HVAC Systems Encyclopedia

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

IQF Berry Processing

IQF Technology Overview

Individual Quick Freezing (IQF) represents the most advanced freezing method for berry processing, producing free-flowing frozen fruit with superior quality retention. The process freezes individual berries rapidly at temperatures between -35°C and -45°C (-31°F to -49°F) using high-velocity air circulation. This rapid freezing creates small ice crystals that minimize cellular damage, preserving texture, flavor, and nutritional content.

The fundamental principle relies on maximizing heat transfer coefficient through turbulent airflow while minimizing freezing time to cross the critical temperature zone of 0°C to -5°C (32°F to 23°F) as quickly as possible.

Freezer System Types

Fluidized Bed Freezers

Fluidized bed systems suspend individual berries on a cushion of high-velocity cold air, providing optimal heat transfer through complete surface exposure. Air velocity must exceed the terminal velocity of the berry to achieve fluidization while preventing excessive product damage.

Design Parameters:

  • Air velocity: 4-8 m/s (800-1600 fpm) depending on berry size
  • Air temperature: -35°C to -40°C (-31°F to -40°F)
  • Bed depth: 25-75 mm (1-3 inches)
  • Retention time: 8-15 minutes for small berries
  • Fluidization pressure drop: 150-400 Pa (0.6-1.6 in. w.g.)

Belt Freezers

Continuous belt freezers transport berries through multiple zones of refrigerated air, with the product spread in a thin layer on a perforated or mesh belt. Air flows perpendicular to the belt, providing consistent cooling across the product layer.

Belt Freezer Specifications:

ParameterSpecificationNotes
Belt width1.0-2.5 m (40-100 in)Capacity dependent
Belt speed0.5-2.0 m/min (1.6-6.6 ft/min)Product specific
Layer thickness20-50 mm (0.8-2.0 in)Single layer preferred
Air velocity3-6 m/s (600-1200 fpm)Through product layer
Temperature zones2-4 zonesProgressive cooling
Total residence time15-30 minutesBerry type dependent

Spiral Freezers

Spiral belt systems maximize freezing capacity within limited floor space by stacking the conveyor belt in a helical configuration. The system provides continuous operation with consistent product quality.

Critical Design Factors:

  • Tier spacing: 300-450 mm (12-18 inches)
  • Spiral diameter: 3-10 m (10-33 ft)
  • Total belt length: 50-150 m (165-490 ft)
  • Air distribution: Horizontal across tiers
  • Refrigeration capacity: 100-500 kW (28-140 tons)

Tunnel Freezer Design

Tunnel freezers provide linear product flow through refrigerated zones, suitable for batch or continuous processing. Design requires careful attention to air distribution, velocity control, and temperature uniformity.

Air Distribution System

Supply Air Configuration:

  • Ceiling-mounted diffusers with adjustable louvers
  • Lateral supply ducts for cross-flow patterns
  • Perforated floors for upward air flow through product
  • Combined systems for enhanced heat transfer

Return Air System:

  • Multiple return air points to minimize temperature stratification
  • Adjustable dampers for zone balancing
  • Evaporator coil placement for optimal defrost management

Temperature and Velocity Requirements

Zone-Specific Parameters:

ZoneAir TemperatureAir VelocityPurpose
Pre-cooling-15°C to -20°C (5°F to -4°F)2-3 m/s (400-600 fpm)Initial cooling
Primary freezing-35°C to -40°C (-31°F to -40°F)5-7 m/s (1000-1400 fpm)Rapid phase change
Final hardening-40°C to -45°C (-40°F to -49°F)3-5 m/s (600-1000 fpm)Core temperature reduction
Tempering-25°C to -30°C (-13°F to -22°F)2-3 m/s (400-600 fpm)Surface warming

Freezing Time Calculations

Freezing time depends on product geometry, initial temperature, final temperature, thermal properties, and heat transfer coefficient. For spherical berries, Plank’s equation provides a reasonable approximation.

Modified Plank’s Equation:

t = (ρ × L_f / (T_f - T_a)) × (P × D / h + R × D² / k)

Where:

  • t = freezing time (seconds)
  • ρ = product density (kg/m³)
  • L_f = latent heat of fusion (kJ/kg)
  • T_f = freezing point temperature (°C)
  • T_a = air temperature (°C)
  • P = shape factor (0.167 for sphere)
  • R = shape factor (0.042 for sphere)
  • D = characteristic dimension (m)
  • h = surface heat transfer coefficient (W/m²·K)
  • k = thermal conductivity of frozen product (W/m·K)

Berry-Specific Freezing Times

Typical Freezing Times at -40°C Air Temperature:

Berry TypeDiameterInitial TempFreezing TimeAir Velocity
Blueberries12-15 mm20°C (68°F)8-12 minutes6 m/s (1200 fpm)
Raspberries15-20 mm20°C (68°F)10-15 minutes5 m/s (1000 fpm)
Blackberries18-25 mm20°C (68°F)12-18 minutes5 m/s (1000 fpm)
Strawberries (sliced)10-15 mm thick15°C (59°F)10-14 minutes6 m/s (1200 fpm)
Strawberries (whole)25-35 mm15°C (59°F)18-25 minutes4 m/s (800 fpm)

Heat Transfer Coefficient

The surface heat transfer coefficient in IQF systems depends primarily on air velocity, product geometry, and surface characteristics.

