Performance Analysis of Different Borehole Heat Exchanger Configurations: A Case Study in NW Italy
Abstract
Highlights
- A good knowledge of the underground parameters and of the aquifer characteristics are essential in the design of borehole heat exchangers as part of a shallow geothermal plant integrated in a district heating and cooling grid.
- Borehole heat exchangers with a coaxial configuration outperform double U pipes in terms of energy efficiency, especially during intermittent operation modes of the geothermal heating system.
- Proper design of a shallow geothermal plant can potentially reduce the cost of drilling boreholes and make the installation easier on site, also improving the sustainability of urban environments.
- A geothermal-based district heating and cooling grid can be combined with other renewable energies, achieving the best thermal energy performance, improving smart energy systems, and the decarbonisation of the building sector.
Abstract
1. Introduction
2. Geological Setting
- “Marne di Sant’Agata Fossili” (Tortonian/Lower Messinian), bioturbated clayey to calcareous foraminifers-rich marl sediments, showing a gradual transition toward the top into a rhythmic alternation of marls and organic-rich, extremely laminated mudstones (VGS3, in Figure 1);
- “Membro di Nizza Monferrato” (Messinian), belonging to the “Gessoso-Solfifera” geological unit mainly composed of clays, silts, and subordinate sandstones with a variable colour including dark yellow, grey, cream-white, and purple, in which a primary laminated microcrystalline gypsum bed is recognizable (CCS, in Figure 1);
- “Quaternary succession” (Holocene–present), consisting of sandy-gravelly and silty-sandy fluvial deposits which overlie all the stratigraphic succession; it is present in the shallower 30 m (MEA3 and CMT3, in Figure 1).
3. Materials and Methods
- 2U150 m: polyethylene double U pipe with a depth of 150 m, which corresponds to the pilot borehole (borehole diameter: 0.152 m; pipe diameter: 0.032 m; pipe wall thickness: 0.0029 m);
- 2U36 m: polyethylene double U pipe with a depth of 36 m, in light of the base of the aquifer highlighted by the pilot drilling (borehole diameter: 0.152 m; pipe diameter: 0.032 m; pipe wall thickness; 0.0029 m);
- Coax 36 m: coaxial configuration with stainless steel outer casing (outer diameter: 0.061 m; wall thickness: 0.008 m) and polyethylene inner pipe (outer diameter: 0.025 m; wall thickness: 0.0023 m) with a depth of 36 m.
3.1. Field Tests
- Tf(t) is the average fluid temperature (Tin and Tout) depending on the test time, expressed in °C.
- q is the injected power in the unit of time and depth, expressed in W/m and is equal to Q/H (H is the drilling depth), in which Q is the injected power in the unit of time, expressed in W.
- λ is the ground thermal conductivity, expressed in W/m/K.
- γ is the Eulero constant, equal to 0.5772.
- α is the thermal diffusivity, expressed in m2/s.
- t is the test time, expressed in s.
- r is the borehole radius, expressed in m.
- Rb is the borehole thermal resistance, expressed in K/(W/m).
- Tg is the undisturbed temperature, expressed in °C.
3.2. Numerical Simulations
- Tf is the average fluid temperature (Tin and Tout) depending on the test time, expressed in °C.
- q is the injected power in the unit of time and depth, expressed in W/m and is equal to Q/H (H is the drilling depth), in which Q is the injected power in the unit of time, expressed in W.
- Tb is the borehole wall temperature expressed in °C.
- Rb is the borehole thermal resistance, expressed in m K W−1.
4. Results
4.1. Thermo-Geological Conceptual Model
4.2. Comparison of Different BHE Configurations
- With the same BHE geometry and material, the 2U 36 m BHE allowed for better linear thermal power extraction (56.03 W/m) compared to the 2U 150 m, which recorded a value of 42.47 W/m.
- Using the coaxial steel geometry (Coax 36 m), the linear thermal power that can be extracted increases to 74.51 W/m.
- The specific thermal power at the end of the first six months of simulation shows very similar values (2U 150 m = 46.24 W/m; 2U 36 m = 58.29 W/m; Coax 36 m = 79.32 W/m) to those recorded at the end of the five years of system operation (2U 150 m = 42.46 W/m; 2U 36 m = 55.51 W/m; Coax 36 m = 74.51 W/m). Therefore, thermal specific power decreases quite slowly after the first six months (about 5% for all the BHEs), then shows a thermal stabilization in the next few months; these results thus confirm how these data can also be used to describe the thermal performance of each BHE in long-term analysis.
5. Discussion
- Knowledge of the right geological, hydrogeological, and thermo-physical properties of the ground is of paramount importance in correctly evaluating the thermal efficiency of BHEs.
- The specific thermal power of each BHEs records similar values to those displayed at the end of the five-year simulation already starting from the fifth month, ensuring the long-term stability of the system.
- Maintaining the same geometry and material (double U pipes in polyethylene), the pipe at −36 m showed a higher specific thermal power than that at −150 m. This confirms how at −36 m the same BHE configuration fully exploits the only aquifer present in the subsurface; as shown in Figure 4, the most favourable thermal conditions indeed occur between −9 and −36 m where the hydrodynamic characteristics of the groundwater can significantly increase the thermal efficiency. This helps in understanding how the 2U 36m BHE can be the best solution than the deeper one with the same geometry, strongly reducing drilling costs.
