Removal of cadmium using MnO2 loaded D301 resin

MnO2 loaded weak basic anion exchange resin D301 （Anion exchange resin, macroreticular weak basic styrene） as adsorbent has been prepared and applied to the removal of cadmium. The adsorption characteristics have been investigated with respect to effect of pH, equilibrium isotherms, removal kinetic data, and interference of the coexisting ions. The results indicated that the Cd^2＋ could be efficiently removed using MnO2 loaded D301 resin in the pH range of 3-8 from aqueous solutions with the co-existence of high concentration of alkali and alkaline-earth metals ions. The saturate adsorption capacity of the Cd^2＋ was 77.88 mg/g. The adsorption process followed the pseudo first-order kinetics. The equilibrium data obtained in this study accorded excellently with the Langmuir adsorption isotherm.     

Experimental investigation of the effect of sediment transport patterns on the adsorption of cadmium ions onto sediment particles

The mechanism of flow turbulence, sediment supply conditions, and sediment transport patterns that affect the adsorption of cadmium ions onto sediment particles in natural waters are experimentally simulated and studied in this study both in batch reactors and in a turbulence simulation tank. By changing the agitation conditions, the sediment transport in batch reactors can be categorized into bottom sediment-dominated sediment and suspended sediment-dominated sediment. It is found that the adsorption rate of bottom sediment is much less than that of suspended sediment, but the sediment transport pattern does not affect the final (equilibrium) concentration of dissolved cadmium. This result indicates that the parameters of an adsorption isotherm are the same regardless of the sediment transport pattern. In the turbulence simulation tank, the turbulence is generated by harmonic grid-stirred motions, and the turbulence intensity is quantified in terms of eddy diffusivity, which is equal to 9.84F(F is the harmonic vibration frequency) and is comparable to natural surface water conditions.When the turbulence intensity of flow is low and sediment particles stay as bottom sediment, the adsorption rate is significantly low, and the adsorption quantity compared with that of suspended sediment is negligible in the 6 h duration of the experiment. This result greatly favors the simplification of the numerical modeling of heavy metal pollutant transformation in natural rivers. When the turbulence intensity is high but bottom sediment persists, the rate and extent of descent of the dissolved cadmium concentration in the tank noticeably increase, and the time that is required to reach adsorption equilibrium also increases considerably due to the continuous exchange that occurs between the suspended sediment and the bottom sediment.A comparison of the results of the experiments in the batch reactor and those in the turbulence simulation tank reveals that the adsorption ability of the sediment, and in particular the adsorption rate, is greatly over-estimated in the batch reactor.     

Biosorption and retention of orthophosphate onto Ca(OH)2-pretreated biomass of Phragmites sp.

The biosorption of phosphorus in the form of orthophosphate(Po) from wastewater using biomass as the sorbent is of potential importance because the Po-loaded biomass could be applied in the agricultural sector as fertilizer and soil conditioner. However, biomass generally displays a very low affinity for Posorption and therefore biomass surface modification is required. In the present study, the biomass(as model grinded leaves of Phragmites sp. were used)was pretreated with Ca(OH)2to enhance Pobiosorption capacity(qe). The results indicate that the alkaline pretreatment resulted in a modification of surface functional groups. It was concluded that the main sorption mechanisms were ligand exchange and electrostatic attraction. A series of experiments were conducted to investigate the performance of the pretreated biomass for Pouptake under various conditions. Isotherm and thermodynamic studies were also applied and analyzed. The biosorption process was best described by the pseudo-second order kinetic model and Langmuir isotherm, which gave a qmaxof 12.27 mg P/g at 25°C and p H 7. The Ca(OH)2treated Phragmites biomass applied in this study for Porecovery may present some potential advantages in terms of costs and environmental impact.     

碱性阴离子交换纤维处理印染废水的研究

采用自制的弱碱性阴离子交换纤维处理含活性染料的印染废水,研究了该方法的处理效果及其影响因素。结果表明:弱碱性阴离子交换纤维处理含活性染料的印染废水有良好的效果,接枝率为70%～80%的离子交换纤维处理效果最佳。离子交换纤维用量、pH、反应温度和反应时间对处理效果有重要影响。初步探讨了离子交换纤维的脱色机理。     

Simultaneous adsorption of lead and cadmium on MnO2-loaded resin

MnO2-loaded D301 weak basic anion exchange resin has been used as adsorbent to simultaneously remove lead and cadmium ions from aqueous solution. The e ects of adsorbent dosage, solution pH and the coexistent ions on the adsorption were investigated. Experimental results showed that with the adsorbent dosage more than 0.6 g/L, both Pb2+ and Cd2+ were simultaneously removed at pH range 5–6. Except for HPO4 2??, the high concentration coexistent ions such as Na+, K+, Cl??, NO3??, SO4 2?? and HCO3??, showed no significant e ect on the removal e ciency of both Pb2+ and Cd2+ under the experimental conditions. The coexistence of Mg2+, Ca2+ caused the reduction of Cd2+ removal, but not for Pb2+. The adsorption equilibrium for Pb2+ and Cd2+ could be excellently described by the Langmuir isotherm model with R2 > 0.99. The maximum adsorption capacity was calculated as 80.64 mg/g for Pb2+ and 21.45 mg/g for Cd2+. The adsorption processes followed the pseudo first-order kinetics model. MnO2-loaded D301 resin has been shown to have a potential to be used as an e ective adsorbent for simultaneous removal of lead and cadmium ions from aqueous solution.     

