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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│
│ │
└────────────────────────────────────────────────────┘
ComponentFunction
Capture hoodCaptures hot air from compressor
DuctsTransport the air
DampersDirect flow
Booster fanOvercomes long duct resistance
FilterCleans return air
ThermostatAutomatic control

Capacity Calculation

Available heat (BTU/h):

Q=V˙×ρ×Cp×ΔT×60Q = \dot{V} \times \rho \times C_p \times \Delta T \times 60

Where:

  • V˙\dot{V} = Air flow (CFM)
  • ρ\rho = Density (0.075 lb/ft³)
  • CpC_p = Specific heat (0.24 BTU/lb·°F)
  • ΔT\Delta T = Temperature rise (°F)

Example (100 HP compressor):

  • V˙=3,000\dot{V} = 3{,}000 CFM (compressor fan)
  • ΔT=40°F\Delta T = 40°F (from 70°F to 110°F)
Q=3,000×0.075×0.24×40×60=129,600 BTU/h38 thermal kWQ = 3{,}000 \times 0.075 \times 0.24 \times 40 \times 60 = 129{,}600 \text{ BTU/h} \approx 38 \text{ thermal kW}

Duct Sizing

CFMDuct DiameterVelocity
1,00012"1,300 fpm
2,00016"1,400 fpm
3,00020"1,400 fpm
5,00024"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

TypeAdvantagesDisadvantages
PlateCompact, efficient, cleanableMedium cost
Shell and tubeRobust, economicalLarge, less efficient
Double pipeSimple, low costLow capacity

Plate Heat Exchanger

       Hot oil inlet

┌─────────▼─────────┐
│ ║ ║ ║ ║ ║ │
│ ║ ║ ║ ║ ║ │◄── Corrugated plates
│ ║ ║ ║ ║ ║ │
│ ║ ║ ║ ║ ║ │
└─────────┬─────────┘

Cold oil outlet

Cold water ──────────────► Hot water

Typical specifications:

ParameterValue
Approach temperature9-18°F
Oil pressure drop7-29 psi
Water pressure drop4-15 psi
Fouling factor0.0001-0.0002

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

AspectAir RecoveryWater Recovery
Initial costLowMedium-High
InstallationSimpleComplex
Transport distanceLimited (100-160 ft)Long (330+ ft)
Temperature104-140°F131-158°F
StorageNoYes (tank)
Summer useDifficultPossible (hot water)
MaintenanceMinimalMedium
Efficiency70-85%80-95%

Project Example

System Data

ParameterValue
Compressor150 HP (112 kW)
Operation6,000 h/year
Recoverable heat80% = 90 kW
Current fuelNatural gas
Gas cost$12/MMBTU
Boiler efficiency85%

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:

  1. Match between heat availability and demand
  2. Distance between compressor and point of use
  3. Process temperature requirements
  4. Summer operation (if applicable)