STUDY ON THE PHYSICAL CHEMICALPROPERTIES OF FFA-1 ION EXCHANGE FIBER

The physical and chemical properties of FFA-1 ion exchange fiber have beencharacterized with IR spectrum. thermal analysis and SEM means. The PH titrationcurve, swelling rate, mechanical properties, resistance drop of filter layer as well asthe dynamic adsorption for SO2 was determined These experiments provided theessential parameters for the practical application of FFA-1 material in adsorption oftoxic gases.

Arsenate Removal by Iron-Modified Ion Exchange Fiber

The adsorption characteristics of arsenate on ion exchange fiber(IEF) and iron-modified ion exchange fiber(FeIEF) were evaluated.Batch adsorption experiments were conducted to study the arsenate adsorption effect by varying contact time,pH,and coexisting anions.Adsorption capacity was found to increase by increasing the contact time and acidic conditions were favorable for arsenate adsorption on IEF and Fe-IEF.Arsenate adsorption data were better consistent with Freundlich equation than Langmuir equation.The maximum monolayer adsorption capacities were 285 and 333 mg/g at 25℃ for IEF and Fe-IEF respectively.The adsorption kinetics was found to follow the pseudo-first-order kinetic model.The existence of HCO 3-,PO34-,SO24-,SiO23-,and NO 3-decreased the arsenate adsorption capacity on IEF.Cl-and F-had little influence on it.When FeIEF was adopted,the effects of HCO 3-,SO24-,Cl-,SiO23-,and NO 3-were negligible,while PO43-could still markedly decrease the adsorption capacity and F-had inhibitory effect on arsenate adsorption.Fe-IEF can be used as a highly selective and efficient sorbent for removal of arsenate from aqueous solutions.

Adsorption of Hg(Ⅱ) from aqueous solution using thiourea functionalized chelating fiber

A fast and selective adsorbent for Hg（ll） from aqueous solutions using thiourea （TU） functionalized polypropylene fiber grafted acrylic acid （PP-g-AA）, PP-g-AA-TU fibers, was characterized by Fourier transform infrared spectroscopy and X-ray photoelectron spectroscopy. The adsorption behavior of the functionalized chelating fibers for Hg（Ⅱ） was investigated by static adsorption experiments, and the effects of some essential factors on adsorption of Hg（Ⅱ） were examined, such as pH, initial concentration, adsorption time, coexisting cations, and temperature, The results showed that the adsorptive equilibrium could be achieved in 10 min, and the equilibrium adsorption quantity of PP-g-AA-TU fibers was 20 times that of PP-g-AA fibers. The PP-g-AA-TU fibers showed a very high adsorption rate and a good selectivity for Hg（Ⅱ） over a wide range of pH. The adsorption isotherm can be well described with Langmuir model, with the maximum adsorption capacity for Hg（Ⅱ） up to 52.04 mg.g-1 and the removal of Hg（Ⅱ） more than 97%. The kinetic data indicate that the adsorption process is best-fitted into the pseudo-second-order model.

Kinetic modeling of adsorption of vanadium and iron from acid solution through ion exchange resins

This study assessed the adsorption process and the reaction kinetics involved in the selective recovery of vanadium from an acid solution containing iron as an impurity.Four commercial resins were studied:Lewatit^(®)MonoPlus TP 209 XL,Lewatit^(®) TP 207,Dowex^(TM)M4195(chelating resin)and Lewatit^(®) MonoPlus S 200 H(strong cationic exchange resin).To investigate the effect of time on the adsorption process,batch experiments were carried out using the following initial conditions:pH 2.0,298 K,and a proportion of 1 g of resin to 50 mL of solution.The variation of pH over time was analyzed.Chelating resin released less H+ions as the adsorption occurred,resulting in a lower drop of pH when compared to S 200 H resin.Ion adsorption by the resins was also evaluated through FT-IR and SEM−EDS before and after the experiments.Among the evaluated kinetic models(pseudo-first order,pseudo-second order,Elovich and intraparticle diffusion models),the pseudo-second order model best fits the experimental data of the adsorption of vanadium and iron by all of the four resins.M4195 resin showed the highest recovery of vanadium and the lowest adsorption of iron.Kinetic data,which are fundamental to industrial processes applications,are provided.

