退耕还湖后湿地土壤对磷的吸附解吸特性

以安徽菜子湖区不同退耕年限(3、5、9和11年)湿地为研究对象,以相邻油菜地和原始湿地为对照(共6个样地),研究退耕还湖后湿地土壤对磷的吸附解吸特性变化.结果表明: 退耕湿地土壤对磷的等温吸附曲线与Langmuir和Freundlich吸附方程拟合程度均达极显著水平(P<0.01);6个样地土壤对磷的最大吸附量(X_m)、吸附常数(K)和最大缓冲容量(MBC)范围分别为478～1074 mg·kg^-1、0.14～0.61和68.6～661.5 mg·kg^-1,且退耕湿地的这些参数均随着退耕年限的延长而升高,但未达到原始湿地水平;6个样地土壤磷的平均解吸率为6.2%～14.6%,且退耕湿地土壤磷解吸率随着退耕年限的延长呈先增高后降低的趋势,但均显著高于原始湿地.表明随着退耕年限的增加,湿地土壤对外源磷的固持能力不断增强,而土壤有机质和粘粒含量是影响湿地土壤对外源磷固持能力的重要因子.     

几种粉煤灰对磷素吸附与解吸特性的研究

通过吸附解吸和培养试验, 研究了几种粉煤灰对磷素吸附与解吸特性.结果表明,粉煤灰的全磷含量和有效磷含量分别为0.545～4.540 g·kg^-1和19.55～163.0 mg·kg^-1,显著高于土壤,粉煤灰对磷吸附量随着加入溶液磷浓度的增加而增加,但其吸附率随着加入溶液磷浓度的增加而减少;粉煤灰的吸磷率比土壤高,但其解吸率低.这主要是由于粉煤灰比土壤存在更多的磷吸附位点且结合能大,不易解吸.Langmuir方程、Freundlich方程和Temkin方程都能很好地拟合粉煤灰对磷吸附,其中Langmuir方程的MBC、Freundlich方程的a和Temkin方程的k2都可以表征粉煤灰对磷吸附能力, MBC、a和k2值越大,则吸磷能力越强.不同来源的粉煤灰的MBC、a和k2值不同,其大小顺序为：湘潭电厂(5 167.7,4 056.2,831.5)>岳阳纸厂(1 650.7,2 803.4,711.9)>华能电厂(303.0,1 677.6,368.7)>株洲电厂(76.2,464.2, 211.0) > 洞庭氮肥厂(34.7,413.48,213.8).粉煤灰对磷吸附固定作用随粉煤灰含水量的增加有增大的趋势.粉煤灰对磷吸附主要是专性吸附和化学沉淀反应,所以在施用粉煤灰改良土壤或利用粉煤灰制造复混肥时,须考虑粉煤灰对磷的固定作用及粉煤灰含水量的影响.     

泉州市不同利用方式下土壤磷的吸附与解吸特性

分析了不同利用方式下泉州市土壤磷素吸附-解吸特征.结果表明:Langmuir等温方程式可以很好地表征土壤磷素的吸附特性;旱地和轮作地土壤对磷的吸附能力较强,而草地和林地土壤对磷的吸附能力较弱;磷的流失风险顺序为轮作地＞草地＞林地＞旱地;指导施磷量与吸附常数、最大缓冲量的大小顺序一致,为旱地＞轮作地＞林地＞草地;轮作地和草地的解吸率高于旱地和林地,土壤的缓冲能力顺序为旱地＞林地＞轮作地＞草地.主成分分析表明,平均解吸率、易解吸磷、磷吸附指数和磷零吸持平衡浓度4个指标最能反映土壤磷素流失潜力,可作为评价流失潜力的主要指标.     

