HVAC Systems Encyclopedia

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

Potato Storage Refrigeration Systems

Storage Temperature Requirements by End Use

Potato storage temperature is determined by the intended market destination. Temperature directly affects sugar accumulation through enzymatic conversion of starch.

End UseTemperature RangeCritical Parameters
Seed potatoes3-4°C (37-39°F)Maintain dormancy, prevent sprouting
Table stock (fresh market)7-10°C (45-50°F)Minimize sugar accumulation, maintain quality
Chipping potatoes7-10°C (45-50°F)Prevent reducing sugars, avoid dark chips
French fry processing7-10°C (45-50°F)Control sugar content for color
Dehydration processing10-13°C (50-55°F)Higher temperature acceptable

Temperature Uniformity: Maintain ±0.5°C throughout storage volume to prevent localized sugar accumulation or sprouting.

Curing Process Requirements

Curing heals mechanical injuries from harvest and develops skin set to reduce moisture loss and disease susceptibility.

Curing Parameters

ParameterValueDuration
Temperature15-20°C (59-68°F)10-14 days
Relative humidity95-99%Throughout curing
Air velocity0.15-0.25 m/sOver potato surface
Oxygen concentration>19%Prevent anaerobic conditions

Wound Healing Process

Curing temperature initiates suberization and periderm formation:

Suberization rate = f(T, RH, O₂)

Where healing rate increases exponentially with temperature up to 20°C. Above 20°C, respiration increases faster than healing.

Heat generation during curing:

  • Fresh potatoes: 0.12-0.18 W/kg at 15-20°C
  • Peak respiration occurs days 3-5 of curing

Curing Load Calculations

Total refrigeration load during curing:

Q_total = Q_resp + Q_infiltration + Q_ventilation + Q_fans

Respiratory heat: Q_resp = m × q_resp × (1 + α(T - T_ref))

Where:

  • m = potato mass (kg)
  • q_resp = specific heat of respiration at reference temperature (W/kg)
  • α = temperature coefficient (0.08-0.12/°C)
  • T = curing temperature (°C)
  • T_ref = reference temperature (typically 0°C)

Storage Humidity Control

Target relative humidity: 95% ± 2%

Moisture Balance

Potatoes contain 78-82% moisture. Weight loss exceeds 5-6% results in visible shriveling and market loss.

Vapor pressure deficit (VPD):

VPD = P_sat(T_potato) - P_air

Where:

  • P_sat(T_potato) = saturation pressure at potato surface temperature
  • P_air = partial pressure of water vapor in air

Maintaining VPD < 0.2 kPa minimizes moisture loss while preventing condensation.

Humidity Generation Systems

Evaporative pad humidifiers:

  • Efficiency: 80-90%
  • Water consumption: 15-25 L/tonne/month
  • Air velocity through pad: 1.5-2.5 m/s

High-pressure fog systems:

  • Droplet size: 5-15 μm
  • Coverage: 50-100 m² per nozzle
  • Pressure: 4000-7000 kPa (580-1015 psi)
  • Evaporation efficiency: >95%

Ultrasonic humidifiers:

  • Frequency: 1.65-2.4 MHz
  • Capacity: 0.5-2.0 kg/h per head
  • Power consumption: 50-150 W per head

Dehumidification Requirements

During warm outdoor conditions or initial storage fill, dehumidification prevents condensation on building surfaces.

Latent load from potato moisture release:

Q_latent = (m_potato × E_rate × h_fg) / 3600

Where:

  • E_rate = evaporation rate (kg/kg/h) = 0.0001-0.0003
  • h_fg = latent heat of vaporization (2450 kJ/kg at 10°C)

Sprouting Prevention

Sprouting reduces market value and increases respiration heat load. Control methods include temperature management, sprout inhibitors, and ethylene application.

Physiological Dormancy

Natural dormancy duration: 60-150 days depending on cultivar.

Dormancy period influenced by:

  • Growing season temperature
  • Maturity at harvest
  • Post-harvest handling
  • Storage temperature

Temperature Effect on Sprouting

Sprouting occurs at temperatures above 4°C after dormancy break:

TemperatureSprout Growth Rate
3-4°CMinimal (<0.5 mm/week)
5-7°CSlow (1-2 mm/week)
8-10°CModerate (3-5 mm/week)
>12°CRapid (>8 mm/week)

Chemical Sprout Inhibitors

CIPC (Chlorpropham):

  • Application rate: 15-30 g/tonne
  • Application timing: Before sprout emergence
  • Effective duration: 3-5 months
  • Temperature requirement: >10°C for vaporization
  • Ventilation: Stop airflow during application

1,4-Dimethylnaphthalene (DMN):

  • Vapor-release formulation
  • Duration: 6-9 months
  • Application: Place sachets in storage

Ethylene Sprout Control

Low-concentration ethylene (10-20 ppm) prevents sprouting:

  • Application: Continuous or pulse dosing
  • Pulse: 100-150 ppm for 24-48 hours every 2-4 weeks
  • Scrubbing required to prevent accumulation

Sugar Accumulation and Sweetening

Low-temperature sweetening results from enzymatic conversion of starch to reducing sugars (glucose and fructose).