Removal of vanadium from ammonium molybdate solution by ion exchange

The separation techniques of vanadium and molybdenum were summarized, and a new method of removal V(Ⅴ) from Mo(Ⅵ) by adsorption with chelate resin was presented. Nine kinds of chelate resins were used to investigate the adsorbent capability of V(Ⅴ) in ammonium molybdate solution with static method. The test results show that DDAS, CUW and CW-2 resins can easily adsorb V(Ⅴ) in ammonium molybdate solution, but hardly adsorb Mo(Ⅵ). The dynamic experimental results show more than 99.5% of V(Ⅴ) can be adsorbed, and the adsorption rate of Mo(Ⅵ) is less than 0.27% at 294-296 K for 60 min at pH 7.42-8.02. The mass ratio of V to Mo decreases to l/5 0000 in the effluent from 1/255 in the initial solution. The loaded resin can be desorbed by 5% NH3·H2O solution, and the vanadium desorption rate can reach 99.6%. The max concentration of vanadium in desorbed solution can reach 20 g/L, while the concentration of molybdenum is less than 0.8 g/L.

Separation and purification of Yb_(2)O_(3) by ion exchange chromatography and preparation of ultra-high purity Yb_(2)O_(3)

Ultra-high purity Yb_(2)O_(3) is the critical material of many high-tech materials such as laser glass and fiber,in which impurities seriously affect the laser color quality,intensity and power.In order to reduce the influence of impurities on the properties of laser materials,the purification process of Yb_(2)O_(3) was studied by comparing two kinds of resins(RT-1 and RS-1)using improved ion-exchange chromatography(IEC)method.In this study,through the synergistic improvement of resin structure and eluting system,the environmental pollution caused by ammonia water in the traditional IEC method was reduced,and the requirements of high temperature and pressure were cut.The ion exchange behavior and impurity removal mechanism in the resin column during the loading and eluting process were compared and analyzed.The experimental results show that RS-1 resin is all superior to RT-1resin in elements selectivity,ion exchange capacity and impurities removal rate.After separation and purification by IEC with RS-1 resin,the total removal rate of rare earth impurities was 77.59%and that of non-rare earth impurities was 95.86%when Yb recovery was more than 70%,both higher than that of RT-1 resin(73.26%and 83.18%).This indicates that the improved IEC method is very effective in separating and removing different metal impurities from Yb_(2)O_(3).The pilot test results of IEC method separating and purifying Yb_(2)O_(3) with RS-1 resin show that the purity of Yb_(2)O_(3) can be increased from 99.9929%to 99.9997%by IEC method.It has exhibited huge potential of preparing ultra-high purity Yb_(2)O_(3),especially the deep removal of non-rare earth impurities.

Fast removal of heavy metal ions and phytic acids from water using new modified chelating fiber

The graft copolymerization of acrylic acid（AA） onto polyethylene glycol terephthalate（PET） fiber initialed by benzoy peroxide （BPO） was carried out in heterogeneous media.Moreover,modification of the grafted PET fiber（PET-AA） was done by changing the carboxyl group into acylamino group through the reaction with dimethylamine.The modified chelating fiber（NDWJN1） was characterized using elementary analysis,SEM and FT-IR spectroscopy.Adsorption kinetic curves indicated that NDWJNl could fast remove heavy metal ions and phytic acids from water effectively.Furthermore,batch kinetic studies indicated that heavy metal ions adsorbed to NDWJNl could be filted well by both pseudo-first-order and pseudo-second-order adsorption equations,but the intra-particle diffusion played a dominant role in the adsorption of phytic acids.

Deep removal of copper from cobalt sulfate electrolyte by ion-exchange

SP-C was applied for the removal of Cu^2＋ from simulated cobalt sulfate electrolyte containing Co2＋ 50 g/L and Cu2＋ 0.5-2.0 g/L. Experimental conditions included pH of 2-4, temperature of 20-60℃ and contact time of 10-40 min. The investigation demonstrated that SP-C had recommendable efficiency in adsorbing Cu2＋ from the electrolyte with 25- to 100-fold of Co2＋ The optimal adsorption conditions of SP-C were pH of 4, contact time of 30 min and ambient temperature. The study also showed that the loaded resin could be effectively eluted with 2.0 mol/L H2SO4 solution at a contact time of 40 min; the peak concentration of Cu2＋ in the eluate was about 35 g/L. The sorption characteristics of Cu2＋ by SP-C could be described by Langrnuir isotherm and the pseudo second-order kinetic equation. Infrared spectra showed that nitrogen atoms in the functional group coordinated with Cu2＋ to form coordination bands.

