壳聚糖对酸性篮黑B废水的处理研究

采用壳聚糖对酸性蓝黑B模拟废水进行处理,研究了溶液的酸度、吸附时间、溶液的初始浓度和溶液温度等对吸附效率的影响。结果表明,壳聚糖对酸性蓝黑B具有优良的吸附效果,在溶液初始浓度小于400 mg/L,pH=3.5~6,温度约为30~40℃,吸附处理30~40 m in,COD去除率可达90%以上。     

粉煤灰/膨润土颗粒的制备与pb2+吸附实验

以天然钙基膨润土和燃料废弃物粉煤灰为原料,工业淀粉为致孔剂,采用挤出-滚圆技术,制备了粉煤灰/膨润土复合颗粒吸附剂,并用于含Pb~(2+)溶液的吸附。研究了吸附时间、pH、投样量和溶液初始浓度对吸附性能的影响。结果表明,采用挤出-滚圆法制得的复合颗粒吸附剂大小均匀,表面没有裂纹,具有良好的机械强度。吸附实验中,在投样量10.0 g/L,溶液pH为6,吸附时间120 min,溶液初始浓度100 mg/L时,复合颗粒吸附剂对Pb~(2+)的去除率达到97.40%,吸附量为9.74mg/g。热力学实验表明吸附剂对Pb~(2+)的吸附更符合Langmuir吸附等温模型。     

热活化过硫酸盐降解氧氟沙星特性及响应面优化

为了探究热活化过硫酸盐（PS）技术对水中氧氟沙星（OFX）的氧化降解作用,考察了反应温度、体系的初始pH、PS的初始浓度、OFX的初始浓度对OFX降解效果的影响;并在单因素实验的基础上,选取反应时间、体系的初始pH、PS的初始浓度和OFX的初始浓度4个因素进行了响应面优化实验。结果表明：最佳降解条件为,反应温度60℃、PS初始浓度4.0 mmol/L、pH=4.7、OFX初始浓度0.03 mmol/L、反应时间60 min,此时OFX的降解率为81.29%;4个因素对热活化PS降解OFX均有影响,其影响显著性从大到小为反应时间、OFX的初始浓度、PS的初始浓度、初始pH。利用响应曲面法模拟出反应体系的最佳条件,经实验验证,OFX降解率为93.78%,与预测最佳结果95.00%基本相符,表明模型可靠有效。     

坡缕石对Zn^2＋的吸附性能及吸附工艺条件优化研究

从坡缕石粘土提纯人手，进行了坡缕石吸附Zn^2 的实验研究，结果表明坡缕石对水中Zn^2 的吸附性能主要受振荡速度、吸附时间、溶液pH值、吸附剂用量等因素影响，30℃时坡缕石对Zn^2 的等温吸附曲线同时符合Langmuir方程和BET方程。在本实验条件下，坡缕石对水中的Zn^2 (20mL，Zn^2 浓度均为50mg／L)的最佳吸附工艺条件为：振荡速度150r／min，吸附时间120min，吸附剂用量0．120g，溶液pH为6．2，此条件下去除率达到T95．5％。     

零价铁吸附-还原溶液中U(VI)的实验研究

研究零价铁(Zero-valent iron,ZVI)去除溶液中的U(VI),分析了pH值、反应时间、ZVI投加量、铀溶液初始浓度、其它离子(Mg2+、Mn2+、Cl-、NO-3、CO2-3和Cu2+)等条件因素对U(VI)去除效果的影响,并讨论其去除机理。结果表明:ZVI对溶液中U(VI)有较好的去除作用,在pH=4,振荡时间为120min,ZVI投加量为1.6g/L,铀溶液初始浓度为10mg/L,铀去除量为4mg/g时,U(VI)的去除率可达到63.7%。其它离子实验结果表明:Mg2+、Mn2+、Cl-、NO-3对ZVI去除U(VI)影响不超过3%,CO2-3和Cu2+影响相对较大。ZVI去除溶液中U(VI)以还原沉淀和吸附作用为主,吸附-还原反应遵循一级化学反应动力学方程。     