不同污染负荷土壤中镉和铅的吸附－解吸行为

采用一次平衡法,对3种不同污染负荷土壤Cd2 和Pb2 的吸附-解吸行为进行了比较.结果表明,低污染负荷土壤对Cd2 和Pb2 的吸附能力高于高污染负荷土壤.3种土壤对Cd2 的吸附等温线与Freundlich方程有较好的拟合性,Pb2 的等温吸附过程可用Langmuir方程与Freundlich方程来描述.双常数方程是描述这3种不同污染负荷土壤中Cd2 和Pb2 吸附动力学行为的最优模型,其次为Elovich方程,最差模型是一级动力学方程.Pb2 的解吸滞后现象较Cd2 明显.高污染负荷土壤的吸附态Cd2 、Pb2 解吸率高于低污染负荷土壤,Cd2 、Pb2 解吸量与其初始吸附量之间的关系符合二次幂方程.3种土壤Cd2 、Pb2 的解吸速率随重金属初始浓度的增加而增加,随解吸时间的延长而降低.     

碳酸钙对土壤镉吸附及解吸的影响

采用等温吸附法,并以1mol/L KNO3进行解吸试验,研究CaCO3对3种土壤镉吸附和解吸的影响。结果表明,3种土壤的原状土样对镉吸附总趋势为：栗钙土＞棕壤＞淋溶褐土,均符合Langmuir方程、Frenudlich方程和Temink方程,其中以Freumdlich方程最佳。镉的专性吸附量表现为栗钙土＞淋溶褐土＞棕壤。添加CaCO3使3种土壤中镉的吸附量增加,增加幅度棕壤为4％－11％,淋溶褐土2％－11％,栗钙土2％－8％。外界加入的镉浓度越高,增加幅度越大。Freundlich方程（lgX=lgK lgC/n）拟合的参数结果表明：加入CaCO3后,K和n值均下降;Langmuir方程中镉最大吸附值增加,吸附平均常数减小。可以推测,CaCO3的存在之所以能够使土壤体系吸附镉能力增加,除CaCO3本身的吸附作用增加,吸附平衡常数减小。可以推测,CaCO3的存在之所以能够使土壤体系吸附镉能力增加,除CaCO3本身的吸附作用外,还可能影响反应体系的平衡系数。加入CaCO3,土壤对镉的专性吸附明显增加,尤其以棕壤专性吸附的镉最多,淋溶褐土其次,而栗钙土增加较少,栗钙土去除CaCO3后,镉的吸附减少了2.0%-26.0%,土壤专性吸附的镉减少4.0%-38.2%。3种土壤镉的解吸能力表现为：棕壤＞淋溶褐土＞栗钙土。添加CaCO3,土壤镉的解吸量下降。去除CaCO3后,栗钙土匐解吸量明显增加。     

湿地沉积物对磷的吸附-解吸动力学模型概述

介绍了常用的吸附-解吸动力学模型(Freundlich方程、Langmuir方程及Temkin模型),分析比较了不同模型之间的相互关系,对目前国内外关于磷吸附-解吸动力学模型研究进行了简要概述,介绍了不同模型的统一表达形式,并提出应加强对不同类型湿地中沉积物对磷的吸附-解吸过程及其动力学模型、对吸附-解吸过程的长期监测和不同环境因子间的交叉效应研究等建议,以深化对动力学模型的认识,从净化机理层面充分理解湿地生态系统的运行机制.     

