Plate Freezer Products
Plate freezers achieve optimal performance when processing products with specific geometric and physical characteristics. Product selection directly influences heat transfer efficiency, freezing time, equipment utilization, and final product quality.
Product Suitability Criteria
Geometric Requirements
Plate freezing operates most efficiently with products meeting specific dimensional criteria:
Optimal Product Characteristics:
- Flat parallel surfaces for maximum plate contact
- Uniform thickness throughout product cross-section
- Rectangular or square footprint
- Minimal surface irregularities
- Consistent product dimensions within batch
Contact Surface Quality: Surface contact area directly affects heat transfer coefficient. Products with rough or irregular surfaces reduce effective contact from 90-95% to 60-70%, increasing freezing time by 30-50%.
Dimensional Constraints
| Parameter | Typical Range | Maximum Practical |
|---|---|---|
| Product thickness | 25-100 mm | 150 mm |
| Block length | 400-800 mm | 1000 mm |
| Block width | 200-400 mm | 600 mm |
| Weight per block | 5-25 kg | 40 kg |
| Surface flatness | ±2 mm | ±5 mm |
Thickness limits result from:
- Extended freezing time beyond economic viability (>4 hours)
- Increased core temperature hold time
- Excessive pressure requirements for contact
- Plate spacing limitations in standard equipment
Fish Products
Fish Blocks
Fish blocks represent the primary application for horizontal plate freezers in the seafood industry.
Groundfish Blocks:
- Minced cod, haddock, pollock
- Block dimensions: 406 x 203 x 64 mm (16 x 8 x 2.5 in)
- Weight: 7.3 kg (16 lb) standard
- Freezing time: 90-120 minutes at -40°C plate temperature
- Heat transfer coefficient: 200-250 W/(m²·K)
Block Formation Process:
- Filleting and deboning
- Mechanical mincing or grinding
- Form filling in cardboard cartons
- Plate loading with carton
- Freezing under pressure (0.5-1.0 bar)
Heat Transfer Calculation:
Freezing time approximation using Plank’s equation modified for plate contact:
$$t_f = \frac{\rho L}{T_p - T_f} \left[\frac{P a}{h} + \frac{R a^2}{k}\right]$$
Where:
- t_f = freezing time (s)
- ρ = product density (kg/m³)
- L = latent heat of fusion (kJ/kg)
- T_p = plate temperature (°C)
- T_f = final product temperature (°C)
- a = thickness (m)
- h = surface heat transfer coefficient (W/(m²·K))
- k = thermal conductivity (W/(m·K))
- P = 1/2 (for infinite slab)
- R = 1/8 (for infinite slab)
Typical Fish Block Values:
- ρ = 1040 kg/m³
- L = 280 kJ/kg (includes sensible and latent heat)
- k_frozen = 1.8 W/(m·K)
- k_unfrozen = 0.5 W/(m·K)
- Initial temperature = 4°C
- Moisture content = 75-80%
Fish Fillets
Product Specifications:
| Fish Type | Thickness Range | Typical Weight | Freezing Time |
|---|---|---|---|
| Cod fillets | 20-35 mm | 200-400 g | 45-75 min |
| Haddock fillets | 18-30 mm | 180-350 g | 40-65 min |
| Sole/Flounder | 12-20 mm | 100-250 g | 25-45 min |
| Salmon portions | 25-40 mm | 150-300 g | 50-80 min |
Fillet Preparation:
- Individual quick frozen (IQF) or block frozen
- Skin-on or skinless affects contact
- Trimmed to uniform thickness
- Glazing after freezing recommended
Quality Factors:
Fillet quality in plate freezing depends on:
Pressure Control: 0.3-0.8 bar contact pressure
- Insufficient pressure: poor contact, slow freezing
- Excessive pressure: product damage, moisture loss
Freezing Rate: Target 5-25 mm/hour through -1 to -5°C zone
- Faster rates: smaller ice crystals, better texture
- Slower rates: drip loss on thawing increases
Temperature Uniformity: ±2°C across plate surface
- Non-uniform temperature creates quality variation
- Affects yield and appearance
Breaded Fish Products
Formed breaded fish sticks and portions:
- Pre-cooked or raw