羟基磷灰石吸附水溶液中Cd~(2 )的影响因素的研究

对羟基磷灰石 (Hap)固定水溶性Cd2 的影响因素进行了较为系统的实验研究。实验表明 :去除率与Cd2 初始浓度呈负相关 ,在Cd2 初始浓度 <10mg/L时 ,与作用时间、pH值、Hap用量呈正相关 ,温度对去除率的影响较小。通过正交实验确定了最佳吸附条件 :Hap用量为 5g/L ,pH值为 6 ,作用时间 5min。     

羟基磷灰石吸附水溶液中Cd^2＋的影响因素的研究

对羟基磷灰石(Hap)固定水溶性Cd2+的影响因素进行了较为系统的实验研究.实验表明去除率与Cd2+初始浓度呈负相关,在Cd2+初始浓度<10 mg/L时,与作用时间、pH值、Hap用量呈正相关,温度对去除率的影响较小.通过正交实验确定了最佳吸附条件Hap用量为5 g/L,pH值为6,作用时间5 min.     

出芽短梗霉吸附水体中共存r(Ⅵ)、Cd(Ⅱ)重金属离子研究

利用出芽短梗霉进行吸附水体中Cr(Ⅵ)、Cd(Ⅱ)共存离子实验, Cr(Ⅵ)、Cd(Ⅱ)毒性浓度均为300 mg/L时,菌种生长良好.吸附性能实验结果表明:出芽短梗霉吸附水中Cr(Ⅵ)的最佳条件是pH值为3.0、时间为2 h、温度为30℃,吸附量为8.575 mg/g;吸附Cd(Ⅱ)的最佳条件是pH为5.0、时间为30 min、温度为30℃,吸附量为15.49 mg/g.     

出芽短梗霉吸附水体中共存Cr（Ⅵ）、Cd（Ⅱ）重金属离子研究

利用出芽短梗霉进行吸附水体中Cr（Ⅵ）、Cd（Ⅱ）共存离子实验, Cr（Ⅵ）、Cd（Ⅱ）毒性浓度均为300 mg/L时,菌种生长良好。吸附性能实验结果表明：出芽短梗霉吸附水中Cr（Ⅵ）的最佳条件是pH值为3.0、时间为2 h、温度为30℃,吸附量为8.575 mg/g;吸附Cd（Ⅱ）的最佳条件是pH为5.0、时间为30 min、温度为30℃,吸附量为15.49 mg/g。     

针铁矿及其前体吸附亚砷酸根离子的反应及预处理方法的影响

观察了针铁矿及其前体对溶液中亚砷酸根离子的吸附过程和吸附性能。3种吸附剂分别为氢氧化铁凝胶、经微波真空干燥的凝胶和80℃烘干的凝胶,它们均转变成了针铁矿。氢氧化铁凝胶与亚砷酸钠溶液混和后,溶液的pH值在6min内从9.71上升到10.36,原因是亚砷酸根离子置换了针铁矿和氢氧化铁中的氢氧根;40min后开始持续下降,和亚砷酸根离子与吸附剂之间的缩合反应有关。pH值的转折点并不意味着吸附反应的结束,但代表了反应类型的转变。这两种类型的反应受温度和气体溶解组分的影响不大。吸附剂经超声波处理后,改善了其在介质中的分散性,吸附效率因此普遍提高,但也造成了固体微粒难以分离的问题。经真空微波处理的凝胶对砷阴离子的吸附率优于另外两种吸附剂,去除率分别提高了53.18%和17.22%。其主要原因可能是凝胶中的水分子在微波辐射场作用下的高频振动,使其内部在干燥脱水过程中保持了较高的孔隙度;此外,吸附剂的表面活性在微波处理过程中亦有可能得到了改善。     

Influence of outside environmental variations on ammonia nitrogen adsorption characteristics of HVMT/PC/EPDM composite