水雾协同微波脱附再生树脂吸附剂

以溶剂热法合成的聚二乙烯苯（PDVB）树脂为吸附剂,苯、甲苯、二氯甲烷为典型的非极性吸附质,对比单一微波和超声雾化水协同微波条件下树脂的脱附再生效果,考察微波功率、水雾量、吸附质种类等对树脂脱附效果的影响.结果表明,PDVB 树脂在单一微波作用下对非极性有机分子的脱附率约为50%,而在超声雾化水协同作用下,PDVB 对苯、甲苯、二氯甲烷的脱附率均可达到90%以上.同时脱附床层的温度始终保持在40℃以下,不会造成树脂高温老化,多次吸附/脱附循环再生后,树脂结构仍能保持稳定,表明在微波条件下引入超声雾化水可强化体系的微波吸收能力,实现树脂吸附剂的快速脱附再生.     

磁性树脂对地下水中硝酸盐的去除效能及影响因素

利用小试实验研究了磁性离子交换树脂对水中硝酸盐的去除效能,并探讨了地下水中常见有机物及无机离子对其去除效能的影响.结果表明,磁性离子交换树脂对纯水中20mg/L的NO3--N的交换容量为55.91mg/mL,且去除速率较快,10min基本达到去除平衡;地下水中的腐殖酸类有机物对NO3--N的去除基本没有影响,而常见阴离子具有较明显的影响,其影响程度为SO42->CO32->Cl->HCO3-;针对徐州某水厂地下水的去除研究表明,通水倍数为500BV时磁性离子交换树脂对地下水中NO3--N的去除率约为50%左右.综上,磁性离子交换树脂可以作为去除地下水中的硝酸盐一种处理技术.     

天然沸石去除氨氮研究

研究了生物膜、悬浮物对天然沸石去除氨氮的影响及其沸石去除氨氮的主要途径。结果表明，沸石去除氨氮主要是离子交换作用，吸附很小，可忽略不计；由于生物膜对氨氮的同化作用，使得有生物膜的沸石对氨氮的交换容量高于无生物膜，其等温交换曲线换符合Freundlich吸附等温式：y/m=KC^l/n；沸石的吸附容量随着悬浮物浓度增高而降低，2者呈负指数关系；悬浮物对沸石离子交换的影响主要在孔扩散控制阶段，在膜扩散控制阶段影响较小；如果停留时间较短（少于3h)，悬浮物对沸石离子交换的影响不大。     

中国植被对氮和盐基阳离子吸收速率及其在土壤酸化中的作用

植被对氮和盐基阳离子的吸收是除酸沉降外另一个重要的土壤酸度来源.本研究基于中国植被的净初级生产力和元素化学组成确定了中国植被对氮和盐基阳离子的吸收速率.结果表明中国东南部,包括东北、华北、华东和华南地区,植被对氮的吸收速率普遍较低,而在中国的西北部吸收速率较高,并且由东南向西北逐渐递减对盐基阳离子来说,吸收速率较高(>2.0 keq·(hm²·a)^-1)的植被有亚热带、热带常绿阔叶林、温带石灰岩落叶阔叶林、温带落叶灌丛和亚热带、热带稀树灌木草原等,它们主要分布在华北西北部、云南南部和海南岛西部,而吸收速率较低(<0.5 keq·hm²·a)^-1)的植被则主要包括分布在东部亚热带地区的常绿针叶林以及分布在西部干旱地区的各种荒漠和草原尽管中国大多数地区不会因为植被吸收而造成显著的土壤酸度增加,但在少数地区,植物吸收造成的土壤酸度输入却不容忽视(>0.5 keq·(hm²·a)^-1)由于这些地区植被吸收造成的土壤酸度输入已经大于或相当于目前的酸沉降水平,而且两者之和也超过了土壤的风化速率,这些地区可能面临土壤的酸化问题.     

生物矿化针铁矿吸附废水中铬的实验研究

在静态条件下,利用生物矿化针铁矿对含铬模拟废水进行吸附实验研究.结果表明,生物矿化针铁矿对质量浓度在5 mg/L以下的含Cr2O72-,Cr3+模拟废水均具有较好的去除效果,平均去除率达94%,出水达到"污水综合排放标准"(GB 8978-1996);其吸附符合Langmuir与Freundlich模型.