正丁醇、乙酸乙酯、正己烷的二元及三元体系的超额焓测量和关联

用等温稀释量热计测定了正己烷+正丁醇、正己烷+乙酸乙酯二元体系在303.15K、308.15K及正丁醇+乙酸乙酯+正己烷三元体系在303.15K的超额焓,用Kretschrner-Wiebe理论组合UNIQUAC方程所得数学模型对二元体系在303.15K的超颠焓进行了关联,并预测了所测三元体系在303.15K的超额焓,预测结果与实验值比较,平均偏差为6％。     

含醇二元体系热力学性质的研究 Ⅱ.C_1～C_5正链醇+1,4-二氧六圜的过量焓

本工作利用Picker混合型流动微量量热器测量了298.15K时,1,4-二氧六圜+甲醇,+乙醇,+正丙醇,+正丁醇和+正戊醇的摩尔过量焓。仪器以苯+环已烷和苯+四氯化碳两个体系校验,x=0.5时的混合热数值,与文献值相符在1％以内。试剂按常规方法处理,纯化液体的折光率,与文献值一致。将测得各体系的摩尔过量焓,拟合为如下的多项式:     

环己酮-醇二元系统超额焓测定和关联的研究

用MS-80型Calvet微热量计首次测定了环己酮＋乙醇、＋正丙醇、＋正丁醇、＋环戊醇、＋环己醇系统在293.15、298.15、303.15及308.15 K四个温度下的超额焓HE,并拟合为平滑方程,拟合方差很小.环己酮和醇组成的二元混合系统的超额焓在全浓度范围内都为正值,其最大值都处在醇浓度为50％附近.超额焓随着醇分子中含碳原子数的增多而增大；超额焓值受温度的影响很大,且随着温度的升高而增大.     

合成介质对稀土铽-邻苯二甲酸有机配合物荧光强度的影响

在不同介质(依次为甲醇、乙醇、正丙醇、正丁醇)中合成了邻苯二甲酸Tb3+稀土二元配合物. 利用元素分析和红外光谱分析等对配合物的组成和结构进行了表征. 荧光光谱结果表明, 直链醇作为合成介质时配合物的荧光强度大小顺序依次为: 甲醇>乙醇>正丙醇>正丁醇. 同时该配合物在2~300 K范围内测定的变温磁化率说明该配合物具有反铁磁性.     

α-蒎烯+对伞花烃和β-蒎烯+对伞花烃二元体系超额焓的测定

采用BT2.15型Calvet微量量热计常压下测定了α-蒎烯+对伞花烃和β-蒎烯+对伞花烃两个二元体系在298.15 K、308.15 K及318.15 K下的超额焓. 实验数据采用Redlich-Kister方程进行关联, 标准偏差较小. 该两个二元体系的超额焓在全浓度范围内均为正值, 其最大值在摩尔分数x1=0.5附近. 温度对超额焓有一定的影响, 超额焓随温度的升高而增大. 相同温度下, α-蒎烯+对伞花烃体系的超额焓比β-蒎烯+对伞花烃体系的大.     

正丁醇/正戊醇+JP-10二元体系的体积性质

在常压下测定了298.15 K时正丁醇/正戊醇+挂式四氢双环戊二烯(C₁₀H₁₆, JP-10)二元体系的黏度和密度. 根据Eyring液体黏性流动理论, 关联了二元体系的黏滞性活化参数, 结果表明, 焓驱动起主要作用. 利用密度数据计算了醇+JP-10二元体系的超额摩尔体积、 超额偏摩尔体积、 表观摩尔体积及偏摩尔体积等体积性质, 结果表明此二元体系的超额摩尔体积为正值.     