- Uniform rectangular shape
- Thickness: 10-15 mm
- Breading provides flat surface
- Freezing time: 15-30 minutes
- Ideal for horizontal plate freezers
Meat Products
Formed Meat Patties
Hamburger Patties:
| Specification | Standard Range | Notes |
|---|---|---|
| Diameter | 100-130 mm | Quarter-pound to third-pound |
| Thickness | 6-12 mm | Thinner freezes faster |
| Fat content | 10-30% | Affects thermal properties |
| Freezing time | 12-20 minutes | At -35°C plate temperature |
| Pressure | 0.2-0.5 bar | Light pressure prevents deformation |
Thermal Properties of Ground Beef:
Fat content significantly affects freezing characteristics:
| Fat Content | Initial Freezing Point | Thermal Conductivity (Frozen) | Freezing Time Factor |
|---|---|---|---|
| 10% lean | -1.7°C | 1.6 W/(m·K) | 1.0 |
| 20% fat | -2.1°C | 1.4 W/(m·K) | 1.15 |
| 30% fat | -2.8°C | 1.2 W/(m·K) | 1.35 |
Higher fat content requires longer freezing time due to:
- Lower thermal conductivity
- Lower latent heat per unit mass
- Depressed freezing point
Sausage Products:
- Breakfast sausage patties: 50-75 mm diameter, 8-12 mm thick
- Formed links in rectangular trays
- Pre-cooked products freeze faster
- Interleaving paper prevents sticking
- Freezing time: 15-25 minutes
Portion-Cut Steaks
Specifications:
- Thickness: 20-35 mm maximum for plate freezing
- Individual vacuum packaging required
- Flat surface essential for contact
- Boneless cuts only
- Freezing time: 60-90 minutes
- Applications: portion steaks, sandwich steaks
Processed Meat Products
Sliced Luncheon Meats:
- Stacked in rectangular blocks
- Interleaving film between slices
- Block height: 40-80 mm
- Excellent plate contact
- Freezing time: 30-50 minutes
- Used for food service distribution
Vegetable Products
Block Frozen Vegetables
Block freezing in plate freezers serves as intermediate storage before retail packaging.
Spinach Blocks:
| Parameter | Specification |
|---|---|
| Block size | 406 x 203 x 76 mm |
| Weight | 10-12 kg |
| Blanched temperature | 85-95°C |
| Cooling before freeze | 10-15°C |
| Freezing time | 120-150 minutes |
| Final temperature | -18°C core |
Blanching Impact:
Blanching affects freezing performance:
- Enzyme inactivation preserves quality
- Cell structure disruption increases thermal conductivity
- Moisture content changes: 85-92%
- Air removal improves plate contact
Other Block Vegetables:
| Product | Block Weight | Moisture % | Freezing Time |
|---|---|---|---|
| Chopped broccoli | 9-11 kg | 88-91 | 100-130 min |
| Cut green beans | 10-13 kg | 89-92 | 110-140 min |
| Corn kernels | 11-14 kg | 73-76 | 90-120 min |
| Peas | 12-15 kg | 78-81 | 100-130 min |
| Diced carrots | 10-12 kg | 87-90 | 100-130 min |
Void Space Considerations:
Particulate vegetables contain interstitial air:
- Reduces effective thermal conductivity
- Increases freezing time by 20-40%
- Compression during freezing minimizes voids
- Pressure: 0.5-1.0 bar typical
Vegetable Purees
Suitable Products:
- Squash puree
- Sweet potato puree
- Pumpkin filling
- Tomato paste blocks
Advantages:
- Excellent plate contact (no voids)
- Uniform heat transfer
- Faster freezing than particulate vegetables
- Freezing time: 60-90 minutes for 50 mm thickness
Product Thickness Limits
Maximum Economical Thickness
Thickness limitation driven by freezing time economics:
Freezing Time vs. Thickness:
For a fish block at -40°C plate temperature:
| Thickness (mm) | Freezing Time (min) | Throughput (kg/hr/m²) |
|---|---|---|
| 25 | 45 | 28 |
| 50 | 90 | 28 |
| 75 | 140 | 27 |
| 100 | 200 | 25 |
| 125 | 270 | 23 |
| 150 | 350 | 21 |
Note: Freezing time increases approximately with square of thickness (Plank’s equation), while throughput remains relatively constant until excessive thickness reduces productivity.
