二氧化氯杀灭小球藻

实验研究了二氧化氯投加量、小球藻的初始浓度、pH、有机物和氨氮含量对ClO2杀灭来自于水库水的小球藻的影响,考察了ClO2氧化与混凝工艺结合时去除小球藻的效果并对工艺条件进行优化。结果表明,ClO2在投加量1.1 mg/L下,接触10 min,小球藻的杀灭率为71.93%。小球藻的杀灭率随着ClO2投加量的增大和藻初始浓度的升高而提高,随水中有机物含量的增加而显著降低,氨氮含量对小球藻杀灭的效果影响很小。在酸性条件和碱性条件下,小球藻的杀灭率均随pH升高而急剧下降,而在中性至弱碱性区间内,藻的杀灭率随pH升高而缓慢下降。对于某以小球藻为优势藻的供水水库源水,ClO2氧化与混凝工艺结合,藻的去除率高达98.47%。除藻的最佳工艺条件为：二氧化氯投加量为0.5 mg/L,聚合氯化铝为5 mg/L,二氧化氯与混凝剂同时投加。     

二氧化氯杀灭小球藻

实验研究了二氧化氯投加量、小球藻的初始浓度、pH、有机物和氨氮含量对ClO2杀灭来自于水库水的小球藻的影响,考察了ClO2氧化与混凝工艺结合时去除小球藻的效果并对工艺条件进行优化。结果表明,ClO2在投加量1.1 mg/L下,接触10 min,小球藻的杀灭率为71.93%。小球藻的杀灭率随着ClO2投加量的增大和藻初始浓度的升高而提高,随水中有机物含量的增加而显著降低,氨氮含量对小球藻杀灭的效果影响很小。在酸性条件和碱性条件下,小球藻的杀灭率均随pH升高而急剧下降,而在中性至弱碱性区间内,藻的杀灭率随pH升高而缓慢下降。对于某以小球藻为优势藻的供水水库源水,ClO2氧化与混凝工艺结合,藻的去除率高达98.47%。除藻的最佳工艺条件为:二氧化氯投加量为0.5 mg/L,聚合氯化铝为5 mg/L,二氧化氯与混凝剂同时投加。     

天然有机物对颗粒活性炭吸附微囊藻毒素的影响研究

通过改变水体中天然有机物(NOM)、腐殖酸(HA)浓度以及pH,测定了不同条件下颗粒活性炭(GAC)吸附微囊藻毒素MCLR的容量变化,研究了NOM对GAC吸附MCLR的影响。结果表明,GAC吸附MCLR的过程中,低浓度溶液中的吸附速率要高于高浓度溶液,且准一级动力学和准二级动力学方程均能较好地描述GAC吸附MCLR的过程;当溶液中含17.6 mg/LNOM或10.0 mg/L HA时,GAC对MCLR的最大吸附容量从17.06μg/g分别降低至13.68、12.89μg/g;GAC对MCLR的平衡吸附容量(qe)随NOM浓度的升高而逐渐降低,但当溶液中NOM超过一定值时,NOM浓度再升高对GAC吸附MCLR的影响程度变化不大,NOM从10.0 mg/L升高至17.6 mg/L时,qe仅降低了0.31μg/g;在中性或偏碱性水体中,HA对GAC吸附MCLR的干扰相对于酸性水体中更小,通过改变溶液pH来改变HA的带电性,对GAC吸附MCLR的影响总体较小。     

小球藻生长及其净化猪场废水条件的优化

为提高小球藻净化猪场废水的效果,在户外条件下系统比较了预处理方式、管道光反应器的种类和光径对蛋白核小球藻生长及其对猪场废水净化效果的影响。结果表明,猪场原废水COD、NH_4~+、PO_4~(3-)、TN、TP含量分别为710、491、54、590和108 mg·L~(-1)时,蛋白核小球藻对经过3级过滤预处理后的猪场废水净化效果最好,其中脱色率及NH_4~+去除率分别高达88.56%和83.48%,显著高于对原废水的处理效果(P0.05)。在夏季户外条件下,用平铺管道反应器对蛋白核小球藻进行放大培养,发现小球藻能耐受夏季户外高温,生长良好,最终藻粉产量达到0.13 g·L~(-1)。采用直径为5 cm的立式光生物反应器培养蛋白核小球藻,通过循环采收,藻粉产量可达到0.93 g·L~(-1),其蛋白质含量最高达到58.9%,汞、砷、镉、铅含量分别小于0.1、1.0、0.5和4.0 mg·kg~(-1),符合《饲料用小球藻粉》(DB32/T 564-2010)标准。采收小球藻后的出水中,NH_4~+、PO_4~(3-)、色度的去除率均高达90%以上,基本达到国家排放要求。该研究结果可为制定猪场废水的净化及蛋白核小球藻的工业化生产方案提供参考。     

