Recovery Systems
There are two main approaches to recovering heat from compressors: hot air recovery and water-based recovery.
Air Recovery
Principle
The compressor's cooling air is directed to spaces requiring heating:
COMPRESSOR ROOM AREA TO HEAT
┌─────────────────┐ ┌─────────────────┐
│ │ │ │
│ ┌───────────┐ │ Insulated │ │
│ │Compressor │══════════════════════► │
│ │ │ │ duct │ Hot │
│ └───────────┘ │ │ air │
│ │ │ 122-140°F │
│ Air 68°F ←───────────────────────────────────│
│ (return) │ │ │
│ │ │ │
└─────────────────┘ └─────────────────┘
Components
Duct system:
┌────────────────────────────────────────────────────┐
│ │
│ Outdoor Indoor Centrifugal Compressor │
│ damper damper fan │
│ │ │ │ │ │
│ ▼ ▼ ▼ ▼ │
│ ═══════════════════════════════════════════════ │
│ ↑ ↑ ↑ ↑ │
│ Outdoor Indoor Forced Hot air │
│(summer) (winter) boost from compressor│
│ │
└────────────────────────────────────────────────────┘
| Component | Function |
|---|---|
| Capture hood | Captures hot air from compressor |
| Ducts | Transport the air |
| Dampers | Direct flow |
| Booster fan | Overcomes long duct resistance |
| Filter | Cleans return air |
| Thermostat | Automatic control |
Capacity Calculation
Available heat (BTU/h):
Where:
- = Air flow (CFM)
- = Density (0.075 lb/ft³)
- = Specific heat (0.24 BTU/lb·°F)
- = Temperature rise (°F)
Example (100 HP compressor):
- CFM (compressor fan)
- (from 70°F to 110°F)
Duct Sizing
| CFM | Duct Diameter | Velocity |
|---|---|---|
| 1,000 | 12" | 1,300 fpm |
| 2,000 | 16" | 1,400 fpm |
| 3,000 | 20" | 1,400 fpm |
| 5,000 | 24" | 1,600 fpm |
Rule: Maintain velocity between 1,000-2,000 fpm for low noise.
Water Recovery
Basic System
┌─────────────────────────────────────────────────────────┐
│ HOT WATER SYSTEM │
│ │
│ Oil ┌──────────────┐ Water │
│ 194°F ═════│Plate heat │═══════► 131°F │
│ │ exchanger │ │
│ 122°F ◄════│ │◄═══════ 59°F │
│ └──────┬───────┘ (inlet) │
│ │ │
│ │ Control │
│ │ │
│ ┌──────┴───────┐ │
│ │ 3-way │ │
│ │ valve │ │
│ └──────────────┘ │
│ │
└─────────────────────────────────────────────────────────┘
Heat Exchanger Types
| Type | Advantages | Disadvantages |
|---|---|---|
| Plate | Compact, efficient, cleanable | Medium cost |
| Shell and tube | Robust, economical | Large, less efficient |
| Double pipe | Simple, low cost | Low capacity |
Plate Heat Exchanger
Hot oil inlet
│
┌─────────▼─────────┐
│ ║ ║ ║ ║ ║ │
│ ║ ║ ║ ║ ║ │◄── Corrugated plates
│ ║ ║ ║ ║ ║ │
│ ║ ║ ║ ║ ║ │
└─────────┬─────────┘
│
Cold oil outlet
Cold water ──────────────► Hot water
Typical specifications:
| Parameter | Value |
|---|---|
| Approach temperature | 9-18°F |
| Oil pressure drop | 7-29 psi |
| Water pressure drop | 4-15 psi |
| Fouling factor | 0.0001-0.0002 |
System Control
Thermostat
│
▼
┌──────────────────────────────────────┐
│ │
│ Hot oil ══════╗ │
│ ║ │
│ ║ │
│ ┌────╨────┐ │
│ │ 3-way │ │
│ │ valve │ │
│ └────┬────┘ │
│ │ │
│ ┌───────────┼───────────┐ │
│ │ │ │ │
│ ▼ ▼ ▼ │
│ Bypass Exchanger Mixed │
│ (if water (heat (proportional│
│ too cold) demand) control) │
│ │
└──────────────────────────────────────┘
Specific Applications
Boiler Feedwater Preheat
Boiler
│
Feedwater ──────────┤
59°F │
│
┌───────────────────┴───────────────────┐
│ │
│ With recovery: │
│ │
│ Water 59°F ──► Exchanger ──► 140°F ──► Boiler
│ ▲ │
│ │ │
│ Compressor Savings:
│ oil 40-60%
│ preheat fuel
│
└────────────────────────────────────────────┘
Domestic Hot Water
┌─────────────────────────────────────────────────────┐
│ │
│ Municipal Heat Storage │
│ cold water ──► exchanger ──► tank │
│ │ │ │ │
│ │ │ │ │
│ │ Compressor │ │
│ │ oil │ │
│ │ ▼ │
│ │ Hot water │
│ │ for use │
│ │ (showers, washing) │
│ │ │ │
│ │ │ │
│ └────── Recirculation ◄────────┘ │
│ │
└─────────────────────────────────────────────────────┘
Radiant Floor Heating
Exchanger ──► Pump ──► Manifold ──► Floor coils
│ │ │
│ │ │
Compressor Zone Comfort
oil control 104-113°F
Comparison
| Aspect | Air Recovery | Water Recovery |
|---|---|---|
| Initial cost | Low | Medium-High |
| Installation | Simple | Complex |
| Transport distance | Limited (100-160 ft) | Long (330+ ft) |
| Temperature | 104-140°F | 131-158°F |
| Storage | No | Yes (tank) |
| Summer use | Difficult | Possible (hot water) |
| Maintenance | Minimal | Medium |
| Efficiency | 70-85% | 80-95% |
Project Example
System Data
| Parameter | Value |
|---|---|
| Compressor | 150 HP (112 kW) |
| Operation | 6,000 h/year |
| Recoverable heat | 80% = 90 kW |
| Current fuel | Natural gas |
| Gas cost | $12/MMBTU |
| Boiler efficiency | 85% |
Savings Calculation
Annual thermal energy:
Q = 90 kW × 6,000 h = 540,000 kWh/year
= 1,843 MMBTU/year
Gas equivalent cost:
= 1,843 MMBTU × $12 / 0.85
= $26,014/year
Investment (water system):
= $25,000
Simple payback:
= $25,000 / $26,014
= 0.96 years ≈ 12 months
Pre-Investment Evaluation
Before investing, verify:
- Match between heat availability and demand
- Distance between compressor and point of use
- Process temperature requirements
- Summer operation (if applicable)