equilibrium data

In the paper , the liquid-liquid equilibrium data of isopropanol-water-benzene-K _ 2 CO _ 3 system has been measured at 30 ℃.

测定了异丙醇 - 苯 - 水 - 碳酸钾体系在30℃时的液液相平衡数据.

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The liquid holdup of ebulliometer used in this research was determined to be 1.56 ml. The vapor-liquid equilibrium data of methanol-ethanol system are measured by the ebulliometer to confirm the reliability of the apparatus used.

本文测定了沸点仪的持液量，其值为1.56cm~3，应用沸点仪测定了甲醇-乙醇二元系的相平衡数据，与文献数据一致，证明了此测定方法的可靠性。

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Vapour-liquid equilibrium data of n-butanol& ethybenzene system at the pressures of 400 and 600 mm Hg by using Rose-williams apparatus are determined.

使用Rose Williams装置：测定正丁醇乙苯体系在400和600mm Hg压力下的汽液平衡数据。

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determination and correlation of liquid-liquid equilibrium data for the methyl acetate-methanol-water ternary system

醋酸甲酯-甲醇-水三元物系液液平衡数据的测定与关联

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An Investigation on Measuring Vapor-Liquid Equilibrium Data by Ebulliometer

用沸点仪测定汽液相平衡数据的研究

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Vapor-liquid phase equilibrium data is important for establishing separation parameters of liquid compound in chemical industry.

汽液相平衡数据对于化工生产中液体混合物分离工艺参数的确定有着十分重要的意义.

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vapor-liquid equilibrium data of ethyl acetate-isopropyl ether and ethyl acetate-tetrahydrofuran systems at atmospheric pressure

乙酸乙酯-异丙醚和乙酸乙酯-四氢呋喃物系常压汽液平衡数据的测定

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The thermodynamic curves showed that adsorption equilibrium data of IIP-PAA/ SiO2 was fitted by the Langmuir isotherm model. The thermodynamic parameters enthalpy of IIP-PAA/ SiO2 was negative, free energy of adsorption Gibbs was negative.

热力学曲线表明IIP-PAA/SiO2对Cu2+的吸附平衡符合Langmuir吸附等温方程，IIP-PAA/SiO2的热力学参数焓变为负，吸附的吉布斯自由能△G0为负值。

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Green Synthesis of Dipropyl Carbonate and Determination of Vapor-liquid Equilibrium Data of Dipropyl Carbonate and Dimethyl Carbonate

碳酸二丙酯的绿色合成及其与DMC相平衡数据测定

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the adsorption equilibrium data of ethylene and ethane could be properly fitted by the models considering respectively physical adsorption and chemisorption. it had good consistency between model calculated value and experimental result.

选用分别考虑物理吸附和化学吸附的模型可以较好的对单组分平衡数据进行关联，模型计算值与实验值具有较好的一致性。

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Constant temperature method for measurement of vapour-liquid equilibrium data of binary system

恒温法测定二元体系气液平衡数据

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The vapor-liquid phase equilibrium data for the binary system of m-xylene-water at 0. 1013 MPa were determined by using an improved pant equilibrium cell. Thermodynamic consistency test indicates that the experimental data are reliable.

采用改进的Partt釜测定了在0.1013MPa下，间二甲苯－水二元部分互溶体系的气液相平衡数据，经热力学一致性检验表明，测定数据是可靠的。

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measurement and correlation of vapor-liquid equilibrium data for dichlorobenzene and diphenylamine system

二氯苯与二苯胺体系汽液平衡数据测定及关联氟代四苯基联苯二胺衍生物的合成与性质

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Vapor-Liquid Equilibrium Data for Water-pyridine-Calcium Chloride System

水吡啶氯化钙体系的气液平衡

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the vapor-liquid equilibrium data of high concentration pinane system were determined at atmospheric pressure, varies pressures ranging from 59.34 kpa to 93.93 kpa and in the temperature range of 421.23~ 441.06k by using the modified ellis still and capillary tube gas chromatograph analysis method.

