乙醇在正己烷中的解缔与超额焓

测定了不同温度和浓度下乙醇与正己烷液体混合物的热压力系数及内压,并用修正的van der Waals模型关联了这些实验数据,从模型参数B/A2得到了一个乙醇自缔合随组成而遭破坏程度的公式.根据这个公式设想了一个醇与烃的混合模型,建立了混合物的超额焓方程,它能够满意地描述上述混合物的超额焓随组成的变化规律,并显示物理和化学作用对HE的贡献     

内压与液体混合物的超额焓

本文在前文提出的通用液体混合模型的基础上, 对其中某些近似假设和混合规则进行了合理的修正, 从而得到了一个液体混合物的超额焓与组分内压间的关系式。对于正常液体混合物, 式中有两个可调的修正系数, 对于醇-烃混合物, 则有三个可调参数。对十六个二元液体混合物的计算结果表明, 关系式不仅能准确地描述一般液体混合物的超额焓随浓度的变化规律, 而且亦适用于具有S型H^E-x曲线的复杂液体混合物。     

计算液态混合物内能和内压的统计热力学理论

假定二元液态混合物分子间的相互作用势能可以表示成多体相互作用势能的和,分子间的力为短程力,相互作用势能只与分子间的相对距离有关.利用分布函数理论导出了二元液态混合物的过剩内能和内压的公式.二元液态混合物的过剩内能和内压可以表示成体积的幂级数形式,其中的系数可以用多体相互作用势和多体径向分布函数表出.讨论了单元液体的内压和过剩内能的表达式,在两种特殊情形下,过剩内能和内压的表达式分别与Egelstaff的微扰论结果及Frank的实验结果具有相同的形式.讨论了二元混合物内压和内能的两个特例,其一,在特殊情形下,给出了混合液体过剩内能的混合规则的一个证明.其二,给出的二元混合物的过剩内能和内压的表达式与Frank的实验结果具有相同的形式.     

聚乙烯醇辐照交联共聚物渗透气化分离膜

研究了聚乙烯醇(PVA)与丙烯酰胺丙烯酸钠共聚物(PcoAANa)的辐照交联共聚物膜用于水-乙醇混合物的渗透气化分离,随着PcoAANa在共聚物中的含量由0%上升到35%,透量及分离系数同时增大,膜材料对混合物中水及乙醇的选择性溶解,对渗透气化过程起重大影响。求出了水、乙醇及其混合物的表现透过活化能.水,乙醇和混合物的平均扩散系数在水含量为40%时出现极大值。     

内压与非电解质溶液理论

本文用热学方法,为非电解质溶液建立了一个无热溶液理论.这个理论不包含任何可调参数,完全可由纯组分的性质来预测液体混合物的过量Gibbs自由能, 倘若以知混合物的体积,还可预测其过量焓和过量熵.而这些纯组分的性质, 都与液体的内压有关, 对37 个二元系统预测结果表明, 实验值的一致性大多优于Scatchrd-Hilderand正规溶液理论及其修正型式SHFH理论.     

水-乙醇二元体系共沸混合物的热力学研究

用全自动低温绝热量热计测定了水、乙醇以及水和乙醇组成的共沸混合物在不同温区的摩尔热容Cp,m. 建立了共沸混合物Cp,m与温度T的函数关系.结果表明,水和乙醇组成的共沸混合物在98.496 K发生玻璃态转化,在158.939 K 和270.95 K发生固-液相变.获得了其相应的相变焓和相变熵.计算了以298.15 K为基准的该共沸混合物的热力学函数和超额热力学函数.     

渗透气化法分离液体混合物

渗透气化法是一种用来分离液体混合物的膜分离方法。本综述简要地讨论了渗透气化法的机理。本法用于乙醇-水混合物的分离,对于从生物源生产乙醇具有重要意义。乙醇-水混合物的分离膜可以分成二类:亲水性膜和亲乙醇膜。使用若干物理方法可改进渗透气化过程。最后,作者认为渗透气化膜的发展趋势是从均质膜,不对称膜向复合膜过渡。     

扩散系数与内压

本文将Eyring的液体粘性流动分子模型推广到了液体混合物,并用热力学方法导出一个无限稀释溶液中溶质的的放散系数与溶剂内压间的关系式.推导表明,扩散所需的空穴大小适为一个溶质分子所占液体的体积.扩散的活化能不仅取决于溶剂对溶质分子的作用能,而且还与在溶剂中形成空穴的难易程度有关.     

