菲在沉积物上的吸附-解吸研究

采用批量实验的方法,研究了盐度对菲在沉积物上的吸附的影响以及菲的初始浓度、沉积物结构性质改变、盐度对菲解吸的影响,并深入讨论了不可逆吸附的机制.结果表明,提高盐度促进菲的吸附,促进程度与沉积物所含有机质（SOM）有关.由菲吸附增加计算得到的盐常数0.299 L·mol^-1高于由菲溶解度降低计算得到的盐常数0.125 L·mol^-1.菲的解吸具有不同程度的迟滞性,实验数据用Freundlich方程拟合,解吸迟滞性用热力学指数TII表征.随着菲初始加入浓度增加,TII值先降低后又增加,以淡水中菲的解吸为例,随着菲初始浓度由0.5 mg·L^-1增加到2.5 mg·L^-1,TII值先由0.80降到0.38又增加到0.55,表明解吸迟滞性呈先下降后增加的趋势.氢氧化钠处理后的沉积物与原沉积物相比解吸迟滞性减弱,TII值由0.55降到0.33,说明对菲的锁定能力变弱.首次报道了盐度对菲解吸的迟滞性影响,结果表明,菲的解吸迟滞性指数TII值由淡水中的0.55减少到盐水中的0.42,说明盐水中菲解吸迟滞性比淡水中弱,解吸迟滞性的变化可以用菲分布到的吸附点位能量高低不同以及菲分子是否能够锁定在吸附剂内部微孔来解释.     

淡水藻类对辛基酚的吸附行为研究

选取辛基酚(4-OP)作为目标物,研究了水中2种常见淡水藻(小球藻和鱼腥藻)对辛基酚的吸附.结果表明,2种藻对辛基酚的吸附量都很大,且吸附迅速.小球藻在混合后的5 min内即吸附了4-OP初始浓度(2 mg/L)的20%,鱼腥藻在混合后的5 min内即吸附了4-OP初始浓度(2 mg/L)的46%.吸附在1 h即达到平衡.模型拟合结果表明,辛基酚在藻表面的吸附符合Langmuir吸附等温式.水溶液pH值的变化对吸附的影响很大,降低pH值有利于2种藻对辛基酚的吸附,pH值对小球藻吸附辛基酚的影响比对鱼腥藻大.用荧光光谱法研究了藻与辛基酚的相互作用,结果表明,藻的加入可使辛基酚荧光强度降低,随着藻浓度的升高,藻/辛基酚体系荧光强度不变,荧光光谱向红端移动,根据此结果推测藻/有机污染物体系能更好地利用太阳光中的近紫外光线,从而促进有机污染物光降解.     

Adsorption characteristics of humic acid-immobilized amine modified polyacrylamide/bentonite composite for cationic dyes in aqueous solutions

Humic acid-immobilized amine modified polyacrylamide/bentonite composite (HA-Am-PAA-B) was prepared and used as an adsorbent for the adsorption of cationic dyes (Malachite Green (MG), Methylene Blue (MB) and Crystal Violet (CV)) from aqueous solutions. The polyacrylamide/bentonite composite (PAA-B) was prepared by intercalative polymerization of acrylamide with Nabentonite in the presence of N,N0-methylenebisacrylamide as a crosslinking agent and hexamethylenediammine as propagater. PAA-B was subsequently treated with ethylenediammine to increase its loading capacity for HA. The surface characterizations of the adsorbent were investigated. The adsorbent behaved like a cation exchanger and more than 99.0% removal of dyes was detected at pH range 6.0–8.0. The capacity of HA-Am-PAA-B was found to decrease in the following order: MG > MB > CV. The kinetic and isotherm data were interpreted by pseudo-second order rate equation and Freundlich isotherm model, respectively. Experiments were carried out using binary solute systems to assess the competitive adsorption phenomenon. The experimental isotherm data for each binary solute combination of MG, MB and CV were analyzed using Sheindrof-Rebhun-Sheintuch (SRS) (multicomponent Freundlich type) equation.     

