活性污泥体系中聚糖菌的富集与鉴定

活性污泥体系中，聚糖菌(GAOs)在厌氧环境下与聚磷菌(PAOs)形成对底物的竞争关系，对聚糖菌的研究对于优化生物除磷工艺有重要意义。以葡萄糖为惟一碳源，在磷限制条件下，利用特殊运行方式对活性污泥进行驯化培养出了稳定的聚糖菌颗粒污泥，厌氧阶段磷释放量与有机物吸收量浓度(mg/L)比从7.4%下降为0.25%。从培养好的活性污泥反应器中分离获得2株聚糖菌，经菌落PCR和16S rRNA序列分析确定了所得聚糖菌菌株G1和菌株G2分别是枯草芽孢杆菌(Bacillus subtilis)和解鸟氨酸克雷伯氏菌(Klebsiella ornithinolytica)。     

一株兼性自养菌硫转化性能的研究

研究了一株具有硫转化性能的兼性自养菌的培养特性,以及不同因素对该菌硫转化纺的影响,结果表明：有机物可促进细菌的生长,合适的氮源、适宜的ｐＨ、添加微量元素,可提高该菌的硫转化率。在约１％接种量时,硫转化率可达８７．４２％。     

强化生物除磷系统中聚磷菌与聚糖菌的种群分析及代谢机制研究进展

强化生物除磷(EBPR)工艺是目前国内外广泛应用的废水除磷技术之一。微生物的研究对于提高EBPR系统的除磷稳定性有着非常重要的意义。综述了EBPR系统中聚磷菌和聚糖菌的种群分析及其代谢机制、聚磷菌与聚糖菌之间竞争的影响因素等方面的研究进展。分析了目前相关研究中存在的不足,并展望了今后相关的研究发展方向。     

DS-EBPR颗粒污泥和絮状污泥除磷效能

为提高反应器的稳定性,同时对硫循环协同反硝化生物除磷(DS-EBPR)颗粒污泥和絮体污泥的脱氮除磷效果以及物质转化规律进行对比研究,实验采用序批式活性污泥反应器(SBR)分别培养DS-EBPR絮体污泥和颗粒污泥。结果表明:GSBR(颗粒污泥SBR)乙酸根平均去除率和磷平均去除率均高于FSBR(絮体污泥SBR);且GSBR中PHA(聚羟基脂肪酸)的作用机制相比于FSBR明显优于glycogen(糖原),表明GSBR具有更好的功能微生物富集作用;反应器运行过程中poly-S(聚硫颗粒)储存形式的转变表明DS-EBPR系统中poly-S的转化形式并不是根据反应阶段固定的,而是根据系统能量供需状态变化的,且对比硫循环转化效果显示GSBR的能量利用效率高于FSBR。     

长期缺氧吸磷驯化下强化生物除磷系统污泥除磷方式的转化

采用交替厌氧/缺氧/好氧运行的序批式活性污泥反应器(SBR),通过梯度投加电子受体NO_3~-,考察长期缺氧吸磷驯化下强化生物除磷(EBPR)系统的性能及除磷方式的转化。结果表明,当进水COD为300～450mg/L、PO_4~(3-)(以P计,下同)和氨氮分别为8、14mg/L时,驯化期间TN去除率均保持在75%以上,长期缺氧吸磷驯化对COD和氨氮的去除没有影响。硝态氮投加量为5mg/L时,EBPR系统因电子受体投加不足除磷性能迅速恶化,增加硝态氮投加量至10mg/L,经过近30d的恢复,缺氧吸磷率最高可达97.67%,进一步提高硝态氮投加量至15mg/L,系统内硝态氮的积累导致缺氧吸磷率下降。污泥吸磷小试结果表明,经缺氧吸磷驯化后,即使除磷性能欠佳的低浓度电子受体系统污泥也具有良好的反硝化吸磷能力,可见经NO_3~-长期驯化的缺氧吸磷系统有利于筛选以NO_3~-为电子受体的反硝化聚磷菌。     

ORP控制在硫化物生物氧化成单质硫过程中的应用

试验采用气升式反应器,接种实验室自行培养的排硫硫杆菌种,在进水pH值为7.0±0.2,温度控制在30±2℃条件下,研究了以ORP为控制参数在硫化物生物氧化成单质硫过程中的应用,并考察了pH和污泥硫负荷对ORP及硫化物生物氧化的影响.结果表明,硫化物去除率和硫酸根生成率均随ORP的降低而下降,不同容积负荷下,控制合适的ORP均可得到单质硫的最大生成率;当ORP为-380～340 mV,pH为7.85～8.63,污泥硫负荷为8.4 kg S/(kg MLSS·d)时,反应器运行状况良好.     