Biochemical Process

Starch → Maltose → Glucose (by amylase)

Temperature effect on sugar content:

Reducing sugars increase exponentially below 7°C:

S(t) = S₀ + k × exp(-E_a/RT) × t

Where:

  • S(t) = reducing sugar content at time t (% fresh weight)
  • S₀ = initial sugar content
  • k = rate constant
  • E_a = activation energy (varies by cultivar)
  • R = universal gas constant
  • T = absolute temperature (K)

Processing Quality Criteria

ProductMax Reducing SugarsMax Sucrose
Chipping0.20-0.35%1.5-2.5%
French fry0.25-0.40%2.0-3.0%
Fresh market<1.0%<3.0%

Reconditioning

Warming potatoes before processing reduces sugar content through respiratory consumption:

Reconditioning protocol:

  • Temperature: 15-20°C
  • Duration: 7-14 days
  • Sugar reduction: 30-50% of accumulated sugars
  • RH: Maintain 90-95%

Respiration during reconditioning:

  • 0.15-0.25 W/kg at 15°C
  • 0.20-0.35 W/kg at 20°C

Carbon Dioxide Management

CO₂ accumulation from potato respiration requires ventilation management.

Respiratory CO₂ Production

CO₂ production rate correlates with respiration heat:

Respiratory quotient (RQ): RQ = CO₂ produced / O₂ consumed = 0.95-1.05 for potatoes

CO₂ generation:

V_CO₂ = m_potato × R_CO₂ × f(T)

Where:

  • R_CO₂ = CO₂ production rate at reference temperature (mL/kg/h)
  • f(T) = temperature factor = Q₁₀^((T-T_ref)/10)
  • Q₁₀ = 2.0-2.5 for potatoes

CO₂ Concentration Limits

ConditionCO₂ LevelImpact
Normal storage<0.5%Optimal conditions
Warning level0.5-1.0%Monitor closely
Blackheart risk>1.5%Anaerobic respiration begins
Critical level>3.0%Severe internal damage

Blackheart disorder:

  • Anaerobic respiration causes internal black discoloration
  • Results from inadequate O₂ (<2%) or excess CO₂ (>3%)
  • Occurs in pile centers with poor air circulation

Ventilation Requirements

Minimum air exchange rate:

Q_vent = (V_CO₂ × 10⁶) / ((C_CO₂,in - C_CO₂,out) × 3600)

Where:

  • Q_vent = ventilation rate (m³/h)
  • V_CO₂ = CO₂ production (mL/h)
  • C_CO₂,in = inlet CO₂ concentration (ppm)
  • C_CO₂,out = target storage CO₂ concentration (ppm)

Typical ventilation rates:

  • Curing: 50-100 m³/tonne/day
  • Early storage (0-30 days): 20-40 m³/tonne/day
  • Mid storage (30-120 days): 10-20 m³/tonne/day
  • Late storage (>120 days): 5-10 m³/tonne/day

Large-Scale Storage Design

Storage Configuration Types

Bulk pile storage:

  • Pile height: 3-5 m (10-16 ft)
  • Floor area: 500-3000 m²
  • Capacity: 500-5000 tonnes per building
  • Air distribution: Pressurized plenum under slatted floor

Pallet box storage:

  • Stack height: 4-6 boxes (4-6 m)
  • Box capacity: 500-1000 kg
  • Aisle spacing: 0.3-0.6 m
  • Air circulation: Horizontal or vertical

Bin storage:

  • Bin depth: 2-3 m
  • Width: 3-6 m
  • Air ducts: Integrated floor or wall systems

Pressure Bruising Prevention

Excessive pile depth causes compression damage to lower layers.

Maximum pile depth:

h_max = (σ_allow × A) / (ρ_bulk × g)

Where:

  • σ_allow = allowable stress (2.5-3.5 kPa for potatoes)
  • A = contact area fraction
  • ρ_bulk = bulk density (650-750 kg/m³)
  • g = gravitational acceleration (9.81 m/s²)

Practical limits:

  • Table stock: 4.5-5.0 m maximum
  • Processing potatoes: 4.0-4.5 m maximum
  • Seed potatoes: 3.0-3.5 m maximum

Air Distribution System Design

Plenum pressure requirements:

ΔP = f × (L/D) × (ρv²/2) + K × (ρv²/2)

Where:

  • f = friction factor (0.02-0.04 for rough surfaces)
  • L = airflow path length through pile (m)
  • D = hydraulic diameter (m)
  • ρ = air density (kg/m³)
  • v = air velocity (m/s)
  • K = minor loss coefficient

Target air velocity through pile:

  • 0.02-0.04 m/s during storage
  • 0.10-0.20 m/s during curing and cooling

Plenum static pressure:

  • Bulk pile: 150-400 Pa (0.6-1.6 in. w.g.)
  • Pallet boxes: 100-200 Pa (0.4-0.8 in. w.g.)

