ISOTHERMAL VAPOR-LIQUID EQUILIBRIUM DATA FOR SYSTEMS HEPTANE-1-PROPANOL AT 75 DEGREES C AND DECANE-1-BUTANOL AT 100 DEGREES C

被引:26
作者
LEE, LL
SCHELLER, WA
机构
关键词
D O I
10.1021/je60035a009
中图分类号
O414.1 [热力学];
学科分类号
摘要
引用
收藏
页码:497 / &
相关论文
共 9 条
[1]  
CHU JC, 1956, VAPORLIQUID EQUILIBR
[2]   THEORY AND OPERATION OF A CARTESIAN DIVER TYPE OF MANOSTAT [J].
GILMONT, R .
INDUSTRIAL AND ENGINEERING CHEMISTRY-ANALYTICAL EDITION, 1946, 18 (10) :633-636
[3]   VAPOR-RECIRCULATING EQUILIBRIUM STILL - DATA ON HEPTANE-TOLUENE AND METHANOL-CARBON TETRACHLORIDE [J].
HIPKIN, H ;
MYERS, HS .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1954, 46 (12) :2524-2528
[4]  
LEE LL, 1966, THESIS U NEBRASKA
[5]  
Lipkin M. R., 1944, INDUST AND ENGINEER CHEM ANALYT ED, V16, P55, DOI 10.1021/i560125a020
[6]   ISOTHERMAL VAPOR-LIQUID EQUILIBRIUM DATA FOR SYSTEM N-HEPTANE-N-VALERIC ACID AT 50 DEGREES 75 DEGREES AND 100 DEGREES C [J].
LODL, SJ ;
SCHELLER, WA .
JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1967, 12 (04) :485-&
[7]   ALGEBRAIC REPRESENTATION OF THERMODYNAMIC PROPERTIES AND THE CLASSIFICATION OF SOLUTIONS [J].
REDLICH, O ;
KISTER, AT .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1948, 40 (02) :345-348
[8]   TESTING CONSISTENCY OF VAPOR-LIQUID EQUILIBRIUM DATA [J].
TAO, LC .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1964, 56 (02) :36-&
[9]  
TIMMERMANS J, 1959, PHYSICOCHEMICAL CONS, V2