Practical Thickness Ranges:
| Product Category | Optimal Thickness | Maximum Thickness | Limiting Factor |
|---|---|---|---|
| Fish fillets | 20-30 mm | 40 mm | Quality degradation |
| Fish blocks | 50-75 mm | 100 mm | Freezing time |
| Meat patties | 8-12 mm | 15 mm | Product standard |
| Vegetable blocks | 60-80 mm | 100 mm | Handling, time |
| Formed products | 15-25 mm | 40 mm | Economics |
Minimum Thickness
Extremely thin products also present challenges:
- Difficult to achieve uniform pressure
- Product damage from excessive pressure
- Poor economics (low weight per plate area)
- Minimum practical thickness: 6-8 mm
Package Requirements
Carton Specifications
Material Selection:
| Carton Type | Thermal Resistance | Freezing Time Impact | Cost Factor |
|---|---|---|---|
| Standard chipboard | Low | +5-10% | 1.0 |
| Wax-coated | Medium | +15-20% | 1.3 |
| Plastic-coated | Medium-high | +20-30% | 1.5 |
| Bare product (no carton) | Minimal | Baseline | 0.8 |
Carton Thermal Resistance:
Typical carton adds thermal resistance:
$$R_{carton} = \frac{t_{carton}}{k_{carton}}$$
Where:
- t_carton = 1.5-2.5 mm thickness
- k_carton = 0.05-0.08 W/(m·K)
- R_carton = 0.019-0.050 m²·K/W
This resistance increases freezing time by 10-25% depending on product thickness.
Structural Requirements:
- Wet strength sufficient for handling
- Dimensional stability under pressure
- Flat surfaces for plate contact
- Corner reinforcement for stacking
- Moisture barrier for product protection
Vacuum Packaging
Film Properties:
| Film Type | Thickness (μm) | Thermal Impact | Oxygen Barrier |
|---|---|---|---|
| Polyethylene | 50-100 | Minimal | Poor |
| Nylon/PE laminate | 75-125 | Low | Good |
| EVOH barrier | 90-150 | Low | Excellent |
| Shrink film | 60-90 | Minimal | Fair |
Advantages for Plate Freezing:
- Eliminates air gaps between product and package
- Improves plate contact
- Reduces freezer burn
- Extends shelf life
- Minimal thermal resistance (film thickness 0.05-0.15 mm)
Vacuum Level:
- 98-99.5% vacuum for irregular products
- Ensures conformance to plate surface
- Critical for products with surface irregularities
Interleaving Materials
For stacked products (patties, fillets):
Material Options:
| Material | Thickness (mm) | Separation Quality | Cost |
|---|---|---|---|
| Waxed paper | 0.03-0.05 | Good | Low |
| Polyethylene film | 0.025-0.040 | Excellent | Medium |
| Silicone-coated paper | 0.04-0.06 | Excellent | High |
Function:
- Prevents product adhesion
- Allows individual piece removal
- Must not interfere with heat transfer
- Adds negligible thermal resistance
Freezing Time by Product Type
Calculation Methodology
Modified Plank’s Equation:
$$t_f = \frac{\Delta H_e}{T_m - T_c} \left[\frac{P a}{h_1 + h_2} + \frac{R a^2}{k_f}\right]$$
Where:
- ΔH_e = effective volumetric enthalpy change (kJ/m³)
- T_m = mean freezing temperature (°C)
- T_c = coolant/plate temperature (°C)
- h_1, h_2 = surface heat transfer coefficients (W/(m²·K))
- k_f = thermal conductivity of frozen product (W/(m·K))
Enthalpy Change:
$$\Delta H_e = \rho \left[c_1(T_i - T_m) + L + c_2(T_m - T_f)\right]$$
Where:
- c_1 = specific heat above freezing (kJ/(kg·K))
- c_2 = specific heat below freezing (kJ/(kg·K))
- T_i = initial temperature (°C)
- T_f = final center temperature (°C)
- L = latent heat of fusion (kJ/kg)
Comparative Freezing Times
Standard Conditions: Plate temperature -35°C, initial product temperature 4°C, final temperature -18°C
| Product | Thickness (mm) | Moisture (%) | Freezing Time (min) | Heat Flux (W/m²) |
|---|---|---|---|---|
| Cod fillet | 25 | 82 | 42 | 1850 |
| Cod block | 64 | 80 | 105 | 1420 |
| Ground beef patty (20% fat) | 10 | 62 | 16 | 1680 |
| Beef patty (20% fat) | 10 | 62 | 16 | 1680 |
| Pork sausage patty | 12 | 55 | 21 | 1420 |
| Spinach block | 76 | 90 | 135 | 1320 |
| Broccoli block | 76 | 89 | 125 | 1380 |
| Pea block | 76 | 78 | 115 | 1450 |
| Bread dough sheet | 20 | 38 | 45 | 980 |
Temperature Profile During Freezing
Characteristic Stages:
Cooling Phase: Product surface to freezing point
- Duration: 5-10% of total freezing time
- Rapid temperature drop
- High heat flux
Phase Change: Latent heat removal
- Duration: 70-80% of total freezing time
- Temperature plateau at freezing point
- Constant heat flux
- Ice crystal formation
Tempering Phase: Frozen product to final temperature
- Duration: 10-20% of total freezing time
- Slower temperature drop
- Decreasing heat flux
Time-Temperature Example (50 mm fish block):
| Time (min) | Surface Temp (°C) | Core Temp (°C) | Phase |
|---|---|---|---|
| 0 | 4 | 4 | Initial |
| 5 | -15 | 2 | Cooling surface |
| 10 | -25 | -1 | Surface freezing |
| 20 | -30 | -1 | Core phase change |
| 40 | -32 | -2 | Core freezing |
| 60 | -33 | -8 | Core freezing |
| 80 | -33 | -15 | Tempering |
| 90 | -33 | -18 | Complete |
Quality Considerations
Ice Crystal Formation
Crystal Size Impact:
Freezing rate directly affects ice crystal size:
| Freezing Rate (cm/hr) | Crystal Size (μm) | Quality Rating | Drip Loss (%) |
|---|---|---|---|
| 0.5-1 (slow) | 100-200 | Poor | 8-12 |
| 1-2 (moderate) | 50-100 | Fair | 5-8 |
| 2-5 (fast) | 20-50 | Good | 2-4 |
| 5-10 (rapid) | 10-20 | Excellent | <2 |
Plate Freezer Performance:
Typical plate freezing achieves 2-6 cm/hr through critical zone (-1 to -5°C), producing good to excellent quality.
