乙酸乙酯与CnH2n+1OH（n=1,2,3）双系统在0.3MPa下的气液平衡（英文）

Vapor-liquid equilibrium data for the binary systems of ethyl acetate + methanol,ethyl acetate + ethanol and ethyl acetate + 1-propanol at 0.3 MPa were determined.The experimental data were verified with the point-to-point test of van Ness(1973).All these systems present an azeotropic point at 0.3 MPa that increases in ester composition for longer alcohol chains.The UNIFAC in different versions and ASOG prediction models were applied.     

水-仲丁醇-乙酸仲丁酯三元体系的液液相平衡研究

测定了水-仲丁醇-乙酸仲丁酯三元体系在303.15,323.15,343.15,353.15 K下的液液相平衡数据,并用NRTL模型和UNIQUAC模型对相平衡数据进行关联,应用单纯形法求得相应的模型参数。计算值与实验值比较结果表明:NRTL模型与UNIQUAC模型的计算值与实验数据吻合良好。     

乙烯-1,3,5-三甲苯的气液相平衡与乙烯回收工艺的流程模拟(英文)

The amount of ethylene in refinery off-gas is high with a mass fraction of 20%,but the refinery off-gas is usually used as fuel gas in most refineries.The separation and recovery of ethylene is of remarkable significance for saving energy and reducing carbon dioxide emission.The aim of this paper is to use a novel absorbent mesitylene for the ethylene absorption process and assess its application feasibility through the ethylene + mesitylene vapor-liquid equilibrium data measurement and its binary interaction parameter correlation,as well as the simulation for ethylene separation process.     

苯基二氯化膦一三氯化磷体系汽液平衡的研究

用静态法测定了苯基二氯化膦的饱和蒸汽压曲线，回归得到了它们的Antoine方程参数。用标准的Swietoslawski型沸点计测定了三氯化磷一苯基二氯化膦二元体系的常压沸点数据，从而推算出两端的无限稀释活度系数，采用Wilson活度系数方程回归出其中的Wilson参数，并对该体系的等温气液平衡数据进行了推算。     

烷烃-叔丁醇二元体系的等压汽液平衡

采用改进的Ｒｏｓｅ－Ｗｉｌｌｉａｍｓ釜测定了等压下正戊烷一叔丁醇（１．０１３×１０５、７９９７４Ｐａ）和叔丁醇-正辛烷（１．０１１０５Ｐａ）体系的汽液平衡数据。实验数据通过了热力学一致性检验,采用Ｐ－Ｔ状态方程和Ｗｉｌｓｏｎ方程关联,获得较满意的结果。     

1,2-环氧环己烷和1,2-二氯乙烷二元体系汽液平衡数据的测定与关联(英文)

Vapor-liquid equilibrium data (T, x, y) of binary system 1,2-epoxycyclohexane + 1,2-dichloroethane were determined experimentally by using a modified ROSE-Williams equilibrium vaporization system at 101.33 kPa. The results show that this binary system does not have azeotropic point. The vapor-liquid equilibrium data are in thermodynamic consistency. The binary interaction parameters in the Wilson equation are presented with the correlation of vapor-liquid equilibrium data. The measurements of liquid phase composition and bubble point temperature are well represented by the Wilson equation. Values of vapor molecular fractions and activity coefficients from the Wilson equation are presented. This work provides important engineering data for the separation of 1,2-dichloroethane and 1,2-epoxycyclohexane .     

C_(11)-C_(14)烷烃与月桂酸甲酯体系等压汽液平衡

在5.00 k Pa下,用Rose釜测定了正十一烷-月桂酸甲酯、正十二烷-月桂酸甲酯、正十三烷-月桂酸甲酯和正十四烷-月桂酸甲酯4个二元体系的汽液平衡数据,并对所测数据进行了热力学一致性检验,结果表明所有的实验数据均符合热力学一致性。分别用NRTL、UNIQUAC和Wilson活度系数模型对实验数据进行关联,得到了各个模型的二元交互作用参数,并用这三个模型及得到的参数计算了平衡温度及汽相组成,计算结果与实验数据吻合较好。     

丁酮肟-水-异辛醇物系液液相平衡的研究

在甲基三丁酮肟基硅烷的生产过程中会产生部分含丁酮肟的废水,用萃取方法可回收丁酮肟。为获得萃取工艺所需的基础数据,在常压、60℃温度下,以工业实际废水为物料,进行液液相平衡实验,用拟三元方法处理丁酮肟-水-异辛醇三元体系的液液相平衡数据,获得了三元体系平衡相图。实验数据用非随机两相液体(NRTL)模型进行了关联,得出了该三元体系的NRTL模型参数。将实验数据与关联结果进行比较,结果表明,NRTL模型能对该三元体系进行较准确的关联。     

Measurement and Correlation of Vapor-Liquid Equilibrium for Binary System 1,2-Epoxycyclohexane+1,2-Dichloroethane

Vapor-liquid equilibrium data (T, x, y) of binary system 1,2-epoxycyclohexane+1,2-dichloroethane were determined experimentally by using a modified ROSE-Williams equilibrium vaporization system at 101....     

