叶茳芏湿地及由其围垦而成的养虾塘为研究对象,2016年5月—2017年3月,分别采用静态箱-气相色谱法和悬浮箱/静态箱-气相色谱法对短叶茳芏湿地和养虾塘白天CH_4排放通量进行观测,并同步测定短叶茳芏湿地和养虾塘水体/沉积物理化指标.观测期间短叶茳芏湿地和养虾塘均表现为大气中CH_4的排放源,释放量变化范围分别为1.09~38.38 mg·m~(-2)·h~(-1)和0.01~65.38 mg·m~(-2)·h~(-1),均值分别为(11.67±1.99)mg·m~(-2)·h~(-1)和(18.69±4.84)mg·m~(-2)·h~(-1),重复测量方差分析统计结果表明:虽然在整个观测时间尺度上,养虾塘CH_4排放通量与短叶茳芏湿地无显著性差异(p0.05),但是在养殖期养虾塘CH_4排放通量显著高于同期短叶茳芏湿地(p0.05),增加了68.0%.短叶茳芏湿地CH_4排放通量与沉积物温度、间隙水总磷含量呈显著正相关关系(p0.01),养虾塘水-气界面CH_4排放通量与养殖水水深呈显著负相关关系(p0.01).亚热带河口感潮沼泽湿地围垦成为陆基养虾塘后增加了CH_4排放通量.     

Biosorption of Cr(III) from aqueous solution by freeze-dried activated sludge: Equilibrium, kinetic and thermodynamic studies

Batch biosorption experiments were conducted to remove Cr(III) from aqueous solutions using activated sludge from a sewage treatment plant. An investigation was conducted on the effects of the initial pH, contact time, temperature, and initial Cr(III) concentration in the biosorption process. The results revealed that the activated sludge exhibited the highest Cr(III) uptake capacity (120 mg·g⁻¹) at 45°C, initial pH of 4, and initial Cr(III) concentration of 100 mg·L⁻¹. The biosorption results obtained at various temperatures showed that the biosorption pattern accurately followed the Langmuir model. The calculated thermodynamic parameters, ΔGo° ( − 0.8–4.58 kJ·mol⁻¹), ΔH° (15.6–44.4 kJ·mol⁻¹), and ΔS° (0.06–0.15 kJ·mol⁻¹·K⁻¹) clearly indicated that the biosorption process was feasible, spontaneous, endothermic, and physical. The pseudo first-order and second-order kinetic models were adopted to describe the experimental data, which revealed that the Cr(III) biosorption process conformed to the second-order rate expression and the biosorption rate constants decreased with increasing Cr (III) concentration. The analysis of the values of biosorption activation energy (E _a = −7 kJ·mol⁻¹) and the intraparticle diffusion model demonstrated that Cr(III) biosorption was film-diffusion-controlled.     

微塑料对膜蒸馏处理含锑高盐废水性能影响研究

研究了微塑料在膜蒸馏过程中不同温度、pH、微塑料浓度和微塑料粒径条件下对含锑高盐废水的处理性能及机理.结果表明,随着进料液温度的升高,饱和蒸汽压的增加提高了传质动力,不含微塑料时膜通量由17.4 L·m^-2·h^-1提高至20.7 L·m^-2·h^-1,通量提升了18.9%,含有微塑料时膜通量由15.6 L·m^-2·h^-1提高至18.5 L·m^-2·h^-1,提升了18.6%;pH由3增大至11时,由于重金属锑在不同pH条件下的价态变化及静电排斥作用,重金属锑截留率由98.2%提升至99.6%;微塑料浓度的增加会降低膜通量,提高锑截留效果,这可能是微塑料对溶液中重金属锑的吸附作用及微塑料在膜表面的积聚产生的筛分效应引起的.     

西藏日太阳总辐射估算模型的优化与时间尺度效应

根据2012～2014年拉萨站点的日太阳辐射观测数据,对3种日太阳总辐射估算模型(左大康、Prescoff和王炳忠等提出的估算模型)的估算结果和实际观测结果进行误差检验分析,结果表明:3种模型都通过了显著性检验,其平均绝对误差(MAE)分别为6.17 MJ/(m~2·d)、6.42 MJ/(m~2·d)和12.31 MJ/(m~2·d),均方根误差(RMSE)分别为1.60 MJ/(m~2·d)、1.65 MJ/(m~2·d)和2.78 MJ/(m~2·d),表明利用地理位置信息和日照时数的左大康估算模型对拉萨日太阳总辐射的估算效果优于Prescoff和王炳忠估算模型。利用左大康估算模型分别估算得到2015年拉萨、那曲和葛尔地区的日太阳总辐射值,并进行模型验证。通过分析拉萨1971～2015年的太阳总辐射变化和周期性特征,研究日太阳总辐射估算模型的时间尺度效应。按照11年和四季两种不同的时间尺度,利用线性回归法对日太阳总辐射估算结果和实际观测结果进行误差和相关性分析,得到经验参数a和b的值与时间尺度有一定关系。11年和四季两种时间尺度除夏季以外,其他时间拟合模型的精度均得到了提高。通过线性回归法得出45年的西藏日太阳总辐射优化估算模型,该模型估算日太阳总辐射的误差小于左大康模型,估算精度较高。     

Preparation of hapten-specific monoclonal antibody for cadmium and its ELISA application to aqueous samples

