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Integrated CASE Assessment

This repository contains inputs for integrated PM-CAES assessment using a set of future energy system scenarios with different fractions of renewable energy supply developed by oemof, as well as different technical options for the power plant topology built via TESPy and subsurface storage configurations modelled in ECLIPSE simulator.

power plant setups

Energy system dispatch model

Optimised dispatch model based on several assumptions, where three shadow electricity pricies (scenario developed within ANGUS project), CO2 emission and fuel prices are inputs for Gurobi.

Scenario year Power plant type Renewable share [%] Average shadow electricity price [EUR/MWh] CO2 emission price [EUR/t] Fuel price [EUR/MWh] Scenario reference
2030 D-CAES 76.3 52.6 29.4 26.40 2030NEPC
2040 D-CAES 85.9 83.7 126.0 30.24 2040GCA
2050 D-CAES 100.0 88.3 150.0 43.72 2050NB
2030 2-AA-CAES 76.3 52.6 - - 2030NEPC
2030 3-AA-CAES 76.3 52.6 - - 2030NEPC
power plant setups

Surface power plant topology

  • diabatic topology with 3-stage compression and 2-stage expansion stages including a heat recuperator to preheat the air from the storage
  • adiabatic plant with 2-stage compression and expansion stages
  • adiabatic plant with 3-stage compression and expansion stages
power plant setups

Coupled power plant-geostorage parameters. The reference temperature and pressure are 273.15 K and 1.013 bar.

Component Parameter Value
Compressors nominal power 230 MW
isentropic efficiency, ηs,cmp 0.92
isentropic efficiency control stage, ηs,cmp,cs 0.85
pressure ratio stages 1 and 2 (diabatic, three-stage adiabatic) 5
pressure ratio at stage 1 (two-stage adiabatic) 10
Turbines nominal power 115 MW
isentropic efficiency, ηs,exp 0.90
isentropic efficiency control stage, ηs,exp,cs 0.85
Coolers temperature after cooling (diabatic) 298.15 K
temperature after cooling (adiabatic) 338.15 K
Generator & Motor efficiency, η(el,mech) 0.97
Combustion fuel type (diabatic) CH4
turbine inlet temperature 1473.15 K
outlet temperature (diabatic) 423.15 K
pressure loss 3 %
Heat exchangers temperature after reheating (adiabatic) 573.15 K
pressure loss 2 %
Storage nominal pressure compression 115 bar
nominal pressure expansion 110 bar
vertical well length, L 1055 m
vertical well number 9 / 3
pipe roughness, ks 0.04 mm
well diameter, D 0.25 m
horizontal well number 2 / 2
horizontal section length, Lh 450 m / 850 m
total completion length, 150 m / 150 m

Plant performance

power plant capacity durining continuous chargining and discharging tests

Power plant performance during continuous charging (top row: a, b, c) and discharging (bottom row: d, e, f) runs

Subsurface storage settings

Main geostorage parameters for scenario simulation.

Parameter Value
Dry air composition N2/O2/Ar/CO2 (0.7553/0.2314/0.0129/0.0004)
Molar mass of air 28.965 g/mol
Critical temperature 132.53 K
Critical pressure 37.86 bar
Air density at standard condition 1.205 kg/m3
Initial pressure gradient 0.105 bar/m
Reservoir temperature (isothermal) 311 K
Permeability 700 mD
Porosity 0.27
Residual water saturation 0.15
Residual gas saturation 0
Max. relative gas permeability 0.9
Max. relative water permeability 1
Capillary entry pressure 0.1 bar
Pore size distribution index 2
Initial air in place mass 5.56 Mt
Maximum/minimum allowable BHP 130 bar / 80 bar
Geostorage configuration schemes

Geostorage configuration schemes for different well setups

Reference

  • Gasanzade, F., Witte, F., Tuschy, I. and Bauer, S., 2023. Integration of geological compressed air energy storage into future energy supply systems dominated by renewable power sources. Energy Conversion and Management, 277, doi:10.1016/j.enconman.2022.116643
  • TESPy Version 0.4.2 - User's Universe, doi:10.5281/zenodo.4534878
  • National scale energy system scenarios, doi:10.5281/zenodo.3714708
  • ECLIPSE Reservoir Simulation Software v2017.2, Schlumberger Ltd.
  • LLC Gurobi Optimization. Gurobi Optimizer Reference Manual, 2021.

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CAES integration into future energy systems

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