A new kind of ammonia nitrogen (AN) sewage water treatment composite was prepared by melt blending, with synthetic rubber ethylene propylene diene monomer (EPDM) and polycarbonate (PC) as the matrix, the natural vermiculite (VMT) powder modified by hydrochloric acid solution (HVMT) as the filler. By Fourier transform infrared (FTIR) measurement and XRD measurement, it was confirmed that the HVMT was more suitable as filler than VMT. By considering the influence of pH, temperature, adsorption composite content and initial mass concentration on removal rate and adsorption capacity, it can be concluded that the removal rate increased first and then decreased with the increasing pH. “Room temperature” was the optimum temperature for the composite. The removal rate of AN increased with the increasing adsorption composite content. When the adsorption reached equilibrium, the removal rate remained unchanged; the adsorption capacity of AN increased with increasing initial concentration. The removal rate increased gradually with lower initial concentration of AN. When the initial concentration increased to a certain level, the removal rate started to decline. When the initial concentration and composite content showed adsorption equilibrium, the adsorption capacity remained unchanged. The composite can be recycled to be reused after regeneration for nine cycles; the AN adsorption capacity of composite was decreased by only 4.5 %. If the composite can be prepared in large-scale production lines, the costs of HVMT/PC/EPDM porous composite can be controlled at less than USD 16/kg.     

黄土对Cr(III)的吸附特性及机理研究

铬是一种重金属痕量元素,人体通过食物链摄入过量的铬会在人体内富集,随之产生中毒反应。研究Cr(III)的浓度、反应时间、反应温度、pH值等因素对Cr(III)在黄土上吸附特性的影响,结果表明黄土对Cr(III)的吸附非常迅速,并且吸附量非常大,等温吸附模型Freundlich和Dubinin-Radushkevich(D-R)模型都能很好地解释Cr(III)在黄土上的吸附过程。热动力学分析表明,吸附是一个自发的过程,升温可促进吸附作用的进行。随着温度的不断升高,Cr(III)的吸附量逐渐增大。溶液的pH值是影响Cr(III)吸附效果的一个重要因素,当pH>6时,Cr(III)几乎完全被去除。利用X光衍射图谱和红外光谱分析,探讨黄土与Cr(III)的结合机制,黄土中的高岭土、石英等黏土矿物以及有机质成分对吸附过程起重要作用。     

Removal of arsenate from aqueous media by magnetic chitosan resin immobilized with molybdate oxoanions

Chitosan was cross-linked using glutaraldehyde in the presence of magnetite. The resin obtained was chemically modified through the reaction with tetraethylenepentamine ligand. The obtained resin was loaded with Mo(VI) and investigated. The adsorption characteristics of the obtained resin toward As(V) at different experimental conditions were investigated by means of batch and column methods. The resin showed high affinity and fast kinetics for the adsorption of As(V) where an uptake value of 1.30 mmol g^?1 was reported in 6 min at 25 °C. Various parameters such as pH, agitation time, As(V) concentration and temperature had been studied. The kinetics and thermodynamic behavior of the adsorption reaction were defined. These data indicated an endothermic and spontaneous adsorption process and kinetically followed pseudo-second-order model, Fickian diffusion low and Elovich equation. Breakthrough curves for the removal of As(V) were studied at different flow rates and bed heights. The critical bed height for the studied resin column was found to be 0.656 cm at flow rate of 4 mL min^?1. The mechanism of interaction between As(V) and resin’s active sites was discussed. Regeneration and durability of the loaded resin toward the successive cycles were also clarified.     