采用改进的Ellis平衡釜和毛细管气相色谱分析方法，测定了常压及在绝对压力59.34~93.93kPa、温度421.23~441.06K条件下高浓度蒎烷体系的汽液平衡数据。

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The principles, advantages and disadvantages of current measuring methods of phase equilibrium data are introduced.

介绍了目前国内外应用汽液相平衡数据测定方法的原理及优缺点.

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determination of gas-liquid equilibrium data of water-triethylene glycol-methyl chloride ternary system

水-三甘醇-一氯甲烷三元体系气液相平衡的测定

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the desorption equilibrium data of moo 3 from the moo 3/ al 2o 3 catalyst was determined under the nitrogen and water vapor atmosphere respectively.

分别测定了在氮，水气氛下MoO3自MoO3／Al2O3催化剂上脱附的平衡数据。

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The dynamic equilibrium data of methyl acetate on Calgon AC could be correlated by Freundlich equation.

由动态吸附数据计算得到的醋酸甲酯的平衡数据,用Freundlich方程进行了关联.

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The isobaric Vapor-liquid equilibrium data of pyridine and dimethylformamide binary system were determined at 760. 0 mm Hg with modified Rose equilibrium still.

本文采用改进式罗斯平衡釜测定了在760.0mm Hg压力下吡啶-二甲基甲酰胺（以下简称DMF）的汽液平衡数据。

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Testing the Vapor Liquid Equilibrium Data of Furfural Thin Liquor Using Improved Rose Cell

用改进Rose釜测取糠醛-水稀溶液的汽液平衡值

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Gas-liquid equilibrium data for binary systems of carbon dioxide-cyclohexanone at 313.

利用气液双循环的高压气液平衡装置,测定了二氧化碳 - 环己烷在313.

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The Liquid Liquid equilibrium data of octane water and octane phosphoric acid water system were measured.

实验测定了不同温度下辛烷水二元体系和辛烷磷酸水三元体系的液液相平衡数据.

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The equilibrium data were well correlated with a three parameter multilayer adsorption isotherm equation.

吸附等温线采用三参数多层吸附方程来拟合，相关性很好。

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The NRTL binary interaction-parameters of the systems are regressed from the vapor-liquid equilibrium data passing through the thermodynamic consistency test.

提出了满足热力学一致性检验的四个二元体系的文献数据，并拟合了NRTL模型的交互作用参数。

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The NPT+ Test Particle method of molecular dynamic simulation was used in the simulation of the vapor-liquid equilibrium data of five alternative refrigerants ( HFC-152a, HFC-143a, HFC-134a, HCFC-142b and HFC-227ea). The simulation results was proved in consistency with the law of thermodynamics.

利用NPT+Test Particle算法对五种制冷剂替代物（HFC-152a，HFC-143a，HFC-134a，HCFC-142b和HFC-227ea）的气液相平衡性质进行了计算，同时验证了计算结果的热力学一致性。

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A recirculating still specially designed for partially miscible systems was used for the determination of isobaric vapor-liquid equilibrium data at 760 mm Hg for the n-butanol-isobutanol-water system.

本文以适用于部分互溶液体的循环式平衡釜，测定760mm Hg柱下的正丁醇-异丁醇-水体系的汽液平衡数据。

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The adsorption equilibrium data of six binary solution systems on KY zeolite at 90 ℃ and 175 ℃ were determined.

测定了碳八芳烃异构体组成的六种二元溶液于90℃和475℃下在KY分子筛上的吸附平衡数据。

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The-liquid equilibrium data for the ternary --- dibromobenzene were determined by differential scanning calorimetry ( DSC ).

采用差示扫描量热法,通过对一系列“拟二元”物系固液平衡数据的测定,得到了 邻二溴苯 、间二溴苯和对二溴苯三元 物 系 的 固液平衡数据.

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Development of Thermodynamic Consistency Test System of Vapor& Liquid Equilibrium Data

汽液相平衡数据热力学一致性检验系统的开发

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