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Title: Vapor-liquid equilibria in the nitrogen + carbon dioxide + propane system from 240 to 330 K at pressures to 15 MPa

Abstract

The design and development of separation processes in the natural gas industry requires accurate knowledge of the vapor-liquid equilibria of multicomponent systems consisting of the alkane hydrocarbons with carbon dioxide and nitrogen. Vapor-liquid equilibria were measured for the nitrogen, carbon dioxide, and propane ternary system and its constituent binaries over the temperature range 240 K to 330 K. The binary systems were measured at 240, 270, and 330 K, and the ternary system was studied at 240 K for 2.0 and 13.0 MPa, 270 K for 2.0, 6,0, and 13.0 MPa, and 330 K and 5 MPa. The Peng-Robinson equation of state was used to model the system.

Authors:
;  [1]
  1. Colorado School of Mines, Golden, CO (United States). Dept. of Chemical Engineering and Petroleum-Refining
Publication Date:
OSTI Identifier:
697120
Resource Type:
Journal Article
Journal Name:
Journal of Chemical and Engineering Data
Additional Journal Information:
Journal Volume: 44; Journal Issue: 5; Other Information: PBD: Sep-Oct 1999
Country of Publication:
United States
Language:
English
Subject:
03 NATURAL GAS; NATURAL GAS; NITROGEN; CARBON DIOXIDE; PROPANE; EQUILIBRIUM; PHASE STUDIES; SEPARATION PROCESSES; EQUATIONS OF STATE

Citation Formats

Yucelen, B., and Kidnay, A.J. Vapor-liquid equilibria in the nitrogen + carbon dioxide + propane system from 240 to 330 K at pressures to 15 MPa. United States: N. p., 1999. Web. doi:10.1021/je980321e.
Yucelen, B., & Kidnay, A.J. Vapor-liquid equilibria in the nitrogen + carbon dioxide + propane system from 240 to 330 K at pressures to 15 MPa. United States. doi:10.1021/je980321e.
Yucelen, B., and Kidnay, A.J. Wed . "Vapor-liquid equilibria in the nitrogen + carbon dioxide + propane system from 240 to 330 K at pressures to 15 MPa". United States. doi:10.1021/je980321e.
@article{osti_697120,
title = {Vapor-liquid equilibria in the nitrogen + carbon dioxide + propane system from 240 to 330 K at pressures to 15 MPa},
author = {Yucelen, B. and Kidnay, A.J.},
abstractNote = {The design and development of separation processes in the natural gas industry requires accurate knowledge of the vapor-liquid equilibria of multicomponent systems consisting of the alkane hydrocarbons with carbon dioxide and nitrogen. Vapor-liquid equilibria were measured for the nitrogen, carbon dioxide, and propane ternary system and its constituent binaries over the temperature range 240 K to 330 K. The binary systems were measured at 240, 270, and 330 K, and the ternary system was studied at 240 K for 2.0 and 13.0 MPa, 270 K for 2.0, 6,0, and 13.0 MPa, and 330 K and 5 MPa. The Peng-Robinson equation of state was used to model the system.},
doi = {10.1021/je980321e},
journal = {Journal of Chemical and Engineering Data},
number = 5,
volume = 44,
place = {United States},
year = {1999},
month = {9}
}