投加聚氨酯泡沫微生物固定化载体的SBBR脱氮除磷实验研究

研究投加聚氨酯泡沫微生物固定化载体的SBBR脱氮除磷效果及机理.在SBR中填充聚氨酯泡沫微生物固定化载体,形成序批式生物膜反应器(SBBR).SBBR以实际生活污水为处理对象,在A/O运行工况下对微生物进行培养驯化,并在SBBR运行稳定时研究其脱氮除磷效果.研究结果表明,SBBR中的聚氨酯泡沫微生物固定化载体在空间上形...     

微氧环境下无色硫细菌和硫酸盐还原菌脱硫

通过间歇曝气形成微氧环境让SRB和CSB实现共生,使含硫酸盐有机废水中硫酸根最终转化成单质硫达到脱硫目的.研究考察了曝气量对SRB还原和CSB氧化的影响,确定了合适的曝气强度和水力停留时间,使得单质硫占系统内总硫比值最大.实验结果显示,在进水COD/SO42-=2000/1500 mg/L、曝气开关时间为2 s/2 min、生化时间为10 h时,单质硫产率最大,为89.53％,SO42-浓度降至最低值72.7 mg/L,还原率达95.1％,此时脱硫效果较好.     

一体式A/O反应器中不同碳硫比对除碳脱臭效率的影响

在污水处理领域同步除碳脱臭研究一直是个难题,本实验开发了一种新型同步除碳脱臭一体式A/O反应器,研究了该一体式A/O反应器处理不同碳硫比有机废水时的同步除碳脱臭功能。结果表明,碳硫比为30∶1时,即进水SO24-浓度为133 mg/L,该反应器总COD去除率可达到95%。在进水SO24-浓度不大于400 mg/L时,中间产物臭气硫化氢气可以完全去除,实现了同步除碳脱臭的功能,减少了在有机废水处理过程中的大量臭气的排放。微生物学角度分析,表明污泥中含有大量的硫细菌。     

超声破解污泥上清液对A~2O工艺脱氮除磷和微生物群落结构的影响

为了提高传统污水处理工艺的脱氮除磷效率、实现污泥资源化,本实验通过超声破解污泥获取碳源,采用耗氧呼吸速率分析上清液作为碳源的可行性,并将上清液回用于生活污水,考察其对A2O工艺长期运行的脱氮除磷效果和微生物群落结构的影响。结果表明,上清液中可降解有机物达到76.2%,具有作为内碳源的潜能;上清液和生活污水按1∶15投入A2O反应器后,氮、磷的去除率分别从63.2%和53.4%提高到了82.1%和94.7%;上清液明显改变了微生物群落结构,使除磷菌Actinobacteia和反硝化聚磷菌Sphingobacterium富集。     

复合固硫剂对型煤固硫的影响研究

固硫型煤作为煤燃烧中脱硫的一种重要方法，在燃煤SO2的减排方面起着重要的作用。为了考察固硫剂和固硫添加剂对型煤固硫及其对型煤燃烧释放SO2的规律的影响，对利用氧化镁和氧化钙为固硫剂，以煤矸石和粉煤灰为固硫添加剂进行了研究，同时通过XRD和SEM表征，进一步探讨了固硫剂及添加剂的固硫作用和机理。研究结果表明：(1)CaO...     