Adsorption Behavior of Hexavalent Chromium in Vadose Zone

Adsorption behavior of Cr (VI) in vadose zone, which is silty clay and clayey soil, was studied through kinetics experiments, isothermal adsorption experiments under various conditions, including different ph, temperature and organic contents. The results from kinetics experiments showed that the sorption progress of Cr (VI) has clear features in different stages, and adsorption equilibrium showed at 30 min, the adsorption rate of silty clay and clayey soil were 60%. The isothermal adsorption curve of Cr (VI) fitted closely with Freundlich equation model. When pH is 3-5 a plateau were seen, thereafter with increase in pH the adsorption rate of Cr (VI) dropped sharply and the minimum achieved at pH 10, the adsorption rate were only 35%. Adsorption rate of Cr (VI) increased gradually with the increase of temperature, the temperature of vadose zone is 14.7 ℃, according to the experimental results, the adsorption rate of Cr (VI) is about 40%. The use of organics represents an important contribution to the sorption of Cr (VI), sorption rate up to 100% when 30% of organic content. These studies will provide basis for manager to minimize the impacts, and provide basic data for pollution prevention and remediation of vadose zone.     

Equilibrium studies on removal of lead (II) ions from aqueous solution by adsorption using modified red mud

In the present experimental study, solid waste was used as an adsorbent and the effectiveness of the adsorbent was increased by novel treatment methods. Red mud, acid-treated activated red mud and iron oxide-coated acid-treated activated red mud were used for the removal of lead (II). The structural and functional groups were identified to confirm the removal of lead (II) by powder X-ray diffraction and Fourier transform infrared spectroscopy analyses. The enhancement of surface area was confirmed by Brunauer–Emmett–Teller analysis. Batch adsorption experiment was also conducted, and various parameters such as the effect of adsorbent dosage, pH, contact time and initial ion concentration were analyzed and reported. Adsorption equilibrium data were investigated using Langmuir, Freundlich and Dubinin–Radushkevich isotherm models with three parameters, and the rate of reaction was examined through kinetic models. The results indicate that in particular a novel modified form of red mud, namely iron oxide-coated acid-treated activated red mud was well fitted in lead (II) removal compared with reported adsorbents. The Langmuir isotherm shows that the maximum adsorption of adsorbate per gram was greater than other adsorbents (27.02 mg/g). In Freundlich isotherm, the Freundlich constant n values lie between 1 and 10 indicate the favorable adsorption. The calculated n values for normal red mud, acid-treated activated red mud and iron oxide-coated acid-treated activated red mud were found to be 1.9, 2.1 and 2.0 respectively. The correlation coefficient value was higher and the rate of reaction follows the pseudo-second-order kinetic model.     

天然黄铁矿对阳离子有机染料RhB吸附特性研究

以黄铁矿作为吸附剂研究罗丹明B(Rhodamine B,RhB)的吸附特性,用X射线衍射仪(XRD)、扫描电子显微镜(SEM)对黄铁矿进行了表征。考察了接触时间、溶液pH值、离子强度、温度等对黄铁矿吸附RhB的影响。结果表明,在吸附平衡时间120 min、pH值4.0时,吸附量达到最大值21.3 mg/g。升高温度,黄铁矿对RhB的吸附量逐渐增大。而离子强度对吸附几乎没有影响。实验数据与Langmuir吸附模型拟合良好,整个吸附动力学模型符合准二级吸附动力学模型。热力学研究证实了该吸附过程是自发进行的。通过对吸附反应结束后的黄铁矿进行煅烧处理,去除表面吸附的RhB,结果表明煅烧一次的黄铁矿仍然可以吸附废水中约50%的RhB,具有重复利用的价值。     

Adsorption of lead using a new green material obtained from Portulaca plant

In the present study the potential of a new green material obtained from Portulaca oleracea plant was investigated. The material was used without any chemical treatment to study the adsorption behavior of lead ions from aqueous solution. Various batch experiments were carried out using different experimental conditions such as pH, contact time, adsorbent concentration, and metal ion concentration to identify the optimum conditions. The influence of these parameters on the adsorption capacity was studied. Results showed the optimum initial pH for adsorption as 6. Adsorption equilibrium was reached in 120?min. The adsorption data were modeled using both the Langmuir and Freundlich classical adsorption isotherms. Results show ~78% removal of lead from aqueous solution. The kinetic data corresponded well with pseudo second-order equation. From the initial results, the green material obtained from the waste of Portulaca seems to be a potential low-cost adsorbent for removal of lead ions from water.     

