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1.
通过吸附实验研究纳米TiO2对Cd(Ⅱ)的吸附行为,考察溶液的pH值、吸附时间和温度等因素对吸附的影响。结果表明:在pH为4~7范围内,纳米TiO2对Cd(Ⅱ)的吸附率均超过97%,吸附于纳米TiO2上的Cd(Ⅱ)可用7.0 mL 0.1 mol/L HCl于70℃恒温水浴中定量洗脱;该吸附过程符合准二级反应动力学模型,其反应的表观活化能为3.16 kJ/mol,粒子内部扩散过程是其吸附过程的速率控制步骤,但液相边界层向粒子表面的扩散过程亦不能忽略;等温吸附数据与Langmuir和D-R等温模型拟合较好。在室温下,纳米TiO2对Cd(Ⅱ)的饱和吸附容量为6.34 mg/g,平均吸附能为11.54 kJ/mol;吸附反应的焓变和熵变均为正值,自由能为负值,说明该吸附过程为自发的吸热过程。  相似文献   

2.
合成了ZnO、NiO和ZnO@NiO纳米晶粒,采用红外光谱(FTIR)、X射线衍射(XRD)和扫描电镜(SEM)技术对其进行表征。ZnO、NiO和ZnO@NiO的平均颗粒尺寸为32、50和48 nm。对这些纳米晶粒去除氰化物的能力进行了测定。实验结果表明,与ZnO和NiO相比较,ZnO@NiO纳米晶粒去除氰化物的能力更强。ZnO@NiO纳米晶粒对氰化铁的去除能力比对氰化钠的更高。研究了反应时间、溶液pH值(2~12)、纳米晶粒用量(0.02~0.4 g)和氰化物浓度(5~50 mg/L)等参数对氰化物去除效果的影响。在最优条件下:pH5,纳米晶粒用量0.2 g,反应时间30 min,ZnO@NiO纳米晶粒对20 mg/L氰化物的去除率可达到90%以上。ZnO@NiO纳米晶粒对氰化物的吸附去除动力学影响规律符合Langmuir准二级吸附动力学模型(k2=4.66×10-2,R=0.999)。热力学研究表明,25°C下,反应的标准焓变化为7.87 kJ/mol,自由能变化为-18.62 kJ/mol。纳米晶粒对氰化物的吸附是一个吸热的自发过程。ZnO@NiO纳米晶粒是一种能有效的去除水或废水中氰化物的吸附剂。  相似文献   

3.
研究了用201×7强碱性阴离子交换树脂对氯化浸出液中低浓度铂的吸附性能,考察了树脂用量、吸附时间、pH值、反应温度等因素对树脂吸附铂的影响。实验结果表明,pH=1.0时树脂的吸附效果最佳,静态饱和吸附容量可达到190 mg Pt/g干树脂,铂在201×7树脂上的吸附是吸热反应,温度升高有利于铂的吸附,吸附反应热焓变ΔH=36.72 kJ/mol,熵变为ΔS=0.190 kJ/(mol·K)。对201×7树脂吸附铂的吸附等温模型及动力学进行了分析,结果表明,吸附平衡过程符合Langmuir等温式,且为优惠吸附;铂的吸附过程符合准二级动力学方程,准二级常数为k2=1.58×10-4g/(mg·min)。用2.4 mol/L的高氯酸可将载铂树脂中的铂洗脱,洗脱率为83%。  相似文献   

4.
研究用D113弱酸性树脂吸附锌(Ⅱ)的过程.结果表明D113树脂对锌离子的吸附在pH=6.20的Hac-NaAc介质中最佳,每克树脂在298 K下静态饱和吸附容量为172 mg;用2~3 mol/L的盐酸溶液进行洗脱,一次洗脱率可达100%.不同温度下,树脂吸附锌的表观吸附速率常数分别为k288k=1.82X 10-5/s、k298K=2.34X 10-5/s、k308k=2.81×10-5/s、k313k=3.26×10-5/s;表观吸附活化能Ea=17.0 kJ/mol.测得热力学参数分别为△H=30.3 kJ/mol,△S=160J/(mol·K),△G=-17.4 kJ/mol等温吸附服从Frcundlich和Langmuir经验式.  相似文献   

