HVAC Systems Encyclopedia

A comprehensive encyclopedia of heating, ventilation, and air conditioning systems

Direct Expansion Evaporators

Direct expansion (DX) evaporators absorb heat from air or fluids by evaporating liquid refrigerant directly within the heat exchanger tubes. Unlike flooded evaporators, DX coils meter refrigerant flow through expansion devices to match system load, achieving complete evaporation before refrigerant exits the coil.

Fin-Tube Coil Construction

Fin-tube coils represent the dominant DX evaporator design in HVAC applications. Copper tubes carry refrigerant while aluminum fins bonded to tube surfaces increase heat transfer area. Fin density ranges from 8 to 16 fins per inch depending on application:

  • Commercial refrigeration: 8-10 FPI minimizes frost accumulation
  • Air conditioning: 12-14 FPI balances capacity and pressure drop
  • High-efficiency systems: 14-16 FPI maximizes surface area for low-temperature differentials

Tube diameter selection impacts refrigerant velocity and oil return. Standard configurations use 3/8 inch or 1/2 inch OD copper tubing. Smaller diameters maintain higher velocities for proper oil entrainment but increase pressure drop. Larger tubes reduce friction losses at the expense of velocity.

Coil Geometry and Performance

Face velocity through the coil directly influences heat transfer coefficient and moisture removal. Recommended face velocities vary by application:

ApplicationFace Velocity RangeNotes
Air conditioning300-500 fpmStandard comfort cooling
Dehumidification250-350 fpmEnhanced moisture removal
Walk-in coolers400-600 fpmHigher velocities acceptable
Process cooling200-400 fpmPrecision temperature control

Excessive face velocity increases air-side pressure drop and can cause moisture carryover. Insufficient velocity reduces heat transfer effectiveness and increases coil depth requirements.

Row depth determines refrigerant-side pressure drop and heat transfer capacity. Configurations range from 2 to 8 rows:

  • 2-3 rows: Minimal pressure drop, common in residential AC
  • 4-6 rows: Balanced performance for commercial applications
  • 6-8 rows: Maximum capacity in limited face area installations

Each additional row increases capacity but also refrigerant pressure drop. Excessive depth causes significant saturation temperature reduction across the coil, reducing system efficiency.

Fin spacing balances heat transfer surface area against airflow resistance and frost accumulation. Standard spacings include:

  • 8 FPI: Low-temperature refrigeration, heavy frost conditions
  • 10 FPI: Medium-temperature refrigeration, moderate frost
  • 12 FPI: Air conditioning, minimal frost concerns
  • 14-16 FPI: High-efficiency AC, no frost operation

Tighter fin spacing increases sensible capacity but requires more frequent defrost in refrigeration applications.

Refrigerant Distribution Systems

Proper refrigerant distribution ensures uniform flow across all coil circuits. Liquid refrigerant from the expansion device enters a distributor that divides flow into multiple tubes. Distribution quality directly affects coil capacity and superheat stability.

Distributor types include:

Orifice distributors use fixed-size holes to split refrigerant flow based on pressure drop. Simple and reliable, but sensitive to liquid level and flash gas distribution. Typically applied in residential and light commercial systems.

Venturi distributors incorporate converging-diverging nozzles that create pressure differentials to distribute refrigerant. Superior performance across varying load conditions. Flash gas distribution remains a challenge.

Nozzle distributors employ precisely machined orifices that create high-velocity jets for improved atomization and distribution. Most effective for maintaining equal flow to all circuits under variable conditions.

Distributor tube length affects distribution quality. Tubes should extend 12-24 inches to allow full expansion and mixing before entering coil circuits. Excessive length increases pressure drop without improving distribution.

Circuit Design Strategies

Circuit arrangement determines refrigerant path through the coil. Two primary configurations exist:

Interlaced circuits alternate tube passes from different circuits throughout coil depth. This arrangement provides uniform air-side temperature distribution and balanced heat transfer across all circuits. Refrigerant pressure drop increases compared to face-split designs.

Face-split circuits divide the coil face into sections, with each circuit handling one section. Simpler manifold construction and lower pressure drop characterize this design. Air-side temperature stratification can occur across the coil face.

Circuit quantity balances refrigerant velocity, pressure drop, and distribution quality. Typical circuit counts range from 2 to 12 depending on coil size:

  • 2-4 circuits: Small capacity units (≤5 tons)
  • 4-8 circuits: Medium commercial units (5-20 tons)
  • 8-12 circuits: Large commercial units (>20 tons)

Excessive circuits reduce refrigerant velocity and compromise oil return. Insufficient circuits cause high pressure drop and capacity reduction.

Superheat Control Methods

Superheat represents the temperature increase of refrigerant vapor above saturation temperature. Proper superheat control prevents liquid refrigerant from entering the compressor while maximizing evaporator capacity.

