Phase Behavior of the Butane plus Decane Binary System

被引：5

作者：

Shariati, Alireza ^{[2
]}

Florusse, Louw J. ^{[3
]}

Peters, Cor J. ^{[1
,4
]}

机构：

[1] Delft Univ Technol, Dept Proc & Energy, Fac Mech Maritime & Mat Engn, NL-2628 CA Delft, Netherlands

[2] Shiraz Univ, Sch Chem & Petr Engn, Nat Gas Engn Dept, Shiraz 71345, Iran

[3] Delft Univ Technol, Fac Sci Appl, NL-2628 BL Delft, Netherlands

[4] Petr Inst, Dept Chem Engn, Abu Dhabi, U Arab Emirates

来源：

JOURNAL OF CHEMICAL AND ENGINEERING DATA | 2011年 / 56卷 / 04期

关键词：

BUBBLE-POINT PRESSURES; VAPOR-LIQUID-EQUILIBRIUM; CARBON-DIOXIDE; METHANE; NITROGEN;

D O I：

10.1021/je1008735

中图分类号：

O414.1 [热力学];

学科分类号：

摘要：

In this work, a series of bubble-point measurements were carried out on the binary system butane + decane. The experiments were carried out using the Cailletet apparatus, and bubble-point pressures were measured in a temperature range of (323.21 to 482.28) K. The corresponding pressures were predicted using the Peng-Robinson equation of state, and the relative errors were estimated. It is shown that this hydrocarbon mixture can be predicted reasonably well by this equation of state.

引用

页码：920 / 922

页数：3

共 17 条

[1]

Danesh A., 2007, PVT and Phase Behaviour of Petroleum Reservoir Fluids

[2] Measurement of phase equilibria of supercritical ethane and paraffins [J].

du Rand, M ;

Nieuwoudt, I .

JOURNAL OF SUPERCRITICAL FLUIDS, 2001, 21 (03) :181-193

[3] Vapor-Liquid Equilibrium Data for the Nitrogen plus n-Decane System from (344 to 563) K and at Pressures up to 50 MPa [J].

Garcia-Sanchez, Fernando ;

Eliosa-Jimenez, Gaudencio ;

Silva-Oliver, Guadalupe ;

Garcia-Flores, Blanca E. .

JOURNAL OF CHEMICAL AND ENGINEERING DATA, 2009, 54 (05) :1560-1568

[4] PHASE-EQUILIBRIA OF (METHANE + N-HEXADECANE) AND (P, VM, T) OF N-HEXADECANE [J].

GLASER, M ;

PETERS, CJ ;

VANDERKOOI, HJ ;

LICHTENTHALER, RN .

JOURNAL OF CHEMICAL THERMODYNAMICS, 1985, 17 (09) :803-815

[5] A New Two-Constant Equation of State [J].

PENG, D ;

ROBINSON, DB .

INDUSTRIAL & ENGINEERING CHEMISTRY FUNDAMENTALS, 1976, 15 (01) :59-64

[6]

Perry R., 1997, PERRYS CHEM ENG HDB, V7th

[7]

Reamer H.H., 1964, J CHEM ENG DATA, V9, P24

[8] PHASE EQUILIBRIA IN HYDROCARBON SYSTEMS - NORMAL-BUTANE DECANE SYSTEM IN THE CONDENSED REGION [J].

REAMER, HH ;

SAGE, BH ;

LACEY, WN .

INDUSTRIAL AND ENGINEERING CHEMISTRY, 1946, 38 (10) :986-989

[9] Effect of pressurized carbon dioxide on mutual miscibility temperatures for methanol plus hydrocarbon binary liquid mixtures [J].

Saito, Tohru ;

Iwai, Yoshio ;

Arai, Yasuhiko ;

Nakada, Futoshi ;

Taniguchi, Daisuke ;

Ochi, Kenji ;

Furuya, Takeshi .

JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2006, 39 (09) :907-914

[10] Phase equilibrium of propane and alkanes - Part III: Beyond hexacontane [J].

Schwarz, C. E. ;

Nieuwoudt, I. ;

Knoetze, J. H. .

JOURNAL OF SUPERCRITICAL FLUIDS, 2007, 41 (03) :327-334

← 1 2 →