Supported transition-metal oxide catalysts for reduction of sulfur dioxide with hydrogen to elemental sulfur

This work is for the purpose to find a high performance catalyst for the catalytic reduction of SO2 with H2 as a reducing agent. NiO/gamma-Al2O3 catalyst was found to be the most active catalyst among the seven gamma-Al2O3-supported metal-oxide catalysts tested. With NiO as the active species, of the supports tested, gamma-Al2O3 was the most suitable one and the optimal Ni content was 16 wt%. Using this NiO/gamma-Al2O3 catalyst, we found that the optimal feed ratio of H2/SO2 is 2:1 and the catalyst presulfided with H2 + H2S exhibits a higher performance than that pretreated with H2 or He. XRD patterns reveal that the nickel oxide experienced a transformation to Ni3S2 and NiS, and then to NiS2, the most active nickel sulfide, during the reaction process. The reason for the highest catalyst activity of 16 wt% Ni was attributed to the largest amount of NiS2. Water vapor in the feed gas reactant caused inhibition of catalyst activity, whereas H2S promoted the reduction of SO2. These phenomena were rationalized with the aid of Claus reaction.     

Catalytic reduction of sulfur dioxide with carbon monoxide over tin dioxide for direct sulfur recovery process

SO(2) reduction by CO over SnO(2) catalyst was studied in this work. The parameters were the reaction temperature, space velocity (GHSV) and [CO]/[SO(2)] molar ratio. The optimal temperature, GHSV and [CO]/[SO(2)] molar ratio were 550 degrees C, 8000 h(-1) and 2.0, respectively. Under these conditions, the SO(2) conversion and sulfur selectivity were about 78% and 68%, respectively. The following reaction pathway involving two mechanisms was proposed in SO(2) reduction by CO over SnO(2) catalyst: in the first step involving Redox mechanism, the elemental sulfur was produced by the mobility of the lattice oxygen between SO(2) and SnO(2) surface. In the second step, COS was formed by the side reaction between elemental sulfur and CO or metal sulfide and CO. In the third step involving COS intermediate mechanism, the abundant elemental sulfur was produced by the SO(2) reduction by COS which was produced in the second step and was more effective reducing agent than CO.     

The physical characteristics of sulfur aerosols

A review of the physical characteristics of sulfur-containing aerosols, with respect to size distribution of the physical distributions, sulfur distributions, distribution modal characteristics, nuclei formation rates, aerosol growth characteristics, and in situ measurement, has been made.Physical size distributions can be characterized well by a trimodal model consisting of three additive lognormal distributions.When atmospheric physical aerosol size distributions are characterized by the trimodal model, the following typical modal parameters are observed:1. Nuclei mode – geometric mean size by volume, DGV_n, from 0.015 to 0.04 μm. σ_gn=1.6, nucler mode volumes from 0.0005 over the remote oceans to 9 μm³ cm⁻³ on an urban freeway.2. Accumulation mode – geometric mean size by volume, DGV_a, from 0.15 to 0.5 μm, σ_ga=1.6–2.2 and mode volume concentrations from 1 for very clean marine or continental backgrounds to as high as 300 μm³ cm⁻³ under very polluted conditions in urban areas.3. Coarse particle mode – geometric mean size by volume, DGV_c, from 5 to 30 μm, σ_gn=2–3, and mode volume concentrations from 2 to 1000 μm³ cm⁻³.It has also been concluded that the fine particles (D_p<2 μm) are essentially independent in formation, transformation and removal from the coarse particles (D_p>2 μm).Modal characterization of impactor-measured sulfate size distributions from the literature shows that the sulfate is nearly all in the accumulation mode and has the same size distribution as the physical accumulation mode distribution.Average sulfate aerodynamic geometric mean dia. was found to be 0.48±0.1 μm (0.37±0.1 μm vol. dia.) and σ_g=2.00±0.29. Concentrations range from a low of about 0.04 μg m⁻³ over the remote oceans to over 8 μg m⁻³ under polluted conditions over the continents.Review of the data on nucleation in smog chambers and in the atmosphere suggests that when SO₂, is present, SO₂-to-aerosol conversion dominates the Aitken nuclei count and, indirectly, through coagulation and condensation, the accumulation mode size and concentration. There are indications that nucleation is ubiquitous in the atmosphere, ranging from values as low as 2 cm⁻³ h⁻¹ over the clean remote oceans to a high of 6×10⁶ cm⁻³ h⁻¹ in a power plant plume under sunny conditions.There is considerable theoretical and experimental evidence that even if most of the mass for the condensational growth of the accumulation mode comes from hydrocarbon conversion, sulfur conversion provides most of the nuclei.     