温度对高硅氧基体玻璃纤维性能的影响及其机理探索

针对经石蜡型浸润剂涂覆后的高硅氧基体玻璃纤维原丝,在高温环境下性能、生产利用率下降的问题,深入研究了温度对其性能的影响规律,并对机理进行了讨论。采用红外、热重、扫描电镜等分析手段,对不同形态的高硅氧基体玻璃纤维原丝在不同温度、不同存放时间下的性能进行了表征。结果表明,随着温度的升高,浸取液碱性增强,机械性能下降,同时纤维丝表面晶体析出越多,且存在碳酸根。因此,可以得出,温度影响高硅氧基体玻璃纤维性能的根本原因,可能在于高温促进了纤维中Na^(+)运动,加快了其与纤维表面水分子中H+的离子交换,从而加速了纤维结构的破坏,导致性能下降。

螯合树脂脱除钨酸盐溶液中铜镁离子的研究

采用离子交换法,选用对铜离子和镁离子具有高选择性的CH-93螯合树脂和LSC-500螯合树脂深度脱除钨酸盐溶液中铜镁离子,探究不同因素对吸附效果的影响,并对吸附类型、吸附热力学及动力学进行分析。结果表明:在不同吸附参数下,铜镁离子的吸附率均可达到99%以上。热力学研究表明,树脂吸附铜镁离子是自发、吸热和熵增的过程。动力学研究表明,树脂吸附铜镁离子的过程符合Langmuir等温吸附模型和准二级动力学模型,液膜扩散是控速步骤。柱上离子交换结果表明,钨酸盐溶液经过12 h的CH-93/LSC-500树脂吸附后,铜镁离子含量分别从60000μg/L降低至14.6,24.4μg/L,且没有出现穿漏现象。

螯合树脂处理含镍废水探究

探究不同工艺联合螯合树脂对游离态及络合态镍的处理效果。通过静态试验发现:高级氧化-混凝沉淀-离子交换(TP207树脂)对含镍废水有较好的处理效果,但TP207树脂对稳定性较强的络合镍的吸附效果有限。

用Purolite S930螯合树脂吸附某选铌尾矿浸出液中的Sc^(3+)

研究了用Purolite S930螯合树脂从白云鄂博选铌尾矿浸出液中吸附Sc^(3+),考察了树脂用量、溶液pH、吸附温度、吸附时间和不同价态(二价,三价)金属离子对Sc^(3+)吸附率的影响,并借助SEM-EDS、FT-IR、XPS对树脂吸附Sc^(3+)前后的形貌进行表征。结果表明:在树脂用量0.1 g/mL、溶液pH=1.2、吸附温度50℃、硝酸浓度0.144 mol/L、吸附24 h条件下,Purolite S930对溶液中Sc^(3+)的吸附率可达99%以上;溶液中金属阳离子的吸附顺序为Sc(Ⅲ)>Fe(Ⅲ)>Al(Ⅲ)>Mn(Ⅱ)>Ca(Ⅱ)>Mg(Ⅱ),其中,三价金属阳离子比二价金属阳离子对Sc^(3+)吸附影响更大;吸附过程中,Sc^(3+)与Purolite S930中的Na+发生离子交换反应,与—COO—产生螯合作用;吸附过程更符合准二级动力学模型。

钩藤碱在离子交换纤维上的吸附动力学研究

采用静态吸附法考察钩藤碱在离子交换纤维上的吸附行为,并研究离子交换纤维对钩藤碱的吸附动力学。结果表明,钩藤碱在离子交换纤维上的吸附过程更好的符合Ho and McKay二级动力学方程,在吸附液初始浓度为100 mg/L,吸附温度323 K的条件下,二级动力学方程为t/q_(t)=0.0012 t+0.0065(R^(2)=0.998);表观吸附活化能Ea为7.003 kJ/mol;速度控制步骤为液膜扩散控制,在吸附液初始浓度为60 mg/L,吸附温度303 K条件下,液膜扩散模型方程为-ln(1-q_(t)/q_(e))=0.1193 t(R^(2)=0.998)。阳离子交换纤维可以吸附钩藤碱,并且具有良好的吸附性能。

