氨基膦酸树脂对钕(Ⅲ)的吸附性能

研究了氨基膦酸树脂对钕(Ⅲ)的吸附行为。当pH=5.70时,氨基膦酸树脂对钕(Ⅲ)的静态饱和吸附容量为199.74 mg/g,用1moL/L HCl溶液可以定量洗脱,当T=298 K时,表观吸附速率常数为1.68×10~(-4)s~(-1),吸附热力学参数△H=60.68 kJ/mol,△G=-14.91 kJ/mol,△S=253.65 J/(mol·K),等温吸附服从Freundlich曲线,氨基膦酸树脂功能基与钕(Ⅲ)的配位比为2:1。用红外光谱探讨了氨基膦酸树脂与钕(Ⅲ)的成键情况。     

氨基膦酸树脂对汞的吸附性能及其机理

研究了Hg2+在氨基膦酸树脂上的吸附行为。结果表明:静态饱和吸附容量为 581.9mg/g树脂,用0.5mol/L的HCl和0.2~0.3mol/L的EDTA洗脱,洗脱率分别为:97%和99%以上;测得吸附热力学参数分别为: △H=8.45kJ/mol,△G=-3.02kJ/mol,△S= 38.5J/mol稫。等温吸附服从Freundlich经验式;表观活化能Ea=13.6kJ/mol,表观速率常数k298=2.46×10-5/s;树脂功能基与Hg2+的配位比为1∶1;并用化学和红外光谱的方法探讨了树脂对Hg2+的吸附机理。     

氨基膦酸树脂对溶液中锌的吸附研究

研究了Zn2+在氨基膦酸树脂上的吸附行为。结果表明,静态饱和吸附容量为209.2mg.g-1树脂,用2.0 mol.L-1的HCl溶液洗脱,洗脱率为98%以上;测得吸附热力学参数分别为:ΔH=8.14 kJ.mol-1,ΔG=-3.06 kJ.mol-1,ΔS=37.6 J.mol-1.K-1。等温吸附服从Freundlich吸附等温式;表观活化能Ea=14.7 kJ.mol-1,表观速率常数k298=4.26×10-5s-1;树脂功能基与Zn2+的配位比约为1∶1;并用化学和红外光谱的方法探讨了树脂对Zn2+的吸附机理。     

DH-2树脂对镝的吸附及机理

研究了镝离子在HD-2树脂上的吸附行为。在HAc-NaAc体系pH=6.20时吸附最佳,测得静态饱和吸附容量为356mg/g(树脂),用0.1~2.0 mol/L HC l可定量洗脱,表观速率常数k198=1.16×105s-1,表观活化能Ea=16.1kJ/mol。等温吸附服从Freun ilich经验式,吸附热力学参数△H=16.5kJ/mol,△S=58.2 J/(mol.K),△G298=-0.859kJ/mol。用化学和红外光谱等方法讨论了吸附机理。     

甲壳素对铅(Ⅱ)的吸附研究

进行了铅离子在甲壳素上的吸附行为实验,结果表明在pH=4.46时吸附最佳。测得静态饱和吸附容量为478mg.g-1(树脂);用0.5mol.L-1HCl可洗脱,洗脱率达98.8%;测得表观速率常数k298=8.53×10-5s-1;表观活化能Ea=16.54kJ.mol-1;等温吸附服从Freundlich经验式;吸附热力学参数△H=8.70kJ.mol-1,△S=41.7J.mol-1.K-1,△G=-3.71kJ.mol-1。     

4—氨基—三氮唑树脂对铬（Ⅵ）的吸附,机理及应用

4-氨基-三氮唑树脂(4-ATR)对Cr(Ⅵ)的吸附在pH=1时最佳,Cr~(3+)基本不被吸附。两者分离系数β_(CrVI/Cr~(3+)=5.52×10~3.静态饱和容量为179.4mg Cr(Ⅵ)/g树脂。用5mol/L HCl能还原洗脱。测得不同温度下的吸附速率常数k_(21·c)=1.59×10~(-3)S~(-1)、K_(25·c)=1.87×10~(-3)S~(-1)、K(30·c)=2.2×10~(-3)S~(-1);表观吸附活化能E_a=26.26kJ/mol;吸附热力学函数ΔH=6.16kJ/mol,ΔG~(298)=-15.1kJ/mol,ΔS~(298)=339.8J.mol·K.吸附机理表明4-ATR功能基上的N与Cr(Ⅵ)发生配位键合,配位摩尔比为1∶1.利用此树脂处理含Cr(Ⅵ)电镀废水,铬回收率可达95.7%。     

D160大孔吸附树脂对染料木黄酮吸附性能的研究

研究了D160大孔吸附树脂对染料木黄酮的吸附性能.结果表明,在pH4.00时,该树脂对染料木黄酮有较好的吸附性能;静态饱和吸附容量为64.5mg/g树脂;用95%乙醇溶液作解吸剂,二次累计解吸率接近100%;表现速率常数k298=1.01×10-4s-1;测得吸附热力学参数分别为:△H=32.2kJ/mol,△S=119J/(mol·K),△G288=-2.03kJ/mol,△G298=-3.22kJ/mol,△G308=4.41kJ/mol.等温吸附服从Freundlich和Langmuir等温吸附规律;研究还表明,提高振荡频率对吸附有利.     