巢湖蓝藻酸提取液提高玉米秸秆的酶解效率

资源化利用是避免富营养化水体打捞得到的蓝藻二次污染的有效方法途径。本研究以巢湖蓝藻为例,利用稀硫酸处理得到酸提取液并将其用于玉米秸秆的酶解过程。以主要成分还原糖和蛋白质的提取量为目标,优化了稀硫酸处理条件(处理时间、温度和硫酸浓度)。结果表明,从巢湖蓝藻提取还原糖的效率随着处理温度和硫酸浓度的升高而升高。在处理温度为125℃,处理时间为2 h,稀硫酸浓度为5%时,提取的还原糖最多为(152.8±12.6)mg/g。稀硫酸处理条件对蛋白质的提取效果影响并不显著。在处理温度为105℃,处理时间为1 h,稀硫酸浓度为5%时,最大提取量为(1.55±0.00)mg/g。提取的藻液中和后可以用于玉米秸秆的酶解过程,同对照相比酶解效率能够提升10%左右。结果表明,藻液中的小分子物质和钙离子是主要的作用组分,推测其和木质素表面官能团结合,从而降低了木质素对纤维素酶的非再生吸附。     

纯二氧化碳条件下小球藻固定CO2

微藻固碳已经成为消减温室气体排放的新的研究热点。利用静态吸收方法,考查了通人纯CO2对普通小球藻生长特点、固定CO2效率以及藻液pH值变异的影响。结果表明：通入纯CO2使小球藻生长延滞期显著延长,比普通培养延长10～12d,对其他生长阶段的影响不大;小球藻固定CO2速率可分为2个过程,即物理固碳过程和生物固碳过程,前者在藻细胞延滞期发生,峰值由CO。溶解于培养液造成,后者在藻细胞生长的指数期、稳定期和衰退期发生,峰值由藻细胞指数生长造成,2个过程中,固定CO2速率的变化趋势都是先增大后降低;纯CO2条件下,藻液pH值变化速率高,4d内,藻液即被酸化,随后藻液pH值变化速率逐渐降低,且pH值稳定在适宜水平。因此,采用小球藻固定高浓度CO2时,建议提高接种量并加强培养前期的pH值监测和调控,以保证藻液保持适宜的pH值,并缩短培养时间,提高生物固碳效率。     

非活性原始铜藻对水中Cr(Ⅵ)的生物吸附

以非活性原始铜藻(Sargassum horneri)(以下简称铜藻)为生物吸附剂处理含Cr(Ⅵ)废水,考察了溶液pH、铜藻投加量、Cr(Ⅵ)初始浓度、反应时间及温度对Cr(Ⅵ)去除效果的影响。结果表明,当pH在1~9时,pH越低时铜藻对Cr(Ⅵ)的吸附效果越好;降低铜藻投加量或增加Cr(Ⅵ)初始浓度均能提高铜藻对Cr(Ⅵ)的吸附容量,但会降低溶液中Cr(Ⅵ)的去除率。铜藻对Cr(Ⅵ)的吸附过程更遵循准二级动力学模型,且颗粒内扩散并不是该吸附过程的唯一速率控制步骤。Langmuir和Freundlich等温吸附模型均能较好地描述铜藻对Cr(Ⅵ)的吸附,20、30、40、50℃下铜藻对Cr(Ⅵ)的最大吸附容量分别为19.14、18.79、20.96、23.62mg/g。热力学分析显示,铜藻对Cr(Ⅵ)的吸附为吸热反应,可自发进行,升温可促进铜藻对Cr(Ⅵ)的吸附。此外,铜藻对Cr(Ⅵ)的吸附过程中物理吸附和化学吸附并存。     

