Micro Gas Turbines in the Global Energy Landscape: Bridging the Techno-Economic Gap with Comparative and Adaptive Insights from Internal Combustion Engines and Renewable Energy Sources
Abstract
:1. Introduction
2. MGT Potential and Position as a Prime Mover in the Dispatchable Energy Sector
3. Why Techno-Economic Assessment (TEA) Studies Are Crucial for MGT Sector Development
3.1. Comparative Assessment of MGT Sector Growth Compared to RES-Based TEA Activities: Insights, Trends, and Adaptable Strategies
3.2. Comparative Assessment of MGT Sector Growth Compared to ICE Activities: Insights, Trends, and Adaptable Strategies
4. Novel Calculation Procedure for Assessing Learning and Experience Effects in MGT-TEA
4.1. Percentage Learning and Experience Effects of Recent Studies Integrating MGT-TEA with RES and ICE
4.2. Development and Application of a Novel Calculation Procedure for Assessing Learning and Experience Effects in MGT-TEA
4.2.1. Introduction to the Mathematical Model and Procedure
Understanding Learning and Experience Curves
- = Cost per unit after units are produced;
- = Initial cost per unit;
- = Cumulative production or experience;
- = Learning elasticity (typically between 0.2 and 0.3 for most technologies). The exponent determines the rate at which costs decrease. A higher indicates faster learning.
Calculating the Learning Rate
Incorporating Experience Curve Effects
- = Cost per unit after units are produced;
- = Cost per unit at baseline experience level ;
- = Cumulative production or experience;
- = Experience elasticity, which is typically derived from empirical data.
4.2.2. Application to MGT-TEA with ICE and RES
- Determine Initial Costs: Establish the initial cost per unit for MGT, ICE, and RES systems. These costs should reflect the current state of technology;
- Estimate Learning and Experience Elasticities: Based on historical data and the literature, estimate the learning elasticity and experience elasticity for each technology;
- Calculate Cumulative Production or Usage: Determine the cumulative production or usage of for each technology. For MGTs, this may be lower than for ICEs and RESs, reflecting the earlier stage of commercialization;
- Model Cost Reduction: Use the combined learning and experience curve (Equation (4)) to model the cost reductions for MGTs, ICEs, and RESs as production or usage scales up;
- Comparison and Sensitivity Analysis: Compare the projected costs for MGTs against ICEs and RESs over time. Conduct sensitivity analyses by varying and to explore different scenarios.
4.3. Analysis and Implications of Learning and Experience Effects
4.3.1. Key Elements and Methodology
- Initial Cost (CAPEX): The initial capital expenditure for each system, reflecting the current state of technology and market conditions;
- Learning Effect: The percentage reduction in cost due to the learning curve, as cumulative production increases and efficiency improvements are realized;
- Experience Effect: The reduction in cost attributed to technological advancements and operational efficiencies gained over time;
- LCoE (Levelized Cost of Energy): The calculated cost per unit of energy over the system’s lifecycle, both before and after learning and experience effects;
- NPV (Net Present Value): The overall profitability of the system over its operational lifetime, considering both initial investment and operational costs.
4.3.2. Data Extraction and Assumptions
- Learning Elasticity (α): Assumed values are 0.2 for MGTs, 0.25 for RESs, and 0.15 for ICEs;
- Experience Elasticity (β): Assumed values are 0.1 for MGTs, 0.15 for RESs, and 0.05 for ICEs;
- Initial Costs (CI): Extracted from recent literature under Section 3 and gray literature;
- Cumulative Production (n): Estimated based on the stage of commercialization, with MGTs assumed to be in earlier stages compared to RESs.
