碧螺春绿茶对碱性染料灿烂绿的吸附

为了探讨碧螺春茶叶用于吸附灿烂绿的可能性,研究了碧螺春绿茶吸附灿烂绿的最佳吸附条件及解吸附条件。研究结果表明,在吸附条件为当溶液起始p H值为4.1,茶叶与灿烂绿质量比为833∶1,接触时间为45 min,室温(25±1)℃时,茶叶对灿烂绿吸附率达80%,吸附量为0.96 mg/g。对Na OH、CH_3COOH和HCl3种解吸附剂的研究表明,最佳解吸附剂是Na OH,解吸1.5 h解吸率最高达93.20%。该吸附过程符合Langmuir等温吸附方程,属于单分子层吸附。吸附过程热力学参数自由能变化ΔG0,焓变ΔH=102.32 k J/mol0,熵变ΔS=0.33 k J/(mol·K)0,说明吸附过程是自发的吸热熵增过程。     

四乙烯五胺功能化纳米高分子材料对Cr(VI)与磷酸盐共存体系的吸附机理

合成了四乙烯五胺功能化纳米高分子材料(TEPA-NP),采用傅里叶变换红外光谱分析(FTIR)、有机元素分析(EA)、X射线光电子能谱分析(XPS)等手段对其进行了表征,重点考察了其对水中Cr(VI)与磷酸根离子共存时的吸附机理.结果表明,溶液p H对TEPA-NP的吸附性能影响较大.对于Cr(VI)或磷酸盐单一体系,p H 2.5时TEPA-NP的吸附效果最佳;吸附热力学均符合Langmuir模型,吸附动力学均符合准二级速率方程.TEPA-NP对Cr(VI)的饱和吸附量为123.5 mg/g;吸附过程为吸热熵增的自发过程,ΔH为16.06 k J/mol,ΔS为59.02 J/(mol K),308 K时ΔG为-2.10 k J/mol;吸附活化能为30.28 k J/mol.TEPA-NP对磷酸盐的饱和吸附量为149.2 mg/g;吸附过程为放热熵增的自发过程,ΔH为-1.74 k J/mol,ΔS为1.91J/(mol K),308 K时ΔG为-2.32 k J/mol;吸附活化能为18.85 k J/mol.当磷酸盐的共存浓度小于100 mg/L时,磷酸盐对TEPA-NP吸附Cr(VI)几乎没有影响;而当Cr(VI)的共存浓度大于5 mg/L时,Cr(VI)对TEPA-NP吸附磷酸盐的影响已较为明显,可使TEPA-NP吸附磷酸盐的饱和吸附量减小17.3%;结合红外和XPS表征可以推测TEPA-NP对Cr(VI)的吸附涉及静电与配位相互作用,而对磷酸盐以静电吸附为主;Cr(VI)与磷酸盐共存时,TEPA-NP优先吸附Cr(VI).Cr(VI)可以通过竞争取代吸附在TEPA-NP上的磷酸根,且随着Cr(VI)初始浓度增大,TEPA-NP上吸附的总磷脱附的比例增大;而磷酸根对Cr(VI)的竞争吸附较难实现.     

Mg/Al-NO_3 LDH吸附诺氟沙星的热力学和动力学研究

采用平衡吸附实验,研究了诺氟沙星在自制焙烧态镁铝水滑石(Mg/Al-NO_3 LDH)上的吸附热力学和动力学行为。结果表明,在固液比1∶500、p H=5.0、吸附温度25℃、离子强度0.1 mol/L的条件下,吸附1 h对诺氟沙星(20 mg/L)的吸附过程符合Langmuir等温线方程和准二级动力学,理论平衡吸附量达到32.05 mg/g。其热力学参数ΔG0 KJ/mol,ΔH0 KJ/mol,由此推断焙烧态镁铝水滑石对诺氟沙星的吸附是自发放热反应。     

Fe3O4/HA复合吸附剂对Ni(Ⅱ)的吸附性能研究

采用碱溶酸析法提取腐植酸(HA),通过CaCl₂对其改性后与Fe₃O₄进行复合,制备出不同配比的Fe₃O₄/HA复合吸附剂。利用SEM、BET、FT-IR、XRD分析方法对HA、钙改性HA、Fe₃O₄/HA复合吸附剂进行了表征,考察了物料配比及吸附时间、pH值、温度、投加量和初始浓度对Ni(Ⅱ)吸附率的影响。结果表明:质量复合比mHA:mFe₃O₄:mCaCl₂为3∶2∶2的Fe₃O₄/HA复合吸附剂(HA2)对Ni(Ⅱ)吸附效果最佳。当加入0.8 g吸附剂,Ni(Ⅱ)初始浓度为0.1 g·L^-1,吸附5 h,pH=5,温度40℃,吸附剂对Ni(Ⅱ)的吸附率为92.57%。复合吸附剂在4次吸附脱附后,对Ni(Ⅱ)的吸附率仍达到52%。吸附过程符合准二级动力学方程和Freundlich吸附等温式。在20℃~40℃条件下,热力学参数ΔG<0、ΔS=37.57 J/(mol·K)、ΔH=11.07 kJ·mol^-1,表明该吸附是自发、熵增、吸热的过程。     