Retention of sulfur dioxide by nylon filters

Based on laboratory studies, recovery efficiencies of sulfur dioxide (SO₂) were determined for nylon filters. The nylon filters used in these experiments were found to retain SO₂. A relatively uniform amount (1.7%) was recoverable from each nylon filter, independent of relative humidity. An appreciable portion of SO₂ was unrecoverable, and this increased from 5 to 16% as the RH increased from 28 to 49%. This unrecoverable SO₂ may account for previous reports of a low bias for SO₂ determinations employing filter packs using nylon filters. Additional characterization of nylon filters is recommended prior to their future deployment as an integrative sampling medium for ambient air.     

Global sulfur emissions from 1850 to 2000

The ASL database provides continuous time-series of sulfur emissions for most countries in the World from 1850 to 1990, but academic and official estimates for the 1990s either do not cover all years or countries. This paper develops continuous time series of sulfur emissions by country for the period 1850-2000 with a particular focus on developments in the 1990s. Global estimates for 1996-2000 are the first that are based on actual observed data. Raw estimates are obtained in two ways. For countries and years with existing published data I compile and integrate that data. Previously published data covers the majority of emissions and almost all countries have published emissions for at least 1995. For the remaining countries and for missing years for countries with some published data, I interpolate or extrapolate estimates using either an econometric emissions frontier model, an environmental Kuznets curve model, or a simple extrapolation, depending on the availability of data. Finally, I discuss the main movements in global and regional emissions in the 1990s and earlier decades and compare the results to other studies. Global emissions peaked in 1989 and declined rapidly thereafter. The locus of emissions shifted towards East and South Asia, but even this region peaked in 1996. My estimates for the 1990s show a much more rapid decline than other global studies, reflecting the view that technological progress in reducing sulfur based pollution has been rapid and is beginning to diffuse worldwide.     

Variations of sulfur isotope ratios in a single lichen thallus: A potential historical archive for sulfur pollution

Utilizing the analytical capability to measure S isotope ratios of small quantities of S in biological material without any chemical pretreatment, the variation of δ³⁴S within a lichen thallus was investigated using old and young segments of fruticose lichen thalli (Alectoria sarmentosa) from an oil refinery area in Come-By-Chance and two coastal areas, Newfoundland, Canada. Old segments of lichen samples from the oil refinery area showed significantly higher δ³⁴S values (1.0-2.5‰) than their corresponding young segments. Lichen samples from two coastal areas showed no noticeable differences in δ³⁴S values between old and young segments. These results demonstrate that lichen thalli record temporal changes in the isotopic composition of atmospheric S and hence constitute a historical archive of atmospheric S pollution.     

Natural sulfur dioxide emissions from sulfuric soils

Soils have long been recognised as sulfur dioxide (SO₂) sinks, but we show that they can also be sources of atmospheric SO₂. Using static chambers and micrometeorological techniques, we have measured emissions of SO₂ from coastal lowland soils containing sulfides (mostly pyrite), commonly referred to as acid sulfate soils in Australia. SO₂ evolution seems coupled to evaporation of soil water containing sulfite. The global emissions of S from acid sulfate soils is estimated at about 3 Tg/year, which is of the same order as emissions from terrestrial biogenic sources and biomass burning and is about 3% of known anthropogenic emissions of S.     

均匀设计法处理含硫废水的研究

对钠盐型和铵盐型含硫工业废水进行脱硫处理,采用均匀设计法设计试验,得到定量描述试验内在规律的多元非线性回归方程.用该回归方程计算的预测值与试验结果一致.对影响脱硫效果和脱硫效率的影响因素--絮凝剂投加量、pH以及废水含硫量进行了考察.利用回归方程,对反应体系进行了模拟优化处理.研究表明,在试验条件下,用聚合氯化铝作为絮凝剂、pH=7的条件下,采用两段工艺,可以使脱硫后废水含硫量降至40 mg/L以下,满足下游污水处理装置对含硫量的要求.