4.3.3. Variation in Learning and Experience Effects
4.3.4. Highest and Lowest Learning Effects
4.3.5. Impact on LCOE and NPV
4.3.6. High CAPEX as a Barrier
4.3.7. Strategic Importance of Hybrid Systems
5. Conclusions and Future Direction
Supplementary Materials
Author Contributions
Funding
Data Availability Statement
Conflicts of Interest
Nomenclature
MGT | Micro Gas Turbine |
ICE | Internal Combustion Engine |
TEA | Techno-Economic Assessment |
RES | Renewable Energy Sources |
CHP | Combined Heat and Power |
CCHP | Combined Cooling, Heating, and Power |
LCOE | Levelized Cost of Energy |
NPV | Net Present Value |
CAPEX | Capital Expenditure |
OPEX | Operating Expenditure |
NG | Natural Gas |
PV | Photovoltaic |
H2 | Hydrogen |
WWTP | Wastewater Treatment Plant |
BESS | Battery Energy Storage System |
VRE | Variable Renewable Energy |
FC | Fuel Cell |
SE | Stirling Engine |
ORC | Organic Rankine Cycle |
FW | Flywheel |
PBP | Payback Period |
NSGA-II | Non-Dominated Sorting Genetic Algorithm II |
LCPV/T-HP | Low-Concentration Photovoltaic/Thermal-Heat Pump |
ABC | Absorption Chiller |
m-CHP | Micro-Combined Heat and Power |
P2P | Peer-to-Peer |
ESS | Energy Storage System |
sCO2 | Supercritical Carbon Dioxide |
MCDA | Multi-Criteria Decision Analysis |
PESTLE | Political, Economic, Social, Technological, Legal, Environmental (analysis framework) |
TOT | Turbine Outlet Temperature |
rpm | Revolutions Per Minute |
Mathematical Symbols | |
α (Alpha) | Learning Rate Coefficient |
β (Beta) | Experience Rate Coefficient |
LR | Learning Rate |
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Study and Year | Microgrid or Distributed Power Generation | Renewable Energy Sources | Internal Combustion Engines | Micro Gas Turbine | Relationship to MGT-TEA Learning Effect | Relationship to MGT-TEA Experience Effect | Percentage (%) of RES-TEA Learning | Percentage (%) of ICE-TEA Learning | Remarks and Highlights |
---|---|---|---|---|---|---|---|---|---|
X. Ding et al. (2024) [78] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 10 | 0 | Solar-assisted MGT-CCHP system, variants with and without solar energy storage. |
Bellos et al. (2024) [79] | ✔ | ✔ | X | X | ✔ | ✔ | 20 | 0 | Solar-driven tri-generation system coupled with ORC and vapor compression refrigeration cycle. |
Zheng et al. (2024) [80] | ✔ | ✔ | X | X | ✔ | ✔ | 15 | 0 | New solar-driven distributed energy system. |
Li et al. (2024) [81] | ✔ | ✔ | X | X | ✔ | ✔ | 25 | 0 | Evaluated TE performance by centralized and decentralized frameworks. |
Zhong et al. (2024) [82] | ✔ | ✔ | X | X | ✔ | ✔ | 30 | 0 | Novel solar-driven distributed energy system converting electricity to methane. |
Song et al. (2024) [83] | ✔ | ✔ | X | X | ✔ | ✔ | 35 | 0 | CCHP system integrating solar energy and hydrogen production. |
Ma et al. (2024) [84] | ✔ | ✔ | ✔ | X | ✔ | ✔ | 40 | 30 | Hybrid renewable energy CCHP system with an Internal Combustion Engine. |
Allouhi et al. (2024) [85] | ✔ | ✔ | X | X | ✔ | ✔ | 20 | 0 | Multi-objective optimization of a solar-driven power–thermal supply system. |
Zhang et al. (2024) [86] | ✔ | ✔ | X | X | ✔ | ✔ | 25 | 0 | Indirect expansion solar-assisted air source heat pump system. |
H. Yazdani et al. (2023) [87] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 20 | 0 | TEA studies and multi-objective optimization for a complex hybrid energy system (HES) including various technologies. |
