Abstract
Carbon capture and storage (CCS) is one of the dominant technologies to tackle the global warming issue. The transport of CO2 for geological storage is economically feasible by ship when the storage site location is off-shore and instalment of an off-shore pipeline requires a huge capital cost. Ship transportation requires the captured CO2 to be in liquid phase under pressurized thermodynamic conditions. The injection of liquid CO2 into the geological reservoir involves pressurization and heating in order to maintain the safe well head operating conditions. This study presents two alternative top side injection process designs that can reduce the power requirement compared to the base case design. The base case design and alternative designs are simulated using Aspen HYSYS® in order to decide the process design variables. The study employed two-stage rankine cycle in order to extract the cold energy available from the liquid CO2 before its injection into the reservoir. The alternative designs also proposed to utilize a vapor return line in order to maintain the vessel pressure within safe limits by performing a dynamic simulation. Finally, a sensitivity analysis has been done in order to investigate the effect of some important variables in the study.
| Original language | English |
|---|---|
| Title of host publication | Computer Aided Chemical Engineering |
| Publisher | Elsevier B.V. |
| Pages | 733-738 |
| Number of pages | 6 |
| DOIs | |
| State | Published - Oct 2017 |
Publication series
| Name | Computer Aided Chemical Engineering |
|---|---|
| Volume | 40 |
| ISSN (Print) | 1570-7946 |
Bibliographical note
Publisher Copyright:© 2017 Elsevier B.V.
Keywords
- CO injection
- Economic analysis
- Top side process
ASJC Scopus subject areas
- General Chemical Engineering
- Computer Science Applications