Duct sizing for uniform distribution:

  • Velocity reduction method: End velocity ≤ 25% of inlet velocity
  • Cross-sectional area increase along duct length
  • Dampers every 3-6 m for balancing

Refrigeration Load Calculations

Total Refrigeration Load Components

Q_total = Q_resp + Q_field + Q_infiltration + Q_walls + Q_floor + Q_ceiling + Q_lights + Q_fans + Q_defrost

Respiratory Heat Load

Peak respiratory load:

Q_resp = m_potato × q_resp × F_peak

Where:

  • m_potato = total potato mass (kg)
  • q_resp = specific heat of respiration at storage temperature (W/kg)
  • F_peak = peak factor (1.2-1.5 during initial cooldown)

Respiration rates at storage temperature:

TemperatureHeat OutputCO₂ Production
3°C0.025-0.035 W/kg8-12 mL/kg/h
5°C0.035-0.050 W/kg12-16 mL/kg/h
7°C0.050-0.070 W/kg16-22 mL/kg/h
10°C0.080-0.110 W/kg25-35 mL/kg/h
15°C0.150-0.200 W/kg45-60 mL/kg/h

Field Heat Removal Load

Potatoes enter storage at 15-25°C and must be cooled to storage temperature.

Field heat load:

Q_field = m_potato × c_p × (T_harvest - T_storage) / t_cooldown

Where:

  • c_p = specific heat of potatoes (3.6 kJ/kg·K)
  • t_cooldown = cooling period (typically 14-21 days)

Example: 1000 tonne storage, harvest at 20°C, cool to 7°C in 14 days:

Q_field = (1,000,000 kg × 3.6 kJ/kg·K × 13 K) / (14 d × 86,400 s/d) Q_field = 38.7 kW

Transmission Loads

Wall, floor, and ceiling heat gain:

Q_transmission = Σ(U × A × ΔT)

Typical U-values for potato storage:

  • Walls: 0.15-0.25 W/m²·K (R-23 to R-38)
  • Roof: 0.12-0.20 W/m²·K (R-28 to R-48)
  • Floor: 0.30-0.50 W/m²·K (R-11 to R-19)

Infiltration Load

Sensible infiltration:

Q_inf,sens = ρ × c_p × V_inf × (T_out - T_in)

Latent infiltration:

Q_inf,lat = ρ × h_fg × V_inf × (ω_out - ω_in)

Where:

  • V_inf = infiltration rate (m³/s)
  • ω = humidity ratio (kg water/kg dry air)

Infiltration reduction methods:

  • Vestibule doors: Reduce infiltration 70-80%
  • Air curtains: 50-60% reduction
  • High-speed doors: 80-90% reduction
  • Pressure staging: Maintain 5-10 Pa positive pressure

Fan Heat Load

Fan motor heat:

Q_fan = (P_motor × η_motor) / η_fan

Where:

  • P_motor = motor input power (W)
  • η_motor = motor efficiency (0.85-0.92)
  • η_fan = fan efficiency (0.65-0.80)

Approximately 80-90% of fan power becomes heat in conditioned space.

Equipment Selection Summary

Total design capacity:

Q_design = Q_resp + 0.3 × Q_field + Q_transmission + Q_infiltration + Q_fans + 1.15 × (safety factor)

Typical capacity requirements:

  • 60-100 W/tonne for storage maintenance
  • 150-250 W/tonne for initial cooldown
  • Size equipment for 1.15-1.25 × steady-state load

Equipment Specifications

Refrigeration System Types

Direct expansion (DX) systems:

  • Capacity range: 50-500 kW per circuit
  • Evaporator temperature: -2 to 2°C
  • Refrigerant: R-404A, R-448A, R-449A, R-407F
  • Applications: Small to medium storage (<2000 tonnes)

Flooded ammonia systems:

  • Capacity: 200-2000 kW per system
  • Evaporator temperature: -4 to 2°C
  • Liquid recirculation ratio: 3:1 to 5:1
  • Applications: Large facilities (>2000 tonnes)

Glycol secondary loop systems:

  • Glycol temperature: -2 to 4°C
  • Glycol concentration: 25-35% propylene glycol
  • Flow rate: 0.05-0.08 L/s per kW
  • Applications: Distributed loads, multiple buildings

