CYCLOPENTADIENE DICYCLOPENTADIENE PHASE-EQUILIBRIA AND REACTION-RATE BEHAVIOR USING THE TRANSIENT TOTAL PRESSURE METHOD

被引：6

作者：

HOWAT, CS

SWIFT, GW

机构：

来源：

INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH | 1988年 / 27卷 / 08期

关键词：

D O I：

10.1021/ie00080a022

中图分类号：

TQ [化学工业];

学科分类号：

0817 ;

摘要：

引用

页码：1487 / 1493

页数：7

共 11 条

[1] DETERMINATION OF ACTIVITY COEFFICIENTS FROM TOTAL PRESSURE MEASUREMENTS [J].

BARKER, JA .

AUSTRALIAN JOURNAL OF CHEMISTRY, 1953, 6 (03) :207-210

[2] MODIFIED SOAVE EQUATION OF STATE FOR PHASE-EQUILIBRIUM CALCULATIONS .1. HYDROCARBON SYSTEMS [J].

GRABOSKI, MS ;

DAUBERT, TE .

INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1978, 17 (04) :443-448

[3] NEW CORRELATION FOR SATURATED DENSITIES OF LIQUIDS AND THEIR MIXTURES [J].

HANKINSON, RW ;

THOMSON, GH .

AICHE JOURNAL, 1979, 25 (04) :653-663

[4] VAPOR LIQUID-PHASE EQUILIBRIA FOR THE BINARIES ISOPRENE DICYCLOPENTADIENE AND NORMAL-PENTANE DICYCLOPENTADIENE AT 313-K AND 323-K [J].

HOWAT, CS ;

SWIFT, GW .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 1985, 30 (03) :281-285

[5] A PROCEDURE FOR THE DESIGN OF EXPERIMENTS IN FLUID PHASE-EQUILIBRIA [J].

HOWAT, CS ;

SWIFT, GW .

FLUID PHASE EQUILIBRIA, 1983, 14 (OCT) :289-301

[6]

HOWAT CS, 1983, THESIS U KANSAS

[7]

HULL HS, 1965, AUST J CHEM, V18, P549

[8] ESTIMATING VAPOR PRESSURES-COMPARISON OF EQUATIONS [J].

MILLER, DG .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1964, 56 (03) :46-&

[9] *KINETISCHE UNTERSUCHUNGEN DER DIMERISIERUNG VON CYCLOPENTADIEN [J].

SCHMID, H ;

KUBASSA, F ;

HERDY, R .

MONATSHEFTE FUR CHEMIE, 1948, 79 (05) :430-438

[10] VAPOR-LIQUID-EQUILIBRIA FOR 2-METHYLBUTENE-1 AND 2-METHYL-1,3-BUTADIENE AT 310.93, 316.48 AND 322.03-K [J].

SHANKER, G ;

HOWAT, CS ;

TORRES, RR ;

SWIFT, GW .

FLUID PHASE EQUILIBRIA, 1981, 5 (3-4) :305-321

← 1 2 →