MCFs吸附纤维素酶的研究

采用水热法成功合成出了介孔泡沫(Mesocellular foams,MCFs)二氧化硅材料,本文采用物理吸附法将纤维素酶(1,4-β-D-葡聚糖葡糖苷水解酶)成功地吸附到介孔分子筛MCFs中,吸附的酶容量为65.42 mg/g。通过对MCFs对纤维素酶的吸附条件进行优化,得到的吸附最佳条件为pH 5.0,MCFs∶纤维素酶=15∶1(质量比),吸附温度4℃,接触时间20 h。本研究进行了纤维素酶的活性测定,采用羧甲基纤维素钠(CMC)法测得,吸附前CMC酶活性=2.96 mg/g,吸附后CMC酶活性=2.53 mg/g。MCFs吸附纤维素酶的过程属于准二阶动力学。该吸附反应在4-20℃之间,ΔG0,吸附处于自发反应。焓变ΔH=-33.76 kJ/mol0,熵变ΔS=-109.65 J/(mol·K)0,说明MCFs吸附纤维素酶的过程属于放热的熵减过程。本研究所获得的4-20℃之间ΔG~0值在0~-20 kJ/mol之间,说明MCFs吸附纤维素酶属于物理吸附过程。当温度处于298 K及其以上时,吸附处于非自发反应。     

Li~+掺杂TiO_2介孔材料对靛染废液吸附处理的研究

以固相合成法制备的Li-TiO_2介孔材料为吸附剂,对靛染废液进行吸附实验。结果表明,Li-TiO_2介孔材料对靛染废液中靛蓝的吸附动力学规律符合准一级吸附模型,吸附行为与Langmuir和Freundlich方程均吻合;在298K、pH=6时,速率常数k=0.01476min-1,吸附表观活化能Ea=-3.359k J/mol,静态吸附容量达1.068mg/g;热力学参数中,吸附焓变ΔH0,吸附Gibbs自由能变ΔG0,吸附熵变ΔS0,表明该吸附为自发的放热过程。以上实验结果证明,Li-TiO_2介孔材料是一种性能优良的吸附剂,能很好地处理靛染废液。     

三聚磷酸二氢铝吸附Cd~(2+)的动力学研究

采用动态吸附法研究三聚磷酸二氢铝吸附镉离子的动力学行为并进行吸附活化状态热力学参数分析。结果表明,当三聚磷酸二氢铝粒径小于150μm、搅拌器转速大于200r/min、Cd2+的初始浓度为500mg/L时,三聚磷酸二氢铝对镉离子的化学吸附符合二级反应动力学方程,吸附速率常数k与温度T之间的关系符合Arrhenius方程式,吸附的活化能为Ea=27.93kJ/mol,吸附的频率因子A=65.33L/mg·min,ln(k/T)与1/T之间的关系符合Eyring公式,其活化焓ΔH=25.44kJ/mol,活化熵ΔS=-218.54J/mol·K。     

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。     

凹凸棒黏土负载纳米TiO_2-Fe_3O_4吸附剂的制备及Cr(Ⅵ)的脱除

采用溶胶-凝胶法、一锅反应法制备了负载纳米TiO_2和Fe_3O_4的凹凸棒黏土(TiO_2-Fe_3O_4-ATP)吸附剂,并进行了模拟废水中Cr(Ⅵ)的吸附及脱附性能的研究。通过扫描电子显微镜(SEM)、X射线衍射(XRD)、傅里叶变换红外光谱(FT-IR)和EDS等分析方法对ATP负载纳米TiO_2-Fe_3O_4前后结构进行了表征,考察了物料配比及吸附时间、pH值、温度、投加量和初始质量浓度对Cr(Ⅵ)吸附率的影响。结果表明,吸附剂在Ti元素含量与负载总量的摩尔比为3∶4时吸附效果最佳。当吸附剂质量为0. 6 g,Cr(Ⅵ)离子初始质量浓度小于0. 8 mg/L时,pH=6,温度20℃,吸附剂对Cr(Ⅵ)的吸附率为79. 8%。TiO_2-Fe_3O_4-ATP吸附剂对Cr(Ⅵ)离子吸附满足Freundlich模型。在20～40℃条件下,吸附过程ΔG 0、ΔS=-43. 55 J/(mol·K)、ΔH=-14. 36 k J/mol,表明该吸附是个自发、熵减、放热的过程。吸附过程符合准二级动力学模型,吸附速率控制步骤以表面化学反应为主。TiO_2-Fe_3O_4-ATP吸附剂在循环使用4次后,吸附率仍能达到65%以上。     