固定化鼠尾藻Sargassum thunbergii对水中重金属锌的生物吸附效应

采用海藻酸钠-聚乙烯醇联合固定鼠尾藻与活性炭的方法对废水中重金属Zn~(2+)进行生物吸附研究。结果表明:当固定化材料配比为15 g·L~(-1)鼠尾藻粉,2%海藻酸钠溶液、6%聚乙烯醇溶液,1.5%活性炭时,固定化小球对废水中Zn~(2+)的吸附率最大。溶液在不同环境因素条件下吸附率不同,吸附率随着pH升高而升高,当pH为6时吸附率达到最大,随后开始下降;当温度为30℃,投放量为60 g·L~(-1)时吸附率上升至最大值后趋于平衡,吸附率不再随着条件的增加而增加;前30min吸附过程为快速吸附阶段,并在60 min后吸附率趋于平衡。在实验室规模的流化生物反应器中,固定化颗粒可以连续高效处理模拟矿山废水,同时经过多次吸附解吸循环后仍然具有较好的吸附效果,为固定化鼠尾藻的实际应用奠定了基础。     

生物炭-海藻酸钠联合固定化小球藻去除水中的氨氮

以海藻酸钠为包埋材料,生物炭为添加剂,固定小球藻,制得生物炭-海藻酸钠联合固定化小球藻胶球,并将其用于水中氨氮的去除。实验结果表明:生物炭-海藻酸钠联合固定化小球藻具有生物炭吸附和小球藻吸收协同作用,促进了小球藻的生长和水中氨氮的去除,且氨氮的去除率随着胶球加入量和胶球粒径的增加而提高。生物炭-海藻酸钠联合固定化小球藻胶球制备最优方案为:生物炭浓度为0.26 g·L~(-1)、海藻酸钠质量分数为1.8%、胶球中藻细胞密度为3.0×10~6个·mL~(-1)、CaCl_2质量分数为1%;胶球重复使用一次的氨氮去除率可达66.87%。生物炭促进了固定化微藻对高浓度氨氮废水的资源化利用。     

固定化小球藻与活性污泥的共生系统处理含锌废水

研究固定化小球藻与活性污泥的共生系统对含锌废水中Zn2+的去除效果,分析菌藻状态、初始Zn2+浓度、pH、固定化菌藻小球投加量和菌藻体积比等5个因素对固定化菌藻共生系统去除Zn2+的影响。结果表明,固定化活性污泥、固定化小球藻和固定化菌藻对Zn2+的去除效果均优于悬浮小球藻,其中固定化菌藻对Zn2+的去除效果最好;废水中初始Zn2+浓度小于100 mg/L时,固定化菌藻系统对废水中Zn2+的去除率达到90.5%;固定化菌藻系统去除废水中Zn2+的最佳条件是:初始Zn2+浓度为80 mg/L,pH=7,固定化小球投加量为80 mL,菌藻体积比为1∶2。     

Effective sorption of perfluorooctane sulfonate (PFOS) on hexadecyltrimethylammonium bromide immobilized mesoporous SiO2 hollow sphere

The hexadecyltrimethylammonium bromide (HDTMAB) immobilized hollow mesoporous silica spheres were prepared for the efficient removal of perfluorooctane sulfonate (PFOS) from aqueous solution. Besides the traditional sorption behavior including sorption kinetics as well as effect of solution pH and temperature, the effect of increasing volume which simulated the natural river where the rate of solute and solvent was relatively constant and solution volume was always changing was investigated. The result indicated that the residual PFOS concentrations in aqueous phase decreased with increasing solution pH and ionic strength, whereas they increased with increasing temperature. The HDTMAB immobilized material still maintained high efficiency after increasing volume, that is, the removal kept more than 99% after the treatment when the initial PFOS concentration was 1 mg L^?1. The uptake behavior and morphology of spheres which was characterized by transmission electron microscopy (TEM) revealed that the additional HDTMAB and mesoporous shell were responsible for the enhanced sorption of PFOS. It was concluded that electrostatic interaction and Ca-bridge role played an important role in the sorption of PFOS on the mesoporous SiO₂ hollow spheres, whereas, hydrophobic interaction contributed to the nice sorption performance of PFOS on the HDTMAB immobilized sorbent.     