- The higher specific power of 80 [W/m] for the coaxial configuration differs from values found in the literature for which the highest value recorded is equal to 42.2 W/m [46], which is, however, based only on the thermo-technical characteristics of the BHE without considering the hydrogeological and geological parameters that can potentially contribute to the heat power also exceeding 80 W/m in some scenarios.
- The coaxial geometry proved to be not only the most efficient among the scenarios in terms of thermal power extracted but also the most thermally stable, as evidenced during intermittent operating modes with daily-on and -off cycles (12 h each); it was also easier to install on site.
6. Conclusions
- Geological, hydro-geological, and thermo-physical models should be validated through a back-analysis of the ground response test, especially for medium-large systems.
- Numerical simulations help in selecting the best heat exchanger geometry, based not only on the design or on the duty cycle but also on the thermal efficiency of the ground in terms of the amount of heat which can be extracted from it.
- Where there are lithologies with an overall thermal conductivity from medium to high, steel coaxial pipes usually perform better than conventional double U BHEs.
- The coaxial configuration outperforms the double U pipes, especially during intermittent operation modes.
- Using the coaxial loop design could potentially reduce the cost of drilling boreholes and make the installation easier on site, as the effective diameter would be smaller than a comparable double U BHE.
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
Abbreviations
BHE | borehole heat exchanger |
DH | district heating |
DHC | district heating and cooling |
GSHP | ground source heat pump |
2U BHE | double u borehole heat exchanger |
Coax BHE | coaxial borehole heat exchanger |
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BHE Configuration | L (m) | din (m) | bin (m) | dout (m) | bout (m) | D (m) | λin (W × m−1 K−1) | λout (W × m−1 K−1) | Shank Spacing (m) | Grout Sealing Wall BHE |
---|---|---|---|---|---|---|---|---|---|---|
Double U (PE100 SDR11) | 150 | 0.026 | - | 0.032 | 0.0029 | 0.152 | - | 0.42 | 0.12 | Bentonite |
Double U (PE100 SDR11) | 36 | 0.026 | - | 0.032 | 0.0029 | 0.152 | - | 0.42 | 0.12 | Bentonite |
Coaxial | 36 | 0.025 | 0.0023 | 0.065 | 0.0080 | 0.178 | 0.42 | 52 | - | Bentonite |
Depth b.g.l. (m) | Lithology | Temperature (°C) |
---|---|---|
10 | Sands | 13.9 |
30 | Sands and saturated silts | 14.2 |
60 | Silts and clays | 14.6 |
100 | Marls | 15.6 |
120 | Marls | 16.2 |
150 | Marls | 16.7 |
Depth (m) | Lithology | λs (W × m−1 K−1) | Φ | Kxx (m/s) | Kyy (m/s) | Kzz (m/s) | T (°C) |
---|---|---|---|---|---|---|---|
0–9 | Sands | 0.48 | 0.40 | 1.00 × 10−4 | 1.00 × 10−4 | 1.00 × 10−5 | 15.2 |
9–36 | Sands and saturate silts | 2.58 | 0.30 | 5.00 × 10−5 | 5.00 × 10−5 | 5.00 × 10−6 | 15.2 |
36–113 | Silts and clays | 2.56 | 0.45 | 1.00 × 10−6 | 1.00 × 10−6 | 1.00 × 10−7 | 15.2 |
113–150 | Marls | 2.46 | 0.20 | 1.00 × 10−7 | 1.00 × 10−7 | 1.00 × 10−8 | 15.2 |
BHE Type | Power 0–36 m [W] | Specific Power [W m−1] | Rb [m K W−1] |
---|---|---|---|
2U 150 m | 1869.63 | 45.26 | 0.085 |
2U 36 m | 2084.05 | 57.89 | 0.081 |
Coax 36 m | 2839.88 | 78.89 | 0.020 |
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Chicco, J.M.; Giordano, N.; Comina, C.; Mandrone, G. Performance Analysis of Different Borehole Heat Exchanger Configurations: A Case Study in NW Italy. Smart Cities 2025, 8, 121. https://doi.org/10.3390/smartcities8040121
Chicco JM, Giordano N, Comina C, Mandrone G. Performance Analysis of Different Borehole Heat Exchanger Configurations: A Case Study in NW Italy. Smart Cities. 2025; 8(4):121. https://doi.org/10.3390/smartcities8040121
Chicago/Turabian StyleChicco, Jessica Maria, Nicolò Giordano, Cesare Comina, and Giuseppe Mandrone. 2025. "Performance Analysis of Different Borehole Heat Exchanger Configurations: A Case Study in NW Italy" Smart Cities 8, no. 4: 121. https://doi.org/10.3390/smartcities8040121
APA StyleChicco, J. M., Giordano, N., Comina, C., & Mandrone, G. (2025). Performance Analysis of Different Borehole Heat Exchanger Configurations: A Case Study in NW Italy. Smart Cities, 8(4), 121. https://doi.org/10.3390/smartcities8040121