Effect of background electrolytes on the adsorption of nitroaromatic compounds onto bentonite

To further elucidate interaction of nitroaromatic compounds with mineral surface, the sorption of m-dinitrobenzene (m-DNB) and nitrobenzene to original bentonite in aqueous solution containing di erent electrolytes (i.e., KCl, NH4Cl, CaCl2 and Tetramethylammonium bromide (TMAB)) was studied. The sorption of m-DNB was greatly enhanced with the presence of KCl and NH4Cl, while little influence was observed with CaCl2 and TMAB, following the order of KCl > NH4Cl TMAB, CaCl2, or DI water. For nitrobenzene, sorption enhancement only occurred at high nitrobenzene concentrations in the presence of KCl, and the solute equilibrium concentration at inflexion point was lowered with increasing KCl concentration. These sorption enhancements were significantly promoted with the increase of electrolyte concentration. The salting-out e ect is insu cient to account for the sorption enhancement by original bentonite with increasing KCl or NH4Cl concentration. X-ray di raction patterns of bentonite suspensions indicated that the sorption enhancement of m-DNB was attributed to the intercalation of K+ or NH4 + into bentonite interlayer and then dehydration with m-DNB to form inner-sphere complexes, which caused previously expanded bentonite interlayers to collapse in aqueous suspension, thus further enhanced the interaction of phenyl with siloxane surface. In comparison, the sorption enhancement of NB is attributed to the formation of outer-sphere complexes with K+ at high solute-loadings (> 200–400 mg/kg). The sorption of m-DNB to initially modified TMA+-bentonite and K+-bentonite was almost the same as respective sorption to original bentonite in solution containing TMA+ and K+.     

Influence of the wastewater composition on denitrification and biological P-removal in the S-DN-P process： （c） Dissolved and undissolved substrates

The denitrification and P-removal in the sorption-denitrification-P-removal (S-DN-P) process were carried out under various wastewater compositions. It is noted that P-removal largely depends on the wastewater composition as well to the quantity of the substrates present in wastewater fraction. Three different wastewater fractions are obtained as: raw wastewater, dissolved wastewater (obtained with filtration using 0.45 μm filter), and undissolved wastewater (i.e., infiltrate obtained by above filtration). ...     

Sorption of Triton X-100 on soil organic matter fractions：Kinetics and isotherms

Kinetics and isotherms of Triton X-100 sorption on soil,base-extracted soil(BE),humic acid (HA) and humin (HM) were investigated respectively to get better understanding on characteristics of the surfactant sorptiun onto different soil organic matters(SOMs).It was demonstrated that the kinetics results could be satisfactorily described by the pseudo-second order model.The half of the time to reach equilibrium(t1/2) for different sorbents followed the sequence of soil>HA>BE>HM.Furthermore,the calculated equilibrium sorption capacity(Ceq) was found in the sequence of HA>BE>HM>soil,which agreed well with the experimental results.The isotherms of Triton X-100 sorption on soil and HA could be well described by the S-type isotherm,but BE and HM by the L-type.The isotherms of all the four sorbents were found reasonably fitted to the Langmuir equation.The Kd value,defined as the ratio of Triton X-100 in sorbent and in the equilibrium solution for given concentrations,generally followed the order of HM>HA>soil>BE.Separated HM and HA showed high affinity for Triton X-100,but the HA and HM in soil and BE were tightly bounded by the minerals.Thus,the HA on the soil surface might dominate the sorption,whereas the bounded HM would play a key role upon the surfactants being penetrated inside the soil.     

