NEW ALGORITHM FOR CALCULATION OF AZEOTROPES FROM EQUATIONS OF STATE

被引:23
作者
WANG, SH [1 ]
WHITING, WB [1 ]
机构
[1] W VIRGINIA UNIV,DEPT CHEM ENGN,MORGANTOWN,WV 26506
来源
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT | 1986年 / 25卷 / 02期
关键词
D O I
10.1021/i200033a035
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
引用
收藏
页码:547 / 551
页数:5
相关论文
共 54 条
[1]   EVALUATION OF PARAMETERS FOR NON-LINEAR THERMODYNAMIC MODELS [J].
ANDERSON, TF ;
ABRAMS, DS ;
GRENS, EA .
AICHE JOURNAL, 1978, 24 (01) :20-29
[2]   COMPUTATIONAL METHODS FOR HIGH-PRESSURE PHASE-EQUILIBRIA AND OTHER FLUID-PHASE PROPERTIES USING A PARTITION-FUNCTION .2. MIXTURES [J].
ANDERSON, TF ;
PRAUSNITZ, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1980, 19 (01) :9-14
[3]   COMPUTATIONAL METHODS FOR HIGH-PRESSURE PHASE-EQUILIBRIA AND OTHER FLUID-PHASE PROPERTIES USING A PARTITION-FUNCTION .1. PURE FLUIDS [J].
ANDERSON, TF ;
PRAUSNITZ, JM .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1980, 19 (01) :1-8
[4]  
ANDERSON TF, 1978, THESIS U CALIFORNIA
[5]   The determination of vapour and liquid compositions in binary systems II Acetone-water at 25(o)c [J].
Beare, WG ;
McVicar, GA ;
Ferguson, JB .
JOURNAL OF PHYSICAL CHEMISTRY, 1930, 34 (06) :1310-1318
[6]   LIQUID-VAPOUR EQUILIBRIA .9. THE SYSTEMS NORMAL-PROPANOL+BENZENE AND NORMAL-BUTANOL+BENZENE AT 45-DEGREES-C [J].
BROWN, I ;
SMITH, F .
AUSTRALIAN JOURNAL OF CHEMISTRY, 1959, 12 (03) :407-412
[7]  
BROWN I, 1955, AUST J CHEM, V8, P501
[8]  
Carr A.D., 1962, J CHEM ENG DATA, V7, P26, DOI [10.1021/je60012a007, DOI 10.1021/JE60012A007]
[9]   EXTRACTION OF ACETIC ACID FROM WATER .3. BINARY VAPOUR-LIQUID EQUILIBRIUM DATA [J].
GARNER, FH ;
ELLIS, SRM ;
PEARCE, CJ .
CHEMICAL ENGINEERING SCIENCE, 1954, 3 (02) :48-54
[10]   VAPOR-LIQUID-EQUILIBRIUM DATA AT ATMOSPHERIC-PRESSURE FOR TERNARY AND SUB-BINARY SYSTEMS CONTAINING N-HEXANE-BENZENE-1-BUTANOL [J].
GOVINDASWAMY, S ;
ANDIAPPAN, AN ;
LAKSHMANAN, SM .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1976, 21 (03) :366-369