四元液液相平衡,quaternary liquid-liquid equilibria
1)quaternary liquid-liquid equilibria四元液液相平衡
2)ternary liquid-liquid equilibria三元液液相平衡
3)three phases gas-liquid equilibrium三元汽液相平衡
4)binary vapor-liquid equilibria二元气液相平衡
5)multicomponent vapour-liquid equilibrium多元汽液相平衡
1.The principle ofmulticomponent vapour-liquid equilibrium was applied in mathematical modelling of extractive distillation for alcohol-water systems with glycol and diethylene glycol.应用多元汽液相平衡原理进行了乙二醇、二甘醇对醇-水萃取精馏影响的数模计算,并予以实验验证。
6)liquid-liquid equilibrium液-液相平衡
1.Theliquid-liquid equilibrium(LLE) data for acrylonitrile-water-KF and acrylonitrile-water-K_2CO_3 systems are measured at 40 ℃,a theoretical calculation of LLE data is calculated from the Pitzer theory and the NRTL equation.测定了丙烯腈-水-氟化钾、丙烯腈-水-碳酸钾体系在40℃时的液-液相平衡数据,用Pitzer理论和NRTL方程对液-液相平衡数据进行了理论计算。
2.In this paper,the data about theliquid-liquid equilibrium(LLE) of sec-butanol-water-KF and sec-butanol-water-K_2CO_3 systems are measured at 25℃,showing that the sec-butanol phase contains negligible salt and the water phase contains negligible sec-butanol when the mass fraction of KF or K_2CO_3 in the water phase is not less than 26.文中通过实验测定了仲丁醇-水-氟化钾、仲丁醇-水-碳酸钾体系在25℃时的液-液相平衡数据,发现当水相中氟化钾或碳酸钾含量分别大于或等于26。
3.Theliquid-liquid equilibrium data for system of acrylonitrile-water-potassium carbonate was determined at 25℃.测定了丙烯腈-水-碳酸钾体系在25℃时的液-液相平衡数据,相平衡结果表明当水相中K_2CO_3浓度为52。
英文短句/例句
1.VLE AND LLE OF n-BUTYL ACRYLATE--n-BUTANOL-WATER SYSTEM丙烯酸正丁酯-正丁醇-水体系汽-液、液-液相平衡研究
2.Construction of Double Circulating Vapor-Liquid Equilibrium Device and Measurement of Vapor-Liquid Equilibrium Data;汽液双循环相平衡装置的建立与汽液相平衡数据测定
3.Liquid and vapor phases cannot coexist in equilibrium.液相和气相不能在平衡中共存。
4.The Calculation of Liquid Activity Coefficient and Vapor Liquid Equilibrium Data from Excess Volume Data从过量体积推算液相活度系数与汽液平衡数据
5.Study on Multicomponent Liquid-Liquid Equilibrium Properties of Dimethyl Carbonate;碳酸二甲酯的多元组分液液相平衡的研究
6.Measurements of Multicomponent Liquid-Liquid Equilibrium for Fuel Additives;含汽油添加剂的多元体系液液相平衡的测定
puter drawing of the phase diagram of completely mutually soluble double-fluid system and it s application;互溶双液系气液平衡相图计算机绘制及其应用
8.Improvement on Experiment of Vapor-liquid Equilibria Diagram in Double Liquids;双液体系气—液平衡相图测定方法的探讨
9.Measurement and Correlation of Liquid-Liquid Equilibrium Data for H_2O-CH_2Cl_2-[Bmim]BF_4 SystemH_2O-CH_2Cl_2-[Bmim]BF_4体系的液液相平衡测定及其关联
10.Liquid-liquid equilibria for quaternary systems with 1,1-dimethylethyl methyl ether含甲基叔丁基醚的四元体系液液相平衡
11.FLASH COMPUTATION OF MULTICOMPONENT SYSTEM ATH COMPLEX REACTION EQUILIBRIA IN THE LIQUID PHASE液相中伴有复杂反应平衡的闪蒸计算
12.Study on the Vapor-Liquid Equilibra of the Multicomponent Systems Containing Halogenated Silane;多元卤代硅烷体系的汽液相平衡研究
13.Dynamic Simulation Study of Gas-Liquid Two-Phase Flow for Underbalanced Drilling欠平衡钻井气液两相流动态模拟研究
14.VAPOR-LIQUID EQUILIBRIUM FOR ALCOHOL+HALOGENATED HYDROCARBON SYSTEMS USING THE CPA EQUATION OF STATECPA方程计算醇+卤代烃体系气液相平衡
15.Study on calculation of phase equilibrium in mixed aqueous electrolyte solutions混合电解质水溶液相平衡计算的研究
16.Solid-liquid equilibrium study of p-xylene crystallization process对二甲苯结晶过程的固液相平衡研究
17.Progress in Phase Equilibria Studies of CO_2/Ionic Liquids MixtureCO_2/离子液体混合物相平衡的研究进展
18.The Water-pyridine Liquid Vapor Equilibrium Phasigram Mensurated with Refractive Index折光指数法测定水-吡啶液平衡相图
相关短句/例句
ternary liquid-liquid equilibria三元液液相平衡
3)three phases gas-liquid equilibrium三元汽液相平衡
4)binary vapor-liquid equilibria二元气液相平衡
5)multicomponent vapour-liquid equilibrium多元汽液相平衡
1.The principle ofmulticomponent vapour-liquid equilibrium was applied in mathematical modelling of extractive distillation for alcohol-water systems with glycol and diethylene glycol.应用多元汽液相平衡原理进行了乙二醇、二甘醇对醇-水萃取精馏影响的数模计算,并予以实验验证。
6)liquid-liquid equilibrium液-液相平衡
1.Theliquid-liquid equilibrium(LLE) data for acrylonitrile-water-KF and acrylonitrile-water-K_2CO_3 systems are measured at 40 ℃,a theoretical calculation of LLE data is calculated from the Pitzer theory and the NRTL equation.测定了丙烯腈-水-氟化钾、丙烯腈-水-碳酸钾体系在40℃时的液-液相平衡数据,用Pitzer理论和NRTL方程对液-液相平衡数据进行了理论计算。
2.In this paper,the data about theliquid-liquid equilibrium(LLE) of sec-butanol-water-KF and sec-butanol-water-K_2CO_3 systems are measured at 25℃,showing that the sec-butanol phase contains negligible salt and the water phase contains negligible sec-butanol when the mass fraction of KF or K_2CO_3 in the water phase is not less than 26.文中通过实验测定了仲丁醇-水-氟化钾、仲丁醇-水-碳酸钾体系在25℃时的液-液相平衡数据,发现当水相中氟化钾或碳酸钾含量分别大于或等于26。
3.Theliquid-liquid equilibrium data for system of acrylonitrile-water-potassium carbonate was determined at 25℃.测定了丙烯腈-水-碳酸钾体系在25℃时的液-液相平衡数据,相平衡结果表明当水相中K_2CO_3浓度为52。
延伸阅读
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