Carbon Sequestration in HVAC Systems
Carbon Sequestration in HVAC Systems
Carbon sequestration technologies integrated with HVAC systems represent an emerging approach to achieve net-negative carbon emissions in buildings. These systems actively remove CO₂ from the atmosphere or capture it from building exhaust streams, converting atmospheric carbon into stable forms for long-term storage.
Direct Air Capture Integration
Direct air capture (DAC) systems can be integrated with building HVAC equipment to remove CO₂ directly from ventilation air streams. The fundamental mass transfer equation governing CO₂ absorption is:
$$N_{CO_2} = k_L a (C_{bulk} - C_{interface})$$
Where:
- $N_{CO_2}$ = CO₂ mass transfer rate (kg/m³·s)
- $k_L$ = liquid-phase mass transfer coefficient (m/s)
- $a$ = interfacial area per unit volume (m²/m³)
- $C_{bulk}$ = bulk CO₂ concentration (kg/m³)
- $C_{interface}$ = interfacial CO₂ concentration (kg/m³)
Absorption Technologies
| Technology | Capture Efficiency | Energy Penalty | Regeneration Temperature | Chemical Stability |
|---|---|---|---|---|
| Amine scrubbing | 85-95% | 2.5-4.0 GJ/tCO₂ | 120-150°C | Moderate (degradation) |
| Solid sorbent | 75-90% | 1.8-3.2 GJ/tCO₂ | 80-120°C | High |
| Membrane separation | 60-85% | 1.2-2.8 GJ/tCO₂ | N/A | Very high |
| Cryogenic separation | 90-98% | 2.0-3.5 GJ/tCO₂ | -100 to -50°C | N/A |
The energy required for DAC scales with atmospheric CO₂ concentration according to thermodynamic limits:
$$W_{min} = RT \ln\left(\frac{P_{pure}}{P_{atm}}\right)$$
Where:
- $W_{min}$ = minimum separation work (kJ/mol)
- $R$ = universal gas constant (8.314 J/mol·K)
- $T$ = absolute temperature (K)
- $P_{pure}$ = pure CO₂ pressure (Pa)
- $P_{atm}$ = atmospheric CO₂ partial pressure (Pa)
At 420 ppm atmospheric CO₂, the theoretical minimum energy is approximately 20 kJ/mol (250 kJ/kg CO₂). Practical systems require 1,500-2,500 kJ/kg due to thermodynamic inefficiencies.
HVAC System Integration Strategies
graph TD
A[Outdoor Air Intake] --> B[DAC Module]
B --> C[Heat Recovery]
C --> D[Cooling Coil]
D --> E[Building Distribution]
E --> F[Return Air]
F --> G{Exhaust or Recirculate}
G -->|Exhaust| H[CO₂ Concentration Analysis]
H --> I[Supplemental Capture]
I --> J[Atmosphere]
G -->|Recirculate| C
B --> K[Sorbent Regeneration]
K --> L[CO₂ Storage/Utilization]
M[Waste Heat Source] --> K
N[Building Thermal System] -.->|Optional Heat Recovery| M
Integration Points
Supply Air Path: DAC modules positioned upstream of cooling coils reduce CO₂ concentration in ventilation air from 420 ppm to 200-300 ppm. This approach provides continuous sequestration proportional to ventilation rate:
$$\dot{m}{CO_2} = \dot{V} \cdot \rho \cdot (C{in} - C_{out})$$
Where:
- $\dot{m}_{CO_2}$ = CO₂ capture rate (kg/s)
- $\dot{V}$ = ventilation rate (m³/s)
- $\rho$ = air density (kg/m³)
- $C_{in}$ = inlet CO₂ concentration (kg/kg)
- $C_{out}$ = outlet CO₂ concentration (kg/kg)
Exhaust Air Path: Capturing CO₂ from exhaust air streams offers higher concentrations (800-1,200 ppm in occupied spaces) reducing separation energy by 40-60% compared to outdoor air capture.
