A Submerged Building Strategy for Low-Carbon Data Centers in Coal Mining Subsidence Areas: System Design and Energy–Carbon Performance Assessment
Abstract
1. Introduction
- Subsided water bodies have yet to be incorporated into infrastructure deployment logic;
- Despite their potential, liquid cooling systems lack integrated frameworks with building and environmental systems;
- Tri-integrated architectural models—spatial, structural, and systemic—have not been quantitatively evaluated for their role in advancing carbon neutrality.
2. Methodology
2.1. Site Selection and Regional Context
- Relatively stable hydrological conditions are suitable for constructing an external thermal sink for cooling systems;
- Preliminary planning control is already in place, making infrastructural access for data centers technically feasible;
- The terrain characteristics support a “submerged deployment with shoreline connection” configuration, offering potential for experimental implementation.
2.2. Building Layout and Structural Strategy
- (a)
- Two water-exposed sides, with a 1500 mm cold aisle and a 1000 mm hot aisle;
- (b)
- Two water-exposed sides, with a 1500 mm cold aisle and a 1200 mm hot aisle;
- (c)
- Three water-exposed sides, with a 1500 mm cold aisle and a 1000 mm hot aisle.
2.3. Model Framework and Boundary Conditions
2.4. Heat Exchange Model and Simulation Implementation
- (1)
- Conductive heat exchange between the IT equipment and the immersion coolant;
- (2)
- Convective heat exchange within the CDU between the immersion coolant and the secondary cooling water;
- (3)
- Heat rejection from the cooling water to the surrounding water body via wall-mounted plate heat exchangers.
- (1)
- Server–coolant heat exchange
- (2)
- Coolant–CDU heat exchange
- (3)
- Cooling water–water body heat exchange
2.5. Model Validation (TRNSYS–MATLAB Comparison)
3. Results and Analysis
3.1. Cooling Energy Consumption and PUE Analysis
- IT equipment consumption: Estimated based on a median rack-level load of 65 kW;
- Non-cooling system consumption: Including UPS, power conversion, networking, and facility operation loads, estimated at 3%, 1.5%, and 1.5% of the IT load, respectively;
- PUE (Power Usage Effectiveness): Calculated as the ratio of total energy consumption to IT energy consumption.
3.2. Assessment of Energy Savings and Carbon Emissions
- Submerged system: 16,682–41,706 t CO2.
- Conventional system: 33,450–66,901 t CO2.
4. Discussion
4.1. Practical Implications of Energy Efficiency and Carbon Reduction
4.2. Redevelopment Potential in Coal Mining Subsidence Regions
- Spatial compatibility: Subaqueous deployment leverages large-scale idle water surfaces. Where necessary, underwater excavation may reduce the influence of unstable strata on the structure’s performance.
- Structural reusability: The combination of pile foundation and grouting techniques accommodates soft ground conditions and allows later transformation into modular or floating platforms.
- Industrial continuity: As a future-oriented digital infrastructure node (e.g., edge computing, AI training centers, or government cloud hubs), the data center can anchor long-term industrial functions in the area.
4.3. Technical Replicability and Applicability Boundaries
4.4. Research Limitations and Future Work
5. Conclusions
- Under typical IT load conditions, the submerged liquid cooling system reduces cooling energy consumption by 42.5–64.3%, maintaining an annual average PUE of 1.06–1.15, outperforming traditional liquid cooling systems;
- Compared to conventional cooling-tower-based systems, the proposed system achieves a 37.7–75.1% reduction in annual carbon emissions, with peak decarbonization rates reaching 50.1% in optimal operating scenarios;
- The heat exchange model was validated using TRNSYS simulation against MATLAB-calculated data, with a deviation of less than 3% in most operating conditions, demonstrating strong thermal accuracy;
- The spatial configuration supports both submerged deployment and shoreline access, making it suitable for redeveloping post-mining water zones and reactivating underutilized regional infrastructure.
- (1)
- Empirical validation: Close the modeling loop with pilot-scale operational data to verify thermal performance and structural durability under real-world conditions.
- (2)
- Energy integration: Explore coupling with clean energy systems such as photovoltaics, storage, or micro-grids to enhance overall system sustainability.
- (3)
- Life-cycle analysis: Conduct comprehensive life-cycle carbon and economic assessments that include construction, operation, and end-of-life phases.
- (4)
- Environmental assessment: Evaluate potential ecological impacts of continuous heat rejection on aquatic ecosystems and propose mitigation strategies.