小球藻(Chlorella vulgaris)净化沼液和提纯沼气

为了研究同时提纯沼气和净化沼液的可能,利用沼液作为小球藻(Chlorella vulgaris)的培养基,同时把沼气中的CO2作为小球藻培养的碳源。在无菌培养条件下,得出了最适生长条件为沼液浓度50%、初始pH值6.0、接种小球藻干重为0.20 mg/mL、光质为红光。在此条件下沼液中的COD、TN、TP和BOD5的去除率分别达到了88.5%、91.2%、95.3%和87.6%,沼气中甲烷含量由原先的40%提升到60.2%。很好地同时解决了沼气品质低下和高浓度污染物沼液污染环境的问题。     

Enhanced sorption of perfluorooctane sulfonate (PFOS) on carbon nanotube-filled electrospun nanofibrous membranes

Multi-walled carbon nanotube-filled electrospun nanofibrous membranes (MWCNT-ENFMs) were prepared by electrospinning. The addition of MWCNTs (0.5 wt.% vs. ENFMs) doubled the specific surface area and tensile strength of the ENFMs. The MWCNT-ENFMs were used to adsorb perfluorooctane sulfonate (PFOS) in aqueous solutions. The sorption kinetics results showed that the sorption rate of PFOS onto the MWCNT-ENFMs was much higher than the sorption rate of PFOS onto the pure ENFMs control, and the pseudo-second-order model (PSOM) described the sorption kinetics well. The sorption isotherms indicated that the sorption capacity of the MWCNT-ENFMs for PFOS (16.29 ± 0.26 μmol g⁻¹) increased approximately 18 times, compared with the pure ENFMs (0.92 ± 0.06 μmol g⁻¹). Moreover, the solution pH significantly affected the sorption efficiency and sorption mechanism. The MWCNT-ENFMs were negatively charged from pH 2.0–10.0, but the electrostatic repulsion between the MWCNT-ENFMs and PFOS was overcome by the hydrophobic interactions between PFOS and the MWCNTs or nanofibers. The strong hydrophobic interactions between PFOS and the MWCNTs played a dominant role in the sorption process. For the pure ENFMs, the electrostatic repulsion was conquered by the hydrophobic interactions between PFOS and the nanofibers at pH > 3.1. In addition to the hydrophobic interactions, an electrostatic attraction between PFOS and the pure ENFMs was involved in the sorption process at pH < 3.1.     

固定化菌藻微球的制备、表征及其对富营养化湖水的修复

以聚乙烯醇(PVA)和海藻酸钠(SA)为主要包埋材料,以活性炭、SiO2和CaCO3作添加剂,采用普通小球藻(Chlorella vulgaris)和活性污泥制备固定化菌藻微球。采用正交实验对微球的制备条件进行了优化,并对最优化条件下制得的微球进行了表征,还考察了固定化菌藻微球对某富营养化湖水的修复效果。结果表明,固定化菌藻微球的最优化制备条件为:PVA用量10%(m/v),微生物包埋量15 mL,海藻酸钠用量0.6%(m/v),氯化钙浓度2.0%(m/v)。制得的微球具有较大的比表面积,内部呈网状结构,孔径分布均匀,中孔居多,适合小球藻和微生物生长。采用固定化菌藻微球可有效修复上述湖泊的实际富营养化湖水,微球可重复使用3~4个循环,在前4个循环中,每个循环历时96 h,TN平均去除率达80%以上;TP平均去除率达90%以上;COD平均去除率达85%以上,表明固定化菌藻微球在富营养化湖水的修复方面具有潜在的应用价值。     

地表水中隐孢子虫和贾第鞭毛虫微球的混凝去除

以向地表水中投加的隐孢子虫微球和贾第鞭毛虫微球为对象,研究通过对给水混凝工艺对其的去除效果进行比较,着重考察了不同混凝剂种类、投加量及水样pH值对去除效果的影响.结果表明,混凝工艺可较为有效地去除地表水中的两虫微球,去除率最高可达4 lg.相比常规的金属盐类混凝剂,高分子的PAC、PAFC混凝剂对两虫微球的混凝去除率更...     

