龙口褐煤对Ni^2＋,Mn^2＋,Hg^2＋等重金属离子的吸附特性

本文以龙口褐煤作吸附剂,对重金属离子Ｎｉ＾２,Ｍｎ＾２＋,Ｈｇ＾２＋的单组分水溶液进行吸附研究,探讨了吸附剂的吸附性能,影响吸附的因素和吸附机理。结果表明：褐煤对Ｎｉ＾２＋,Ｍｎ＾２＋,Ｈｇ＾２＋的吸附均表现出Ｌａｎｇｍｕｉｒ特征,ＰＨ值是影响吸附的一个重要因素。     

褐煤经磺化及碱化处理对重金属离子吸附性能研究

褐煤经磺化和碱化处理对褐煤吸附重金属的性能影响显著,通过对金属离子Ｃｕ＾２＋,Ｐｂ＾２＋,Ｚｎ＾２＋,Ｃｄ＾２＋,Ｎｉ＾２＋的单组分或多组分溶液进行吸附研究,对比了吸附速率、吸附容量、吸附选择性、耐酸性以及抗干扰能力等方面的差异,探讨了磺化褐煤和碱化褐煤对重金属离子的吸附机理,指出了今后的研究方向。     

水杨醛改性壳聚糖对金属离子的吸附性能

研究了以水杨醛改性的壳聚糖及其衍生物对Ｐｂ＾２＋、Ｚｎ＾２＋，Ｃｏ＾２＋的静态吸附性能，结果表明，该类吸附剂对Ｐｂ＾２＋，Ｚｎ＾２＋具有良了的吸附性能，其吸附量可分别达４５５．２和１０５．５ｍｇ·ｇ＾－１，并能在Ｃｏ＾２＋存在下选择吸附Ｐｂ＾２＋，Ｚｎ＾２＋。     

可变电荷土壤和矿物表面Cu^2＋吸附过程中H^＋释放动力学

本文以硝酸根离子选择电极为参比电极,低阻ｐＨ玻璃电极为指示电极,研究了红壤和高岭石体系Ｃｕ＾２＋吸附过程中ｐＨ的变化情况,并通过红壤和高岭石的酸碱滴定曲线求得了不同反应时间Ｈ＾＋释放的绝对量,即Ｈ＾＋释放动力学。结果表明,Ｃｕ＾２＋吸附过程中Ｈ＋释放大部分在反应刚开始时进行,反应进行５ｍｉｎ后,两种Ｃｕ＾２＋起始反应浓度的高岭石和红壤体系Ｈ＋分别释放了９２％和８２％以上。Ｃｕ＾２＋起始反应浓度愈大     

离子强度对恒电荷土壤胶体吸附Cu2+和Pb2+的影响

采用平衡法研究了离子强度、表面电位对恒电荷土壤胶体吸附Ｃｕ２＋和Ｐｂ２＋的影响．结果表明,离子强度越小,表面电位越高,土壤胶体对Ｃｕ２＋和Ｐｂ２＋的吸附量越大．在离子强度小于１．０ｍｏｌ·ｋｇ－１范围内,土壤胶体对Ｃｕ２＋和Ｐｂ２＋的吸附包括静电吸附和专性吸附;离子强度大于１．０ｍｏｌ·ｋｇ－１以后,土壤胶体对Ｃｕ２＋和Ｐｂ２＋的吸附受专性吸附控制．     

可变电荷土壤和矿物对Pb~（2＋）和Cu~（2＋）的吸附动力学Ⅵ．搅拌速度和土

利用双离子选择电极法研究了搅拌速度和土／水比对Ｐｂ２＋和Ｃｕ２＋在可变电荷土壤和矿物表面的吸附动力学的影响。结果表明：当搅拌器上所加电压为０—１００Ｖ时，Ｐｂ２＋和Ｃｕ２＋的吸附转化率随电压的增加而增大；当电压＞１００Ｖ后，吸附转化率不再变化。这表明在＜１００Ｖ的低速搅拌下，外扩散是Ｐｂ２＋和Ｃｕ２＋吸附反应的速率控制步骤，而在＞１００Ｖ的高速搅拌下，吸附步骤为速率控制步骤。Ｐｂ２＋和Ｃｕ２＋的吸附量随土／水比的增大而减小。在二级动力学方程中，最大吸附量Ｘｍ随土／水比的增大而减小，动力学常数Ｋ随土／水比的增加而增大。Ｐｂ２＋的Ｘｍ和水／土比（ｍｌ／ｇ）呈极显著正相关。     