青海湖鸟岛地区不同淹水条件下土壤酶活性的差异及其影响因素

湿地以常年性或周期性积水为特征,而水分条件的改变可直接影响湿地生态系统的结构和功能。为探究淹水条件对土壤酶活性的影响以及驱动酶活性变化的因素,在青海湖鸟岛地区选择长期淹水、周期性淹水和很少淹水的湿地,比较了土壤化学性质、微生物生物量碳氮以及酶活性的差异。结果表明:周期性淹水的湿地土壤β-葡萄糖苷酶、纤维二糖酶和甘氨酸氨基肽酶的活性较长期淹水的湿地分别下降了24.01%、18.80%和2.96%;而很少淹水的湿地较周期性淹水的湿地分别下降了33.65%、18.84%和63.47%。周期性淹水与长期淹水湿地的土壤N-乙酰氨基葡萄糖苷酶和亮氨酸氨基肽酶活性显著高于很少淹水的湿地,而很少淹水的湿地土壤碱性磷酸酶和酚氧化酶活性最高。冗余分析发现,土壤易氧化碳、全氮、有机碳、微生物生物量碳氮、水溶性有机氮与土壤酶活性显著相关,其中,有机碳与纤维二糖酶活性的相关性较高;易氧化碳能很好地解释β-葡萄糖苷酶、N-乙酰氨基葡萄糖苷酶和甘氨酸氨基肽酶活性的变化。总的来说,长时间淹水更有利于碳氮的积累,提高水解酶活性。     

香兰素在大孔吸附树脂上的吸附平衡、动力学及动态吸附过程

研究香兰素在大孔吸附树脂LX-02上的吸附平衡、动力学以及动态吸附和解吸过程。考察p H对香兰素吸附的影响,并测定不同温度条件下香兰素的吸附等温线。结果表明:树脂LX-02吸附香兰素的最适p H为4.5;Freundlich模型可以更好地拟合香兰素吸附等温线(R2=1),香兰素在LX-02树脂上的吸附为放热过程,最大吸附量为162.96 mg/g。吸附动力学结果表明,香兰素吸附动力学符合准二阶动力学模型。香兰素在树脂上的传质速率随着温度和浓度的增加而增加,且20 min内即可达到吸附平衡。动态吸附和解吸实验发现,温度升高会导致香兰素在树脂上的吸附量降低,而流量对树脂吸附香兰素的影响可忽略不计,因此,最佳上柱条件为温度298.15 K、流量2 m L/min,最适解吸剂为0.05 mol/L Na OH。     

湿地林土壤的Fe2+,Eh及pH值的变化

通过在不同含水量 (田间持水量的 6 0 % :对照处理 ;田间持水量的 2 5 0 % :淹水处理 )和不同温度 (2 0℃ ,2 5℃ ,30℃ )条件下的室内培养 ,对江苏省里下河地区池杉湿地林土壤的二价铁离子 (Fe2 )浓度 ,氧化还原电位 (Eh)及 p H值进行了研究。结果表明 ,与对照处理相比 ,淹水土壤的 p H值和 Fe2 浓度明显提高 (P<0 .0 1) ,而 Eh值则明显降低 (P<0 .0 1)。在淹水条件下 ,高温处理的土壤 p H值和 Fe2 浓度明显高于低温处理土壤 (P<0 .0 1) ,Eh值则相反。研究表明 ,土壤 Eh值与 p H值之间存在着密切的 3次方程式关系 (P<0 .0 0 1)。就里下河地区湿地林土壤而言 ,Eh值下降至 2 0 0 m V以下时 ,才会有大量的铁元素被还原为Fe2 。     

茶树根细胞壁对铅的吸附作用

以提取的水培茶树龙井43根细胞壁为供试材料,研究了茶树根细胞壁对Pb的吸附作用.结果表明:酸性条件下茶树根细胞壁对Pb的吸附量随着吸附液初始pH值的升高而增大,当初始pH值在2.0~4.5时Pb吸附量快速上升.在吸附液初始pH值为4.5的条件下,当吸附达到平衡时,随着吸附液Pb浓度的提高,茶树根细胞壁对Pb的吸附量增大,其吸附行为更适合用Freundlich吸附模型拟合.当达到吸附平衡时,根细胞壁的Pb吸附总量为9.7mg·g-1,当吸附时间达到320 min时根细胞壁对Pb的吸附量可以达到平衡吸附量的90%,从解吸动力学曲线来看,在60 min时Pb的解吸量可以达到平衡解吸量的50%,吸附、解吸动力学方程更适合用二级速率方程描述.根细胞壁分别经酯化、果胶酶改性、氨基甲基化改性处理后,其对Pb的累积吸附量与未改性处理相比分别降低了51.1%、41.3%和10.8%,表明根细胞壁上的-COOH、半乳糖醛酸多聚物果胶质及-NH2在一定程度上参与了Pb在茶树根细胞壁上的吸附.     

