Measurement and modelling of the vapor-liquid equilibrium of (CO2 + CO) at temperatures between (218.15 and 302.93) K at pressures up to 15 MPa

Autor: Saif Z.S. Al Ghafri, J. P. Martin Trusler, Lorena F.S. Souza
Jazyk: angličtina
Rok vydání: 2018
Předmět:
Vapor pressure
0306 Physical Chemistry (Incl. Structural)
Thermodynamics
CO2 TRANSPORT
02 engineering and technology
CARBON-DIOXIDE SYSTEM
010501 environmental sciences
Flory–Huggins solution theory
GASES
Mole fraction
0915 Interdisciplinary Engineering
01 natural sciences
REGION
chemistry.chemical_compound
020401 chemical engineering
PHASE-EQUILIBRIA
Critical point (thermodynamics)
TEMPERATURES
Carbon capture
transport and storage

General Materials Science
0204 chemical engineering
Physical and Theoretical Chemistry
Carbon monoxide
0105 earth and related environmental sciences
Science & Technology
Chemistry
Chemistry
Physical

Vapor-liquid equilibrium
PRESSURES
MIXTURES
Chemical Engineering
Thermodynamic model
EQUATION-OF-STATE
Atomic and Molecular Physics
and Optics

Carbon dioxide
Physical Sciences
Vapor–liquid equilibrium
Phase behavior
BEHAVIOR
Popis: Precise knowledge of vapor–liquid equilibrium (VLE) data of (CO2 + diluent) mixtures is crucial in the design and operation of carbon capture, transportation and storage processes. VLE measurements of the (CO2 + CO) system are reported along seven isotherms at temperatures ranging from just above the triple-point temperature of CO2 to 302.93 K and at pressures from the vapor pressure of pure CO2 to approximately 15 MPa, including near-critical mixture states for all isotherms. The measurements are associated with estimated standard uncertainties of 0.006 K for temperature, 0.009 MPa for pressure and 0.011x(1 − x) for mole fraction x. The new VLE data have been compared with two thermodynamic models: the Peng-Robinson equation of state (PR-EOS) and a multi-fluid Helmholtz-energy equation of state known as EOS-CG. The PR-EOS was used with a single temperature-dependent binary interaction parameter, which was fitted to the experimental data. In contrast, EOS-CG was used in a purely-predictive mode with no parameters fitted to the present results. While PR-EOS generally agrees fairly well with the experimental data, EOS-CG showed significantly better agreement, especially close to the critical point.
Databáze: OpenAIRE