Thermostatic expansion valves (TXV) mechanically modulate refrigerant flow based on evaporator superheat. Bulb pressure proportional to suction line temperature actuates valve position against spring force and evaporator pressure. Target superheat typically ranges from 8-12°F for standard applications.

TXV advantages include independence from electrical systems and proven reliability. Disadvantages include slower response to load changes and potential hunting under light load conditions.

Electronic expansion valves (EEV) use stepper motors or pulse-width modulated solenoids to adjust orifice position. Controllers monitor suction temperature and pressure to calculate real-time superheat and adjust valve position accordingly.

EEV systems provide faster response, precise control under varying loads, and ability to maintain lower superheat for increased capacity. Target superheat of 4-8°F achieves maximum evaporator utilization.

Hunting phenomenon occurs when control devices oscillate rather than stabilize at setpoint. Oversized valves, excessive static superheat, or improper bulb location cause hunting. Reducing valve capacity or increasing static superheat spring pressure typically resolves hunting issues.

Face Velocity and Air-Side Design

Air velocity across coil faces affects both sensible and latent heat transfer. Velocity directly influences the air-side heat transfer coefficient according to:

h = C × V^0.8

Where h represents heat transfer coefficient, V is velocity, and C is a constant depending on fin geometry.

Higher velocities increase sensible capacity but reduce moisture removal effectiveness. The ratio of sensible to total capacity (sensible heat ratio) decreases as face velocity increases due to shorter air contact time.

Recommended practice limits face velocity based on application requirements. Dehumidification applications require longer air residence time achieved through lower face velocities. Process cooling demanding tight temperature control benefits from reduced velocities that enhance temperature approach.

Defrost Methods

Frost accumulation on evaporator surfaces insulates fins and tubes, reducing heat transfer capacity. When coil surface temperature drops below 32°F and moisture contacts surfaces, frost forms. Regular defrost cycles maintain system capacity.

Hot gas defrost diverts high-temperature discharge gas from the compressor through the evaporator. Condensing refrigerant rapidly melts frost. Defrost cycles typically complete in 10-20 minutes. This method proves most efficient for medium and low-temperature refrigeration.

Hot gas defrost requires additional piping, valves, and controls. Discharge gas enters the evaporator outlet, flowing reverse direction through coils. Trapped liquid must drain before restarting refrigeration to prevent compressor slugging.

Electric defrost employs resistance heaters mounted near coil surfaces. Electric current generates heat that melts frost. Simple installation and precise heat application characterize this method. Higher operating cost compared to hot gas defrost limits application to smaller systems or locations where hot gas defrost is impractical.

Heater capacity typically ranges from 300-800 watts per ton of refrigeration capacity. Defrost duration extends 20-30 minutes due to lower heat flux compared to hot gas methods.

Off-cycle defrost relies on ambient air temperature above 32°F to melt frost when the compressor shuts off. Fans may continue operating to accelerate melting. This passive method works only in medium-temperature applications where space temperature exceeds freezing.

Off-cycle defrost incurs no additional equipment cost but results in longer defrost periods and product temperature increase in refrigerated spaces.

Defrost initiation methods include:

  • Time-based: Fixed intervals (6-12 hours typical)
  • Demand defrost: Monitors coil performance parameters
  • Temperature-based: Initiates when coil temperature drops indicating frost buildup

Termination typically occurs when coil temperature reaches 45-60°F, indicating complete frost removal.

Applications

Air conditioning systems employ DX evaporators in residential split systems, rooftop units, and packaged equipment. Coil face areas range from 2-6 square feet per ton of cooling capacity. Standard operating conditions maintain coil temperatures 35-45°F, well above freezing under normal humidity conditions.

Multi-circuit designs ensure uniform air-side temperature distribution. Electronic expansion valves increasingly replace TXVs in higher-efficiency systems requiring precise capacity modulation.

Commercial refrigeration applications include walk-in coolers, reach-in cases, and display fixtures. Medium-temperature systems (28-40°F coil temperature) require periodic defrost. Low-temperature systems (below 0°F) demand frequent defrost cycles and wide fin spacing to accommodate frost accumulation.

Unit coolers, also called evaporator coils, suspend from ceilings in walk-in boxes. Face velocities of 500-800 fpm overcome temperature stratification in large spaces. Multiple fan speeds optimize efficiency across varying load conditions.

Transport refrigeration utilizes compact DX evaporators in trucks, trailers, and shipping containers. Vibration-resistant construction and brazed joints prevent refrigerant leaks. Tight fin spacing maximizes capacity in space-constrained installations.

Defrost challenges intensify in transport applications due to varying ambient conditions and frequent door openings introducing moisture. Electric defrost predominates due to system simplicity despite higher energy consumption.