- (5)
- Policy alignment: At the policy level, the proposed system demonstrates how China’s dual-carbon strategy can be advanced through both industrial decarbonization and adaptive spatial planning. By reactivating subsidence lakes as productive assets, the approach provides a model for integrating ecological restoration with digital infrastructure, aligning with national targets for energy efficiency and sustainable land use.
Author Contributions
Funding
Data Availability Statement
Acknowledgments
Conflicts of Interest
Abbreviations
PUE | Power Usage Effectiveness |
ICT | Information and Communication Technology |
CDU | Coolant Distribution Unit |
TRNSYS | Transient System Simulation Tool |
LCA | Life Cycle Assessment |
CO2 | Carbon Dioxide |
kW | Kilowatt |
kWh | Kilowatt-Hour |
R-1234ze | Refrigerant Type R-1234ze |
IT | Information Technology |
Nomenclature | |
Qrack | The heat dissipation rate of a single server rack (W) |
ṁcl | The mass flow rate of the coolant (kg/s) |
ccl | The specific heat capacity of the coolant (J/kg·K) |
Tcl,out | The outlet temperatures of the coolant (°C) |
Tcl,in | The inlet temperatures of the coolant (°C) |
QCDU | The heat transfer rate across the CDU (W) |
UCDU | The overall heat transfer coefficient (W/m2·K) |
ACDU | The heat transfer area of the CDU (m2) |
ΔTlm,CDU | The logarithmic mean temperature difference (LMTD) between the coolant and cooling water |
Qexchanger | The heat transfer from cooling water to the external subsided water (W) |
Uplate | The plate exchanger’s heat transfer coefficient (W/m2·k) |
Aplate | The effective surface area of the plate heat exchanger (m2) |
ΔTHE | The temperature difference between cooling water and the surrounding water body (K) |
The total rated power of 32 cooling tower fans (kW) | |
ηload | A load ratio estimated based on the proportion of thermal load (%) |
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Parameter Type | Value |
---|---|
Water depth of subsidence area | 20 m |
Hydrostatic pressure of subsidence water | 196.5 kPa |
Server specification | 1U (half-height) |
Specific heat capacity of coolant | 1402.58 kJ/kg·K |
Coolant density | 1146.92 kg/m3 |
Coolant pipe specification | DN80 (inner diameter: 0.080 m) |
Internal flow path length of CDU heat exchanger | 15 m |
Dynamic viscosity of coolant | 0.00047 Pa·s |
Total local resistance coefficient of coolant | 8.7 |
Heat transfer area of CDU | 17 m2 |
Specific heat capacity of cooling water | 4180 J/kg·K |
Cooling water density | 997 kg/m3 |
Cooling water pipe specification | DN40 (inner diameter: 0.040 m) |
Heat transfer area of wall-mounted plate heat exchanger | 32.84 m2 |
Dynamic viscosity of cooling water | 0.000715 Pa·s |
Thermal conductivity of cooling water | 0.63 W/m·K |
Carbon emission intensity | 0.6782 kg CO2/kWh [47] |
Variable Type | Season | Value |
---|---|---|
Flow velocity of subsidence water | Annual | 0.1–0.5 m/s [48,49] |
Mixed-layer water temperature of subsidence area | Annual | 15.91 °C |
Summer | 26.91 °C | |
Winter | 3.73 °C | |
Mixed-layer water temperature range | Summer | 24.38–28.18 °C |
Winter | 2.65–4.39 °C | |
Overall-layer average water temperature | Annual | 15.82 °C |
Summer | 26.65 °C | |
Winter | 3.74 °C | |
Overall-layer water temperature range | Summer | 24.24–28.10 °C |
Winter | 2.65–4.42 °C | |
Water density of subsidence area | Annual | 1000.024–1000.048 kg/m3 |
Server power consumption | 600–850 W | |
Rack-level power consumption | 55.2–78.2 kW | |
Coolant inlet temperature at CDU side | 40.0–48.0 °C | |
Coolant outlet temperature at CDU side | 30.0–35.0 °C | |
