气相色谱吸附过程的热力学函数变化及规律探讨 Ⅰ.某些直链烷和醇在Porapak上的吸附

用气相色谱法测定了28个吸附体系的吸附热、吸附熵变、吸附自由能和平衡常数;总结了同系物吸附过程热力学函数变化的一些规律:发现在某一温度T_(iso)时,同系物的吸附自由能相等,建议将该点称为“等热力学点”。     

异丁烷脱氢反应的热力学分析

利用HSC5.0软件对异丁烷脱氢反应进行热力学分析,计算了异丁烷脱氢过程中各反应的平衡常数和不同温度、压力及氢烃比的异丁烷脱氢反应的平衡转化率.结果显示,裂解反应平衡常数比脱氢反应大约3个数量级,在热力学上裂解反应更易进行.在异丁烯异构化产物中,trans-C4 H8生成的平衡常数最大,cis-C4 H8其次,1-C4...     

NH+O3→ONH+O2反应热力学和动力学研究

在量子化学对 NH自由基与臭氧 O3反应计算的基础上,应用统计热力学方法研究了 100～ 1600 K温度范围内 NH和 O3反应过程的各热力学量的变化及平衡常数,用经 Wigner校正的 Eyring过渡态理论计算了不同温度下该反应两不同反应通道的活化热力学量、反应速率常数及频率因子.计算表明,相对于反应通道 II,反应通道 I不仅有很强的反应自发性,而且在动力学上也是较容易实现的反应.     

甲醇制烃（MTH）反应热力学研究

对甲醇制烃反应体系进行了热力学分析,计算了不同温度下各反应的焓变、吉布斯自由能变和反应平衡常数,采用平衡常数联立方程法估算了甲醇转化生成C2-C10烃的热力学平衡组成.计算结果表明：甲醇制烃为强放热反应,1 mol甲醇转化最大放热量约为90 kJ/mol;甲醇制烃体系中除甲醇脱水之外,大部分反应均可视为不可逆过程;高温低压不利于烷烃生成物,有利于芳烃和烯烃生成物.对计算结果与实验结果进行了比较,数据变化趋势较为一致.计算结果表明,甲醇制烃体系不受热力学的控制,催化剂的选择和反应条件的选择至关重要.     

NH＋O3→ONH＋O2反应热力学和动力学研究

在量子化学对NH自由基与臭氧O3反应计算的基础上，应用统计热力学方法研究了100～1600 K温度范围内NH和O3反应过程的各热力学量的变化及平衡常数，用经Wigner校正的Eyring过渡态理论计算了不同温度下该反应两不同反应通道的活化热力学量、反应速率常数及频率因子.计算表明，相对于反应通道II，反应通道I不仅有很强的反应自发性，而且在动力学上也是较容易实现的反应.     

SH15树脂吸附胞二磷胆碱的热力学及动力学研究

静态条件下,研究了SH15树脂吸附水溶液中胞二磷胆碱(CDPC)的热力学和动力学特性.测定了不同温度下,热力学性质的变化.实验结果表明,SH15树脂对CDPC吸附平衡数据符合Langmmuir吸附等温方程,吸附过程为自发的物理吸附过程.考察了温度、溶液浓度、树脂粒径和搅拌速率对吸附过程的影响.运用动边界模型(MBM)描述了SH15树脂吸附CDPC的动力学过程,确定在实验条件范围内,SH15树脂吸附CDPC的吸附速度受颗粒扩散控制,并计算出吸附过程的表观活化能为9.73kJ/mol,反应级数为0.47,速率常数为0.0744,并推导出CDPC:在SH15树脂上的动力学总方程.     

亚稳平衡吸附态与亚稳平衡系数关系的热力学研究

在相同温度、压力、pH值和离子强度等条件下．同一种金属离子在无机矿物表面上发生的吸附反应可以形成能量不同的吸附状态(如Zn可以边-边和角-角两种方式吸附在水锰矿表面上),因而反应终了时吸附质可处于不同的亚稳平衡吸附态(MEA)．应用MEA理论,针对吸附反应A -H2O-x -A1 y -A2 H2O。推导出实际吸附反应“平衡常数”(Kreal)与亚稳平衡系数(Kme)的热力学关系式,从理论上分析了吸附反应MEA状态的变化对实际吸附反应平衡性质的影响．分析结果表明,Kme值与两种MEA状态之间的能量差呈指数关系,通过影响吸附反应的MEA状态(包括能量和组成)的反应动力学因素可影响吸附平衡常数和吸附等温式(线)等吸附热力学性质．     

