TY - JOUR
T1 - Effects of Carbon Monoxide and Dimethyl Ether on the Bubble Points of CO2 Streams from 247.15 K to Critical Conditions
AU - Okoro, Franklin
AU - Chapoy, Antonin
AU - Ahmadi, Pezhman
AU - Burgass, Rod
PY - 2025/2/13
Y1 - 2025/2/13
N2 - The quality of CO2 streams in carbon capture, utilization, and storage is critical, as even small amounts of impurities can significantly affect phase behavior and operational integrity. This study investigated how carbon monoxide (CO) and dimethyl ether (DME), at concentrations of 0.5–5%, impact the bubble points of CO2 streams compared to pure CO2 at equal temperatures. Experiments were conducted from 247.15 K to near-critical conditions using constant composition expansion methods. The measurement uncertainties were 0.14 K and 0.03 MPa for the temperatures and pressures, respectively, and the composition uncertainties were 0.0009 and 0.0011 mol/mol for CO2–CO and CO2–DME systems, respectively. Results showed that CO had a greater effect on the bubble points of CO2 than DME, attributed to CO’s lower molecular weight. In contrast, DME caused a negative deviation from pure CO2 vapor pressures due to its heavier molecular weight. Model validations using the Peng–Robinson and Multi-Fluid Helmholtz Energy Approximation equations of state revealed that both provided accurate predictions, with MFHEA outperforming PR, achieving deviations below 2.5%. These findings indicate that noncondensable gases like CO increase the risk of two-phase flow during CO2 transport, particularly at low temperatures, emphasizing the need for careful impurity management in CCUS systems.
AB - The quality of CO2 streams in carbon capture, utilization, and storage is critical, as even small amounts of impurities can significantly affect phase behavior and operational integrity. This study investigated how carbon monoxide (CO) and dimethyl ether (DME), at concentrations of 0.5–5%, impact the bubble points of CO2 streams compared to pure CO2 at equal temperatures. Experiments were conducted from 247.15 K to near-critical conditions using constant composition expansion methods. The measurement uncertainties were 0.14 K and 0.03 MPa for the temperatures and pressures, respectively, and the composition uncertainties were 0.0009 and 0.0011 mol/mol for CO2–CO and CO2–DME systems, respectively. Results showed that CO had a greater effect on the bubble points of CO2 than DME, attributed to CO’s lower molecular weight. In contrast, DME caused a negative deviation from pure CO2 vapor pressures due to its heavier molecular weight. Model validations using the Peng–Robinson and Multi-Fluid Helmholtz Energy Approximation equations of state revealed that both provided accurate predictions, with MFHEA outperforming PR, achieving deviations below 2.5%. These findings indicate that noncondensable gases like CO increase the risk of two-phase flow during CO2 transport, particularly at low temperatures, emphasizing the need for careful impurity management in CCUS systems.
UR - http://www.scopus.com/inward/record.url?scp=85216198553&partnerID=8YFLogxK
U2 - 10.1021/acs.jced.4c00606
DO - 10.1021/acs.jced.4c00606
M3 - Article
SN - 0021-9568
VL - 70
SP - 1004
EP - 1012
JO - Journal of Chemical and Engineering Data
JF - Journal of Chemical and Engineering Data
IS - 2
ER -