Kinetics and equilibrium of adsorption of dissolved organic matter fractions from secondary effluent by fly ash

Fly ash was used as a low-cost adsorbent for removing dissolved organic matter (DOM) in secondary effluent. Batch experiments were conducted under various adsorbent dosages, pH, contact time, temperatures and DOM fractional characteristics. Under the optimum conditions of fly ash dosage of 15 g/L, temperature of 303 K and contact time of 180 min, a removal of 22.5% of the dissolved organic carbon (DOC), 23.7% of UV-254, 25.9% of the trihalomethanes precursors in secondary effluent was obtained. The adsorption of DOM fractions onto fly ash all followed the pseudo second-order kinetic model, and the hydrophilic fraction adsorption by fly ash also fitted the intraparticle diffusion model quite well. Freundlich and Langmuir models were applicable to the fly ash adsorption and their constants were evaluated. The maximum adsorption capacities of the adsorptions revealed that fly ash was more effective in adsorbing hydrophilic fraction than the acidic fractions. Structure changes of the DOM fractions after fly ash adsorption were also characterized via spectrum analyzing. Those mechanisms presented critical step toward improved efficiencies of fly ash adsorption via further surface-modification.     

Removal of trace arsenic（V） and phosphate from water by a highly selective ligand exchange adsorbent

The ligand exchange adsorbent could be used to remove the toxic arsenic(V) and phosphate efficiently from water even in the presence of foreign anions and possible to apply in chemical industry.     

Removal of microcystin-LR from drinking water using a bamboo-based charcoal adsorbent modified with chitosan

The bamboo charcoal adsorbent modified with chitosan can effectively remove microcystin-LR from drinking water.     

Mechanism of Cd（II） adsorption by macrofungus Pleurotus platypus

The mechanism of Cd(II) uptake by the dead biomass of macrofungus Pleurotus platypus was investigated using di erent chemical and instrumental techniques. Sequential removal of cell wall components of the biosorbent revealed that structural polysaccharides play a predominant role in the biosorption of Cd(II). The adsorption kinetics fitted well with the pseudo second-order model suggested that the adsorption of Cd(II) on P. platypus involved a chemisorption process. Transmission electron microscopy of the cadmium exposed biomass confirmed the deposition of the metal mainly in the cell wall. Fourier transform infrared spectroscopic analysis of the metal loaded biosorbent confirmed the participation of –OH, –NH and C–O–C groups in the uptake of Cd(II). Energy dispersive X-ray analysis of the biosorbent before and after metal uptake revealed that the main mechanism of adsorption was ion-exchange. The e ectiveness of CaCl2 in the desorption of cadmium perhaps suggested the exchange of Ca2+ with Cd(II).     

Removal of Crystal Violet from aqueous solution using powdered mycelial biomass of Ceriporia lacerata P2

A simple and efficient biosorbent prepared from powdered mycelial biomass of Ceriporia lacerata was used to removal Crystal Violet, poorly degraded as recalcitrant molecule by microorganism.     

树脂吸附法处理黄连素模拟废水

利用树脂吸附法对黄连素模拟废水进行了试验研究,对5种大孔吸附树脂进行初步筛选,从中优选出最佳吸附树脂(大孔树脂H103)。考察了pH和树脂投加量对吸附效果的影响,绘制了动力学曲线和吸附等温线。结果表明:在黄连素浓度为1 000 mg/L,最佳初始pH为7.0的条件下,树脂最佳投加量为3.0 g。在最佳pH条件下,吸附等温线可用Freundlich等温吸附方程描述。     

树脂吸附法回收BIT的实验研究

BIT(1,2-苯并异噻唑-3-酮)是一种广谱高效的工业杀菌防霉剂,也是其他高档产品用的生物杀菌防霉剂的初始原料.其生产过程所产生的母液和和废水中残留较多的BIT,如直接排放不仅造成产品损失而且增加后续处理的难度,实验通过研究A、B、C型三种大孔吸附树脂对BIT的静态吸附性能,筛选出适于实际应用的A型树脂,并对其进行动...     

PVA大孔载体固定化微生物SBBR脱氮

用课题组研究开发的纳米复合聚氨酯大孔载体固定化微生物SBR脱氮.SBR一个运行周期按进水5 min,曝气2.5 h,沉淀l h,排水30min的方式连续进行.系统稳定后,考察其脱氮效率,结果表明,进水COD为30～l00mg/L,经过一个周期,出水COD达到饮用水一级标准;进水NH4+-N的浓度为4.5～24.2mg....     

介孔磁性微球的制备表征及其在环境中的应用

文章在Fe3O4(magnetite)纳米粒子的表面包覆一层SiO2(silica),再以十六烷基三甲基溴化铵(CTAB)表面活性剂作为结构导向剂,包覆一层介孔SiO2,形成一种核壳式介孔磁性二氧化硅材料(MS),然后在其表面引进巯基(mercapto)从而成为一种新型巯基修饰的磁性二氧化硅载体(MMS).这种材料是介...     

镁砂吸附剂的制备及其脱硫性能研究

以辽宁省大石桥市廉价镁砂为主原料,制备具有吸附功能的氧化镁吸附剂.活化后的吸附剂硫容较低,本文采用添加Na2CO3的方法提高吸附剂硫容.结果表明,采用饱和Na2CO3浸渍100 min,吸附剂硫容比原来提高两倍多.利用活化并添加助剂后的吸附剂进行脱硫试验,结果表明,当V(O2)∶V(SO2)=6～8、烟气温度为120～150 ℃、气体流量比V(H2O)∶V(O2)=2～4、SO2初始质量浓度为1 500～3 000 mg/m3、床层高度为5～7 cm时,脱硫效率达到92%.