5.
光化学还原过程中纳米TiO2表面 Hg(Ⅱ)的吸附与脱附   总被引:4,自引:0,他引:4  
采用石英晶体微天平现场技术研究了Hg(Ⅱ)离子在纳米TiO2表面的吸附及光化学还原过程.结果表明:Hg(Ⅱ)离子借助于纳米TiO2表面羟基发生吸附,吸附平衡常数约为3.9×105L/mol,且Hg(Ⅱ)离子的吸附量受溶液的pH值、浓度和共存阴离子的影响;在pH值为4的HgCl2溶液中,Hg(Ⅱ)离子在纳米TiO2上的饱和吸附量约为0.85 mmol/g;在UV光照射下,初始阶段TiO2表面水光解产生的质子可使吸附的Hg(Ⅱ)离子从TiO2表面脱附下来,而且Hg(Ⅱ)浓度和pH值越大,脱附现象越明显;随后Hg(Ⅱ)光还原沉积逐渐占主导地位,且光沉积速率受Hg(Ⅱ)浓度、溶液pH值和有机物加入的影响.  相似文献   

6.
研究了未溶和回火析出的(Ti,Mo)C析出相的氢陷阱作用对调质铬钼钢的超高周疲劳性能的影响。结果表明:球形未溶(Ti,Mo)C析出相的氢解吸附激活能为142.6 kJ/mol,这种强氢陷阱在电化学充氢条件下不会捕获氢;细小的回火(Ti,Mo)C析出相是有效的氢陷阱,其捕获的氢的解吸附激活能为17.0 kJ/mol,这部分氢的扩散系数较小,室温放置336 h仍不能扩散出试样,但在循环载荷下能够从氢陷阱处解吸附并且向裂纹尖端或应力集中处扩散,仍能在一定程度上降低钢的超高周疲劳强度;位错和晶界处的可逆氢的解吸附激活能为16.9 kJ/mol,这部分氢扩散系数较大,室温放置96 h就能全部扩散出试样,在循环载荷下这部分氢能够迅速向裂纹尖端或应力集中处扩散,显著降低疲劳裂纹扩展应力强度因子门槛值,最终显著降低超高周疲劳强度;考虑到两者捕获的氢含量相当,被细小的回火(Ti,Mo)C析出相捕获的氢对超高周疲强度的有害作用要远小于位错、晶界处的可扩散氢对超高周疲劳强度的有害作用。非金属夹杂物的氢解吸附激活能为70.9 kJ/mol,这种强氢陷阱在电化学充氢条件下同样不会捕获氢。  相似文献   

7.
以钛酸四丁酯为钛源,NH4Br为溴源,应用水热技术制备Br掺杂纳米多孔TiO2材料(Br/TiO2)。利用X射线衍射仪和场发射扫描电镜表征材料的结构和形貌,并从热力学和动力学角度研究Br/TiO2对阳离子蓝X-GRL的吸附行为。结果表明:Br掺杂有利于形成棒状交联的多孔结构,增强TiO2对阳离子蓝X-GRL的吸附性能,吸附效率为92.2%,是空白样品的1.56倍。动力学研究表明:该吸附行为符合准二级动力学模型,测得其表观活化能为14.551 kJ/mol,说明该吸附属于物理吸附。热力学研究表明:Br/TiO2对阳离子蓝X-GRL吸附自由能变为8.343-5.600 kJ/mol,吸附熵变为137.10 J/(K.mol),吸附焓变为33.773 kJ/mol,该吸附过程是一个自发的吸热过程。  相似文献   

8.
对Mo和Al 2 O 3/Mo纳米粉末进行模压成形,研究纯Mo和Al 2 O 3/Mo压坯在1700~2000℃温度范围内的等温烧结过程,并结合烧结模型分析材料烧结过程中的动力学;利用SEM和TEM分析复合材料的显微组织。结果表明:压坯密度与Al2O3的加入量有关,高温烧结时Al2O3/Mo复合材料的致密度高于纯Mo的致密度;在Al2O3/Mo复合材料烧结过程中,烧结机制既有体积扩散又有晶界扩散,且随着Al2O3含量的增加,晶界扩散趋势明显;纯Mo和Al 2 O 3体积分数为5%、10%和15%Al 2 O 3/Mo复合材料的烧结激活能分别为254.24、234.04、221.40和164.37 kJ/mol;Al 2 O 3的加入可促进晶粒的均匀化和组织的细化。  相似文献   

9.
通过溶胶?凝胶法制备氨基修饰的磁性纳米粒子。以紫外分光光度法为检测手段,采用静态批次实验研究不同实验参数(吸附时间、溶液 pH 和溶液温度)对铜离子吸附的影响。对铜离子的动力吸附学过程符合准二级动力学模型。准一级动力学模型证明其对铜离子的吸附是一个基于内部粒子扩散的过程。吸附等温线数据既符合Langmuir吸附等温模型又符合Dubinin?Radushkevich吸附等温式。随着溶液pH的增加和温度的升高,水中铜离子的去除效率也增加。另外,铜离子在低 pH 时可以很容易地从吸附材料上面洗脱下来,并且在材料重复使用5次之后,铜离子的回收率仍然保持在90.0%以上。根据吸附活化能和热力学实验结果,可以推断铜离子在吸附剂上的吸附机制是离子交换?表面络合。  相似文献   