717型阴离子交换树脂吸附水溶性芳香族有机污染物研究

研究了717型阴离子交换树脂对苯酚、苯甲酸和十二烷基苯磺酸钠(SDBS)等水溶性芳香族污染物吸附过程的基本化学问题.研究结果表明:717型树脂对苯酚、苯甲酸和SDBS的吸附过程均符合Lagergren二级吸附动力学方程,吸附速率均随着温度的升高而加快,吸附表观活化能Ea分别为13.2kJ/mol、59.5kJ/mol和48.1kJ/mol,吸附过程△H0和△S0均为正值,△G0均为负值,吸附能够自发进行;吸附等温模型符合Langmuir等温式;318K时,717型树脂在pH=9.1对SDBS的饱和吸附容量为360mg/g;在pH=10.2,对苯酚和苯甲酸的饱和吸附容量分别为194mg/g和286mg/g.用浓度均为0.5mol/L,体积比为5∶1的NaCl-NaOH混合溶液可快速洗脱树脂上吸附的污染物,洗脱率达98％以上.该树脂对水溶性芳香族污染物吸附容量大,易于再生和循环利用,可用于环境水体中水溶性芳香族有机污染物的吸附治理.     

共振二胺树脂吸附铂的行为及热力学性质

测定了共振二胺树脂吸附铂的活化能E_a=2908kJ/mol、热焓△H=-17.23kJ/mol,自由能文化△G~(298)=-33.1kJ/mol.熵变△S~(298)=168J/mol·K。讨论了吸附行为。树脂吸附铂的摩尔比(功能基/Pt(Ⅳ)～2),树脂吸附铂的反应符合Freundlich等温吸附式。用硫脲-盐酸-乙醇水溶液能定量脱洗吸附在树脂上的Pt(Ⅳ),且树脂可再生使用。利用此树脂从含铂废催化剂中回收纯铂获初步成功。     

D201×4树脂对铼(Ⅶ)的交换性能研究

研究了D201×4树脂对铼(Ⅶ)的吸附性能,实验结果表明,在pH=2.7的HAc-NaAc缓冲体系中,静态饱和交换容量为634mg/g树脂;用4.0mol/LNaOH作为解吸剂,一次解吸率达93.5%;等温吸附服从Freundlich经验式;反应开始阶段的表观吸附速率常数k298K=9.58×10-5s-1;反应的△H=-12.10kJ/mol;吸附物中树脂功能基与Re(Ⅶ)的摩尔比约为1:1,并用红外光谱初步探讨了树脂吸附铼的反应机理。     

SORPTION BEHAVIOR AND MECHANISM OF SAMARIUM(III) ON AMINO METHYLENE PHOSPHONIC ACID RESIN

Sm(III) was quantitatively adsorbed by amino methylene phasphonic acid resin (APAR)in the medium of pH=5.0. The statically saturated sorption capacity is 251mg/g @ resin. Sm(III)adsorbed on APAR can be reductively eluted by 2.0mol/L HCl. The sorption rate constant is k2gs=1.35 ×1O-Ss-1. The sorption behavior of APAR for Sm(I) obeys the Freundlich isotherm. The enthalpy change △H° of sorption is 24.9k J/mol. The apparent activation energy is Ea= ll. 7kJ/mol.The sorption mechanism shows that the nitrogen and oxygen atoms of the functional group of APAR coordinated with Sm(Ⅲ) to form coordination bond.     

Studies on Adsorption Behavior and Mechanism of Copper（ Ⅱ ） onto Amino Methylene Phosphonic Acid Resin

IntroductionThe adsorption ability of the functional poly-mer used to enrich metal ions is strong and the op-eration of the functional polymer is convenient.The polymer having adsorbed metal ions can be re-covered by means of an acid or an alkaline solutionand the recovered polymeric material can bereused.The adsorption ability of the polymer withvarious functional groups is different for differentmetals.Because nucleophilic atoms such as oxy-gen,nitrogen,sulphur and phosphorous atoms cancoord…     

大孔膦酸树脂吸附镱的研究

In this paper the sorption behavior of Yb(Ⅲ) onto the macroporous phosphonic acid resin (MPAR) is reported.Experimental results show that the statically saturated sorption capacity is 328 mg/g*resin;Yb(Ⅲ) adsorbed on MPAR can be eluted by 1mol*L-1 HCl,elution percentage is 91.5%.The apparent rate constant is k298=4.63×10-5s-1.The sorption behavior of MPAR for Yb(Ⅲ) abides the Freundlich isotherm.The themodynamic parameter of sorption:enthalpy change ΔH for Yb(Ⅲ) is 50.4kJ*mol-1.The coordination molar ratio of the functional group of MPAR to Yb(Ⅲ) is 3∶1.The bondforming conditions of MPAR for Yb(Ⅲ) is examined by IR spectrometry.     