Application of dried plant biomass as novel low-cost adsorbent for removal of cadmium from aqueous solution

Heavy metals are a threat to human health and ecosystem. These days, great deal of attention is being given to green technologies for purification of water contaminated with heavy metal ions. Biosorption is one among such emerging technologies, which utilizes naturally occurring waste materials to sequester heavy metals from wastewater. Cadmium has hazardous impact on living beings; therefore, its removal through green and economical process is an important task. The aim of the present study was to utilize the locally available Portulaca oleracea plant biomass as an adsorbent for cadmium removal from aqueous solution. The biomass was obtained after drying and grinding the portulaca leaves and stem. No chemical treatment was done on the adsorbent so that it remained green in a true sense. Batch experiments were performed at room temperature. The critical parameters studied were effects of pH, contact time, initial metal ion concentration and adsorbent dose on the adsorption of cadmium. The maximum adsorption was found to be 72 %. The kinetic data were found to best fit the pseudo-second-order equation. High adsorption rates were obtained in the initial 45 min, and adsorption equilibrium was then gradually achieved in about 100 min. Adsorption increased with increase in pH for a range 2 and 6. The equilibrium adsorption results closely followed both the Langmuir and Freundlich isotherms. The values of constants were calculated from isotherms. Results indicated that portulaca plant biomass could be developed as a potential material to be used in green water treatment devices for removal of metal ions.     

Removal of chromium (VI) from aqueous solutions using Lewatit FO36 nano ion exchange resin

The removal of the chromium (VI) ion from aqueous solutions with the Lewatit FO36 ion-exchange resin is described at different conditions. The effects of adsorbent dose, initial metal concentration, contact time and pH on the removal of chromium (VI) were investigated. The batch ion exchange process was relatively fast and it reached equilibrium after about 90 min of contact. The ion exchange process, which is pH dependent showed maximum removal of chromium (VI) in the pH range 5.0–8.0 for an initial chromium (VI) concentration of 0.5 mg/dm³. The equilibrium related to Lewatit FO36 ion- exchange capacity and the amounts of the ion exchange were obtained using the plots of the Langmuir adsorption isotherm. It was observed that the maximum ion exchange capacity of 0.29 mmol of chromium (VLVg for Lewatit FO36 was achieved at optimum pH value of 6.0. The ion exchange of chromium (VI) on this cation-exchange resin followed first-order reversible kinetics.     

Removal of ibuprofen from aqueous solution by functionalized strong nano-clay composite adsorbent: kinetic and equilibrium isotherm studies

The functionalized nano-clay composite adsorbent was prepared, and its properties were characterized using FT-IR, XRD and SEM techniques. The synthesized nano-clay composite was studied with regard to its capacity to remove ibuprofen under different adsorption conditions such as varying pH levels (5–9), initial ibuprofen concentrations (3, 5 and 10 mg L^?1), contact time, and the amount of adsorbent (0.125, 0.25, 0.5 and 1 g). In order to evaluate the nanocomposite adsorption capacity, the adsorption results were assessed using nine isotherm models. The results showed that the optimum adsorption pH was 6 and that an increase or decrease in the pH reduced the adsorption capacity. The adsorption process was fast and reached equilibrium after 120 min. The maximum efficacy of ibuprofen removal was approximately 95.2%, with 1 g of adsorbent, 10 mg L^?1 initial concentration of ibuprofen, 120 min contact time and pH = 6. The optimal adsorption isotherm models were the Freundlich, Fritz–Schlunder, Redlich–Peterson, Radke–Prausnitz, Sip, Toth and Khan models. In addition, four adsorption kinetic models were employed for adsorption system evaluation under a variety of experimental conditions. The kinetic data illustrated that the process is very fast, and the reaction followed the Elovich kinetic model. Therefore, this nano-clay composite can be used as an effective adsorbent for the removal of ibuprofen from aqueous solutions, such as water and wastewater.