Coolant temperature difference (inlet–outlet) | 5.0–18.0 K | |
Cooling water inlet temperature at CDU side | Summer | 26.24–32.10 °C |
Winter | 4.65–8.42 °C | |
Cooling water outlet temperature at CDU side | Annual | 35.0–38.0 °C |
Cooling water temperature difference (plate HX side) | Summer | 2.9–11.8 K |
Winter | 26.58–33.35 K | |
Coolant flow rate | Annual | 34.31–350.01 L/min |
Coolant velocity range | 0.1138–1.1605 m/s | |
Coolant total pressure drop | 0.1006–8.8198 kPa | |
CDU heat transfer coefficient | 2000–3000 W/m2·K | |
Cooling water temperature rise | 2.9–33.35 K | |
Cooling water flow rate | 11.8–230.57 L/min | |
Cooling water velocity range | 0.0122–0.4650 m/s | |
Heat transfer coefficient (cooling water side of plate HX) | 232.22–5670.88 W/m2·K | |
Heat transfer coefficient (subsidence water side of plate HX) | 290–1460 W/m2·K | |
Overall heat transfer coefficient of plate HX | 280–1230 W/m2·K |
Calculated Heat Load (kW) | Waste Heat Recovery Rate (%) | Heat Exchange Temperature Difference (K) | Coolant Mass Flow Rate (kg/s) | Simulated Heat Load (kW) |
---|---|---|---|---|
55.20000 | 0.00000 | 18.00000 | 2.18645 | 55.20008 |
55.20000 | 0.00000 | 5.00000 | 7.87121 | 55.20001 |
33.20000 | 40.00000 | 18.00000 | 1.31187 | 33.12005 |
33.20000 | 40.00000 | 5.00000 | 4.72273 | 33.12003 |
27.20000 | 50.00000 | 18.00000 | 1.09322 | 27.59991 |
27.20000 | 50.00000 | 5.00000 | 3.93560 | 27.59996 |
16.20000 | 70.00000 | 18.00000 | 0.65593 | 16.55990 |
16.20000 | 70.00000 | 5.00000 | 2.36136 | 16.55998 |
78.20000 | 0.00000 | 18.00000 | 3.09747 | 78.20009 |
78.20000 | 0.00000 | 5.00000 | 11.15088 | 78.20001 |
47.20000 | 40.00000 | 18.00000 | 1.85848 | 46.92000 |
47.20000 | 40.00000 | 5.00000 | 6.69053 | 46.92002 |
39.20000 | 50.00000 | 18.00000 | 1.54873 | 39.09992 |
39.20000 | 50.00000 | 5.00000 | 5.57544 | 39.10000 |
23.20000 | 70.00000 | 18.00000 | 0.92924 | 23.46000 |
23.20000 | 70.00000 | 5.00000 | 3.34526 | 23.45997 |
System Type | Minimum Estimate | Maximum Estimate |
---|---|---|
Submerged Architecture | 24,598,080 | 61,495,200 |
Conventional Cooling Tower | 49,322,304 | 98,644,608 |
Scenario | Water Temperature (°C) | IT Load (% of Design) | Submerged System PUE | Cooling Energy Saving vs. Tower (%) | CO2 Reduction vs. Tower (%) |
---|---|---|---|---|---|
(A) Low-T water + high load | 5 | 95 | 1.06 | ~66 | ~75 |
(B) High-T water + low load | 25 | 40 | 1.15–1.18 | ~40–45 | ~46–52 |
(C) Baseline | 15 | 70 | 1.10–1.12 | ~55 | ~60 |
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Share and Cite
Hu, Y.; Tang, Y.; Ji, X.; Chen, Y. A Submerged Building Strategy for Low-Carbon Data Centers in Coal Mining Subsidence Areas: System Design and Energy–Carbon Performance Assessment. Buildings 2025, 15, 3148. https://doi.org/10.3390/buildings15173148
Hu Y, Tang Y, Ji X, Chen Y. A Submerged Building Strategy for Low-Carbon Data Centers in Coal Mining Subsidence Areas: System Design and Energy–Carbon Performance Assessment. Buildings. 2025; 15(17):3148. https://doi.org/10.3390/buildings15173148
Chicago/Turabian StyleHu, Yixiao, Yuben Tang, Xiang Ji, and Yidong Chen. 2025. "A Submerged Building Strategy for Low-Carbon Data Centers in Coal Mining Subsidence Areas: System Design and Energy–Carbon Performance Assessment" Buildings 15, no. 17: 3148. https://doi.org/10.3390/buildings15173148
APA StyleHu, Y., Tang, Y., Ji, X., & Chen, Y. (2025). A Submerged Building Strategy for Low-Carbon Data Centers in Coal Mining Subsidence Areas: System Design and Energy–Carbon Performance Assessment. Buildings, 15(17), 3148. https://doi.org/10.3390/buildings15173148