Chitosan and chemically modified chitosan beads for acid dyes sorption

The capabilities of chitosan and chitosan-EGDE (ethylene glycol diglycidyl ether) beads for removing Acid Red 37 (AR 37) and Acid Blue 25 (AB 25) from aqueous solution were examined. Chitosan beads were cross-linked with EGDE to enhance its chemical resistance and mechanical strength. Experiments were performed as a function of pH, agitation period and concentration of AR 37 and AB 25. It was shown that the adsorption capacities of chitosan were comparatively higher than chitosan-EGDE for both acid dyes. This is mainly because cross-linking using EGDE reduces the major adsorption sites -NH3+ on chitosan. Langmuir isotherm model showed best conformity compared to Freundlich and BET. The kinetic experimental data agreed very well to the pseudo second-order kinetic model. The desorption study revealed that after three cycles of adsorption and desorption by NaOH and HCl, both adsorbents retained their promising adsorption abilities. FT-IR analysis proved that the adsorption of acid dyes onto chitosan-based adsorbents was a physical adsorption. Results also showed that chitosan and chitosan-EGDE beads were favourable adsorbers and could be employed as low-cost alternatives for the removal of acid dyes in wastewater treatment.     

Mechanism and kinetics of aluminum dissolution during copper sorption by acidity paddy soil in South China

Soil aggregates were prepared from a bulk soil collected from paddy soil in the Taihu Lake region and aluminum (Al) dissolution, solution pH changes during copper (Cu^2 +) sorption were investigated with static sorption and magnetic stirring. Kinetics of Cu^2 + sorption and Al dissolution were also studied by magnetic stirring method. No Al dissolution was observed until Cu^2 + sorption was greater than a certain value, which was 632, 450, 601 and 674 mg/kg for sand, clay, silt, and coarse silt fractions, respectively. Aluminum dissolution increased with increasing Cu^2 + sorption and decreasing solution pH. An amount of dissolved Al showed a significant positive correlation with non-specific sorption of Cu^2 + (R² > 0.97), and it was still good under different pH values (R² > 0.95). Copper sorption significantly decreased solution pH. The magnitude of solution pH decline increased as Cu^2 + sorption and Al dissolution increased. The sand and clay fraction had a less Al dissolution and pH drop due to the higher ferric oxide, Al oxide and organic matter contents. After sorption reaction for half an hour, the Cu^2 + sorption progress reached more than 90% while the Al dissolution progress was only 40%, and lagged behind the Cu^2 + sorption. It indicated that aluminum dissolution is associated with non-specific sorption.     

高岭土对喹诺酮类抗生素吸附特性的初步研究

以高岭土为吸附剂进行2种喹诺酮类抗生素(诺氟沙星和环丙沙星)的静态吸附实验,考察平衡时间、初始浓度、pH值、阳离子种类与强度等对吸附性能的影响.结果表明,高岭土对诺氟沙星和环丙沙星的吸附过程均符合二级反应动力学方程,吸附速率常数分别为0.021 kg/(mg·h)和0.156 ks/(mg·h);诺氟沙星和环丙沙星可划...     

菲与吡啶在沉积物及粘土矿物上的吸附行为

研究了菲和吡啶在天然沉积物及粘土矿物(高岭土、蒙脱土)上的吸附行为.结果表明,含有天然有机质的沉积物对菲的吸附最为显著,而高岭土和蒙脱土对菲也能发生一定程度的吸附.菲在3种吸附剂上的吸附行为比较符合线性模型,Kd分别为594.7L·kg-1(沉积物),405.OL·kg-1(高岭土)和286.7L·kg-1(蒙脱土).吡啶在3种吸附剂上吸附的Kd明显低于菲,在沉积物、高岭土和蒙脱土颗粒上分别为1.18,9.03和0.94 L·kg-1.CEC较大的沉积物和蒙脱土上吡啶的吸附量更低,这可能是背景溶液中Na+向此两种吸附剂表面大量聚集所致.总体上溶液pH值对于菲在3种吸附剂上的吸附影响较小,而对于吡啶而言,酸性和碱性条件均较中性条件更有利于其在粘土矿物上的吸附,其在沉积物上的吸附则随溶液pH值的增大而降低.