异丁烷与丁烯烷基化反应的热力学分析

对异丁烷与丁烯烷基化反应进行了较为详尽的热力学分析和计算，得到了不同反应温度下的焓值、吉布斯自由能和反应平衡常数，并且对温度、压力和惰性物质对热力学平衡的影响进行了分析。得到了详细的烷基化反应热力学基础数据，这些数据对研究异丁烷与丁烯的烷基化反应具有重要的参考价值。     

钠型斜发沸石Na+-K+离子交换特性研究(I)-离子交换过程热力学特性

测定出斜发沸石的阳离子交换容量为 192.18mmol/100g 沸石;通过 10℃、25℃、50℃、75℃钠型斜发沸石 Na+–K+离子交换等温线、温度对选择性校正系数的影响及 Kielland 图研究表明:钠型斜发沸石对钠钾混合体系中的钾具有很高的选择性,且随着温度的上升,沸石对钾的选择性下降,并回归出 Langmuir 模型;依据热力学平衡原理,导出了钠型斜发沸石 Na+–K+离子交换过程平衡常数表达式,并计算出该过程的焓、吉布斯自由能和熵变化,进一步验证该过程可自发进行,且为放热反应,低温有利于钾离子吸附。     

气液色谱法测定双-(O,O′-二正辛基二硫代磷酸酯)合镍(Ⅱ)和三乙胺加合反应的热力学参数

本文报道了用气液色谱法测定不同温度下,酸碱加合反应:的平衡常数,根据热力学公式,并利用最小二乘法求得。在实验温度范围内,实验数据可以用公式:来描述。     

Temperature dependent thermodynamic model of the system H(+)-NH₄(+)-Na(+)-SO₄²⁻-NO₃⁻-Cl⁻-H₂O

A thermodynamic model of the system H(+)-NH?(+)-Na(+)-SO?2?-NO??-Cl?-H?O is parametrized and used to represent activity coefficients, equilibrium partial pressures of H?O, HNO?, HCl, H?SO?, and NH?, and saturation with respect to 26 solid phases (NaCl(s), NaCl·2H?O(s), Na?SO?(s), Na?SO?·10H?O(s), NaNO?·Na?SO?·H?O(s), Na?H(SO?)?(s), NaHSO?(s), NaHSO?·H?O(s), NaNH?SO?·2H?O(s), NaNO?(s), NH?Cl(s), NH?NO?(s), (NH?)?SO?(s), (NH?)?H(SO?)?(s), NH?HSO?(s), (NH?)?SO?·2NH?NO?(s), (NH?)?SO?·3NH?NO?(s), H?SO?·H?O(s), H?SO?·2H?O(s), H?SO?·3H?O(s), H?SO?·4H?O(s), H?SO?·6.5H?O(s), HNO?·H?O(s), HNO?·2H?O(s), HNO?·3H?O(s), and HCl·3H?O(s)). The enthalpy of formation of the complex salts NaNH?SO?·2H?O(s) and Na?SO?·NaNO?·H?O(s) is calculated. The model is valid for temperatures < or approximately 263.15 up to 330 K and concentrations from infinite dilution to saturation with respect to the solid phases. For H?SO?-H?O solutions the degree of dissociation of the HSO?? ion is represented near the experimental uncertainty over wide temperature and concentration ranges. The parametrization of the model for the subsystems H(+)-NH?(+)-NO??-SO?2?-H?O and H(+)-NO??-SO?2?-Cl?-H?O relies on previous studies (Clegg, S. L. et al. J. Phys. Chem. A 1998, 102, 2137-2154; Carslaw, K. S. et al. J. Phys. Chem. 1995, 99, 11557-11574), which are only partly adjusted to new data. For these systems the model is applicable to temperatures below 200 K, dependent upon liquid-phase composition, and for the former system also to supersaturated solutions. Values for the model parameters are determined from literature data for the vapor pressure, osmotic coefficient, emf, degree of dissociation of HSO??, and the dissociation constant of NH? as well as measurements of calorimetric properties of aqueous solutions like enthalpy of dilution, enthalpy of solution, enthalpy of mixing, and heat capacity. The high accuracy of the model is demonstrated by comparisons with experimentally determined mean activity coefficients of HCl in HCl-Na?SO?-H?O solutions, solubility measurements for the quaternary systems H(+)-Na(+)-Cl?-SO?2?-H?O, Na(+)-NH?(+)-Cl?-SO?2?-H?O, and Na(+)-NH?(+)-NO??-SO?2?-H?O as well as vapor pressure measurements of HNO?, HCl, H?SO?, and NH?.     