Thermodynamics of ouabain binding to human erythrocytes

A previous study reported that the uptake and release kinetics of ouabain by human erythrocytes in suspension could well be explained by a physical model which involves the slow Langmuir binding of the drug to the erythrocyte membrane. The purpose of the present investigation was to assess quantitatively the thermodynamics of this drug-membrane receptor interaction in order to evaluate the consistency of these parameters with the proposed kinetics model.Cellular drug uptake and release experiments were conducted at 20, 30 and 40°C, and the Langmuir adsorption and desorption rate constants as well as the Langmuir adsorption isotherms determined from the rate data. With the knowledge of these Langmuir parameters, it was possible to estimate the magnitude of all relevant thermodynamic properties by the use of established physicochemical theories.The activation energies and entropies for the ouabain adsorption and desorption processes were computed as 105 kJ/mol, 231 J/K per mol, 180 kJ/mol and 245 J/K per mol, respectively. The kinetic and isosteric heats of adsorption were found to be ?75.0 and ?72.4 kJ/mol, respectively. These findings suggest that the ouabain-erythrocyte membrane interaction represents a case of activated chemisorption which follows the Langmuir isotherm, thus, further underscoring the appropriateness of the Langmuir binding kinetics model.     

Batch and continuous adsorption of strontium by plant root tissues

Strontium (Sr) ions in aqueous solutions could be adsorbed by root tissue powders of Amaranthus spinosus, a common weed found in the fields. The adsorption isotherm could be fitted by either the Langmuir or the Freundlich model with the maximum adsorption capacity being 12.89 mg/g from the Langmuir isotherm. The maximum adsorption capacity of the biosorbent decreased with increasing temperature, whereas alkaline pretreatment enhanced the adsorption capacity 1.9 fold. Alginate gel beads (1 mm diameter) containing the root tissue powders were prepared and packed in a column for continuous adsorption/desorption of Sr in solution. Efficient desorption of Sr could be carried out with 0.1 CaCl₂ to give a concentrated Sr solution with 94% recovery.     

Adsorptive recovery and purification of prodigiosin from methanol/water solutions of Serratia marcescens fermentation broth

The use of macroporous polymeric adsorption resins for the recovery and purification of prodigiosin from fermentation broth of Serratia marcescens SMDR was systematically studied, in which the broth was pretreated by coagulation with alum and the resulting precipitate was leached by methanol/water solution. Of the seven resins tested, Diaion HP-20 resin was selected considering the adsorption and desorption abilities for prodigiosin at the same time. The optimal compositions of liquid phases for adsorption and desorption were also examined. Batch experiments were performed at 15 ～ 35°C by varying initial prodigiosin concentration in solution (0.05 ～ 0.5 mmol/L), in which molar fraction of each component in the solution was kept constant. The Freundlich and Langmuir equations were used to describe adsorption isotherms and the related thermodynamic functions were also determined. Fixed-bed experiments were finally conducted to obtain the breakthrough characteristics for the adsorption and desorption of prodigiosin. Under optimized conditions, a purification factor of prodigiosin of 11.4 could be obtained from the pretreated broth after one adsorption-desorption run in fixed bed. The present results had demonstrated the promising potential of HP-20 resins for the recovery and purification of prodigiosin from methanol/water solution of Serratia marcescens fermentation broth.     