泥炭和褐煤对Zn^2＋,Cu^2＋,Pb^2＋等重金属离子的吸附特征

利用天然有机吸附剂泥炭和褐煤对重金属离子Ｚｎ＾２＋，Ｃｕ＾２＋，Ｐｂ＾２＋的单组分水溶液进行吸附研究。对吸附模型，吸附时间，不同吸附剂投放量，金属离子种类等给予表征，基本符合Ｌａｎｇｍｕｉｒ吸附等温线。     

黄棕壤和红壤吸附磷酸根后对Zn^2＋和Cd^2＋次级吸附的动力学

本文用流动法考察湖北省黄棕壤和湖南省红壤吸附磷酸根后，对Ｚｎ＾２＋和Ｃｄ＾２＋次级吸附的动力学。结果表明，Ｚｎ＾２＋和Ｃｄ＾２＋的次级吸附动力学可用一级议程拟合。初级吸附的磷酸根可造成黄棕壤对Ｚｎ＾２＋和Ｃｄ＾２＋次级吸附的速率下降；而红壤对Ｚｎ＾２＋和Ｃｄ＾２＋次级吸附的快反应速率下降，慢反应速率加大。Ｚｎ＾２＋和Ｃｄ＾２＋浓度增高可加快次级吸附反应速率；升高温度也可增快次级吸附速率。扩散作用对     

华北地区城市地下水中主要离子含量升高机理分析——以洛阳市为例

本文以洛阳市为例，讨论了华北地区地下水中主要离子的背景浓度及其形成作用。在此基础上，重点阐述了地下水中Ｃａ＾２＋，Ｍｇ＾２＋浓度升高的若干机理，并对污染源各不相同的三个水源地地下水Ｃａ＾２＋，Ｍｇ＾２＋浓度升高机理进行了定量分析，比较了Ｃａ＾２＋，Ｍｇ＾２＋浓度与其它主要离子浓度的相关特征，研究表明：该区两类地下水主要形成了钙长石和镁榄石的风化作用，地下水中ＣＯ２分压升高，可促进Ｃａ，Ｍｇ硅酸盐，     

经过水泥固化的重金属废物的穿透渗漏实验

采用穿透渗漏实验方法研究了经水泥固化的重金属废物的长期渗漏行为。用由Ｐｂ＾２＋、Ｚｎ＾２＋、Ｃｕ＾２＋、Ｎｉ＾２＋和Ｃｒ＾６＋５种重金属组成的合成废物样品进行２组实验。实验研究了渗漏实验液流速、ＰＨ的变化和金属渗漏能力对固体废物长期渗漏行为的影响。     

森林土壤对几种重金属污染的"记忆"效应

采用一定浓度(40～120 mg·L-1)Cd、Cr、Pb的氯化物溶液多次浇灌森林土壤,研究受以前污灌影响而导致某次污灌后土壤对重金属的吸持率下降的效应--"记忆"效应.结果表明土壤对Cr和Pb环境容量大,"记忆"效应不明显.多次浇灌CrCl3溶液后,土壤剖面20 cm以下采样点约99%的Cr被土壤吸持;3次浇灌PbCl2后各采样点Pb浓度下降率维持在85%以上,但污灌次数进一步增加,则土壤的吸持率下降.Cd的环境容量较小,增加投入会很快使土壤上层对其吸附达到饱和,吸附带随之下移,对地下水的安全构成威胁.     

合成雪硅钙石净化含Hg~(2+)废水的实验

考察了雪硅钙石对水中的重金属Hg2+离子的吸附性能,通过单因素实验及正交实验,研究了试水的pH值、初始浓度、吸附时间、吸附温度等因素对雪硅钙石吸附Hg2+反应的影响,确定了优化吸附条件.测定了雪硅钙石对Hg2+的吸附等温线,并用Langmuir吸附等温式进行了拟合,计算了吸附热力学参数,并对其吸附动力学过程进行了分析计算.     