Critical Zone:
- Temperature range where maximum ice formation occurs
- Residence time in this zone determines crystal size
- Plate freezing minimizes this time through high heat transfer
Texture Preservation
Cell Structure Damage:
Ice crystal formation causes mechanical damage:
- Large crystals rupture cell walls
- Smaller crystals cause less damage
- Rapid freezing preserves texture
- Slow freezing creates mushy texture on thawing
Product-Specific Concerns:
| Product Type | Quality Factor | Plate Freezing Advantage |
|---|---|---|
| Fish fillets | Firm texture, minimal drip | High freezing rate maintains cell structure |
| Meat patties | Texture retention | Uniform freezing prevents moisture migration |
| Vegetables | Color, firmness | Fast freezing preserves cell integrity |
| Formed products | Shape retention | Pressure maintains form during freezing |
Moisture Migration
Sublimation Prevention:
During frozen storage, moisture sublimes from product surface:
- Appears as freezer burn
- Reduces product weight
- Degrades appearance and texture
- Prevented by proper packaging
Plate Freezing Advantages:
- Rapid freezing minimizes surface exposure time
- Smooth frozen surface reduces sublimation sites
- Package contact during freezing creates barrier
- Lower surface temperature differential during storage
Pressure Effects
Contact Pressure Benefits:
Optimal pressure range: 0.3-1.0 bar depending on product
Benefits:
- Eliminates air gaps (reduces thermal resistance)
- Improves heat transfer coefficient from 50 W/(m²·K) to 200+ W/(m²·K)
- Maintains product shape
- Creates flat, uniform surface finish
Excessive Pressure Problems:
- Product deformation
- Moisture expression from product
- Equipment damage
- Uneven pressure distribution
Product-Specific Pressure:
| Product | Recommended Pressure (bar) | Reason |
|---|---|---|
| Fish blocks | 0.7-1.0 | Firm texture, requires good contact |
| Fish fillets | 0.3-0.5 | Delicate, prevent damage |
| Meat patties | 0.2-0.4 | Prevent deformation |
| Vegetable blocks | 0.5-0.8 | Compress voids |
| Formed products | 0.4-0.7 | Maintain shape |
Equipment Specifications
Plate Design Requirements
Surface Finish:
| Finish Type | Surface Roughness (Ra, μm) | Heat Transfer Impact |
|---|---|---|
| Standard mill | 3.2-6.3 | Baseline |
| Machine finished | 1.6-3.2 | +5% improvement |
| Ground | 0.8-1.6 | +8% improvement |
| Polished | 0.4-0.8 | +10% improvement |
Smoother surfaces provide better contact, especially with irregular products.
Plate Spacing:
Adjustable spacing accommodates various product thicknesses:
- Minimum spacing: 15-20 mm
- Maximum spacing: 150-200 mm
- Adjustment increment: 5-10 mm
- Manual or hydraulic adjustment
Refrigeration System Requirements
Evaporator Temperature:
Plate temperature driven by product requirements:
| Product Category | Plate Temperature (°C) | Evaporator Temperature (°C) | ΔT Approach |
|---|---|---|---|
| Fish products | -35 to -40 | -40 to -45 | 5°C |
| Meat products | -30 to -35 | -35 to -40 | 5°C |
| Vegetables | -35 to -40 | -40 to -45 | 5°C |
| Bakery products | -25 to -30 | -30 to -35 | 5°C |
Refrigeration Capacity:
Average heat load calculation:
$$Q = \frac{\dot{m} \cdot \Delta H}{t_{cycle}}$$
Where:
- Q = refrigeration capacity (kW)
- ṁ = product mass flow rate (kg/s)
- ΔH = enthalpy change (kJ/kg)
- t_cycle = cycle time including loading/unloading
Example Calculation:
Horizontal plate freezer specifications:
- Plate area: 20 m² total
- Product: fish blocks, 64 mm thick
- Loading: 12 kg/m²
- Freezing time: 105 minutes
- Loading/unloading: 15 minutes
- Cycle time: 120 minutes
Product throughput: (20 m² × 12 kg/m²) / (120 min / 60) = 120 kg/hr
Enthalpy change for fish: 280 kJ/kg
Refrigeration load: (120 kg/hr × 280 kJ/kg) / 3600 s/hr = 9.3 kW average
Peak load during initial cooling: 15-20 kW
Product Handling Systems
Automatic Loading:
For high-volume operations:
- Robotic cartridge loading systems
- Pneumatic plate opening/closing
- Automated product transport
- Reduces cycle time by 5-10 minutes
- Improves consistency
Cartridge Systems:
Pre-loaded cartridges with products:
- Slide into horizontal plate freezers
- Eliminates manual loading
- Reduces labor requirements
- Improves safety
- Standard cartridge: 400-600 mm wide
Quality Control Integration:
Inline systems monitor:
- Product weight (±1% accuracy)
- Dimensional compliance
- Temperature verification
- Reject non-conforming products before freezing