10.
研究了未溶和回火析出的(Ti,Mo)C析出相的氢陷阱作用对调质铬钼钢的超高周疲劳性能的影响.结果表明:球形未溶(Ti,Mo)C析出相的氢解吸附激活能为142.6 kJ/mol,这种强氢陷阱在电化学充氢条件下不会捕获氢;细小的回火(Ti,Mo)C析出相是有效的氢陷阱,其捕获的氢的解吸附激活能为17.0kJ/mol,这部分...  相似文献   

11.
To understand the mechanism of fluoride removal from the simulated zinc sulfate solution by the La(III)-modified zeolite, the adsorbent was characterized by XRD, SEM and EDS. The effects of absorbent dose and contact time, the adsorption isotherms and the sorption kinetics were investigated. The experimental results were compatible with the Langmuir isotherm model. The theoretical maximum adsorption capacities are 20.83 and 23.04 mg/g at 303 and 313 K, respectively. And the physisorption is revealed using the Temkin isotherm model and the D–R isotherm model. The sorption process is more suitable by the pseudo-second-order kinetic models. Thermodynamic parameters such as standard free energy change (ΔGΘ<0 kJ/mol), standard enthalpy change (ΔHΘ=8.28 kJ/mol) and standard entropy change (ΔSΘ=0.030 kJ/(mol·K)) indicate the spontaneity of adsorption and endothermic physical sorption. Furthermore, the fluoride concentration in the industrial zinc sulfate solution decreases from 98.05 to 44.09 mg/L with the adsorbent dosage of 15 g/L.  相似文献   

12.
The adsorption properties of XSD-296 for Cr(Ⅵ) were studied by using chemical analysis and infrared spectrometry. Experimental results show that XSD-296 resin has a good adsorption ability for Cr(Ⅵ) at pH=2.6 in the HAc-NaAc medium. The statically saturated adsorption capacity is 235 mg/g resin. The apparent activation energy of adsorption reaction, Ea, is 16.73 kJ/mol, and the thermodynamic parameters are △H=11.62 kJ/mol, △G298 K=-4.13 kJ/mol. The adsorption behavior of resin for Cr(Ⅵ) is in accordance with Freundlich adsorption isotherm. Cr(Ⅵ ) adsorbed on resin can be eluted by 5%NaCl-5%NaOH or 5%NH4Cl-5%NH3-H2O quantitatively. Infrared spectra and adsorption mechanism show that the functional group of resin coordinates with Cr(Ⅵ) to form co-ordination compound. The coordination molar ratio of the functional group of resin to Cr(Ⅵ) is 1:1.  相似文献   

13.
A strong acidic ion exchange resin(NKC-9)was used as a new adsorbent material for the removal of Co(Ⅱ)from aqueous solutions.The adsorption isotherm follows the Langmuir model.The maximum adsorption capacity of the resin for Co(Ⅱ)is evaluated to be 361.0 mg/g by the Langmuir model.It is found that 0.5 mol/L HCl solution provides effectiveness of the desorption of Co(Ⅱ)from the resin.The adsorption rate constants determined at 288,298 and 308 K are 7.12×10-5,8.51×10-5and 9.85×10-5s-1, respectively.The apparent activation energy(Ea)is 12.0 kJ/mol and the adsorption parameters of thermodynamic are-H Θ=16.1 kJ/mol,-SΘ=163.4 J/(mol·K),-G Θ 298 K=-32.6 kJ/mol,respectively.The adsorption of Co(Ⅱ)on the resin is found to be endothermic in nature.Column experiments show that it is possible to remove Co(Ⅱ)ions from aqueous medium dynamically by NKC-9 resin.  相似文献   

14.
使用乙二胺改性的木屑黄原酸盐对水溶液中的Cu(II)、Ni(II)离子进行吸附。在单离子体系中,考虑影响因素(温度、投加量)对Cu(II)、Ni(II)单离子吸附等温线的影响;并计算Cu(II)、Ni(II)离子吸附的热力学参数:吸附吉布斯自由能(△GΘ)、吸附过程的焓变(△HΘ)以及熵变(△SΘ),表明此吸附是一个放热自发的过程。在 Cu(II)和Ni(II)双离子体系中,采用修正后的拓展Langmuir模型对体系的吸附情况可以进行很好的预测。在单离子体系和双离子体系中,吸附过程的数据均可通过准二级动力学模型进行描述;计算得到其对Cu(II)和Ni(II)单离子的吸附活化能分别为59.12和55.92 kJ/mol。结果表明,金属离子在改性木屑表面的吸附效果会受到另一离子存在的影响。  相似文献   

