High-Temperature Geothermal Utilization in the Context of European Energy Policy—Implications and Limitations
Abstract
:1. Introduction
1.1. Overview of Current EU Energy and Climate Policy
- No less than a 40% reduction of greenhouse gas emissions compared to 1990 levels. The target is twofold, where sectors under the EU emissions trading system (ETS) must cut emissions by 43%, and non-ETS sectors (emissions under each Member State) need to reduce emissions by 30%, both compared to 2005 levels [11].
1.2. Indicators for Energy Technologies Affecting Key EU Energy and ClimateT
1.2.1. Greenhouse Gas Emission Factors
1.2.2. Primary Energy Factors (PEF) for Different Energy Systems
- For directly combustible energy resources (e.g., lignite, natural gas, gasoline, biogas, firewood, and combustible municipal waste), their primary energy form is defined as the heat generated during combustion [3].
- For energy resources that are not directly combustible, the primary energy form is chosen as:
- -
- the heat content of the working fluid (the fluid that delivers the primary energy to the conversion cycle) for nuclear, geothermal, solar thermal, and ambient heat, and;
- -
- the produced electricity output from the energy conversion cycle for solar photovoltaic, wind, hydro, tide, wave and other ocean energy [3].
1.2.3. Adding Life Cycle Perspectives into the PEF
1.2.4. Possible Implications of PEFs for Different Energy Systems on EU Climate and Energy Targets
1.2.5. Response to Criticism on the Definition of Primary Energy Content for Renewable Energy Technologies
1.3. High-Temperature Geothermal Energy in the EU’s Energy Policy
1.3.1. GHG Emissions from High-Temperature Geothermal
1.3.2. Primary Energy Factor for Geothermal
1.3.3. Combined Heat and Power Production from High-Temperature Geothermal Resources in Context with EU’s Energy Policy
2. Materials and Methods
2.1. Case Study: Hellisheidi Geothermal Combined Heat and Power Plant
2.2. Life Cycle Assessment (LCA) of the Hellisheidi GCHP Plant
- To provide a detailed dataset for high-temperature geothermal heat- and power generation technology to be used in other LCA studies as a reference, as these studies are scarce [48].
- To investigate the life cycle environmental impacts of high-temperature geothermal heat and power production [8].
- To examine the contribution of different life cycle stages of high-temperature geothermal heat- and power production to the overall environmental impacts to see if hidden impacts occur in upstream or downstream life cycle stages compared to the operational life cycle stage [8].
- To investigate the effects of operational improvements implemented during the first decade of operation of the Hellisheidi CHP plant on the overall life cycle environmental impacts compared to a base case scenario. This was done by comparing the operation scenario from 2012, where no abatement system for gaseous emissions was present, to the operation scenario from 2017 when abatement methods had been installed for gaseous emissions [8].
2.3. Calculation of Primary Energy Factor for Geothermal Utilization
- (1)
- Calculating the primary energy content with basic thermodynamic equations based on the enthalpy (heat content) of the geothermal fluid extracted from the resource as instructed by the EU climate and energy policy framework. Since the spent geothermal fluid is reinjected back down to the reservoir after utilization within the power plant, the primary energy content of the reinjected fluid is subtracted from the extracted primary energy.
- (2)
- Using historical and forecasted operational input and output parameters of primary energy flow and corresponding production of electricity and heat from the plant to calculate the average PEF for the energy products over a 30-year technical lifetime scenario.
- (3)
- Using life cycle assessment (LCA) to account for primary energy use to extract, supply, and convert the geothermal energy to electricity and heat. LCA considers the whole value-chain within the system boundary of the power plant, as explained above in Section 2.2. The Cumulative Energy Demand (CED) method was used to calculate the final primary energy use of the power plant per produced unit of electricity and heat. The results generated by the CED method allows for a break-down of the primary energy factor into non-renewable and renewable PEFs.
- (4)
- Using different allocation methods to divide the primary energy input between electricity and heat outputs to calculate the separate PEF for each energy product. These are further discussed in Section 2.4.
2.4. Allocation of Environmental Impacts and Primary Energy Use
- (1)
- Construction phase: Steam collection and reinjection system that collects, transports, and disposes of the geothermal fluid used for energy production. The processes included here are the energy and material intensive drilling activities (subsurface), as well as the well completion and the construction of the collection pipeline system for transporting the geothermal fluid above-surface.
- (2)
- Operational phase: Includes the use of geothermal fluid. Here, the fluid’s thermal energy content defines the primary energy form for the energy conversion cycle, and its gas- and mineral content is the cause of various potential environmental effects.
- (3)
- Maintenance phase: Includes drilling and completion of make-up wells for maintaining energy supply during the lifetime of the power plant. These wells sustain a constant flow of primary energy needed to produce electricity and heat, as older wells decline during production.
2.4.1. Method A: Avoidance of Allocation with Electricity as a Primary Product
2.4.2. Method B: Avoidance of Allocation with Heat as a Primary Product
- B1
- For steam collection and reinjection during the construction phase: An estimation of the minimum requirement of steam collection and reinjection infrastructure to produce and sustain the heat production throughout the 30-year technical lifetime of the plant was made based on thermodynamic energy balance for stand-alone heat production and the known energy output from wells drilled at Hellisheidi. Here, it is evaluated that a minimum of five out of the 64 production wells and four out of the 17 reinjection wells would have to be drilled solely for the 133 MWth heat production that was installed during the construction phase of the CHP plant (prior to the year 2012 when operation phase is assumed to start in the study).
- B2
- For geothermal fluid: The geothermal energy extraction essential for heat production is calculated separately and compared to the overall energy extraction from the geothermal fluid for the total CHP plant production to calculate the partitioning factor. However, for mass flow and direct emissions due to the use of the geothermal fluid by a heat-alone plant, the same partitioning factor is used for B1, as explained above.