醇类在惰性溶剂中的缔合溶液热力学

用Kretschmer-Wiebe模型结合Hildebrand-Scatchard公式处理含醇体系的活度系γ_i,得到醇类的自身缔合平衡常数K_A和氢键生成焓h_A。在烷烃溶剂中,K_A与烷烃的碳原子数关系不显著。在同一溶剂中,K_A依下列顺序减小: 甲醇>乙醇>正丙醇>正丁醇; 正丙醇>异丙醇; 正丁醇>异丁醇>仲丁醇>叔丁醇。所测醇类的h_A的平均值为:k_A=-24.3±0.6kJmol~(-1),与醇类的碳原子数及异构关系不显著计算出醇类-角鲨烯体系偏离Hildebrand-Scatchard公式的相互作用常数l_(AB),l_(AB)均为负值,|l_(AB)|依下列顺序减小: 甲醇>乙醇>正丙醇>正丁醇; 正丙醇>异丙醇; 正丁醇>异丁醇>仲丁醇>叔丁醇     

含醇二元体系热力学性质的研究 Ⅰ. C1至C5正链醇+苯体系的过量焓

使用Picker流动微量量热器系统测量了298.15 K和常压下甲醇+, 乙醇+, 正丙醇+, 正丁醇+和正戊醇+苯体系的摩尔过量焓。所得结果, 一般较间歇式量热器的测量数据稍高。这些体系的最大过量焓在~x醇=0.30～0.33。正链醇+苯体系的摩尔过量焓的数值, 在C_1～C_5之间, 随着醇分子中碳原子的数目增多而升高, 但两相邻醇H~E的差值, 则随碳链的增长而逐渐减小。     

N-甲基哌嗪与乙酸乙酯、乙酸丁酯二元混合体系在298.15～313.15K的体积及黏度性质

测定了N-甲基哌嗪+乙酸乙酯和N-甲基哌嗪+乙酸丁酯2个二元混合体系在298.15,303.15,308.15和313.15 K的密度和黏度数据,并计算了N-甲基哌嗪+酯二元混合体系的超额摩尔体积(VEm)和黏度偏差(Δη),用Redlich-Kister多项式关联了二元体系的超额摩尔体积与组成的关系,用4个半经验公式关联黏度数据并关联了二元体系的黏滞性活化参数.结果表明,N-甲基哌嗪+乙酸乙酯和N-甲基哌嗪+乙酸丁酯二元体系在所测温度范围内的超额摩尔体积为正值,黏度偏差为负值,且二元混合体系在混合过程中焓驱动居于主导地位.     

正烷醇/异丙醇二元体系过量焓的测定

用LKB 2277 Bioactivity Monitor测定了一些正烷醇(甲醇到正己醇)与异丙醇二元体系在298.15K的常压过量焓H^E的数据, 对丙醇/异丙醇, 正丁醇/异丙醇和正戊醇/异丙醇还测定了308.15K和313.15K的常压过量焓数据。同时给出了关联实验结果的多项式方程的各参数。     

Excess molar enthalpies for ternary mixtures of (methanol or ethanol + water + tributyl phosphate) at <Emphasis Type="Italic">T</Emphasis> = 298.15 K

Excess molar enthalpies for two ternary mixtures of {x ₁ tributylphosphate (TBP) + x ₂ water + x ₃ methanol/ethanol} were measured at T = 298.15 K and atmospheric pressure using a TAM Air isothermal calorimeter, by mixing methanol or ethanol with binary mixtures of (water + TBP). Excess enthalpies for initial binary mixtures of (water + TBP) were also measured under the same conditions, which showed phase separation at low molar fraction of TBP. Experimental results of the ternary mixtures were expressed with constant excess molar enthalpy contours on Roozeboon diagrams.     

Excess Thermodynamic Properties of Binary Liquid Mixtures Containing N,N -Dimethylacetamide with Some Alkan-1-Ols (C 1 -C 6 ) At 298.15 K

Excess molar enthalpies, $ H_m^E $ of N , N -dimethylacetamide + methanol, + ethanol, + propan-1-ol, + butan-1-ol, + pentan-1-ol, and + hexane-1-ol have been determined at 298.15 K and atmospheric pressure using a Parr 1455 solution calorimeter. While the excess molar enthalpies are negative for methanol and ethanol mixtures, those for propan-1-ol, butan-1-o1, pentane-1-ol, and hexan-1-ol mixtures are positive over the entire range of composition of N , N -dimethylacetamide. The $ H_m^E $ at around x , 0.5 follow the order: methanol<ethanol<propan-1-ol<butan-1-ol<pentan-1-ol<hexan-1-ol. The results are explained in terms of the self-association exhibited by the alkan-1-ols and the formation of aggregates between unlike molecules through OHO hydrogen bonding. The experimental results for mixtures are well represented by the Redlich - Kister equation.     