改性柚子皮吸附剂对模拟废水中pb2+的吸附性能

以废柚子皮为原料,经ZnCl2浸泡-加热的化学改性手段制备改性柚子皮生物吸附剂,并通过模拟试验研究该吸附剂对废水中pb2+的去除.考察了模拟废水的pH、吸附时间、吸附剂用量和pb2+初始浓度、温度等因素对柚子皮吸附剂去除pb2+的影响,并研究柚子皮吸附剂对pb2+的吸附动力学及吸附特征.结果表明,模拟废水的pH、吸附时间、吸附剂用量和pb2+初始浓度、温度等因素对柚子皮吸附剂吸附废水中pb2+均有显著影响.适宜的吸附条件为pH5.3～6.5,吸附时间1.5h,吸附剂用量10g· L-1,pb2初始质量浓度100 mg·L-1,温度30℃.在该条件下,废水中pb2+去除率在90％以上.柚子皮吸附剂对废水中pb2+的吸附符合动力学二级反应方程,等温吸附规律可用Langmuir、Freundlich和Temkin模型进行较好的描述.     

海泡石黏土矿物对Cu2+的吸附动力学研究

研究分析了海泡石黏土矿物对铜离子的吸附性能和动力学特征,结果表明,海泡石黏土矿物对Cu~(2 )吸附的最佳pH值为6.0左右,随着pH值的增大,吸附作用减弱;在[Cu~(2 )]=100mg·l~(-1),溶液pH值为6,吸附时间为2h时,添加0.1 g海泡石,海泡石对Cu~(2 )的吸附去除率仅为39.5%,当海泡石用量提高至0.4 g时,其对Cu~(2 )的吸附去除率提高到94.8%;实验结果同样显示,18min内有90%的Cu~(2 )被海泡石吸附,随着吸附时间的增加,吸附作用趋于稳定,2h可达到吸附平衡。该吸附过程符合Langmuir和Freundlich等温吸附方程.同时,分别采用拟一级模型和拟二级模型考察了吸附动力学,并计算了这些动力学模型的速率常数.实验数据和拟二级模型计算结果之间有较好的相关性.     

Characterisation of an extracellular polysaccharide produced by Bacillus mucilaginosus MY6-2 and its application in metal biosorption

A novel extracellular bioflocculant from Bacillus mucilaginosus MY6-2 was obtained by alcohol precipitation, dialysis and lyophilisation. The chemical analysis indicated that the bioflocculant was mainly composed of extracellular polysaccharide (named EPS MY6-2). Monosacchride composition result analysed by Gas chromatography indicated that EPS MY6-2 was mainly composed of Man, Glc, Gal, GlcA and GalA. The result of flocculating characteristics indicated that pH, EPS dosage and cation supplement had evident effect on flocculating activity of EPS MY6-2. The biosorption of iron ions from aqueous solution was tested with respect to pH, initial metal ion concentration and EPS dosage. The optimum biosorption conditions were as follows: pH 5.0, initial ion concentration from 200 to 800 mg/L and EPS dosage of 60 mg/L ion solution. The adsorption rates are maintained above 95% under these conditions. The adsorption data provided an excellent fit to both Langmuir and Freundlich isotherms, implying that the binding of the iron ions took place as a monolayer on the surface of the EPS.     

活性炭吸附水中铅离子的动态研究

本文采用两种煤质活性炭，研究了其对不同浓度二价铅离子溶液的吸附，应用固定床吸附动力学模型，Ｍａｒｑａｄｔ方法非线性回归固定床吸附流出曲线，获得了铅离子在活性炭上的扩散传质系数。结果发现，孔扩散系数Ｄｐ强裂地依赖于铅离子入口浓度，随着入口浓度的升高，孔扩散系数变小，随后用上述扩攻系数理论预测了其它操作条件下的流出曲线，结果表明实验曲线与理论预测曲线能很好地相符，动态法能可靠地获取固吸附过程的吸附及扩     

Lead(II) and cadmium(II) removal from aqueous solution using processed walnut shell: kinetic and equilibrium study