改性聚丙烯腈纤维对铅镉汞离子的吸附性能研究

以改性聚丙腈纤维(简称改性纤维,用L表示)为吸附剂,对水溶液中的重金属离子Pb2+、Cd2+、Hg2+进行螯合吸附。实验证明,L对它们有很强的吸附能力,通过实验确定出L对各离子吸附的最佳条件参数:温度、时间、pH值、离子浓度等;并发现L对Pb2+、Hg2+有累积吸附作用;吸附后的纤维可以反复再生使用,并找出再生的最佳条件。而且,在一定的浓度范围内三种离子的吸附都能符合Freundlich型等温方程式。

新型离子交换纤维去除水中砷酸根离子的研究

制备了一种新型离子交换纤维 .研究表明 ,该离子交换纤维对砷酸根离子具有较高的吸附容量和较快的吸附速度 ,吸附动力学数据完全符合Lagergren二级速度方程 ,在所研究的砷浓度范围内 ,Freundlich型吸附等温式能很好地描述吸附平衡数据 ,去除砷酸根离子的最佳 pH值范围是 3 5～ 7 0 .离子交换纤维柱吸附实验表明了较好的动态吸附特性 ,稀NaOH溶液是砷酸根离子的有效洗脱剂 ,3 0mL 0 5mol/LNaOH溶液可定量将 96

偕胺肟基纤维对Sm(Ⅲ)、Nd(Ⅲ)、Pr(Ⅲ)的吸附与富集

以偕胺肟基纤维 (用 L 表示 )为吸附剂 ,对 Sm( )、Nd )、Pr( )进行螯合吸附 ,再将螯合后的纤维进行解吸 ,使稀土离子得到富集。通过实验确定出最佳吸附条件为 :温度 5 0℃、时间 30～ 6 0 m in、p H3～ 4 ;最佳解吸条件为 :0 .0 2～ 0 .0 8m ol· L- 1 HCl、室温、30～ 6 0 min。纤维 L 对 Sm( )、Nd( )、Pr( )三种离子的一次吸附的最大量分别为 2 .99、2 .86、4 .11mg· g- 1 (被吸附离子的初始浓度 C0 =0 .0 0 1mol· L- 1 )。L 对三种离子均可进行三次以上累积吸附。

离子交换纤维对Cr(Ⅵ)的交换性能研究

研究了苯乙烯系聚丙烯基阴离子交换纤维对Cr(Ⅵ)的交换性能,考察了酸度、温度和流速等因素对交换性能的影响。实验结果表明,在 pH 值为 3时交换性能最好。离子交换纤维对 Cr(Ⅵ)的交换以液膜扩散为主,交换速度很快,8min 即可达到交换饱和,交换反应速率常数为0.015s-1,离子交换过程服从Freundlish等温式。测定了纤维静态饱和交换量为257.6mg/g。温度和流速影响动态交换性能,使得穿透曲线和穿透时间发生改变。与离子交换树脂相比具有交换速度快、交换量大的优点,是一种交换性能优良的分离材料。

强酸型离子交换纤维PVF-g-SO_3H对碱性氨基酸的分离研究

研究强酸型阳离子交换纤维PVF g SO3 H对碱性氨基酸L 组氨酸和L 赖氨酸的吸附分离性能 ,并与 73 2号树脂进行比较 .结果表明PVF g SO3 H纤维不仅对单组份赖氨酸或组氨酸的吸附率比 73 2号树脂高约 1 5%～ 3 9% ,而且其洗脱率高约 1 2 5%～ 1 3 4 % ,同时对混合氨基酸的洗脱峰既强而且分辨率高 .再生后纤维和树脂的总提取率都有微小的下降 ,但纤维的再生提取率仍高于 73 2号树脂 1 0 %以上 .实验的最佳洗脱条件为 :洗脱液柠檬酸 柠檬酸钠的pH值为 4 6,填充柱长径比为 2 0 ,洗脱速率为 1mL/min .

膜法处理高浓度氨氮废水的研究

采用电渗析法和聚丙烯(PP)中空纤维膜法处理高浓度氨氮无机废水可取得良好的效果。电渗析法处理氨氮废水,浓度2000～3000mg/L,氨氮去除率可在85%以上,同时可获得8.9%的浓氨水。此法工艺流程简单、投资省、不消耗药剂、运行过程中消耗的电量与废水中氨氮浓度成正比。PP中空纤维膜法脱氨效率≥90%,回收的硫酸铵浓度在25%左右。此法工艺流程短、技术先进、省电,无二次污染,运行中需加碱,加碱量与废水中氨氮浓度成正比。