Excess enthalpies of alcohol + amine mixtures. Experimental results and theoretical description using the ERAS-model

New experimental data of the molar excess enthalpy H^E of mixtures containing eight liquids - propylamine + methanol, ethanol, propan-1-ol, butan-1-ol, butylamine + methanol, ethanol, propan-1-ol, butan-1-ol - are presented using a quasi-isothermal flow calorimeter. The results are used for testing the ERAS-model which provides a theoretical concept accounting for the self-association and cross-association of alcohol and amine molecules, as well as for non-associative intermolecular interactions. Excess molar volumes V^E are also successfully described by the model. It turns out that the strong cross-association occurring between alcohol and amine molecules is the predominant reason for the remarkably low exothermic values of H^E observed for the mixtures studied.     

Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15 K and atmospheric pressure

Excess molar enthalpies and heat capacities of binary mixtures containing dimethyl sulfoxide (DMSO) + seven normal alkanols, namely methanol, ethanol, propan-1-ol, butan-1-ol, hexan-1-ol, octan-1-ol, and decan-1-ol, have been determined at 303.15 K and atmospheric pressure. With the exception of the DMSO-methanol system, which shows negative values, all mixtures show positive values of excess molar enthalpies over the whole range of mole fraction, increasing as the number of carbon atoms increases. Heat capacities of pure components have been determined in the range 288.15 < T (K) < 325.15. Molar heat capacities of the mixtures are always positive and decrease as the number of carbon atoms decreases. The results were fitted to the Redlich-Kister polynomial equation. Molecular interactions in the mixtures are interpreted on the basis of the results obtained.     

Ternary excess molar enthalpies for the mixtures of methanol and ethanol with tetrahydropyran or 1,4-dioxane at 298.15 K

Ternary excess molar enthalpies, H_m^E, at 298.15 K and atmospheric pressure measured by using a flow microcalorimeter are reported for the (methanol+ethanol+tetrahydropyran) and (methanol+ethanol+1,4-dioxane) mixtures. The pseudobinary excess molar enthalpies for all the systems are found to be positive over the entire range of compositions. The experimental results are correlated with a polynomial equation to estimate the coefficients and standard errors. The results have been compared with those calculated from a UNIQUAC associated solution model in terms of the self-association of alcohols as well as solvation between unlike alcohols and alcohols with tetrahydropyran or 1,4-dioxane. The association constants, solvation constants and optimally fitted binary parameters obtained solely from the pertinent binary correlation predict the ternary excess molar enthalpies with an excellent accuracy.     

Densities, Viscosities, Speeds of Sound, FT-IR and 1H-NMR Studies of Binary Mixtures of n-Butyl Acetate with Ethanol, Propan-1-ol, Butan-1-ol and Pentan-1-ol at?298.15, 303.15, 308.15 and 313.15?K

Densities, viscosities and speeds of sound of binary mixtures of ethanol, propan-1-ol, butan-1-ol and pentane-1-ol with n-butyl acetate have been measured over the entire range of composition at temperatures of 298.15, 303.15, 308.15 and 313.15 K and atmospheric pressure. From the experimental densities, viscosities and speeds of sound, the excess molar volumes V ^E, deviations in viscosity ????, and deviations in isentropic compressibility ???? _S have been calculated. The excess molar volumes and deviations in isentropic compressibility are positive for all the binary systems studied over the whole composition, while deviations in viscosities are negative for all of the binary mixtures. The excess molar volumes, deviations in viscosity, and deviations in isentropic compressibility have been fitted to a Redlich?CKister type polynomial equation. FTIR and ¹H-NMR studies of these mixtures are also reported.     

Spectroscopic and acoustic study in binary mixtures of glycerol with several alkanols

Speeds of sound and densities of glycerol + methanol, glycerol + ethanol and glycerol + 2-propanol, were measured over the entire composition range at 298.15 K. The excess volumes, the isentropic compressibilities, molar isentropic compressibilities and excess molar isentropic compressibilities and excess speeds of sound were estimated from the densities and speeds of sound. The results indicated the presence of interactions between unlike molecules through intermolecular hydrogen bonding. The excess volumes, excess molar isentropic compressibilities and excess speeds of sound of the binary mixtures were fitted to the Redlich–Kister equation. The infrared spectra of glycerol + methanol, glycerol + ethanol and glycerol + 2-propanol have been recorded for various concentrations at room temperature. IR stretching frequencies, bandwidths and relative intensities have been estimated and analysed. Acoustic and spectroscopic measurements showed a good correlation to explain the existence of interactions between unlike molecules through intermolecular hydrogen bonding.     