Empirical Correlation for Forced Convection:

h = C × v^n

For berries in turbulent flow:

  • C = 15-25 (coefficient)
  • n = 0.6-0.8 (velocity exponent)
  • v = air velocity (m/s)

Typical values range from 40-120 W/m²·K (7-21 Btu/hr·ft²·°F) depending on air velocity and product arrangement.

Refrigeration System Requirements

Evaporator Coil Design

Specifications for IQF Systems:

  • Fin spacing: 4-6 mm (0.16-0.24 inches) to minimize frost buildup
  • Tube diameter: 16-25 mm (0.63-1.0 inches)
  • Face velocity: 2.5-4.0 m/s (500-800 fpm)
  • Temperature difference (TD): 8-12 K (14-22°F)
  • Defrost cycle: Hot gas or electric, every 6-12 hours

Refrigerant Selection

Low-Temperature Applications:

  • Ammonia (R-717): Most common for large installations
  • R-404A / R-507A: Phasing out due to GWP concerns
  • R-448A / R-449A: Lower GWP alternatives
  • R-744 (CO₂): Cascade systems for ultra-low temperatures

Compressor Capacity

Load Components:

  • Product load: 60-70% of total
  • Infiltration/air change: 10-15%
  • Equipment heat gain: 5-10%
  • Lighting and other: 5-10%
  • Defrost load: 5-10%

Product Quality Considerations

Ice Crystal Formation

Rapid freezing produces ice crystals of 30-50 μm diameter, compared to 100-200 μm for slow freezing. Smaller crystals minimize cell membrane rupture and preserve product integrity upon thawing.

Critical Temperature Zone: The range from 0°C to -5°C (32°F to 23°F) represents the maximum ice crystal formation zone. Transit time through this zone should be minimized to 10-15 minutes for optimal quality.

Drip Loss Prevention

Quality Metrics:

Freezing RateIce Crystal SizeDrip Loss on ThawingQuality Rating
Very rapid (IQF)30-50 μm3-5%Excellent
Rapid50-100 μm5-8%Good
Moderate100-150 μm8-12%Fair
Slow>150 μm>12%Poor

Color and Flavor Retention

Low-temperature processing and rapid freezing preserve anthocyanins and volatile flavor compounds. Storage at -23°C (-9°F) or below maintains quality for 18-24 months.

Process Control Parameters

Temperature Monitoring

Critical Measurement Points:

  • Product inlet temperature: ±1°C accuracy
  • Air supply temperature per zone: ±0.5°C accuracy
  • Product center temperature: ±1°C accuracy
  • Return air temperature: ±1°C accuracy
  • Refrigerant temperatures: ±0.5°C accuracy

Air Velocity Control

Variable frequency drives (VFD) on circulation fans enable precise velocity adjustment based on product type and load. Velocity uniformity across the product layer should be within ±10% of setpoint.

Energy Efficiency Optimization

Strategies for Reduced Energy Consumption:

  • Heat recovery from compressor discharge for plant heating
  • Economizer circuits to reduce compression ratio
  • Variable speed fan drives to match airflow to load
  • Optimized defrost schedules based on frost accumulation sensors
  • Thermal insulation minimum R-35 (RSI-6.2) for -40°C spaces

Specific Energy Consumption

Typical energy use for IQF berry processing:

  • 0.15-0.25 kWh/kg (0.07-0.11 kWh/lb) for efficient systems
  • 0.25-0.40 kWh/kg (0.11-0.18 kWh/lb) for older installations

Packaging and Post-Freezing

Tempering Requirements

Product exiting the freezer at -40°C must be tempered to -18°C to -20°C (-0.4°F to -4°F) before packaging to prevent:

  • Condensation and frost formation during packaging
  • Thermal shock to packaging materials
  • Excessive brittleness causing product breakage

Tempering Zone Design:

  • Air temperature: -25°C to -30°C (-13°F to -22°F)
  • Residence time: 3-5 minutes
  • Air velocity: 2-3 m/s (400-600 fpm)

Storage Conditions

Optimal Parameters for Frozen Berry Storage:

ParameterSpecificationImpact on Shelf Life
Temperature-23°C to -25°C (-9°F to -13°F)Every 3°C increase halves shelf life
Relative humidity90-95%Prevents sublimation/freezer burn
Air movementMinimalReduces sublimation rate
Light exposureNonePrevents color degradation
Storage duration12-24 monthsTemperature dependent

Safety and Sanitation

Food Safety Requirements

All IQF equipment must meet FDA, USDA, and 3-A Sanitary Standards where applicable:

  • Stainless steel contact surfaces (304 or 316 grade)
  • Cleanable design with no product entrapment areas
  • Smooth surfaces with 0.8 μm Ra or better finish
  • Self-draining configurations
  • Accessible for inspection and cleaning

Personnel Safety

Low-temperature environments require specific safety measures:

  • Emergency stop systems at all access points
  • Interior lighting minimum 200 lux (20 fc)
  • Interior release mechanisms on all doors
  • Personnel protective equipment for -40°C exposure
  • Maximum exposure time limits without proper clothing