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。     

Kinetics and Thermodynamics of Adsorption of VB12 onto Mesoporous Carbon Coated with PMMA

Ordered mesoporous carbons CMK-3, CMK-1 coated with poly(methyl methacrylate)(PMMA)(CMK-3- PMMA and CMK-1-PMMA) and pristine mesoporous carbons CMK-3, CMK-1 were employed to adsorb vitamin B12(VB12) from water solution. Adsorption isotherm and kinetics of adsorption were investigated via batch experi- ments. It was found that the adsorption capacity of VB12 at 30, 40 and 50 °C can reach 688.2, 572.4 and 428.7 mg/g, respectively. The adsorption isotherm can be described by Langmuir model. The pseudo first- and second-order kinetic models were employed to fit the dynamic adsorption. It was found that the dynamic adsorption follows the pseudo second-order model. The thermodynamic equilibrium coefficients obtained at different temperatures were used to evaluate the thermodynamic constants ΔG0, ΔH0 and ΔS0. The negative value of Gibbs free energy, ΔG0 indicates that the adsorption occurred via a spontaneous process. The increase in the value of –ΔG0 with increasing temperature indicates that higher temperatures were favourable to the sorption process. The enthalpy values of ΔH040 kJ/mol(66.36 kJ/mol and 56.43 kJ/mol) for CMK-3-PMMA and CMK-1-PMMA confirm that chemisorption were involved in the adsorption process. This is consistent with the IR spectra and is another evidence for the formation of hydrogen bond between PMMA in the pore of CMK-3 and VB12.     

The removal of uranium(VI) from aqueous solutions onto activated carbon: kinetic and thermodynamic investigations

The adsorption of uranium(VI) from aqueous solutions onto activated carbon has been studied using a batch adsorber. The parameters that affect the uranium(VI) adsorption, such as contact time, solution pH, initial uranium(VI) concentration, and temperature, have been investigated and optimized conditions determined (contact time 240 min; pH 3.0+/-0.1; initial uranium concentration 100 mg/L; temperature 293.15 K). The experimental data were analyzed using sorption kinetic models (pseudo-first- and pseudo-second-order equations) to determine the equation that fits best our experimental results. Equilibrium isotherm studies were used to evaluate the maximum sorption capacity of activated carbon and experimental results showed this to be 28.30 mg/g. The Freundlich, Langmuir, and Dubinin-Radushkevich (D-R) models have been applied and the data correlate well with Freundlich model and that the sorption is physical in nature (the activation energy Ea=7.91 kJ/mol). Thermodynamic parameters (DeltaHads0=-50.53 kJ/mol, DeltaSads0=-98.76 J/mol K, DeltaGads(293.15 K)0=-21.61 kJ/mol) showed the exothermic heat of adsorption and the feasibility of the process.     

2,4-/2,6-二氨基甲苯在D151树脂上的吸附分离

从10种树脂中筛选出D151树脂对2,4-二氨基甲苯和2,6-二氨基甲苯的吸附分离及其热力学性质进行了研究。 测定了吸附等温线,Freundlich模型对实验的拟合度大于Langmuir模型,其相关系数大于0.99。 热力学研究结果表明,在293～313 K条件下,初始质量浓度为60～80 g/L时,2,4-二氨基甲苯的吸附焓变为-4.3490～-5.7558 kJ/mol,自由能变为-0.2911～-1.0346 kJ/mol,吸附熵变为-12.965～-16.150 J/(mol·K);而2,6-二氨基甲苯的吸附焓变为-2.9645～-3.6054 kJ/mol,自由能变为-0.1610～-0.6384 kJ/mol,吸附熵变为-7.939～-11.005 J/(mol·K)。 进一步研究了D151树脂对二氨基甲苯的动态吸附分离,可以将2,6-二氨基甲苯含量从20%提高至99.93%,将2,4-二氨基甲苯含量从80%提高至99.42%。     