水-乙醇-1-丁基-3-甲基咪唑乙酸盐三元体系汽液平衡测定及模型

Vapor-liquid equilibrium (VLE) data were measured for ternary system water + ethanol + 1-butyl-3- methylimidazolium acetate ([bmim][OAc]), in a relatively wide range of ionic liquid (IL) mass fractions up to 0.8. Six sets of complete T-x-y data were obtained, in which the mole fraction of ethanol on IL-free basis was fixed separately at 0.1, 0.2, 0.4, 0.6, 0.8, and approximate 0.98. The non-random-two-liquid (NRTL) and electrolyte non-random-two-liquid (eNRTL) equations were used for correlation, showing similar deviations. The ternary VLE was also modeled with the correlation from two data sets, with the mole fractions of ethanol on IL-free basis being 0.1 and approximate 0.98. The VLE data were also reproduced satisfactorily. With the eNRTL model, the root-mean-square deviation for temperature is 0.79 K and that for vapor-phase mole fraction is 0.0094. The calculations are in good agreement with experimental data. The effect of the IL on the VLE behavior of the volatile components is also illustrated.     

乙酸异戊酯+异戊醇和乙酸异戊酯+正己醇体系汽液平衡

在50.00和101.33 kPa下,采用改进的Rose汽液平衡釜测量乙酸异戊酯+异戊醇和乙酸异戊酯+正己醇体系的汽液平衡数据。乙酸异戊酯+异戊醇在50.00 kPa下形成最低共沸物。使用Herington法对汽液平衡数据进行热力学一次性检验,结果表明测得的汽液平衡数据符合热力学一致性。对实验数据使用NRTL、Wilson和UNIQUAC活度系数模型进行关联,回归获得相应的二元交互参数,模型计算的温度和组成与实验值相比均方差小于0.20 K和0.0050,表明3种模型的拟合结果与实验数据吻合较好。通过Wilson模型预测乙酸异戊酯+异戊醇体系在98.4 kPa时共沸点消失。为化工数据库增添了内容,为乙酸异戊酯体系的工程设计和进一步深入研究奠定了基础。     

101.3 kPa 下环氧环己烷-环己酮气液平衡的测定及关联简

Many by-products are generated in the process of oxidizing cyclohexene to produce 1,2-epoxycyclohexane by hydrogen peroxide, including cyclohexanol, cyclohexanone, etc. To obtain high-purity 1,2-epoxycyclohexane, the by-products must be removed through rectification. Refining 1,2-epoxycyclohexane through rectification requires vapor-liquid equilibrium （VLE） data of the related system. Therefore, the VLE data of 1,2-epoxycyclohexane- cyclohexanone system were measured at 101.3 kPa using an improved EC-2 VLE still. The thermodynamic consistency of the data was then tested by Herington＇s method and the rigorous point-to-point method. The results obtained were exemplary. The VLE data were correlated by the Wilson and non-random two-liquid （NRTL） equations, using the error sum squares of the vapor composition as the objective function to obtain the model parameters. The difference between the calculated values and the experimental data is minor, indicating that the VLE data are suitable for engineering design.     

常压下环己烯-环氧环己烷-环己酮三元系汽液平衡的测定、预测及关联

H2O2氧化环己烯制备环氧环己烷时会产生环己酮等副产物,同时还有未反应完的环己烯。为了获得较纯的环氧环己烷需采用精馏将副产物和环己烯分离出来,精馏提纯需要相关体系的汽液平衡数据,因此采用改进的EC-2汽液平衡釜测定常压(101.33k Pa)下环己烯-环氧环己烷-环己酮三元体系汽液平衡数据。利用二元系汽液平衡数据拟合得到的Wilson方程配偶参数预测该三元体系的汽液平衡数据,并以汽相组成的误差平方和作为目标函数,用Wilson方程关联实验数据,结果表明预测值及关联值与实验值偏差较小,可满足工程上分离设计的需要。     

Instability of Thallium-Containing Superconductor Phases in Isothermal Equilibrium with Thallium Oxide

Knowledge of the equilibrium conditions under which the superconducting phases in the Tl-Ca-Ba-Cu-O system are stable would enable the controlled preparation of these materials. Isothermal equilibrium between samples in this quaternary system and Tl₂O vapor from a condensed thallium oxide source has been studied. None of the superconductor phases coexisted in equilibrium with thallium oxide under the conditions employed. Instead, two previously unknown ternary thallium-calcium-barium oxides and one previously unknown thallium-calcium oxide were observed. The equilibrium phase assemblage at temperatures between 825° and 925°C consisted of the most thallium-rich ternary oxide plus CuO, although small amounts of the other thallium-rich phases may be required to balance stoichiometry. The vapor pressure of Tl₂O established by pure, condensed thallium oxide clearly exceeds the stability limit for the superconductor phases. If the thallium-containing superconductors are stable phases at high temperature, they will exist over some range of lower Tl₂O partial pressure.     