基于多参数融合的红外光谱对混合物的组分识别研究

为解决混合物组分的识别问题,该文以7种标准品以及由7种标准品配制的26种混合物为研究对象,以准确率与误判率为混合组分识别效果的评价指标,在研究谱峰匹配算法、非负最小二乘匹配算法与相关系数匹配系数算法的基础上,采用一种基于多特征融合的BP神经网络模型红外光谱技术对混合物组分进行识别,并与逻辑回归模型进行了对比。结果表明,3种单一匹配算法的识别准确率均低于76.31%,多特征融合的逻辑回归模型与多特征融合的BP神经网络模型预测集的识别准确率分别为83.33%和98.18%,误判率分别为4.76%和1.82%。研究结果表明,中红外光谱技术结合BP神经网络模型可以更好地进行混合物的组分识别。为了进一步探究模型对混合组分最低浓度的检测能力,采用香兰素和乙醇两组分溶液进行检出限的研究。结果表明混合物中香兰素的质量浓度为0.03 g/mL时准确率为100.00%,误判率为14.29%;香兰素质量浓度低于0.03 g/mL时,准确率下降20.00%,误判率上升19.04%。故可认为该研究能识别出的香兰素乙醇溶液中香兰素的最低质量浓度为0.03 g/mL。     

醇的触媒氧化

醇在催化剂作用下的氧化是很有趣的有机化学实验课之一。把灼热的铜币投入乙醇中的实验是大家所熟悉的,在实验时铜币表面亮红色的铜被还原,而乙醇转变为具有果香的乙醛。少许铂丝在醇和空气的混合物中也有同样的影响是人所共知的。在小瓶内滴入几滴醇,     

Preferential solvation of indomethacin and naproxen in ethyl acetate + ethanol mixtures according to the IKBI method

The preferential solvation parameters of indomethacin and naproxen in ethyl acetate + ethanol mixtures are derived from their thermodynamic properties by using the inverse Kirkwood–Buff integrals method. It is found that both drugs are sensitive to solvation effects, so the preferential solvation parameter, δx_EA,D, is negative in ethanol-rich and ethyl acetate-rich mixtures but positive in compositions from 0.36 to 0.71 in mole fraction of ethyl acetate. It is conjecturable that in ethanol-rich mixtures, the acidic interaction of ethanol on basic sites of the analgesics plays a relevant role in the solvation. The more solvation by ethyl acetate in mixtures of similar co-solvent compositions could be due to polarity effects. Finally, the slight preference of these compounds for ethanol in ethyl acetate-rich mixtures could be explained as the common participation of basic sites in both solvents and the acidic site of ethanol. Nevertheless, the specific solute–solvent interactions remain unclear.     

Low pressure vapor–liquid equilibrium in ethanol + congener mixtures using the Wong–Sandler mixing rule

Phase equilibrium in binary ethanol mixtures found in alcoholic beverage production has been analyzed using a cubic equation of state (EoS) and suitable mixing and combining rules. The main objective of the study is the accurate modeling of the congener concentration in the vapor phase (substances different from ethanol), considered to be an important enological parameter in the alcohol industry. The Peng–Robinson (PR) equation of state has been used and the Wong–Sandler (WS) mixing rules, that include a model for the excess Gibbs free energy, have been incorporated into the equation of state constants. In the Wong–Sandler mixing rules the van Laar (VL) model for the excess Gibbs energy has been used. This combination of equations of state, mixing rules and combining rules are commonly applied to high pressure phase equilibrium and have not yet been treated in a systematic way to complex low pressure ethanol mixtures as done in this work. Nine binary ethanol + congener mixtures have been considered for analysis. Comparison with available literature data is done and the accuracy of the calculations is discussed, concluding that the model used is accurate enough for engineering applications.     

Experimental and predicted solubilities of 3,4-dichlorobenzoic acid in select organic solvents and in binary aqueous–ethanol mixtures

Experimental solubilities are reported for 3,4-dichlorobenzoic acid dissolved in methyl butyrate, and in 16 alcohol, 5 alkyl acetate, 5 alkoxyalcohol and 6 ether solvents. Solubilities were also measured in nine binary aqueous–ethanol solvent mixtures at 298.15?K. The measured solubility data were correlated with the Abraham solvation parameter model. Mathematical expressions based on the Abraham model predicted the observed molar solubilities to within 0.12 log units.     