A. Escamilla et al. (2023) [88] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 15 | 0 | Hybridization of MGT in P2P-ESS with battery energy storage system (BESS) to reduce H2 demand and seasonal storage needs. |
M. A. Khan et al. (2023) [89] | ✔ | ✔ | ✔ | ✔ | ✔ | ✔ | 30 | 30 | TEA and risk assessment of m-CHP systems for households, including PESTLE and MCDA analysis. |
Barun K. Das et al. (2022) [90] | ✔ | ✔ | ✔ | ✔ | ✔ | ✔ | 35 | 30 | TEA of hybrid RESs for electrifying a remote village, compared PV/biomass, PV/diesel, and PV/MGT systems. |
B.K. Das et al. (2022) [91] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 40 | 0 | Optimization of hybrid energy systems combining MGT with PV, WT, and various battery storage options. |
Barun K. Das et al. (2018) [92] | ✔ | ✔ | ✔ | ✔ | ✔ | ✔ | 25 | 30 | Performance analysis of baseline PV/battery system and hybrid systems with ICE or MGT supplementary prime movers. |
Farah Nazifa N. et al. (2020) [93] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 20 | 0 | TEA study on integrating MGT-CHP systems in wastewater treatment plants, focusing on biogas utilization. |
Domenico B. et al. (2017) [94] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 30 | 0 | Coupling of an 800-kW updraft gasifier with a 200 kWe-MGT for CHP, evaluating economic performance and investment profitability. |
S. Chu et al. (2022) [95] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 35 | 0 | MGT-CCHP system coupled with LCPV/T-HP and absorption chiller, evaluating performance under different operation strategies. |
Ramin M. et al. (2022) [96] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 40 | 0 | Comparison of MGT system and sCO2 system fueled by a biomass gasifier for residential users. |
Peloriadi, K. et al. (2022) [97] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 25 | 0 | Feasibility of SOFC-MGT system for Patmos Island, Greece. |
A.H. Eisapour et al. (2022) [98] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 20 | 0 | Feasibility of integrated energy system including MGT with CHP module for meeting load demand of case study. |
Paepe et al. (2019) [99] | ✔ | ✔ | ✔ | ✔ | ✔ | ✔ | 15 | 30 | Optimizing MGT operation for grid connection, controlling key parameters like turbine outlet temperature (TOT) and rpm. |
A. di Gaeta et al. (2017) [100] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 30 | 0 | Simplified MGT model coupled with hybrid energy grid simulation for fossil fuel savings. |
M. Sharf et al. (2022) [101] | ✔ | ✔ | X | ✔ | ✔ | ✔ | 35 | 0 | Economic feasibility of using MGT-based m-CHP unit in various scenarios with different operational modes. |
Study and Year | System | Initial Costs (CAPEX) (USD/kW) | LCOE (USD/kWh) | Learning Effect (α) | Experience Effect (β) | Estimated LCOE After Learning and Experience (USD/kWh) | NPV (Million USD) | Remarks |
---|---|---|---|---|---|---|---|---|
X. Ding et al. (2024) [78] | Solar-assisted MGT-CCHP | 2500 | 0.0417 | 0.2 | 0.1 | 0.033 | 0.252 | Less economical with solar energy storage, competitive without it. |
Bellos et al. (2024) [79] | Solar-driven TGS | 3000 | 0.054 | 0.25 | 0.15 | 0.0405 | 50 | PBP of 8.5 years; high investment, suitable for large-scale deployment. |
Zheng et al. (2024) [80] | New solar-driven distributed energy system | 3500 | 0.0615 | 0.25 | 0.15 | 0.04613 | 40 | Proposed system shows high CAPEX but promising NPV. |