择伐干扰对小兴安岭阔叶红松林土壤磷吸附解吸的影响

以小兴安岭地区阔叶红松林经过轻度、中度和强度择伐干扰后形成的天然林以及未经干扰的原始林(对照)林地表层(0～10 cm)土壤为对象,对土壤磷素的最大吸附量、吸附强度、最大缓冲容量、最大解吸量、平均解吸率和易解吸磷量等指标进行测定,研究不同干扰强度导致土壤磷吸附解吸的规律性变化,分析择伐干扰对阔叶红松林土壤磷吸附解吸特征的影响.结果表明: 各林地土壤磷最大吸附量为1383.93～1833.34 mg·kg^-1,中度和强度干扰林地显著高于轻度干扰林地和原始林地;磷吸附强度为0.024～0.059 L·mg^-1,强度和轻度干扰显著增加了林地土壤磷吸附强度;最大缓冲容量为35.68～97.97 L·kg^-1,强度干扰林地土壤的最大缓冲容量最高.择伐干扰显著降低了林地土壤的供磷潜力.各样地土壤磷最大解吸量、平均解吸率和易解吸磷量分别为526.32～797.54 mg·kg^-1、14.7%～25.5%和1.79～5.41 mg·kg^-1,林地土壤磷素释放能力随干扰强度的增加显著降低.择伐干扰通过降低林地土壤磷的供应及释放能力改变了阔叶红松林土壤磷吸附与解吸特征.     

Fast separation of bromelain by polyacrylic acid-bound iron oxide magnetic nanoparticles

The adsorption of bromelain from an aqueous solution by polyacrylic acid (PAA)-bound iron oxide magnetic nanoparticles was studied. The magnetic composite nanoparticles were shown to be efficient for the separation of bromelain. Except at pH <3, the adsorption of bromelain increased with the decrease in solution pH and reached almost 100% at pH 3–5. The adsorbed bromelain could be desorbed by the addition of KCl and complete desorption was achieved at pH 7 when [KCl]>0.6 M. The adsorption behaviour followed the Langmuir isotherm with a maximum adsorption amount of 0.476 mg/mg and a Langmuir adsorption equilibrium constant of 58.4 ml/mg at pH 4 and 0.1 M phosphate. In addition, it was notable that both the adsorption and desorption of bromelain were quite fast and could be completed in about 1 min due to the absence of internal diffusion resistance. Bromelain retained 87.4% activity after adsorption/desorption.     

Recovery of Acinetobacter radioresistens lipase by hydrophobic adsorption to n-hexadecane coated on nonwoven fabric

A simple and clean adsorption/desorption process was proposed for recovering Acinetobacter radioresistens lipase from fermentation broth. The adsorbent used was n-hexadecane coated on a hydrophobic nonwoven fabric (NWF). n-Hexadecane has a melting point of 16-18 degrees C, and its affinity for lipase decreases markedly from liquid to solid state. Accordingly, performing the adsorption and desorption above and below, respectively, the melting point would need no extraneous materials for separation. The adsorption isotherms at various temperatures were found to follow the Langmuir model. Simulation of the batch adsorption/desorption process showed that there exists an optimal amount of adsorbent for both concentration factor and enzyme recovery; the process is restrained by equilibrium. The performance of column adsorption/desorption could also be simulated using the adsorption isotherm, and it was shown that the concentration factor was proportional to the amount of adsorbent used. The benefits of this process include easy preparation of adsorbent, low operational cost, no extraneous materials needed, negligible enzyme denaturation, high efficiency, and simple process simulation.     

