When sufficient ground area is available, as mentioned, horizontal GHEs present the most cost-effective option. However, if the available area is limited, the ground surface is rocky, and visual interference with the landscape is not welcome, vertical GHEs are applied. Vertical ground heat exchangers (VGHE) are also referred to as borehole heat exchangers (BHEs). In comparison with horizontal GHEs, BHEs have higher installation costs and more stable performance, as they are not affected severely by ambient air
[65][18]. Vertical GHEs are divided into two groups depending on the depth of the borehole and, consequently, the type of heat exchanger. The first group, shallow boreholes GHE (<400 m), are usually used in combination with heat pumps (ground-coupled heat pumps—GCHP) as a source or sink for thermal energy (). A traditional configuration consists of the borehole with a diameter usually around 100–200 mm containing U-tubes with a diameter in the range of 19–38 mm for working fluid to circulate
[65][18]. Besides the most common single U-tube configuration, other configurations that can be used are double or triple U-tube, W-shaped tube, coaxial tube, and helical-shaped tube
[53][19]. The annulus section of the borehole is made from various backfill materials referred to as grout, which reduces the thermal resistance between the pipes and ground and ensures good contact between materials. As the heat transfer area of such systems is limited, consequently, the thermal capacity (thermal power) of such systems is also limited. To achieve a higher thermal capacity of such systems, there are two possible solutions—increasing the number of boreholes (most of today’s installations) or increasing the depth of the borehole
[66][20]. Increasing the number of boreholes is only available when there is sufficient available space.
Figure 3. Vertical borehole heat exchanger coupled to the heat pump (1–evaporator, 2—compressor, 3—condenser, 4—expansion valve, 5—borehole heat exchanger).
The second option, to increase the thermal capacity of GHE, uses the technology of the deep borehole heat exchangers (DBHE), which can be also classified as the second category of vertical BHE. DBHE can extract medium-deep geothermal energy at high temperatures
[67][21]. Although the literature does not give, to our knowledge, strict classification of BHEs by depth, a good definition is proposed by Sapinska-Sliwa et al.
[67][21]. They proposed that deep borehole heat exchangers (DBHE) are those where there is a possibility that the extracted heat can be used directly (without the aid of HP). When using the technology of DBHE, classical U-tubes configurations are usually replaced with coaxial (pipe in a pipe) borehole heat exchangers, which have a larger heat transfer area and can sustain a larger flow rate (lower pumping costs)
[68][22]. As over 50% of the total cost of the geothermal project can be drilling costs
[69][23], a good solution to reduce high drilling costs is presented by using depleted and abandoned gas and oil wells, which has been extensively investigated recently
[70,71,72,73][24][25][26][27]. Depending on the obtained temperature in DBHE, these systems can be used for direct space heating
[74[28][29],
75], coupled with heat pumps
[76[30][31][32],
77,78], or even in power production systems
[79][33].
2.3. Shallow Ground Heat Exchanger Configurations
Most prevailing GHE configurations include horizontal and vertical design, the former having low installation costs and the latter having superior thermal performance due to ground temperature stability. In between, shallow systems incorporate advantages of both systems: less expensive excavation works and use of ground layers where the effect of surface conditions are damped
[80][34]. The application of this GHE layout is interesting in urban environments with increased ground temperature and limited installation area or in locations where deep drilling is prohibited to prevent disturbance of aquifers
[81][35]. Shallow systems include a large diameter, to increase the heat transfer area, conically or helically shaped configurations
[82[36][37][38],
83,84], or pipes embedded in building piles (energy piles)
[85][39] (). An alternative configuration of a coil GHE inserted in a water tank with PCM and used as an underground thermal battery was proposed by Warner et al.
[86][40]. The authors concluded that the performance of this layout is comparable with vertical BHE with the same heat transfer surface area.
Figure 4. Shallow heat exchanger coupled to the heat pump (1—evaporator, 2—compressor, 3—condenser, 4—expansion valve, 5—energy piles, 6—large diameter coil GHE).
2.4. Direct Expansion Systems
R&D in the field of ground physics allowed us to determine accurate soil temperature profiles and thermal properties. Modeling these properties in cooperation with advanced control systems and overcoming some of the design challenges was a prerequisite for use of direct expansion (DX) systems
[87][41]. Compared to previously mentioned heat exchangers with water or glycol mixtures often used as indirect heat pump secondary circuit, DX systems act as evaporators or condensers of a heat pump whose working fluid is heat pump refrigerant (). This setup removes the need for a heat exchanger between the fluid circles as well as a circulation pump. A ground heat exchanger design with the DX of refrigerant needs to follow some specific rules concerning the type of refrigerant, refrigerant charging, oil return to the compressor, depth of the vertical borehole heat exchanger, and possible ground pollution due to refrigerant leak
[88][42]. The ground heat exchanger can be placed horizontally, vertically, or in a slinky manner. Exchangers with vertical configuration are predominant
[36][43]. Several researchers have investigated dynamic heat transfer analysis of the two-phase flow in the ground evaporator and the heat exchange with ground
[89,90,91,92][44][45][46][47]. De Carli et al.
[89][44] developed the mathematical models of evaporation in the vertical U-tube. Li et al.
[91][46] developed and validated numerically and experimentally a three-dimensional transient thermal resistance and capacity model of a novel direct expansion downhole heat exchanger. Additionally, Nguyen et al.
[92][47] evaluated a pressure-enthalpy coupled thermal resistance and capacity model for a direct expansion vertical borehole heat exchanger for supercritical CO2 application.
Figure 5. Direct expansion borehole heat exchanger (1—evaporator/BHE, 2—compressor, 3—condenser, 4—expansion valve).