more complicated the refinery complex, the easier the conversion becomes (Rutz, et al. , 2020), (Bacovsky, et al., 2010). Conversion to a biorefinery will likely follow a phased approach. The first step in the conversion is removing carbon from fired sources, while the reduction of fossil feedstocks and replacement with biofeeds and renewable sources will occur over a longer duration. The biorefinery will combine renewable feed sources and fossil sources to manage and reduce Scope 1, 2 and 3 fossil CO₂ emissions (Ohmes, et al., 2022). The power requirements of the refinery will be satisfied from green sources or highly integrated systems. Electricity will increasingly be generated from low-carbon sources such as wind
turbines, solar panels, and nuclear energy. The co-processed steam from gasification or steam methane reforming (SMR) and/or auto thermal reforming (ATR) operations will supplant the steam from on-demand boilers, thereby reducing fired duty, while hydrogen will replace fossil fuel combustion in higher-temperature furnaces. Reducing precombustion emissions entails removal of carbon from the fuel gas system using reforming (SMR and ATR) or gasification technologies (Eide, et al., 2005). The CO₂ from the reforming processes is captured, and the hydrogen is used for the downstream fired sources to produce only water in the flue gas. Oxygen injection is also possible to increase the CO₂ in the stack, thereby improving CO₂ removal (Sharma, et al., 2021). Pre-combustion
Post - combustion carbon capture
Absorption
Adsorption
Cryogenic
Membranes
Pressure or temperature Swing Design
Physical
Chemical
Gas absorption
Gas separation
Alumina
Zeolite
Activated carbon
Dimethyl ethers
Amines
Chilled ammonia
Caustic
Others
Others
Post - combustion removes the carbon after burn ing FG2 FG3 FG4 FG5
Flue gas or vent
FG1
FG5+n
Total FG
Total ue gas + air
5 Pre - combustion removes the carbon prior to burning 2 3 4
Unit No
5+n
1
Fired heaters
Boilers
Other sources
CO pph
R2
R3
R4
R5
R5+n
R1
Pre - combustion fuel or combustion gas
Oxygen
H production
Cryogenic pure oxygen
Membranes enriched air
SMR with CO capture
Gasication
Figure 2 Pre- and post-combustion carbon removal
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