腐殖酸对砂质土壤吸附Cr(VI)的影响

利用系列摇瓶振荡实验,研究了在砂质土壤介质中腐殖酸(HA)对Cr(VI)还原作用及增强土壤表面对其吸附的影响.通过改变反应接触时间、pH值、HA投加量等条件,确定了最佳吸附反应条件.结果表明:砂质土壤中存在HA时,可使Cr(VI)还原为毒性较小的Cr(Ⅲ),明显增强土壤对可溶态Cr离子的吸附能力,比同等条件下无HA的土壤吸附量增大1倍以上.一般整个反应过程约8 h即可达到稳定.pH值对Cr的还原和吸附有很大的影响,酸性条件下的吸附量比碱性条件可增大1倍,最佳pH值为2～4;当pH＞5时吸附能力急剧下降,pH=10时吸附去除量降为20%.有HA存在时砂质土壤土对Cr(VI)的吸附反应为一级动力学反应,K298=0.033 5 min-1,砂土对CrO2-4的等温吸附曲线较好地满足Langmuir公式.     

Removal effect on Mesocyclops leukarti and mutagenicity with chlorine dioxide

Introduction The eutrophication of surface water is a worldwide problem, which is increasing in significance (Ma and Liu, 2002). Mesocyclops leukarti, a kind of Cyclops, is a waterborne animal that excessively propagates in eutrophic reservoirs and fresh …     

Promotion of hexadecyltrimethyleamine bromide to the damage of Alexandrium sp. LC3 by cupric glutamate

The effect of hexadecyltrimethyleamine bromide （HDTMAB） on the removal of A lexandrium sp. LC3 under cupric glutamate stress was investigated. Toxic effect of cupric glutamate on A lexandrium sp. LC3 was significantly promoted in the presence of HDTMAB, especially at 3.0 cmc of HDTMAB. It was found that the sulfhydryl group content of the cell decreased, while the malonaldehyde content and membrane permeability increased when A lexandrium sp. LC3 was treated with HDTMAB and cupric glutamate complex, compared with cupric glutamate alone. The data suggest that HDTMAB might stimulate the damage of A lexandrium sp. LC3 by enhancing the membrane permeability.     

Al2O3催化臭氧化处理邻苯二甲酸二甲酯

'Al₂O₃催化剂对邻苯二甲酸二甲酯(DMP)溶液臭氧化过程的影响结果表明:Al₂O₃可以显著提高臭氧氧化的效果,反应120min后,TOC的去除率从单独臭氧氧化的23.9%提高到55.1%.实验中还考察了制备条件对Al₂O₃催化剂活性的影响并确定了反应的最佳工艺条件.在实验考察的范围内:焙烧温度600℃,Al₂O₃粒径为0.5～1.0mm时催化活性最高;最佳反应工艺条件为:催化剂投加量20g/L,混和气体流速200mL/min,反应温度15℃.通过单独臭氧氧化,单独臭氧氧化后再进行催化剂吸附,催化臭氧化的对比实验证明了Al₂O₃催化剂对体系TOC的去除主要是基于催化作用.     

Partitioning and removal of dioxin-like congeners in flue gases treated with activated carbon adsorption

Activated carbon adsorption is commonly used to control dioxin-like congener (PCDD/Fs and PCBs) emissions. Partitioning of PCDD/Fs and PCBs between vapor and solid phases and their removal efficiencies achieved with existing air pollution control devices (APCDs) at a large-scale municipal waste incinerator (MWI) and an industrial waste incinerator (IWI) are evaluated via intensive stack sampling and analysis. Those two facilities investigated are equipped with activated carbon injection (ACI) with bag filter (BF) and fixed activated carbon bed (FACB) as major PCDD/F control devices, respectively. Average PCDD/F and PCB concentrations of stack gas with ACI+BF as APCDs are 0.031 and 0.006ng-TEQ/Nm(3), and that achieved with FACB are 1.74 and 0.19ng-TEQ/Nm(3) in MWI and IWI, respectively. The results show that FACB could reduce vapor-phase PCDD/Fs and PCBs concentrations in flue gas, while the ACI+BF can effectively adsorb the vapor-phase dioxin-like congener and collect the solid-phase PCDD/Fs and PCBs in the meantime. Additionally, the results of the pilot-scale adsorption system (PAS) experimentation indicate that each gram activated carbon adsorbs 105-115ng-PCDD/Fs and each surface area (m(2)) of activated carbon adsorbs 10-25ng-PCDD/Fs. Based on the results of PAS experimentation, this study confirms that the surface area of mesopore+macropore (20-200A) of the activated carbon is a critical factor affecting PCDD/F adsorption capacity.     

Removal of cyanobacterial blooms in Taihu Lake using local soils. I. Equilibrium and kinetic screening on the flocculation of Microcystis aeruginosa using commercially available clays and minerals

Algal removal abilities of 26 clays/minerals were classified into three categories according to the 8-h equilibrium removal efficiency (Q8h) and removal rate at a clay loading of 0.7 g/L. Type I clays (sepiolite, talc, ferric oxide, and kaolinite) had a Q8h > 90%, a t50 (time needed to remove 50% of the algae) < 15 min, and a t80 < 2.5 h. Type II clays (6 clays) had a Q8h 50-90%, a t50 < 2.5 h, and a t80 > 2.5 h. Type III clays (14 clays) with Q8h < 50%, t50 > 8 h and t80 > 14 h had no practical value in removal of algal blooms. When the clay loading was reduced to 0.2 g/L, Q8h for all the 25 materials decreased to below 60%, except for sepiolite whose Q8h remained about 97%. The high efficiency for sepiolite to flocculate M. aeruginosa cells in freshwaters was due to the mechanism of netting and bridging effect.     