3-羟基丁酸乙酯-巴豆酸乙酯-乙醇三元体系等压汽液平衡

在汽液双循环玻璃平衡釜中测定3-羟基丁酸乙酯、巴豆酸乙酯、乙醇的二元及三元体系的等压汽液平衡数据,用积分法对其进行了热力学一致性检验.回归实验数据得到3-羟基丁酸乙酯和巴豆酸乙酯的Antoine方程参数.用Wilson活度系数方程对实验数据进行了关联,取得了较好的结果.     

常减压下乙酸乙酯-吡啶体系的汽液平衡测定

用循环式玻璃釜测定了101.33kPa,66.66kPa和40．00kPa下的乙酸乙酯－吡啶体系的汽液平衡，用Herington面积检测法则检验结果表明，实验数据满足热力学一致性.分别用Wilson和NRTL活度系数模型并联了实验数据，两者结果较为接近，汽相组成和泡点温度的最大误差分别为0．0075和0．29℃。     

Vapor-Liquid Equilibrium of Copolymer＋ Solvent Systems： Experimental Data and Thermodynamic Modeling with New UNIFAC Groups

Vapor-liquid equilibrium （VLE） data for copolymer solutions are necessary for several chemical processes. However, VLE data for copolymer solutions in the published report are rare. In this study, experimental VLE data for binary systems copolymer＋solvent were obtained using a gravimetric-sorption apparatus. The studied systems were hexane＋poly （21% acrylonitrile-co-butadiene）, hexane＋poly （33% acrylonitrile-co-butadiene）, hexane＋poly （51% acrylonitrile-co-butadiene）, hexane＋poly （23% styrene-co-butadiene）, hexane＋poly （45% styrene-co-butadiene）, and benzene＋poly （44% styrene-co-methyl methacrylate） in the range 50-70℃. The experimental data were correlated with the UNIFAC and Elbro-FV group contribution models for the activity coefficient. Two sets of functional groups had been used to represent the monomers in copolymers： literature groups and new proposed groups. The mean deviations between experimental and calculated mass fractions about 2.4% with Elbro- FV and 13.3% with Zhong were observed when the groups proposed in this study were used, and of 3.5% for E1- bro-FV and 13.2% for Zhong, when literature grouns were used.     

羟乙基乙二胺-乙二胺体系的汽液平衡

引　言羟乙基乙二胺 (Ｈ2 ＮＣＨ2 ＣＨ2 ＮＨＣＨ2 ＣＨ2 ＯＨ ,简称ＡＥＥＡ)是有机碱类化合物 ,分子中同时含有活泼的氨基和羟基 ,属氨基醇的一个品种 ,是香波、润滑油、树脂等重要原料 ,特别在表面活性剂合成方面的应用越来越广 .它是由过量的乙二胺(Ｈ2 ＮＣＨ2 ＣＨ2 ＮＨ2 ,简称ＥＤＡ)和环氧乙烷 (ＥＯ)合成的 ,产品混合物中必须将ＥＤＡ和ＡＥＥＡ彻底分离 .计算、设计ＡＥＥＡ精馏分离过程的有关热力学数据尤为重要 .本文将着重对ＡＥＥＡ的蒸气压及ＡＥＥＡ与ＥＤＡ的相平衡数据 ,用改进的静态平衡釜进行测定、关联 .而相应的这…     

醋酸脱水过程中对二甲苯+(醋酸,醋酸甲酯,醋酸正丙酯)和醋酸甲酯+醋酸正丙酯的二元汽液相平衡(英文)

The vapor-liquid equilibrium data of four binary systems (acetic acid +p-xylene, methyl acetate +n-propyl acetate, n-propyl acetate +p-xylene and methyl acetate +p-xylene) are measured at 101.33 kPa with Ellis equilibrium still, and then both the NRTL and UNIQUAC models are used in combination with the HOC model for correlating and estimating the vapor-liquid equilibrium of these four binary systems. The estimated binary VLE results using correlated parameters agree well with the measured data except the methyl acetate +p-xylene system which easily causes bumping and liquid rushing out of the sampling tap due to their dramatically different boiling points. The correlation results by NRTL and UNIQUAC models have little difference on the average absolute deviations of temperature and composition of vapor phase, and the results by NRTL model are slightly better than those by UNIQUAC model except for the methyl acetate +n-propyl acetate system, for which the latter gives more accurate correlations.     

CO2-H2O-HAc三组分系统高压相平衡

超临界状态下的CO2在含有有机溶剂的水溶液中可作为萃取剂。这种情况可用于水和有机酸的分离，也可以用于从水溶液中萃取产品。要设计这样的过程，CO2-H2O-有机酸系统相平衡的数据是必不可少的。为此，在实验室建立了一套高压相平衡装置。为了验证这套装置的可靠性，测定了CO2-H2O-HAc体系在313K以及压力在15、20、25和30MPa下的相平衡数据，用Peng-Robinson方程^[1,2]进行了计算，并与文献值进行了比较。