Evaporator Selection

Unit cooler specifications:

ParameterValueNotes
Face velocity2.0-3.0 m/sBalance capacity and throw
Fin spacing6-8 mm (0.24-0.31 in)Wide spacing for low fouling
TD (temperature difference)4-6 KMinimize dehydration
Defrost methodOff-cycle, hot gas, or electricMinimize temperature swing
Air throw20-35 mEnsure circulation to pile center

Capacity derating:

  • Frost accumulation: 10-15% capacity reduction
  • Air blockage: 5-10% reduction
  • Refrigerant charge variations: 5-8% reduction

Defrost Strategies

Off-cycle defrost:

  • Duration: 2-4 hours
  • Frequency: Every 6-12 hours
  • Application: Storage temperature >6°C, RH <92%

Hot gas defrost:

  • Duration: 20-40 minutes
  • Frequency: Every 4-8 hours
  • Temperature spike: <2°C in storage
  • Application: Lower temperatures, higher humidity

Electric defrost:

  • Power: 250-400 W/m² of coil face area
  • Duration: 30-60 minutes
  • Efficiency: Lower than hot gas
  • Application: Small units, DX systems

Fan Specifications

Circulation fans:

  • Type: Axial or mixed-flow
  • Capacity: 20-40 m³/tonne/h (curing), 5-15 m³/tonne/h (storage)
  • Static pressure: 200-500 Pa
  • Power: 0.8-1.5 W per m³/h
  • Control: VFD for load matching

Variable frequency drives (VFD):

  • Energy savings: 40-60% compared to constant speed
  • Control strategy: CO₂-based or temperature-based modulation
  • Minimum speed: 30-40% of rated

Temperature Monitoring and Control

Sensor Placement

Critical monitoring points:

  • Plenum inlet and outlet
  • Multiple depths in pile (surface, 1 m, 2 m, pile center)
  • Return air to evaporator
  • Outdoor ambient
  • Product temperature (wireless probes)

Sensor density:

  • 1 sensor per 100-200 tonnes of potatoes
  • Minimum 4 sensors per storage room
  • Wireless sensors: Battery life 2-5 years

Control Strategies

Proportional-integral (PI) control:

u(t) = K_p × e(t) + K_i × ∫e(τ)dτ

Where:

  • u(t) = control output
  • e(t) = error (setpoint - measured)
  • K_p = proportional gain (0.5-2.0)
  • K_i = integral gain (0.01-0.1)

Adaptive control:

  • Adjust setpoint based on storage duration
  • Gradual temperature reduction: 0.5-1.0°C per week after curing
  • Anticipatory control for load changes

Outdoor air economizer:

  • Engage when T_outdoor < T_storage and ΔT > 1°C
  • Free cooling potential: 30-50% of annual load
  • Mixed air dampers with minimum ventilation interlock

USDA Storage Guidelines Summary

USDA Agricultural Handbook 66 and related publications provide baseline storage recommendations:

Temperature recommendations:

  • Immediate storage after harvest: Begin cooling within 24 hours
  • Cooling rate: Not to exceed 0.5°C per day to prevent condensation
  • Storage temperature stability: ±0.5°C

Humidity recommendations:

  • Target RH: 95%
  • Acceptable range: 90-98%
  • Measure with chilled mirror hygrometers for accuracy

Storage life by temperature:

  • 3-4°C: 8-10 months
  • 7-10°C: 5-7 months
  • 12-15°C: 3-4 months

Quality loss rates:

  • Weight loss: 0.5-1.0% per month at 95% RH
  • Sprouting loss: 2-5% per month after dormancy (no inhibitor)
  • Disease loss: 1-3% per month (proper storage)

Air exchange requirements:

  • Curing phase: 60-100 m³/tonne/day
  • Storage phase: 10-30 m³/tonne/day
  • Base on CO₂ concentration: Maintain <0.5%

Recommended practices:

  • Grade and sort before storage
  • Remove diseased or damaged tubers
  • Maintain separate storage for different cultivars
  • Monitor for diseases weekly during first month
  • Temperature uniformity checks biweekly
  • Calibrate sensors quarterly

Storage Duration and Quality Management

Storage DurationKey Management Activities
0-14 days (Curing)Maintain 15-20°C, 95-99% RH, monitor wound healing
14-30 days (Cooling)Gradual cooling 0.5°C/day, monitor condensation
30-90 days (Early storage)Stabilize at target temperature, initiate sprout control
90-180 days (Mid storage)Monitor sugar accumulation, adjust ventilation
180-270 days (Late storage)Increase monitoring frequency, prepare for market

Potato storage facility design requires integration of refrigeration capacity, air distribution, humidity control, and monitoring systems to maintain product quality throughout the storage season while managing respiratory heat loads and preventing physiological disorders.