Vapor-liquid equilibria in the nitrogen + carbon dioxide + propane system from 240 to 330 K at pressures to 15 MPa
Journal Article
·
· Journal of Chemical and Engineering Data
- Colorado School of Mines, Golden, CO (United States). Dept. of Chemical Engineering and Petroleum-Refining
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.
- OSTI ID:
- 697120
- Journal Information:
- Journal of Chemical and Engineering Data, Vol. 44, Issue 5; Other Information: PBD: Sep-Oct 1999
- Country of Publication:
- United States
- Language:
- English
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