Isentropic expansion and related thermodynamic properties of non-ionic amphiphile-water mixtures

A concise thermodynamic formalism is developed for the molar isentropic thermal expansion, ES,m = ( partial differential Vm/ partial differential T)(Sm,x), and the ideal and excess quantities for the molar, apparent molar and partial molar isentropic expansions of binary liquid mixtures. Ultrasound speeds were determined by means of the pulse-echo-overlap method in aqueous mixtures of 2-methylpropan-2-ol at 298.15 K over the entire composition range. These data complement selected extensive literature data on density, isobaric heat capacity and ultrasound speed for 9 amphiphile (methanol, ethanol, propan-1-ol, propan-2-ol, 2-methylpropan-2-ol, ethane-1,2-diol, 2-methoxyethanol, 2-ethoxyethanol or 2-butoxyethanol)-water binary systems, which form the basis of tables listing molar and excess molar isobaric expansions and heat capacities, and molar and excess molar isentropic compressions and expansions at 298.15 K and at 65 fixed mole fractions spanning the entire composition range and fine-grained in the water-rich region. The dependence on composition of these 9 systems is graphically depicted for the excess molar isobaric and isentropic expansions and for the excess partial molar isobaric and isentropic expansions of the amphiphile. The analysis shows that isentropic thermal expansion properties give a much stronger response to amphiphile-water molecular interactions than do their isobaric counterparts. Depending on the pair property-system, the maximum excess molar isentropic value is generally twenty- to a hundred-fold greater than the corresponding maximum isobaric value, and occurs at a lower mole fraction of the amphiphile. Values at infinite dilution of the 9 amphiphiles in water are given for the excess partial molar isobaric heat capacity, isentropic compression, isobaric expansion and isentropic expansion. These values are interpreted in terms of the changes occurring when amphiphile molecules cluster into an oligomeric form. Present results are discussed from theoretical and experimental thermodynamic viewpoints. It is concluded that isentropic thermal expansion properties constitute a new distinct resource for revealing particular features and trends in complex mixing processes, and that analyses using these new properties compare favourably with conventional approaches.     

Thermodynamics of mixtures with strongly negative deviations from Raoult’s law: Part 5. Excess molar volumes at 298.15 K for 1-alkanols+dipropylamine systems: characterization in terms of the ERAS model

Excess molar volumes, V_m^E, at 298.15 K and atmospheric pressure over the entire composition range for binary mixtures of methanol, ethanol, 1-propanol, 1-butanol, 1-pentanol, 1-hexanol, 1-heptanol and 1-octanol with dipropylamine are reported from densities measured with a vibrating-tube densimeter. All the excess volumes are large and negative over the whole mole fraction range, indicating strong interactions between unlike molecules, which are more important for the system involving methanol, characterized by the most negative V_m^E. For the remainder mixtures, V_m^E at equimolar composition, is approximately constant. The V_m^E curves are nearly symmetrical.

V_m^E and excess molar enthalpies, H_m^E, of the mixtures studied are consistently described by the ERAS model. The ERAS parameters confirm that the strongest interactions between unlike molecules are encountered in the methanol+dipropylamine system.     

Thermodynamics of the ternary mixture propan-1-ol + tetrahydrofuran + n-heptane at 298.15 K. Experimental results and ERAS model calculations of G, H and V

Excess molar enthalpies H^E and excess molar volumes V^E have been measured at 298.15 K and 0.1 MPa for the ternary mixture tetrahydrofuran (THF) + propan-1-ol (PrOH) + n-heptane including the three binary mixtures using flow calorimetry and a vibrating tube densitometer, respectively.

Molar excess Gibbs energies G^E have been measured at 298.15 K using a static VLE apparatus equipped with a chromatographic sampling technique for the vapor phase as well as for the liquid phase. Experimental results have been compared with predictions of the ERAS model.