耕作制度对川中丘陵区冬灌田CH4和N2O排放的影响

采用静态暗箱/气相色谱法连续2 a田间原位测定,研究川中丘陵区冬灌田CH₄和N₂O的排放特征和不同耕作制度对冬灌田CH₄和N₂O排放的影响.结果表明,1a只种1季中稻冬季灌水休闲的冬灌田(PF),在水稻生长期,CH₄平均排放通量为(21.44±1.77)mg·(m²·h)^-1,非水稻生长期为(3.77±0.99)mg·(m²·h)^-1,分别大大低于以前文献报道的在西南其它地方观测值;全年CH₄排放量以水稻生长期CH₄排放量为主,非水稻生长期CH₄排放量仅占全年总排放量的23.2%.冬灌田N₂O排放通量年均值为(0.051±0.008)mg·(m²·h)^-1,且主要集中在水稻生长季,非水稻生长期N₂O排放量仅占全年总排放量的8.1%.在采用水旱轮作制后,冬灌田CH₄排放量大大降低,稻-麦轮作(RW)和稻-油菜轮作(RR)全年CH₄排放量分别为PF的43.8%和40.6%.但冬灌田改为水旱轮作制后,N₂O排放量显著增大,RW和RR的N₂O年排放量分别是PF的3.7倍和4.5倍.综合考虑冬灌田在采用不同耕作制度后排放CH₄和N₂O的全球增温潜势(GWP),无论是短时间尺度还是长时间尺度,采用3种耕作制度全年所排放的CH₄和N₂O所产生的综合GWP都为:PF RW≈RR.在20a、100a和500a时间尺度上,PF分别约是RW和RR的2.6、2.1和1.7倍.冬灌田改为水旱轮作制度后能大大减少CH₄和N₂O所产生的综合GWP.     

潮土施镍对小白菜的生物效应及其临界值研究

研究潮土施Ni对盆栽蔬菜的生态效应,并通过小白菜生物量的变化、地上部茎叶Ni质量比及土壤有效态Ni质量比来表征土壤Ni污染的毒性临界值.结果表明,潮土施Ni对蔬菜未表现出增产效应.施Ni量低于25 mg/kg,其生物产量无明显降低.随施Ni量的增加,生物产量呈显著下降,生物量变化与Ni质量比呈高度负相关.潮土施Ni增加茎叶和根系中Fe,Mn,Ca,Mg元素质量比,降低Cu,Zn元素质量比.4种性质不同的提取试剂提取的土壤有效态Ni质量比与植物Ni吸收均呈高度正相关,较好地反映了植物的危害状况,且以DTPA提取效果最佳.以生物减产量突变点为依据,确定潮土施Ni毒害临界值为:土壤全量Ni为41.86 mg/kg,有效态Ni质量比为2.55mg/kg(DTPA)和茎叶Ni质量比为22.39 mg/kg.     

示踪技术用于气体泄漏扩散模拟的多元线性回归分析

采用江苏工业学院油气储运安全综合实验模型平台,利用示踪技术(以CO2为示踪剂),模拟了有害气体瞬时泄漏扩散的整个过程.并结合多元线性回归分析的基本方法,定量分析了气体泄漏扩散过程,建立了多元线性回归模型,初步确定了泄漏气体浓度与相关物理量的变化关系,在此基础上得到了2个定量评价指标:确定性系数R=0.991,相关系数r=0.995.研究表明,在实验室建立的试验模型能较好地反映现实情况,模型仿真度较高,数据拟合效果较好.研究可为评价模型的相似性提供理论参考,对有害气体泄漏扩散事故应急救援、实施有效的现场控制,具有一定的科学参考价值.     

微生物法液相氧化SO2

通过对酸性水溶液、含Fe³⁺水溶液、含Fe²⁺水溶液、细菌菌液和细菌培养基水溶液脱除二氧化硫的实验,探讨了微生物液相氧化二氧化硫的途径.以液相中SO₄^2-浓度考察了Fe³⁺浓度、Fe²⁺浓度、进口SO₂浓度以及温度对脱硫成酸的影响.微生物脱硫有2种机制:一是直接氧化作用,即氧化亚铁硫杆菌(Thiobacillus ferrooxidans)将S(IV)氧化成S(VI);二是间接催化氧化,氧化亚铁硫杆菌在酸性条件下具有快速氧化Fe²⁺成Fe³⁺,增强Fe³⁺对SO₂的液相催化氧化能力,研究表明微生物脱硫以间接催化氧化为主.在浓度0～1.2g/L之间,Fe³⁺和Fe²⁺浓度越高,脱硫效果越好,氧化亚铁硫杆菌表现出对Fe³⁺/Fe²⁺体系氧化SO₂的强化效果.入口SO₂浓度越高,细菌脱硫效率越低,但液相中SO₄^2-浓度随进口SO₂浓度增加变化不大.温度对微生物脱硫影响较大,最佳脱硫温度为30～40℃.