A comparative study on sorption of perfluorooctane sulfonate (PFOS) by chars, ash and carbon nanotubes

Perfluorooctane sulfonate (PFOS), as one of emerging contaminants, has been attracting increasing concerns in recent years. Sorption of PFOS by maize straw- and willow-derived chars (M400 and W400), maize straw-origin ash (MA) as well as three carbon nanotubes (CNTs) was studied in this work. The sorption kinetics of PFOS by the six adsorbents was well fitted by the pseudo-second-order model. CNTs reached equilibrium in 2 h, much faster than those by chars (384 h) and ash (48 h). According to the sorption isotherms, both single-walled carbon nanotubes (SWCNT) and MA had high sorption capacities (over 700 mg g⁻¹), while the two chars had low sorption capacities (below 170 mg g⁻¹) caused by their small BET surface area. In the case of MA, due to its positively charged surface, both hydrophobic interaction and electrostatic attraction involved in the sorption, and the formation of hemi-micelles further favored the sorption. This study suggested that SWCNT and MA were effective adsorbents for PFOS removal from water. Compared to SWCNT, MA is low cost and easy to obtain, so it could be a preferred adsorbent for PFOS removal.     

Sorption of perfluoroalkyl substances in sewage sludge

The sorption behaviour of three perfluoroalkyl substances (PFASs) (perfluorooctanesulfonic acid (PFOS), perfluorooctanoic acid (PFOA) and perfluorobutanesulfonic acid (PFBS)) was studied in sewage sludge samples. Sorption isotherms were obtained by varying initial concentrations of PFOS, PFOA and PFBS. The maximum values of the sorption solid–liquid distribution coefficients (K_d,max) varied by almost two orders of magnitude among the target PFASs: 140–281 mL g^?1 for PFOS, 30–54 mL g^?1 for PFOA and 9–18 mL g^?1 for PFBS. Freundlich and linear fittings were appropriate for describing the sorption behaviour of PFASs in the sludge samples, and the derived K_F and K_d,linear parameters correlated well. The hydrophobicity of the PFASs was the key parameter that influenced their sorption in sewage sludge. Sorption parameters and log(K_OW) were correlated, and for PFOS (the most hydrophobic compound), pH and Ca?+?Mg status of the sludge controlled the variation in the sorption parameter values. Sorption reversibility was also tested from desorption isotherms, which were also linear. Desorption parameters were systematically higher than the corresponding sorption parameters (up to sixfold higher), thus indicating a significant degree of irreversible sorption, which decreased in the sequence PFOS?>?PFOA?>?PFBS.     

Sorption of perfluorooctane sulfonate to carbon nanotubes in aquatic sediments

To date, sorption of organic compounds to nanomaterials has mainly been studied for the nanomaterial in its pristine state. However, sorption may be different when nanomaterials are buried in sediments. Here, we studied sorption of Perfluorooctane sulfonate (PFOS) to sediment and to sediment with 4% multiwalled carbon nanotubes (MWCNTs), as a function of factors affecting PFOS sorption; aqueous concentration, pH and Ca²⁺ concentration. Sorption to MWCNT in the sediment–MWCNT mixtures was assessed by subtracting the contribution of PFOS sorption to sediment-only from PFOS sorption to the total sediment–MWCNT mixture. PFOS Log K_D values ranged 0.52–1.62 L kg^?1 for sediment and 1.91–2.90 L kg^?1 for MWCNT present in the sediment. The latter values are relatively low, which is attributed to fouling of MWCNT by sediment organic matter. PFOS sorption was near-linear for sediment (Freundlich exponent of 0.92 ± 0.063) but non-linear for MWCNT (Freundlich exponent of 0.66 ± 0.03). Consequently, the impact of MWCNT on sorption in the mixture was larger at low PFOS aqueous concentration. Effects of pH and Ca²⁺ on PFOS sorption to MWCNT were statistically significant. We conclude that MWCNT fouling and PFOS concentration dependency are important factors affecting PFOS–MWCNT interactions in sediments.