Ma et al. (2024) [84] | Hybrid renewable energy CCHP with ICE | 2000 | 0.02 | 0.15 | 0.1 | 0.017 | 130 | Significant reduction in costs and CO2 emissions. |
Farah Nazifa N. (2020) [93] | MGT-CHP in (WWTPs) | 4000 | 0.095 | 0.1 | 0.05 | 0.0855 | 0.5 | High initial investment, justified by long-term benefits. |
Ramin M. et al. (2022) [96] | MGT vs. sCO2 system fueled by biomass gasifier | 5000 | 0.145 | 0.2 | 0.1 | 0.116 | 70 | sCO2 system shows better performance and higher efficiency. |
A. Escamilla et al. (2023) [88] | Hybrid MGT in P2P-ESS with BESS | 7000 | 0.356 | 0.1 | 0.05 | 0.2704 | 85 | High CAPEX due to integration costs, significant storage needs. |
B.K. Das et al. (2022) [91] | Hybrid RES for village electrification | 3000 | 0.314 | 0.25 | 0.15 | 0.2355 | 0.65 | Best performance with biomass, higher CAPEX for MGT. |
Domenico B. et al. (2017) [94] | MGT-gasifier CHP system | 5300 | 0.227 | 0.15 | 0.1 | 0.198 | 1.7 | Best performance with industrial heat demand; high investment, but profitable. |
S. Chu et al. (2022) [95] | MGT-CCHP with LCPV/T-HP and ABC | 4000 | 0.165 | 0.2 | 0.1 | 0.132 | 95 | Complex system, high CAPEX but strong potential for cost-effectiveness and efficiency. |
H. Yazdani et al. (2023) [98] | TEA of complex HES including MGT | 4500 | 0.205 | 0.18 | 0.09 | 0.1681 | 55 | Incorporation of MGT in a complex HES shows moderate CAPEX, with improved overall system performance. |
M.A. Khan et al. (2024) [102] | Economic feasibility of low-carbon fuels in MGT-CHP | 5500 | 0.25 | 0.22 | 0.11 | 0.195 | 75 | Green H2 shows potential, but currently high costs are a barrier. |
W.D Paepe et al. (2019) [99] | MGT connected to the grid | 4800 | 0.21 | 0.19 | 0.09 | 0.1743 | 60 | Grid-connected MGT offers significant benefits in energy markets, especially during peak demand. |
A. di Gaeta et al. (2017) [100] | Simplified MGT model in hybrid energy grid | 4600 | 0.225 | 0.18 | 0.1 | 0.1845 | 65 | Hybrid energy grids with MGT show fossil fuel savings and strong potential for H2 integration. |
M. Sharf et al. (2022) [101] | Economic feasibility of MGT-CHP in various scenarios | 4900 | 0.215 | 0.2 | 0.1 | 0.172 | 63 | Smart grid-connected MGT-CHP units provide significant economic benefits in multiple operational modes. |
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Weerakoon, A.H.S.; Assadi, M. Micro Gas Turbines in the Global Energy Landscape: Bridging the Techno-Economic Gap with Comparative and Adaptive Insights from Internal Combustion Engines and Renewable Energy Sources. Energies 2024, 17, 5457. https://doi.org/10.3390/en17215457
Weerakoon AHS, Assadi M. Micro Gas Turbines in the Global Energy Landscape: Bridging the Techno-Economic Gap with Comparative and Adaptive Insights from Internal Combustion Engines and Renewable Energy Sources. Energies. 2024; 17(21):5457. https://doi.org/10.3390/en17215457
Chicago/Turabian StyleWeerakoon, A. H. Samitha, and Mohsen Assadi. 2024. "Micro Gas Turbines in the Global Energy Landscape: Bridging the Techno-Economic Gap with Comparative and Adaptive Insights from Internal Combustion Engines and Renewable Energy Sources" Energies 17, no. 21: 5457. https://doi.org/10.3390/en17215457
APA StyleWeerakoon, A. H. S., & Assadi, M. (2024). Micro Gas Turbines in the Global Energy Landscape: Bridging the Techno-Economic Gap with Comparative and Adaptive Insights from Internal Combustion Engines and Renewable Energy Sources. Energies, 17(21), 5457. https://doi.org/10.3390/en17215457