STUDIES ON THE SORPTION OF MACROPOROUS PHOSPHONIC ACID RESIN FOR LANTHANUM

The influences of Medium pH,sorption temperature,sorption time,etc.on the sorption capacity of macroporous phosphonic acid resin for La^3+ were determined.The sorption rate constant was k298=7.64×10^-5 s^-1. The complex ratio of phosphonic groups of the resin to La^3+ was 3:1.The basic sorption parameters were determined. The sorption mechanism of macroporous phosphonic acid resin for La^3+ was examined by chemical analysis and IR-spectrometry.     

Cation-exchange separations in organic solvent-dithizone media

Numerous elements can be adsorbed on a column of the strongly acidic cation-exchange resin Dowex 50 from a mixture consisting of tetrahydrofuran and 1 M nitric acid (19:1). These elements include Ag, Cu, Bi, Pb, rare earths, alkaline earth metals, alkali metals, U, Th, Fe, Co, Zn and Cd; Hg and Sb are not retained and so can be separated from the adsorbed elements. Fractionation of the adsorbed elements can be effected by using as eluent 0.01 M dithizone in tetrahydrofuran-1 M nitric acid(19:1);; the dithizonates of silver, copper and bismuth are selectively eluted while the other adsorbed metal ions are still retained. The technique is suitable for the separation of tracer and macro amounts of elements.     

D152树脂对铜(Ⅱ)的吸附性能

The sorption behavior and mechanism of D152 resin for Cu~(2+) is investigated.D152 resin has a good adsorptivity for Cu~(2+) in the HAc-NaAc medium at pH=4.73.The statically saturated sorption capacity is 309mg/g·(resin).Cu~(2+)adsorbed on D152 resin can be eluted quantitatively by using 0.1-2.0mol/L hydrochloric acid as an eluant.The apparent rate constant and activation energy are k_(298)=1.86×10~(-5) sec~(-1) and Ea=12.3kJ/mol.The sorption behavior of D152 resin for Cu~(2+) obeys the Freundlich isotherm.The sorption thermodynamic parameters of D152 resin for Cu~(2+)are enthalpy change ΔH=14.6 kJ/mol,free energy change ΔG=-0.72kJ/mol,entropy change ΔS=51.4J/(mol·K).respectively.     

聚丙烯接枝丙烯酸(PP-g-AA)对稀土离子吸附反应的研究

通过聚丙烯电子束预辐照接枝丙烯酸得到PP g AA ,对PP g AA在弱酸性溶液中对稀土离子的吸附规律进行了考察 ,测定了PP g AA对 1 1种稀土离子的吸附速率常数k及吸附量Q ,观察了在PP g AA吸附稀土离子反应中 ,可能存在的“斜W效应”和“四分组效应” .     

ADSORPTION OF SAMARIUM(Ⅲ) ON DIGLYCOLAMIDIC ACID RESIN

The sorption behavior and mechanism of a novel chelate resin, diglycolamidic acid resin(DAAR), for Sm(Ⅲ) were investigated. The optimal sorption condition of DAAR for Sm(Ⅲ) is pH=6.0 in HAc-NaAc medium. The statically saturated sorption capacity is 190mg/g resin at 298K.The Sm(Ⅲ) adsorbed on DAAR can be ehuted reaching 100% by 0.5～2.0mol/L HCl used as eluant.The resin can be regenerated and reused without apparent decrease of sorption capacity. The apparent sorption rate constant is k29s= 1.96 × 10-5 s-1. The apparent activation energy is 26k J/mol.The sorption behavior of DAAR for Sm(Ⅲ) obeys the Freundlich isotherm. The thermodynamic sorption parameters, enthalpy change △H of DAAR for Sm(Ⅲ) is 16. 9kJ/mol. The molar coordination ratio of the functional group of DAAR to Sm (Ⅲ) is 3. The sorption mechanism of DAAR for Sm(Ⅲ)was examined by using chemical method and IR spectrometry. The coordination bond was formed between oxygen atoms in the functional group of DAAR and Sm(Ⅲ).     

Cation-exchange separation of hafnium and zirconium from accompanying ions

Hafnium and zirconium are not retained on the strongly acidic cation-exchange resin Dowex 50 from a mixture consisting of methanol and 12M nitric acid (19:1) which is 0.1M in trioctylphosphine oxide. On the other hand most other elements investigated are strongly adsorbed on the resin from this medium so that they are readily separated from hafnium and zirconium. These elements include titanium, rare earths, alkali metals, alkaline earth metals, iron, cobalt, manganese and zinc. This separation technique has been found to be suitable for the separation of tracer and milligram amounts of hafnium and zirconium from accompanying metal ions. If in place of methanol other organic solvents such as acetone, tetrahydrofuran and methyl glycol are used the selectivity of the separation of zirconium and hafnium from the other elements is decreased. The same effect is observed when hydrochloric acid is used in the mixtures instead of nitric acid.