改性沸石(Na-Y型)对Ni2+的吸附行为

将天然沸石熔融制得新型改性沸石(Na-Y型),研究Na-Y型沸石对Ni2 的吸附行为.结果表明,对Ni2 的饱和吸附量,Na-Y型沸石为31.04mg·g-1,而天然斜发沸石和Na型沸石(NaCl改性)仅为3.60mg·g-1和7.64 mg·g-1.Na-Y型沸石对Ni2 的等温吸附行为符合Freundlich方程.对溶液中Ni2 的吸附量在初始阶段(0-5h)快速上升,而后趋于平缓.共存阳离子对Na-Y型沸石吸附Ni2 的影响为:Co2 》Ca2 》Fe3 》 K .     

热改性斜发沸石对富营养化水体的脱氮除磷效果

氮、磷是导致水体富营养化且又较难去除的一类物质。实验采用模拟的方法研究了天然沸石和不同温度改性沸石的脱氮除磷效果。结果表明,天然沸石对氮、磷静态吸附去除率分别达71%和91%。随着改性温度的升高,350℃改性沸石振荡吸附氮、磷效果最好,较之天然沸石提高了18%,改性温度继续上升则呈下降趋势。不同沸石对氮、磷的吸附特征可用一级动力学方程进行描述,其中350℃改性沸石对氮、磷的吸附特征在不同的固液比情况下均符合一级动力学方程。     

斜发沸石在废水处理中的应用研究进展

天然斜发沸石是一种廉价矿物,经改性后可有效去除废水中氨氮、有机物、重金属离子、砷及放射性物质,并可用作杀菌剂。文章简述了天然斜发沸石的主要改性技术,并着重论述了近年来天然斜发沸石及各种改性斜发沸石在废水处理中的应用研究动态。同时,展望了其应用前景,探讨了目前应用斜发沸石处理废水时仍亟待解决的一些问题。     

天然沸石中离子交换平衡的离子特异性研究

沸石在改良土壤和保护环境等方面有着广泛的应用,研究沸石离子交换中的特异性效应对更好地利用沸石有着重要意义.碱金属离子在天然斜发沸石中的交换平衡时的最大吸附量存在着明显的特异性效应;对于同价的碱金属离子,其交换吸附能力差异随着离子浓度的降低而增大.这种实验现象不能用库仑力、离子体积、水合作用、色散力、经典诱导力以及表面络合等相关理论进行完整解释.分析发现,根本原因来自离子因量子涨落而产生的极化与沸石颗粒表面电荷产生的强电场之间的相互作用,这种相互作用导致了离子间偶极矩差异随着表面电位的升高而增大,进而使离子-表面吸附能差异增大,并出现不同的交换吸附能力.由于沸石表面电荷密度较高,离子体积效应对其在双电层中的分布也起着比较重要的作用,导致碱金属离子在沸石表面的交换平衡结果在高表面电位(绝对值大于0.2 V)下才表现出较大选择性,与低电荷密度表面上的交换平衡结果存在一定差异.     

热水环境中Na+活化斜发沸石吸附钙离子除硬过程研究

本实验以Na+活化天然斜发沸石为吸附剂模拟研究其在工业热水环境中对钙离子(Ca2+)吸附除硬,考察了吸附剂的活化/再生条件、溶液p H等影响因素,并对Ca2+吸附动力学和热力学行为进行了分析探讨.结果表明:1该吸附过程具有准二级动力学特征且更符合Langmuir吸附等温模型;2温度升高可有效提升Ca2+吸附效率,而对其最大吸附量影响较小;3过程属化学吸附且为自发、吸热的熵增反应;4建议溶液p H控制在6~10之间,且当初始Ca2+浓度小于20 mg·L-1时活化斜发沸石可再生高效使用9次以上.研究证明活化斜发沸石是一种工业热能动力系统高温在线除硬的理想吸附剂.     

斜发沸石处理氨氮废水

以斜发沸石为吸附剂处理氨氮废水,研究了斜发沸石粒径、反应时间、废水pH、废水氨氮初始浓度、斜发沸石用量对吸附的影响,分析了斜发沸石的吸附动力学和热力学特征。结果表明,在298 K下,当斜发沸石用量为7 g/100 mL,沸石粒径小于74μm,废水氨氮初始浓度为200 mg/L,pH为7,吸附时间为3 h时,废水中氨氮的去除率可达到92.71%,斜发沸石吸附氨氮符合拟二级动力学方程。在温度为298~318 K之间时,吸附等温线更好地符合Freundlich方程。在此基础上,热力学计算发现,ΔH00、ΔG00、ΔS00,表明氨氮在斜发沸石上的吸附是自发吸热过程,以物理吸附为主。     

Preparation and characterization of calcium alginate-based composite adsorbents for the removal of Cd,Hg, and Pb ions from aqueous solution

