📋 Case Study

Food Processing Steam Peak-Shaving with Bio-Based PCM

Steam demand spikes (up to 12 MW) during sterilization cycles exceeding boiler capacity

🏗️ Project Overview

Nestlé dairy facility, Wisconsin, USA

🎯 Challenge

Steam demand spikes (up to 12 MW) during sterilization cycles exceeding boiler capacity

🔧 Design Approach

Encapsulated stearic acid PCM (52°C melt point) integrated into shell-and-tube latent heat exchangers

📐 Design Diagram

Boiler (8 MW)SterilizerPCM ModuleStearic Acid(52°C melt)N_f = 14,200Q_in = ?ΔP spike12 MW peakt_charge = 18.3 minFood Processing Steam Peak-ShavingBio-Based PCM Integration • Shell-and-Tube Latent HX

AI-generated project design illustration

📐 Key Calculations

PCM Encapsulation Fatigue Cycles

N_f = (σ'_f / σ_a)^b × (ε'_f / ε_a)^c
Result: 14,200 cycles
Exceeds 15-year operational requirement

Charge Time Compliance

t_charge = m·h_sf / Q_in
Result: 18.3 min
Meets <20-min sterilization prep window

📊 Results

Boiler oversizing reduced by 35%, steam pressure stability improved by 94%, ROI achieved in 3.2 years

💡 Lessons Learned

  • Microencapsulation shell thickness must exceed 120 µm to prevent leakage after 5000+ thermal cycles
  • Glycol-water mixture required as HTF to prevent PCM solidification in piping

Key Takeaways

  • 1Microencapsulation shell thickness must exceed 120 µm to prevent leakage after 5000+ thermal cycles
  • 2Glycol-water mixture required as HTF to prevent PCM solidification in piping