Abstract
In the development of energy efficient solvents for advanced CO2 capture processes, it has often been the case that potentially excellent solvents are overlooked or set aside because of perceived process difficulties or extra costs due to the physical, chemical or thermodynamic properties of the solvent. This chapter considers the process implications of solvent selection with the objective of selecting and designing the process to suit the solvent rather than forcing the solvent into an existing process. The chapter discusses the design, modelling and costing of conventional amine processes insofar as advanced energy efficient solvents still rely on this process. Individual solvent properties, including reaction kinetics, thermodynamics and physical properties are outlined and their impact on design are discussed. Aspects such as degradation products, corrosivity and environmental considerations will impact the selection of process equipment and materials of construction. The impact of these properties of energy efficient solvents on individual unit operations are also discussed in some detail.
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Abbreviations
- FDG:
-
Flue gas desulphurization
- HPLC:
-
High pressure liquid chromatography
- HSS:
-
Heat stable salts
- HTU:
-
Height of a transfer unit
- IC:
-
Ion chromatography
- LP:
-
Low pressure
- MDEA:
-
Methyldiethanolamine
- MEA:
-
Monoethanolamine
- MNPZ:
-
Mono-nitrosopiperazine
- MP:
-
Medium pressure
- PCC:
-
Post-combustion capture
- PZ:
-
Piperazine
- SCR:
-
Selective catalytic reduction
- VLE:
-
Vapour-liquid-equilibrium
- Cp :
-
Heat capacity (constant pressure)
- E:
-
Efficiency; capture efficiency; Energy
- G:
-
Mass flowrate of gas
- H:
-
Height (of packing)
- \(\Delta H_{{CO_{2} }}^{vap}\) :
-
Desorption enthalpy for CO2
- I:
-
Interest
- L:
-
Mass flowrate of liquid
- m:
-
Mass flowrate
- MW:
-
Molecular weight
- P:
-
Pressure, Plant capacity
- Q:
-
Heat, Energy
- T:
-
Temperature
- v :
-
Volumetric fraction of a component in a gas
- w:
-
Weight fraction
- α:
-
CO2 loading (moles CO2/moles active solvent component)
- Δ:
-
Difference
- 0:
-
Unloaded solvent
- am:
-
Amine or other active component of the capture solvent
- cap:
-
Capital (cost)
- CO2 :
-
Value for CO2 or its fraction of a stream
- cond:
-
Condenser, Condensate
- cw:
-
Cooling water
- DES:
-
Desorber (stripper)
- FG:
-
Flue Gas
- in:
-
Inlet flow
- L:
-
Lean (stripped) solvent
- out:
-
Outlet flow
- R:
-
Rich (containing captured CO2) solvent
- sens:
-
Sensible heat
- tot:
-
Total
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Wardhaugh, L.T., Cousins, A. (2017). Process Implications of CO2 Capture Solvent Selection. In: Budzianowski, W. (eds) Energy Efficient Solvents for CO2 Capture by Gas-Liquid Absorption. Green Energy and Technology. Springer, Cham. https://doi.org/10.1007/978-3-319-47262-1_3
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