Promoted potassium
carbonate with glycine has been actively investigated
as a chemical solvent for the removal of CO
2
. Though a
vast number of studies have been reported for potassium carbonate,
dynamic studies regarding this promoted solvent are not yet extensively
reported in the literature. In this work, a steady-state simulation
has been performed via an equilibrium stage model in Aspen Plus V10
using the experimental data of an absorber from the bench scale pilot
plant (MINI CHAS) located in Universiti Teknologi PETRONAS. In this
study, 15 wt % K
2
CO
3
+ 3 wt % glycine is utilized
as the medium for absorption, and the operating pressure is set at
40 bar to imitate the natural gas treatment process. The removal observed
from the pilot plant is about 75% and the steady-state simulation
with a tuned vaporization efficiency managed to replicate a similar
result. The transient analysis is performed via activating a flow-driven
method, and the simulation is transferred into Aspen Dynamic. A simple
control strategy using a proportional–integral (PI) controller
is installed at the gas outlet to monitor the CO
2
composition,
and further disturbances are introduced at the inlet gas flow rate
using a step test and ramp test. The controller is tuned using a trial-and-error
method and a satisfactory response is achieved under varying changes
in the inlet gas flow rate. Further investigation is carried out using
the model predictive controller (MPC), in which 5000 data points are
generated through pseudorandom binary sequence (PRBS) analysis for
state-space model system identification. The state-space model identified
as the best is then used to design the MPC controller. A disturbance
rejection test on the MPC controller is conducted via changing the
gas flow rate at 5% and a quick response is observed. In conclusion,
both MPC and PI controllers managed to produce a good response once
the disturbance was introduced within the CO
2
–potassium
carbonate–glycine (PCGLY) system.