- B3
- For the need of make-up wells for maintaining heat production: The assumed decline of geothermal well output due to production was estimated for the maintenance phase of a stand-alone heat plant. Here, the assumption is made that at least one make-up well is needed exclusively for the maintenance of heat production at the plant over a 30-year lifetime (compared to an estimate of 15-60 make-up wells being necessary for the overall CHP plant to sustain both heat and electricity production). The assumed need for make-up wells includes future expansions above the original 133 MWth installed thermal capacity, e.g., the recent 200 MWth expansion in 2020.
2.4.3. Method C: Energy Allocation
2.4.4. Method D: Exergy Allocation
2.4.5. Method E: Economic Allocation
2.4.6. Method F: Alternative Generation Method (AGM)
3. Results
3.1. Allocation Factors
3.2. Indicator Results for Electricity and Heat from Hellisheidi CHP Plant
4. Discussion
5. Conclusions
Author Contributions
Funding
Acknowledgments
Conflicts of Interest
Abbreviations
ACER | Agency for the Cooperation of Energy Regulators |
AGM | Alternative Generation Method |
CED | Cumulative Energy Demand |
CEN | The European Committee for Standardization (French: Comité Européen de Normalisation) |
CHP | Combined Heat and Power |
CML-IA | Impact Assessment method of the Centrum voor Milieuwetenschappen, Leiden University |
CT | Cooling tower |
CW | Coldwater well |
CWP | Coldwater pumps |
CWT | Coldwater tank |
DA | Deaerator |
DHHX | Heat exchanger District Heat |
DHT | Hot water tank District Heat |
ED | Electricity Directive |
EED | Energy Efficiency Directive |
EOL | End of life |
EPB | Energy Performance in Buildings |
EPBD | Energy Performance in Buildings Directive |
EPC | Energy Performance Certificate |
ETS | Emission Trading System |
EU | European Union |
FV | Flashing valve |
GHG | Greenhouse Gas Emissions |
GW | Geothermal well |
HPC | High-pressure condenser with preheater |
HPM | method moisture remover |
HPS | High-pressure steam separator |
HPTG | High-pressure turbine-generator set |
HWP | Hot water pump |
IEA | International Energy Agency |
IPCC | Intergovernmental Panel on Climate Change |
IRES | International Recommendations for Energy Statistics |
ISO | International Organization for Standardization |
LCA | Life Cycle Assessment |
LCI | Life cycle inventory |
LPC | Low-pressure condenser |
LPM | Low-pressure moisture remover |
LPS | Low-pressure steam separator |
LPTG | Low-pressure turbine-generator set |
PEF | Primary Energy Factor |
PEFnon-ren | Non-Renewable Primary Energy Factor |
RED | Renewable Energy Directive |
RW | Reinjection well |
WE | Wellhead |
WS | Well silencer |
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Legislative Act | Official Journal Publication (Date and Official Document) |
---|---|
Energy Performance in Buildings Directive (EPBD) | 19/06/2018 - Directive 2018/844 |
Renewable Energy Directive (RED) | 21/12/2018 - Directive 2018/2001 |
Energy Efficiency Directive (EED) | 21/12/2018 - Directive 2018/2002 |
Governance of the Energy Union | 21/12/2018 - Regulation 2018/1999 |
Electricity Regulation | 14/06/2019 - Regulation 2019/943 |
Electricity Directive (ED) | 14/06/2019 - Directive 2019/944 |
Risk Preparedness | 14/06/2019 - Regulation 2019/941 |
Agency for the Cooperation of Energy Regulators (ACER) | 14/06/2019 - Regulation 2019/942 |
Allocation Methods | Electricity | Heat |
---|---|---|
A. Electricity (system expansion) | ||
A1 Construction: Steam collection and reinjection | 100% | 0% |
A2.1 Operation: Geothermal fluid, primary energy flow | 94% | 6% |
A2.2 Operation: Geothermal fluid, material flow | 100% | 0% |
A3 Maintenance: Make-up wells | 100% | 0% |
B. Heat (system expansion) | ||
B.1 Construction: Steam collection and reinjection | 86% | 14% |
B.2 Operation: Geothermal fluid, primary energy, and material flow | 91% | 9% |
B.3 Maintenance: Make-up wells | 97% | 3% |
C. Energy | 73% | 27% |
D. Exergy | 92% | 8% |
E. Economic | 86% | 14% |
F. AGM | 92% | 8% |
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Karlsdottir, M.R.; Heinonen, J.; Palsson, H.; Palsson, O.P. High-Temperature Geothermal Utilization in the Context of European Energy Policy—Implications and Limitations. Energies 2020, 13, 3187. https://doi.org/10.3390/en13123187
Karlsdottir MR, Heinonen J, Palsson H, Palsson OP. High-Temperature Geothermal Utilization in the Context of European Energy Policy—Implications and Limitations. Energies. 2020; 13(12):3187. https://doi.org/10.3390/en13123187
Chicago/Turabian StyleKarlsdottir, Marta Ros, Jukka Heinonen, Halldor Palsson, and Olafur Petur Palsson. 2020. "High-Temperature Geothermal Utilization in the Context of European Energy Policy—Implications and Limitations" Energies 13, no. 12: 3187. https://doi.org/10.3390/en13123187
APA StyleKarlsdottir, M. R., Heinonen, J., Palsson, H., & Palsson, O. P. (2020). High-Temperature Geothermal Utilization in the Context of European Energy Policy—Implications and Limitations. Energies, 13(12), 3187. https://doi.org/10.3390/en13123187