Recovery of ganoderic acids from <Emphasis Type="Italic">Ganoderma lucidum</Emphasis> mycelia by macroporous adsorption resins

In this work, the performance and adsorption characteristics of macroporous resins for the recovery and enrichment of ganoderic acid (GA)-Mk and GA-T from Ganoderma lucidum mycelia were systematically evaluated. ADS-8 resin displayed the best adsorption and desorption capacities among the tested resins based on batch experiments. The interaction between solute and ADS-8 resin at different temperatures was described in terms of Langmuir and Freundlich isotherms, and the equilibrium experimental data were well fitted to the two isotherms. Thermodynamic analysis indicated the exothermic and spontaneous nature of the adsorption process. The adsorption capacity of ADS-8 resin was found to depend strongly on the pH value of the initial solution. Dynamic adsorption and desorption tests were performed on an ADS-8 resin-packed column to obtain optimal parameters for recovering GA-Mk and GAT from G. lucidum extract. Under optimized conditions, a laboratory scale-up preparation of GA-Mk and GA-T was carried out. The contents of GA-Mk and GA-T were increased from 45 to 22 mg/g in the crude extract to 352 and 141 mg/g in the final product with recovery yields of 90.1 and 72.2%, respectively. These results demonstrated that ADS-8 resin chromatography could act as a useful approach for obtaining ganoderic acids from G. lucidum mycelia.     

Reactions of boron with soils

Boron is an essential micronutrient for plants, but the range between deficient and toxic B concentration is smaller than for any other nutrient element. Plants respond directly to the activity of B in soil solution and only indirectly to B adsorbed on soil constituents. Soil factors affecting availability of B to plants are: pH, texture, moisture, temperature, organic matter and clay mineralogy. Boron adsorbing surfaces in soils are: aluminium and iron oxides, magnesium hydroxide, clay minerals, calcium carbonate, and organic matter. Boron adsorption reactions can be described empirically using the Langmuir adsorption isotherm equation, the Freundlich adsorption isotherm equation, and the phenomenological Keren model. Chemical models such as the constant capacitance model, the triple layer model, and the Stern VSC-VSP model can describe B adsorption over changing conditions of solution pH and B concentration. Boron desorption reactions often exhibit hysteresis. The rate of B desorption can be described using the first order rate equation, the Elovich reaction rate equation, and the power function equation.     

Adsorption and Desorption of Nickel(II) Ions from Aqueous Solution by a Lignocellulose/Montmorillonite Nanocomposite

A new and inexpensive lignocellulose/montmorillonite (LNC/MMT) nanocomposite was prepared by a chemical intercalation of LNC into MMT and was subsequently investigated as an adsorbent in batch systems for the adsorption-desorption of Ni(II) ions in an aqueous solution. The optimum conditions for the Ni(II) ion adsorption capacity of the LNC/MMT nanocomposite were studied in detail by varying parameters such as the initial Ni(II) concentration, the solution pH value, the adsorption temperature and time. The results indicated that the maximum adsorption capacity of Ni(II) reached 94.86 mg/g at an initial Ni(II) concentration of 0.0032 mol/L, a solution pH of 6.8, an adsorption temperature of 70°C, and adsorption time of 40 min. The represented adsorption kinetics model exhibited good agreement between the experimental data and the pseudo-second-order kinetic model. The Langmuir isotherm equation best fit the experimental data. The structure of the LNC/MMT nanocomposite was characterized by X-ray diffraction (XRD) and transmission electron microscopy (TEM), whereas the adsorption mechanism was discussed in combination with the results obtained from scanning electron microscopy (SEM), energy-dispersive X-ray spectroscopy (EDX), and Fourier-transform infrared spectroscopy analyses (FTIR). The desorption capacity of the LNC/MMT nanocomposite depended on parameters such as HNO₃ concentration, desorption temperature, and desorption time. The satisfactory desorption capacity of 81.34 mg/g was obtained at a HNO₃ concentration, desorption temperature, and desorption time of 0.2 mol/L, 60 ºC, and 30 min, respectively. The regeneration studies showed that the adsorption capacity of the LNC/MMT nanocomposite was consistent for five cycles without any appreciable loss in the batch process and confirmed that the LNC/MMT nanocomposite was reusable. The overall study revealed that the LNC/MMT nanocomposite functioned as an effective adsorbent in the detoxification of Ni(II)-contaminated wastewater.