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液液平衡
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  liquid liquid equilibrium
    In addition,the new activity coefficient model is also applicable to liquid liquid equilibrium(LLE) system,the test results on the LLE calculation for hydrocarbon water systems indicate that better results were obtained as compared with NRTL model.
    其于Newton-Raphson-Gauss液-液平衡算法,应用新模型对烃-水体系的液-液平衡进行了关联计算,结果优于NRTL方程
短句来源
    The liquid liquid equilibrium phase diagram of the components in the organic phase for the system of TRPO n octane with nitric acid aqueous solution was given.
    给出了TRPO-正辛烷萃取硝酸过程中有机相各组分的液-液平衡相图。
短句来源
  liquid-liquid equilibrium
    The liquid-liquid equilibrium binodal curves and the tie-line data of an epoxy cotton seed oil/acetic acid/water ternary system. respectively at 30℃, 40℃, 50℃, 60℃and 40℃, 50℃, 60℃ have been measured and graphically recorded in this work.
    测定了环氧棉籽油-醋酸-水三元系分别在30℃,40℃,50℃,60℃下的液-液平衡双结点曲线,以及在40℃,50℃,60℃下的液-液平衡系线数据;
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  “液-液平衡”译为未确定词的双语例句
    Correlation of liquid liquid phase equilibrium for hydrocarbon water systems based on MPHC activity coefficient model
    基于MPHC活度系数模型关联烃-水体系液-液平衡
短句来源
    LLE data of four series of experiments composed of different molecular weight of PEG(1000, 2000, 4000 and 6000) with PH = 9. 43 and three series of experiments composed of different PH values (6,7 and 8)with PEG (4000) at 25 ℃ were determined.
    实验共测定了pH=9.43及聚乙二醇数均分子量分别为1000,2000,4000和6000四种共41组在25℃下的液-液平衡数据; 测定了聚乙二醇数均分子量为4000和pH值分别为6、7、8时共32组在25℃下的液液平衡数据;
短句来源
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  liquid-liquid equilibrium
The position of the critical curve for the liquid-liquid equilibrium, including that of the critical points on the chemical equilibrium surface, is discussed.
      
Calculation of Multiphase Liquid-Liquid Equilibrium and Automated Synthesis of the Structures of Phase Diagrams
      
A new method is suggested for calculating liquid-liquid equilibrium.
      
A way of optimizing liquid-liquid equilibrium calculations in process design is suggested.
      
Incorporation of a simple method for estimating initial K-values in the present algorithm allows this algorithm to more easily and accurately calculate the composition of each phase in vapor-liquid-liquid equilibrium.
      
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Liquiid-Liquid equilibrium data were determined for the two ternarysystems of MTBE-methanol-water and MTBE-tert-butanol-water at 20℃.Vapor-liquid equilibrium data for their constituent binaries were alsodetermined under atmospheric pressure.The starting values of the parameters were taken from the correspon-ding binary liquid-liquid solubilities and vapor-liquid equilibria.Experimental LLE data of the two ternary systems were comparedwith the results predicted from the data of the constituent binaries byapplying...

Liquiid-Liquid equilibrium data were determined for the two ternarysystems of MTBE-methanol-water and MTBE-tert-butanol-water at 20℃.Vapor-liquid equilibrium data for their constituent binaries were alsodetermined under atmospheric pressure.The starting values of the parameters were taken from the correspon-ding binary liquid-liquid solubilities and vapor-liquid equilibria.Experimental LLE data of the two ternary systems were comparedwith the results predicted from the data of the constituent binaries byapplying the NRTL and UNIQUAC equation.Results are proved to befairly satisfactory for the process design purpose.

测定了在20℃下甲基叔丁基醚-甲醇-水及甲基叔丁基醚-叔丁醇-水两组三元体系的液液平衡数据和在常压下各三元体系中二元配偶物系的汽液平衡数据。并将所测定的两组三元液液平衡数据与二元系数据用NRTL 及UNIQUAC 方程所得的参数推算的结果进行了比较,获得较满意的结果。

Vapor-liquid equilibrium for the ternary system Water4-methyl-2-Pentanone 4-Methyl-2-Pentanol was determined at 760mmHg with a modified circulation still. The experimental data were in good agreement with those estimated from the three binary systems using NRTL parameters

用改进的双循环平衡釜测定了水、4-甲基-2-戊酮、4-甲基-2戊醇三元体系常压下的汽液平衡,将实测值与由二元体系以NRTL模型推算的三元体系汽液平衡计算值进行了比较,结果比较吻合.提出了一种改进的平衡釜用以测定常压、沸点下该体系的液液平衡.

The Liquid-liquid equilibrium (LLE data have been determined for the epoxy propane-water-1, 2-dichloropropane ternary system at 40.0 and 50. 0℃. The solubility data also have been determined for the two partially miscible binary systems-epoxy propane-water and water-1, 2-dichloropropane at 35, 40, 50℃ and 40, 50, 60, 80℃ respectively. In addition, the vapor liquid equilibrium data for epoxy propane-1, 2-dichloropropane system were determined at 760mmHg pressure. The correlation and prediction of the LLE data...

The Liquid-liquid equilibrium (LLE data have been determined for the epoxy propane-water-1, 2-dichloropropane ternary system at 40.0 and 50. 0℃. The solubility data also have been determined for the two partially miscible binary systems-epoxy propane-water and water-1, 2-dichloropropane at 35, 40, 50℃ and 40, 50, 60, 80℃ respectively. In addition, the vapor liquid equilibrium data for epoxy propane-1, 2-dichloropropane system were determined at 760mmHg pressure. The correlation and prediction of the LLE data have been made succes ully by using NRTL equation.

测定了环氧丙烷—水—1,2二氯丙烷三元系在40℃和50℃的三元液液平衡数据;测定了两个部分互溶二元系环氧丙烷—水,水—1,2二氯丙烷分别在35℃,40℃,50℃和40℃,50℃,60℃,80℃的相互溶解度数据及完全互溶二元系环氧丙烷—1,2二氯丙烷在760毫米汞柱压力下的汽液平衡数据。应用NRTL方程对平衡数据进行了成功的关联和预测。

 
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