15.
Pt (Ⅳ) was quantitatively adsorbed by D301R resin in the medium of pH=3.47. The statically saturated adsorption capacity is 410 mg/g.Pt (Ⅳ) adsorbed on D301R resin can be eluted by 1.0-2.0 mol/L NaOH. The rate constant is k298=5.43×10-5s-1. The adsorption of Pt (Ⅳ) on D301R resin obeys the Freundlich isotherm. The adsorption parameters of thermodynamics are as follows: enthalpy change ΔH=4.37 kJ/mol, Gibbs free energy change ΔG=-5.39 kJ/mol, and entropy change ΔS=32.76 J/(mol.K). The apparent activation energy is Ea=22.5 kJ/mol. The coordination molar ratio of the functional group of D301R resin to Pt(Ⅳ) is 2:1.  相似文献   

16.
The comparative study on adsorptions of Pb( Ⅱ ) and Cr(Ⅵ) ions by free cells and immobilized cells of Synechococcus sp. was performed, in which different aspects including Zeta potential of the cells, the influence of pH, temperature and initial concentration of metal ions, as well as adsorption kinetics and mechanism were referred. The lyophilized free cells have a surface isoelectric point at pH 3, and the correlative experiment indicates that there is an electrostatic adsorption feature of Cr(Ⅵ) and Pb( Ⅱ ) The immobilization of the free cells by Ca-alginate does not significantly modify the adsorption features of the biosorbent. The absorption processes of Cr(Ⅵ) and Pb(Ⅱ) on both free and immobilized cells are apparently affected by pH and the initial concentration of metal ions in the bulk solution, but are much weakly affected by temperature in the test range of 10-50 ℃. The slow course of biosorption follows the first order kinetic model, the adsorption of Pb(Ⅱ) obeys both Langmuir and Freundlich isotherm models, while the adsorption of Cr(Ⅵ) obeys only Freundlich model. FT-IR results indicate that carboxylic, alcoholic, amide and amino groups are responsible for the binding of the metal ions, and reduction of Cr(Ⅵ) to Cr(Ⅲ) takes place after Cr(Ⅵ) adsorbs electrostatically onto the surface of the biosorbents.  相似文献   

17.
采用离子交换树脂法吸附铬(Ⅲ),通过树脂选型确定强酸性阳离子交换树脂001×14.5对铬(Ⅲ)吸附容量最大,用所选的001×14.5树脂研究铬(Ⅲ)的吸附性能。静态吸附实验表明:转速大于120 r/min时,对树脂吸附的影响可忽略,即外扩散基本消除,pH=7.0时,吸附最佳,铬(Ⅲ)吸附率随树脂用量的增加而增大;001×14.5树脂吸附铬(Ⅲ)的过程符合Langmuir等温曲线,且为优惠吸附;吸附过程符合拟二级动力学方程,吸附过程的表观活化能Ea=23.4 kJ/mol,颗粒内扩散为吸附速率的主要控制步骤;用1 mol/L的硫酸对吸附后的饱和树脂进行脱附再生,脱附率可达99%。  相似文献   

18.
1 Introduction Many efforts have been made on using ion exchange resin to separate and concentrate certain metal cations [1?11]. However, less research for using it to adsorb noble metal Ag(Ⅰ), and much less research for commercializa- tion has been don…  相似文献   

19.
利用分子印迹技术和甲基丙烯酸对壳聚糖进行改性,并在改变吸附条件、吸附动力学和吸附等温线的基础上,对湘江样水中Cr(Ⅵ)进行吸附研究。结果表明:X射线衍射谱显示印迹聚合物的结晶能力减弱,但非结晶区面积增加,吸附点位数提高,对Cr(Ⅵ)的吸附容量增大;印迹聚合物对Cr(Ⅵ)的吸附能力随时间的延长而增加,8h后达到饱和,最佳吸附时间是吸附后4~8h,对Cr(Ⅵ)的提取率最大值为33.7%。提取液最佳pH值是4.5~7.5;提取率随着壳聚糖脱乙酰度的增大而增大,吸附效果最好的是90%脱乙酰度壳聚糖。吸附量随着壳聚糖的浓度增加而增加,饱和后对Cr(VI)的提取率变化相对平稳,实验测得最高去除率为98.3%。Cr(Ⅵ)印迹壳聚糖吸附的准一级动力学和二级动力学模型线性相关系数分别是0.9013和0.9875,吸附速率分别为0.0091min-’和7.129g/(mg·min)。Cr(VI)印迹壳聚糖的吸附更符合二级动力学模型,与Langmuir吸附等温线的拟合性比Freundlich吸附等温线的更好,计算得到的最大吸附容量为15.784mg/g,对河水中Cr(Ⅵ)的吸附效果明显。  相似文献   

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