Abstract
This study enhances the efficiency of the Fischer-Tropsch process through CO2 injection. Syngas production in the reforming units is simulated for three cases; two cases for auto-thermal reforming (ATR) with varying steam flow rates and a case for steam-methane reforming (SMR). Outcomes demonstrate an enhancement in the total refined production and the optimisation of the growth probability (α) in the Anderson–Schulz–Flory (ASF) relationship and H2:CO proportion. Aspen HYSYS simulation outputs indicate that the ATR reformer at a steam flow rate 3223 T/D and a CO2 flow rate 1500 T/D represents an optimal scenario for product enhancement. Furthermore, a techno-economic analysis indicates that the ATR (C3) option is the best performing economically with a net profit per input of natural gas and refined product output generating 542.94 ($/T) and 722.74 ($/T) respectively. The environmental analysis demonstrates lowest carbon emissions with 1.76 and 2.34 kg CO2-e/T.
Original language | English |
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Article number | 106768 |
Journal | Computers and Chemical Engineering |
Volume | 136 |
DOIs | |
Publication status | Published - 8 May 2020 |
Keywords
- Anderson–Schulz–Flory (ASF)
- Auto-Thermal Reformer (ATR)
- CO utilisation
- Gas-to-Liquid (GTL)
- Steam-Methane Reformer (SMR)