Title: Modeling of a CO2-stripper
1Modeling of a CO2-stripper
Marie Solvik Supervisors Sigurd Skogestad and
Marius Støre Govatsmark
2CO2-stripper
PC
PC
LC
- Objectives
- Produce pure ethane product
- Keep the CO2 content in the sales gas within the
limit.
LT, XLT
FC
F, z, hf
- 75 stages including reboiler and reflux tank
- Bottom product purified ethane
- Distillate Offgas (CO2, ethane and some
methane)
LC
QR
There exist a dynamic model of the system in
D-spice
B, xB
32-component flash tank made in Matlab
- SRK equation of state with binary interaction
parameter found by Kornberg (2007) - 2 components- ethane and CO2
- Compared to simulation done in ProSim
z1 Pbarg TK x1 y1 K
0.99 34.0 288.7 0.9927 0.9873 0.9946
0.90 34.0 283.8 0.9248 0.8752 0.9463
0.80 34.0 279.0 0.8428 0.7572 0.8984
0.60 34.0 271.5 0.6503 0.5497 0.8453
0.40 34.0 267.8 0.4202 0.3798 0.9039
0.20 34.0 268.0 0.1810 0.2190 1.2099
z1 Pbarg TK x1 y1 K
0.99 34.0 288.7 0.9924 0.9868 0.9943
0.90 34.0 283.7 0.9231 0.8727 0.9453
0.80 34.0 278.9 0.8419 0.7561 0.8980
0.60 34.0 271.6 0.6528 0.5520 0.8455
0.40 34.0 267.8 0.4225 0.3812 0.9023
0.20 34.0 268.0 0.1780 0.2166 1.2168
43-component flash tank made in Matlab
- Added an extra component, methane to the model
- Compared with actual process data from the top of
the column and a flash tank model made in D-spice
Real time composition of ethane(red) and CO2
(green) from Aspen process explorer.
5D-spice versus Matlab
yC2 yCO2 Pbarg T?C
Operating point 1 (3h)
Aspen 0.455 0.525 34.7 -3.3
Matlab 0.528 0.458 34.7 -3.3
Malab 0.443 0.527 34.7 -6.0
D-spice 0.455 0.525 34.7 -3.7
Operating point 2 (15h)
Aspen 0.515 0.456 34.5 -2.0
Matlab 0.556 0.420 34.6 -2.7
D-spice 0.515 0.456 34.5 -3.1
6Column model made in Matlab
- SRK function of state
- Builds on the flash tank model
- 75 stages
- Time-consuming
7Conclusion
- The column model needs to be improved before
finding optimal operating points - Flash tank model made in D-spice showed accurate
results when comparing with actual plant data and
with Matlab model.