A cosolvency model to predict solubility of drugs at several temperatures from a limited number of solubility measurements

A cosolvency model to predict the solubility of drugs at several temperatures was derived from the excess free energy model of Williams and Amidon. The solubility of oxolinic acid, an antibacterial drug, was measured in aqueous (water+ethanol) and non-aqueous (ethanol+ethyl acetate) mixtures at several temperatures (20, 30, 35, 40 degrees C). Oxolinic acid displays a solubility maximum in each solvent mixture at solubility parameter values of 32 and 22 MPa(1/2). The temperature and heat of fusion were determined from differential scanning calorimetry. The solvent mixtures do not produce any solid phase change during the solubility experiments. The experimental results and those from the literature were employed to examine the accuracy and prediction capability of the proposed model. An equation was obtained to represent the drug solubility changes with cosolvent concentration and temperature. The model was also tested using a small number of experimental solubilities at 20 and 40 degrees C showing reasonably accurate predictions. This is important in pharmaceutics because it save experiments that are often expensive and time consuming.     

Meloxicam Solubility in Ethanol+Water Mixtures According to the Extended Hildebrand Solubility Approach

In this work the extended Hildebrand solubility approach (EHSA) was applied to evaluate the solubility of the analgesic drug meloxicam in ethanol+water mixtures at 298.15 K. An acceptable correlative capacity of EHSA was found using a regular polynomial model in fifth order (overall deviation 0.52 %), where the W interaction parameter is related to the solubility parameter of the co-solvent mixtures. Nevertheless, the deviations obtained in the estimated solubility with respect to experimental solubility were similar to those obtained directly by means of an empirical regression of the logarithm of the experimental solubility as a function of the same polarity index (near to 0.51 %).     

Fermentation kinetics of ethanol production from glucose and xylose by recombinant Saccharomyces 1400(pLNH33)

Fermentation kinetics of ethanol production from glucose, xylose, and their mixtures using a recombinant Saccharomyces 1400 (pLNH33) are reported. Single-substrate kinetics indicate that the specific growth rate of the yeast and the specific ethanol productivity on glucose as the substrate was greater than on xylose as a substrate. Ethanol yields from glucose and xylose fermentation were typically 95 and 80% of the theoretical yield, respectively. The effect of ethanol inhibition is more pronounced for xylose fermentation than for glucose fermentation. Studies on glucose-xylose mixtures indicate that the recombinant yeast co-ferments glucose and xylose. Fermentation of a 52.8 g/L glucose and 56.3 g/L xylose mixture gave an ethanol concentration of 47.9 g/L after 36 h. Based on a theoretical yield of 0.51 g ethanol/g sugars, the ethanol yield from this experiment (for data up to 24 h) was calculated to be 0.46 g ethanol/g sugar or 90% of the theoretical yield. The specific growth rate of the yeast on glucose-xylose mixtures was found to lie between the specific growth rate on glucose and the specific growth rate on xylose. Kinetic studies were used to develop a fermentation model incorporating the effects of substrate inhibition, product inhibition, and inoculum size. Good agreements were obtained between model predictions and experimental data from batch fermentation of glucose, xylose, and their mixtures.     

醇／水混合液分离用聚乙烯醇复合膜的渗透汽化特性

制备了聚乙烯醇（ＰＶＡ）／聚丙烯睛（ＰＡＮ）渗透汽化复合膜，研究了交联剂用量、底膜结构、进料液组成、操作温度等因素对膜的渗透汽化性能的影响．发现ＰＶＡ／ＰＡＮ复合膜对水／醇混合液表现为水优先透过，进料液中乙醇浓度在６０～９９ｗｔ％的范围内，渗透通量Ｊｔ与温度之间符合Ａｒｒｈｅｎｉｕｓ关系，选择分离系数αＷ／Ｅ也随温度上升而增大．进料液为９５ｗｔ％的乙醇／水混合液时，７５℃下Ｊｔ高达３００～４５０ｇ／ｍ２ｈ，αＷ／Ｅ为８００～１１００．对异丙醇／水、异丁醇／水及甘油／水混合体系，复合膜显示出更为优秀的透过、分离性能．就膜的化学、物理结构与其渗透汽化性能间的关系进行了讨论．