Dedicated Systems: Standalone sequestration units operate independently from HVAC, using building waste heat for sorbent regeneration. These systems decouple sequestration from ventilation requirements.
Mineralization and Material Sequestration
Building materials incorporating captured CO₂ provide permanent sequestration through mineralization reactions. Concrete carbonation follows:
$$Ca(OH)_2 + CO_2 \rightarrow CaCO_3 + H_2O$$
This reaction sequesters 0.79 kg CO₂ per kg Ca(OH)₂, storing carbon in stable calcium carbonate form with million-year permanence.
Carbon-Curing Concrete
| Parameter | Conventional Concrete | Carbon-Cured Concrete | Improvement |
|---|---|---|---|
| Curing time | 28 days | 24 hours | 96% reduction |
| Compressive strength | Baseline | +10 to +20% | Enhanced |
| CO₂ uptake | 0.05 kg/kg | 0.15-0.25 kg/kg | 3-5× increase |
| Embodied carbon | 0.15 kg CO₂/kg | 0.05-0.08 kg CO₂/kg | 50-65% reduction |
Performance Metrics and Assessment
ASHRAE Standard 228-2023 establishes protocols for quantifying building-integrated carbon sequestration. Key metrics include:
Net Carbon Capture Rate:
$$NCR = \dot{m}{captured} - \dot{m}{operational} - \dot{m}_{embodied}$$
Where:
- $NCR$ = net carbon reduction (kg CO₂/year)
- $\dot{m}_{captured}$ = annual CO₂ captured (kg/year)
- $\dot{m}_{operational}$ = operational emissions from sequestration energy (kg/year)
- $\dot{m}_{embodied}$ = annualized embodied carbon (kg/year)
Carbon Capture Efficiency:
$$\eta_c = \frac{\text{CO₂ captured}}{\text{CO₂ emitted for capture energy}} \times 100%$$
Viable building-integrated systems require $\eta_c > 300%$ to justify energy investment. Systems powered by on-site renewable energy or utilizing waste heat achieve $\eta_c$ values of 500-800%.
System Energy Considerations
Regeneration of chemical sorbents dominates energy consumption. Heat integration with building systems reduces parasitic loads:
- Absorption chillers: Waste heat from generator (85-95°C) regenerates low-temperature sorbents
- CHP systems: Exhaust heat (120-180°C) drives medium-temperature regeneration
- Heat pump condensers: Rejected heat (40-55°C) pre-heats regeneration air streams
- Solar thermal: Concentrated solar provides 150-250°C for high-efficiency regeneration
Temperature-swing adsorption efficiency is:
$$\eta_{TSA} = \frac{q_{ads} - q_{des}}{Q_{heating} + W_{compression}}$$
Where:
- $q_{ads}$ = heat of adsorption (kJ/kg)
- $q_{des}$ = heat of desorption (kJ/kg)
- $Q_{heating}$ = regeneration heating energy (kJ/kg)
- $W_{compression}$ = compression work (kJ/kg)
Implementation Framework
Design Phase:
- Quantify building carbon emissions (operational and embodied)
- Assess available waste heat sources and temperatures
- Size capture system for target sequestration rate
- Integrate with HVAC control sequences
- Evaluate storage or utilization pathways for captured CO₂
Operational Phase:
- Monitor capture rates and energy consumption
- Optimize regeneration cycles based on heat availability
- Verify sequestration through third-party protocols
- Adjust operation for grid carbon intensity variations
Economic Analysis: Life-cycle cost analysis must account for carbon credit revenue, avoided emissions costs, and energy penalties. Current capture costs range from $150-400 per tonne CO₂ for building-integrated systems, compared to $600-1,000 for industrial DAC facilities. Integration with existing HVAC infrastructure reduces capital costs by 35-50%.
Building-integrated carbon sequestration transitions HVAC systems from carbon-neutral to carbon-negative operation, supporting aggressive decarbonization targets aligned with ASHRAE’s 2030 commitment and net-zero building standards.