高容量亚胺基二乙酸型螯合树脂的制备及吸附性能

以甲基丙烯酸缩水甘油酯(GMA)为单体, 氯甲基化的交联聚苯乙烯树脂(CMCPS)为大分子引发剂, CuBr/2,2'-联吡啶(Bpy)为催化剂, 采用表面引发原子转移自由基聚合(SI-ATRP)技术, 使甲基丙烯酸缩水甘油酯聚合在CMCPS树脂表面, 制得了环氧化聚合物. 将该聚合物与亚胺基二乙酸(IDA)反应, 制备了高容量亚胺基二乙酸型螯合树脂(IDA-PGMA-CMCPS), 用元素分析对其进行了表征. 考察了螯合树脂对Cu²⁺的吸附性能及动力学和热力学参数. 该螯合树脂表面IDA接枝密度达8.15 mg/m². 研究结果表明, 树脂对Cu²⁺的吸附量随离子浓度和温度的升高而增加, 当pH值为2.2时, 对Cu²⁺离子的吸附效果最佳. 树脂的静态饱和吸附容量为1339.66 mg/g, Langmuir和Freundlich方程均呈现良好的拟合度. 通过热力学平衡方程计算ΔG<0, ΔH=270.60 kJ/mol, ΔS>0, 表明该吸附过程是自发、 吸热、 熵增加的过程. 动力学研究结果表明, 准二级动力学方程能较好拟合动力学实验结果, 该过程符合准二级动力学模型.     

Kinetics and Mechanism of Exothermic First-stage Decomposition Reaction of 2,6-Bis （2,2,2-trinitroethyl）glycoluril

The thermal behavior, mechanism and kinetic parameters of the exothermic first-stage decomposition of the title compound in a temperature-programmed mode were investigated by means of DSC, TG-DTG and IR. The reaction mechanism was proposed. The kinetic model function in differential form, apparent activation energy(Ea) and pre-exponential factor(A) of this reaction are (3/2)(1-a)[-ln(1-a)]1/3, 185.52 kJ/mol and 1017.78 s-1, respectively. The critical temperature of the thermal explosion of the compound is 201.30 ℃. The values of ΔS≠, ΔH≠ and ΔG≠ of this reaction are 72.46 J/(mol · K), 175.1 kJ/mol and 141.50 kJ/mol, respectively.     

Meso-2,3-二氰基-2,3-二苯基丁二酸二乙酯熔融相热异构化反应动力学及中间体EPR测定

测定了2,3-二氰基-2,β-二苯基丁二酸二乙酯meso-异构体熔融相的热异构化反应动力学及苯环对位为X(X=OCH₃,CH₃,H,Cl,NO₂)的相应二乙酯反应中间体自由基的EPR谱,自由基的结构由计算机模拟确定.结果表明,在实验温度范围内,平衡常数随温度的升高而降低.热力学数据为:ΔH_dl-meao= - 18.02 kJ/mol, ΔS_dl-meao= - 26.51 J/mol·K, ΔH^≠ = 151.78 kJ/mol, ΔS^≠ = 71.64 J/mol·K.反应机理是内消旋体的中心碳-碳键发生均裂,生成α-氰基-α-乙氧甲酰基-P-X取代苄基自由基,再重新结合时发生异构化,生成dl-异构体.     

酰胺多胺配体Cu(Ⅱ)配合物的稳定性和酸分解动力学

合成了酰胺多胺配体(L),测定了5,10,15和25℃时其Cu(Ⅱ)配合物的稳定常数,用标准摩尔焓变ΔHm0和标准摩尔熵变ΔSm0解释了温度对稳定性的影响,并利用停流技术(Stopped-flow)研究了CuL配合物在0.04～2.3mol/L(I=2.34mol/LNaCl)盐酸溶液中的酸分解动力学.提出了反应机理,并求得了速控步骤的活化能Ea,标准摩尔活化熵Δ≠Sm0和标准摩尔活化焓Δ≠Hm0     

Effect of various environmental factors on the adsorption of U(VI) onto biochar derived from rice straw

Herein, we used biochar pyrolyzed from rice straw to adsorb uranium (U) from aqueous solutions. The adsorption of U(VI) on biochar was strongly dependent on pH but independent on ionic strength. HA/FA enhanced the sorption at pH <6.8 while inhibited the sorption at pH >6.8. The sorption reached equilibrium within 3 h, which was not mediated by pH. The adsorption process was spontaneous and endothermic, and enhanced at higher temperature. However, the influence of temperature was negligible at low initial U(VI) concentrations. Therefore, biochar derived from rice straw may be a promising adsorbent for the removal of U(VI).

     

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…