Removal of UO2 2+ from aqueous solution by plasma functionalized MWCNTs

The study was undertaken to evaluate the feasibility of functionalized multi-walled carbon nanotubes (MWCNTs) for the removal of UO₂ ²⁺ from aqueous solutions. The MWCNTs was treated by oxygen plasma and characterized by FTIR and XPS. The characterization indicates that MWCNTs is successfully functionalized of oxygen groups such as –COOH on its surface (denote as P-MWCNTs). The sorption of UO₂ ²⁺ from aqueous solution on P-MWCNTs was studied as a function of contact time, solid contents, pH, ionic strength and temperature under ambient conditions using batch experiment. Two simplified kinetic models of pseudo-first-order and pseudo-second-order were tested to determine kinetic parameters such as rate constants, equilibrium sorption capacities and related correlation coefficients for kinetic models of the sorption process. It can be seen that the UO₂ ²⁺ sorption on P-MWCNTs could be described more favorably by the pseudo-second-order model. The thermodynamic parameters (?G°, ?S°, ?H°) calculated from the temperature-dependent sorption isotherms indicated that the sorption of UO₂ ²⁺ on P-MWCNTs were an endothermic and spontaneous processes. The results of the present study suggest that P-MWCNTs can be used beneficially in treating industrial effluents containing radioactive and heavy metal ions.     

DMA水溶液的1H NMR研究

测量了N，N-二甲基乙酰胺(DMA)水溶液体系不同温度下全浓度范围的^1H NMR数据，对体系中的缔合情况进行了讨论。应用化学缔合模型求得了各缔合平衡常数K和缔合平衡的△H，结合N，N-二甲基甲酰胺(DMF)和N-甲基乙酰胺(NMA)水溶液的研究结果，发现酰胺自身结构和酰胺浓度是影响酰胺水溶液性质的主要因素。     

Sorption onto insoluble β-cyclodextrin polymer for 2,4-dinitrophenol

The sorption of β-cyclodextrin polymer (β-CDP) towards 2,4-dinitrophenol (2,4-DNP) in aqueous solutions was investigated. The influence of sorption conditions including initial 2,4-DNP concentration, contact time and pH on sorption capability were discussed. The sorption isotherm can be correlated to Freundlich model. The maximum sorption capacity of 2,4-DNP for β-CDP was measured to be 192?mg/g with the initial concentration at 1,000?mg/L at 303?K. The β-CDP was easily recovered by ethanol as washing solvent and they could be used as a kind of recyclable sorbents.     

Cation exchange and sorption properties of crystalline alpha-titanium(IV) phosphate

The ion-exchange and sorption properties of alpha-titanium bis(monohydrogen orthophosphate) monohydrate of composition Ti(HPO(4))(2).H(2)O was studied in aqueous electrolyte solutions of KCl over the temperature range of 300-320 K, varying the pH and metal ion concentration in the solution. The data were explained on the basis of the law of chemical equilibrium and the metal ion sorption data were fitted to Langmuir parameters. Further, the extent of sorption was found to increase with increasing temperature and metal ion concentration in the selectivity order Fe(3+)>Cu(2+)>Co(2+)>Mn(2+)>Cr(3+)>Ni(2+). The values of Langmuir constants were used to calculate the various thermodynamic parameters, such as DeltaG(0), DeltaH(0), and DeltaS(0), during the sorption process.     