The biosorption potential of processed walnut shell for Pb(II) and Cd(II) ions from aqueous solutions was explored. The effects of pH, contact time, initial ion concentration, and amount of dried adsorbent were studied in batch experiments. The maximum adsorption was achieved within the pH range 4.0–6.0. The equilibrium data were well fitted by the Langmuir isotherm model. The maximum monolayer adsorption capacities were found to be 32?g?kg^?1 and 11.6?g?kg^?1 for Pb(II) and Cd(II) ions, respectively. Kinetic data were best described by the pseudo-second-order model. The structural features of the adsorbent were characterized by Fourier transform infrared spectroscopy, which confirmed the involvement of hydroxyl (–OH), carboxyl (–COO^–), and carbonyl (C=O) groups in metal sorption. This readily available adsorbent is efficient in the uptake of Pb(II) and Cd(II) ions from an aqueous solution and could be used for the treatment of wastewater streams bearing these metal ions.     

Heavy metals uptake from aqueous solutions using marine algae (Colpomenia sinuosa): kinetics and isotherms

The adsorption of copper, zinc, cobalt, lead and cadmium ions onto Colpomenia sinuosa was studied as a function of contact time, initial metal ion concentration and initial pH. In addition, desorption studies were performed. Characterisation of this adsorbent was also confirmed by Fourier transform infrared (FTIR) spectroscopy and scanning electron microscopy (SEM) analysis. Batch adsorption experimental data were analysed using Langmuir, Freundlich and Dubinin–Raduschkevich (D–R) adsorption isotherms. The results indicated that the biosorption equilibrium was well described by both the Freudlich and D–R isotherms. Moreover, sorption kinetics was performed and it was observed that equilibrium was reached in<60 min, which could be described by the pseudo-second-order kinetic model for all heavy metals. The sorption of heavy metals onto the biomass was largely dependent on the initial solution pH. The elution efficiency for heavy metal ions desorption from C. sinuosa was determined for 0.1 M HCl, 1.0 M HCl and 1.0 M HNO₃. Desorption efficiency and also adsorption capacity were highest for Pb(II). The results indicate that C. sinuosa has great potential for the removal of heavy metals in an ecofriendly process.     

不同作物原料热裂解生物质炭对溶液中Cd2+和Pb2+的吸附特性

选择由小麦秸秆、玉米秸秆和花生壳经350~500℃热裂解制成的生物质炭,研究生物黑炭对水溶液中Cd2+和Pb2+的吸附特性,分析了pH值、吸附时间、溶液初始质量浓度、生物质炭粒径和投加量对吸附效果的影响。结果表明:生物质炭对Cd2+和Pb2+的吸附约10 min即达平衡;3种生物质炭对Cd2+和Pb2+的等温吸附均可用Langmuir方程和Freundlich方程拟合,玉米秸秆炭对Cd2+和Pb2+的最大吸附量远大于小麦秸秆炭和花生壳炭;在生物黑炭投加量为150 mg(6 g.L-1)时,3种生物黑炭对溶液Cd2+的去除率均在90%以上,玉米秸秆炭对溶液Pb2+的去除率达90.30%,而小麦秸秆炭和花生壳炭的去除率仅为52%和47%,玉米秸秆炭有望成为处理重金属污染废水的新型吸附材料。     

不同作物原料热裂解生物质炭对溶液中Cd2＋和Pb2＋的吸附特性

选择由小麦秸秆、玉米秸秆和花生壳经350-500℃热裂解制成的生物质炭,研究生物黑炭对水溶液中Cd2＋和Pb2＋的吸附特性,分析了pH值、吸附时间、溶液初始质量浓度、生物质炭粒径和投加量对吸附效果的影响。结果表明：生物质炭对Cd2＋和Pb2＋的吸附约10 min即达平衡;3种生物质炭对Cd2＋和Pb2＋的等温吸附均可用Langmuir方程和Freundlich方程拟合,玉米秸秆炭对Cd2＋和Pb2＋的最大吸附量远大于小麦秸秆炭和花生壳炭;在生物黑炭投加量为150 mg（6 g.L-1）时,3种生物黑炭对溶液Cd2＋的去除率均在90%以上,玉米秸秆炭对溶液Pb2＋的去除率达90.30%,而小麦秸秆炭和花生壳炭的去除率仅为52%和47%,玉米秸秆炭有望成为处理重金属污染废水的新型吸附材料。