TY  - JOUR
Y1  - 2017///
A1  - Isa, F.
A1  - Zabiri, H.
A1  - Ramasamy, M.
A1  - Tufa, L.D.
A1  - Shariff, A.M.
A1  - Saleh, S.F.
ID  - scholars9411
SN  - 17505836
TI  - Pressure modification index based on hydrodynamics and mass transfer effects for modeling of CO2 removal from natural gas via absorption at high pressures
SP  - 173
N1  - cited By 6
PB  - Elsevier Ltd
UR  - https://www.scopus.com/inward/record.uri?eid=2-s2.0-84999788864&doi=10.1016%2fj.ijggc.2016.11.024&partnerID=40&md5=26d4f94043bd4e525910fd674089c769
EP  - 186
KW  - Carbon dioxide; Ethanolamines; Gas absorption; Heat transfer; Natural gas; Natural gasoline plants; Pilot plants; Reaction kinetics
KW  -  CO2 absorption; Comparative studies; Effective interfacial areas; High pressure; Mass transfer effects; Mass transfer rate; Non-equilibrium modeling; Nonequilibrium model
KW  -  Mass transfer
KW  -  absorption; carbon dioxide; error analysis; experimental study; high pressure; hydrodynamics; mass transfer; model validation; natural gas
JF  - International Journal of Greenhouse Gas Control
VL  - 56
N2  - In this paper, experimental works involving high concentration CO2 removal at elevated pressures are conducted using a high pressure CO2 pilot plant and the result is used to validate a simulation model based on established models in the literature. A rate based non-equilibrium model using 20 wt aqueous monoethanolamine (MEA) is developed based on the work of Pandya (1983). The model considers reaction kinetics, mass transfer rate and heat transfer. Since the condition of CO2 removal at atmospheric and high pressure are different, a pressure modification index is proposed and incorporated in the mass transfer flux equation to account for the non-idealities. Comparative study involving the modified model with index-f, original rate-based non-equilibrium model, Aspen Plus equilibrium and non-equilibrium models has also been carried out for the CO2 loading at the top column exit of 1.505 m. It is found that the introduction of the proposed pressure modification index together with proper selection of mass transfer and effective interfacial area correlations results in an improvement in the average error from more than 100 to as low as 18 between the estimated and the pilot plant data. © 2016 Elsevier Ltd
AV  - none
ER  -