Sorption of Cr(VI) ions by oxyhydrates of M x Al1?x O y · nH2O composition, where M is Zr(IV), Ti(IV), or Sn(IV)

The equilibrium and kinetics of Cr(VI) ion sorption from acidic (pH 2.5) and alkaline (pH 10.5) aqueous solutions by oxyhydrates of the M _x Al_{1 ? x} O _y · nH₂O composition, where M is Zr(IV), Ti(IV), or Sn(IV) and x = 0.0?0.7, are studied. It is shown that the sorption equilibrium can be described using the Langmuir model. The effective diffusion coefficients of Cr(VI) ions calculated from the exchange half-time and specific conductivity of oxyhydrates measured after the sorption of the target component are (0.11?C0.28) × 10^?11 m² s^?1.     

Removal of copper (Cu2+) from water by sulfonated cellulose

Water insoluble sulfonated cellulose was prepared and applied for Cu²⁺ removal from water. The effects of sorbent dose, initial solution pH, temperature and initial Cu²⁺ concentration on the removal performance of sulfonated cellulose were investigated. Isothermal data were modeled with the Langmuir and Freundlich isotherm models. The Cu²⁺ sorption onto sulfonated cellulose followed the Langmuir isotherm model with the maximum sorption capacity of 8.2?mg-Cu²⁺/g. Removal of Cu²⁺ showed rapid initial kinetics; in 3?min removal of Cu²⁺ reached equilibrium status. Thermodynamic study revealed an exothermic sorption process. In addition, sulfonated cellulose is a kind of green and renewable sorbent because it can be easily regenerated by 0.1?M HCl.     

Arsenic(III) sorption on nanostructured cerium incorporated manganese oxide (NCMO): a physical insight into the mechanistic pathway

Arsenic(III) sorption was investigated with nanostructured cerium incorporated manganese oxide (NCMO). The pH between 6.0 and 8.0 was optimized for the arsenic(III) sorption. Kinetics and equilibrium data (pH=7.0±0.2, T=303±1.6 K, and I=0.01 M) of arsenic(III) sorption by NCMO described, respectively, the pseudo-second order and the Freundlich isotherm equations well. The sorption process was somewhat complicated in nature and divided into two different segments, initially very fast sorption followed by slow intraparticle diffusion process. Sorption reaction of arsenic(III) on NCMO was endothermic (ΔH°=+13.46 kJ mol(-1)) and spontaneous (ΔG°=-24.75 to -30.15 kJ mol(-1) at T=283-323 K), which took place with increasing entropy (ΔS°=+0.14 kJ mol(-1)K(-1)) at solid-liquid interface. Energy of arsenic(III) sorption estimated by analyzing the equilibrium data using the D-R isotherm model was 15.4 kJ mol(-1), indicating the ion-exchange type mechanism. Raman, FT-IR, pH effect, desorption, etc. studies indicated that arsenic(III) was oxidized to arsenic(V) during the sorption process.     

Ion-exchange selectivity of a sulfonic cation exchanger based on immobilized cis-tetraphenylcalix[4]resorcinolarene

The ion-exchange equilibrium of protons in SO₃H groups of a sulfonic cation exchanger based on immobilized cis-tetraphenylcalix[4]resorcinolarene with cations of Li⁺, Na⁺, Ag⁺, Cu²⁺, In³⁺, and protonated 1,3,5,7-tetraazaadamantane in aqueous solutions of electrolytes at 293 K was studied. The corrected coefficients of the cation exchange selectivity were calculated.     

酚醛型吸附树脂对水体系中吡啶和N,N-二甲基苯胺的吸附性能研究

研究了酚醛型吸附树脂在水体系中对吡啶和N，N-二甲基苯胺的静态和动态吸附行为．结果表明，在水中树脂对吡啶和N，N-二甲基苯胺的吸附主要以疏水吸附机理进行；吸附吡啶和N．N-二甲基苯胺的初始阶段，即达到38．3～48．9％平衡吸附时，吸附速率数据和半经验速率方程很吻合：酚醛型吸附树脂等温吸附吡啶和N，N-二甲基苯胺的平衡吸附数据符合Langmuir方程，相关系数在0．99以上，酚醛型吸附树脂吸附吡啶和N，N-二甲基苯胺属单分子层吸附：用80％的乙醇溶液作洗脱剂来洗脱吸附吡啶已达饱和的JDW-2树脂，效果是很理想的．在3．6个床体积内洗脱率达91．52％，4．8个床体积内洗脱率达到94．85％。表明酚醛型吸附树脂具有优良的洗脱性能．