High-affinity and specific monoclonal antibodies against cadmium-ethylene diamine tetraacetic acid (EDTA) complex have been produced using the hybridoma technique. A hapten was synthesized and characterized by Fourier Transform Infrared Spectroscopy (FT-IR) and UV-Vis. Competitive enzyme-linked immunosorbent assay (ELISA) for quantitative detection of cadmium in aqueous sample was developed. The monoclonal antibody with high level of binding affinity for Cd-IEDTA-BSA and high specificity for soluble Cd-EDTA complex showed less than 0.99% cross-reactivity with other 11 metals. The limit of detection was 0.10 μg·L⁻¹, and the effective linear range was 10⁻¹–10³ μg·L⁻¹. The intra- and inter-assay coefficient variations were 1.5%–6.3% and 3.2%–7.4%, respectively. The spike recovery in different water samples were between 98.5% and 110.3%. The detection limit of this assay was well below the allowable concentration of cadmium (3 μg·L⁻¹), and the working range was wider than that of other methods which showed the range of 2.19–86.38 and 0–10³ μg·L⁻¹. The competitive ELISA established in this paper was sensitive and accurate in the screening of cadmium in aqueous samples. The results will lay a solid foundation for construction of an immunoassay kit for cadmium.     

不同类型紫色土土/气界面汞释放通量及其影响因素

运用动力通量箱与RA-915 汞分析仪联用技术,对重庆市3种类型紫色土的土/气界面汞交换通董进行了实地监测.结果显示,不同类型紫色土的土/气界面汞交换通量有一定差异,随着土壤pH值的增加,汞交换通量值增大,酸性紫色土平均通量值为(30.8±23.7)ng·m-2·h-1,中性紫色土为(34.9±25.7)ng·m-2·h-1,石灰性紫色土为(39.0±27.O)ng·m-2·h-1.土/气界面汞交换量受光照、气温、土壤温度和空气相对湿度等因素的影响,汞交换通量与光照、气温和土壤温度呈显著正相关关系,与相对湿度呈显著负相关关系,与大气压不相关.     

羟基自由基致死船舶压载水海洋有害生物研究

利用大气压强电场电离放电的物理方法,将空气中的O2和海水中H2O(气态)电离、离解生成羟基自由基(.OH)等氧活性粒子,溶于部分压载水中形成高浓度羟基溶液,再注入到输运压载水的主管路中,实现在输送压载水的过程中快速致死海洋有害生物和病原体.在10 t.h-1的船舶压载水处理实验系统中,进行了.OH致死浮游生物和细菌的实验,.OH浓度为0.65mg.L-1时,致死率达100%,达到《国际公约》压载水排放标准.同时选用牟氏角毛藻(Chaetoceros muelleri)、小新月菱形藻(Nitzschia closterium)进行.OH致死生物形态学研究,在显微镜下观察到.OH严重地损害了细胞壁、细胞膜、胞内物质等的重要组成和功能物质.     

Adsorption of fluoride on clay minerals and their mechanisms using X-ray photoelectron spectroscopy

This research investigates the adsorption mechanisms of fluoride (F) on four clay minerals (kaolinite, montmorillonite, chlorite, and illite) under different F⁻ concentrations and reaction times by probing their fluoride superficial layer binding energies and element compositions using X-ray photoelectron spectroscopy (XPS). At high F⁻ concentrations (C ₀ = 5–1000 mg·L⁻¹), the amount of F⁻ adsorbed (Q _F), amount of hydroxide released by clay minerals, solution F⁻ concentration, and the pH increase with increasing C ₀. The increases are remarkable at C ₀>50 mg·L⁻¹. The QF increases significantly by continuously modifying the pH level. At C ₀<5–100 mg·L⁻¹, clay minerals adsorb H⁺ to protonate aluminum-bound surface-active hydroxyl sites in the superficial layers and induce F⁻ binding. As the C ₀ increases, F⁻, along with other cations, is adsorbed to form a quasi-cryolite structure. At C ₀>100 mg·L⁻¹, new minerals precipitate and the product depends on the critical Al³⁺ concentration. At [Al³⁺]>10^−11.94 mol·L⁻¹, cryolite forms, while at [Al³⁺]<10^−11.94 mol·L⁻¹, AlF₃ is formed. At low C ₀ (0.3–1.5 mg·L⁻¹), proton transfer occurs, and the F⁻ adsorption capabilities of the clay minerals increase with time.     

OLR对ABR沿程格室甲烷发酵特征的影响

为高效处理玉米淀粉生产废水,启动并持续运行了一个四格室厌氧折流板反应器（ABR）,通过分阶段提升进水COD的方法,探讨了有机负荷率（OLR）对ABR运行效能的影响,并采用间歇培养方式考察了OLR对沿程格室中不同营养类型产甲烷菌群活性的影响.结果表明,在OLR分阶段从2.7提高到8.0 kg·m^-3·d^-1的过程中,ABR前两个格室（C1和C2）始终呈现出典型的产酸发酵特征,其污泥的有机挥发酸（VFAs）比产率为0.54~0.76 kg·kg^-1·d^-1（以每天每千克MLVSS产出的1千克有机挥发酸计,下同）,而后两个格室（C3和C4）则表现出典型的产甲烷特征,其污泥的比产甲烷速率达98 L·kg^-1·d^-1（以每天每千克MLVSS产出的1升甲烷计,下同）以上.活性污泥产甲烷活性测试结果表明,当OLR为2.7~8.0 kg·m^-3·d^-1时,C3中的氢营养型产甲烷菌群保持了较高的产甲烷活性,其最大甲烷产量（P_max）和最大比产甲烷速率分别达到了20.4 mL和16.5 mL·g^-1·h^-1（以每小时每克MLVSS产出的1毫升甲烷计,下同）以上.乙酸营养型产甲烷菌群的累计甲烷产量由大到小依次为：C3 > C4 > C1 > C2.经过144 h的培养后,C3中乙酸营养型产甲烷菌群的累计甲烷产量为15.1~15.2 mL,最大比产甲烷速率为10.0~10.8 mL·g^-1·h^-1.