Composite adsorbent materials containing calcium alginate, clinoptilolite, and coal-derived humic acid were prepared. Humic acid (HA), clinoptilolite (CL), alginate (AL), alginate-entrapped humic acid (AL/HA), clinoptilolite (AL/CL), and humic acid/clinoptilolite (AL/HA/CL) samples were characterized. The effectiveness of the samples as adsorbents for the removal of cadmium (Cd), mercury (Hg), and lead (Pb) were studied in a series of batch-adsorption experiments. For the AL, AL/HA, AL/CL, and AL/HA/CL adsorbents, uptake versus time data were evaluated using two kinetic models, a linear and a non-linear pseudo-first-order and a pseudo-second-order model. The data for each metal ion on all adsorbents showed good correspondence with the pseudo-second-order kinetic model. The equilibrium data were fitted to Langmuir, Freundlich, Dubinin–Radushkevich, and Temkin isotherm models. The results show that a non-linear method seems more appropriate for obtaining isotherm parameters. The non-linear Freundlich and Langmuir models for Pb and Hg produced a best fit with high R ² value (0.99). For HA adsorbent, the equilibrium data for Cd removal better fit to the non-linear Dubinin–Radushkevich isotherm.     

Adsorption of humic acid from aqueous solution on bilayer hexadecyltrimethyl ammonium bromide-modified zeolite

Surfactant-modified natural zeolites (SMNZ) with different coverage types were prepared by loading hexadecyltrimethyl ammonium bromide (HTAB) onto the surface of a natural zeolite. The adsorption behavior of humic acid (HA) on SMNZ was investigated. Results indicate that the adsorbent SMNZ exhibited a higher affinity toward HA than the natural zeolite. HA removal efficiency by SMNZ increased with HTAB loading. Coexisting Ca²⁺ in solution favored HA adsorption onto SMNZ. Adsorption capacity decreased with an increasing solution pH. For typical SMNZ with bilayer HTAB coverage, HA adsorption process is well described by a pseudo-second-order kinetic model. The experimental isotherm data fitted well with the Langmuir model. Calculated maximum HA adsorption capacities for SMNZ with bilayer HTAB coverage at pH 5.5 and 7.5 were 63 and 41 mg·g^-1, respectively. E2/E3 (absorbance at 250 nm to that at 365 nm) and E4/E6 (absorbance at 465 nm to that at 665 nm) ratios of the residual HA in solution were lower than that of the original HA solution. This indicates that the HA fractions with high polar functional groups, low molecular weight (MW), and aromaticity had a stronger tendency for adsorption onto SMNZ with bilayer HTAB coverage. Results show that HTAB-modified natural zeolite is a promising adsorbent for removal of HA from aqueous solution.     

天然斜发沸石粉对溶液中NH4+的吸附机理研究

采用天然斜发沸石粉(平均粒径30μm)进行吸附溶液中NH4+的试验研究,并对系统中金属阳离子的液相和固相含量进行了全程跟踪测定.等温吸附试验、吸附动力学研究结果表明,天然斜发沸石对溶液中NH4+的吸附过程符合Freundlich线性模型(R2=0.996),该吸附过程属于优惠吸附;吸附动力学符合假二级方程(R2>0.99),且随着初始NH4+浓度的增加,吸附反应的优惠程度降低.沸石粉对NH4+的吸附过程中离子交换以Ca2+和Na+为主,Na+首先被交换出来,随着吸附过程进行,Ca2+交换量逐渐增加并超过Na+,两者交换当量分别占39%~60%和35%~57%.由于沸石粉粒径较小,其对NH4+的去除除了依靠离子交换作用外,物理吸附作用的贡献不容忽视.     

阳离子表面活性剂改性沸石对铬酸根的吸附机制

研究了由十六烷基三甲基溴化铵(CTAB)改性制成的有机沸石对水体中铬酸根的吸附性能及吸附机制.结果表明,与沸石原矿相比有机沸石对铬酸根的吸附容量更高,而铬酸根在有机沸石表面的吸附量随着体系离子强度的增加而显著减小,说明铬酸根的吸附以静电作用为主.研究还发现沸石经有机改性后表面Zeta电位由负变正,说明表面活性剂在沸石表面的吸附改变了沸石表面的电荷性质,这也是有机沸石能够对铬酸根发生静电吸附的主要原因.铬酸根的吸附量及吸附的铬酸根的解吸量均随着体系pH值的升高而增加,分别约在pH=5.0和pH=6.0时达最大,随后铬酸根的吸附量和解吸量随着pH值的进一步增加逐渐减小.铬酸根的吸附量与解吸量之间的差值随pH升高而减小,说明在低pH条件下非静电吸附所占比例较高pH值条件下有所增加.