🔄 Scraped Surface Heat Exchanger Sizer (SSHE)
Size and design Scraped Surface Heat Exchangers (SSHE Votator / Contherm): Trommelen heat transfer model, rotational Reynolds number, product outlet temp, and shaft motor power.
⚡ Fortran 90 Engine
Double Precision (IEEE 754)
✓ ISO / ASME Validated
📊 Solver Telemetry
● ACTIVE
👁️ Consultations
18
⚡ Calculs faits
17
💾 Téléchargements
259
📦 Code Fortran
4.1 KB
📅 Mise en service
Jun 2026
⏱️ Latence
< 1 ms
🔄 SSHE Rotating Scraper Blades & Boundary Layer Scraping
Real-time visual simulation: High-speed scraper blades wiping viscous boundary layer against the cooling jacket📝 Configuration & Presets
🍦 Ice Cream Slush Freezer
🍅 Tomato Paste SSHE Cooler
🧈 Margarine Fat Crystallizer
🍲 Starch Gelatin Cooker
Trommelen & Beek SSHE Formulation:
• Rotational Reynolds: Rer = ρ · (N/60) · Di² / μ
• Scraped Nusselt: Nu = 0.16 · Rer0.50 · Pr0.33 · Nb0.33
• Scraped Film Coeff: hp = Nu · k / Di [W/(m²·K)]
• Total Heat Duty: Q̇ = ṁ · cp · ΔT + ṁ · Δhlatent [kW].
• Rotational Reynolds: Rer = ρ · (N/60) · Di² / μ
• Scraped Nusselt: Nu = 0.16 · Rer0.50 · Pr0.33 · Nb0.33
• Scraped Film Coeff: hp = Nu · k / Di [W/(m²·K)]
• Total Heat Duty: Q̇ = ṁ · cp · ΔT + ṁ · Δhlatent [kW].
📊 SSHE Performance Results
📊 Output Summary
Transferred Thermal Duty (Q̇)
13.8 kW
Overall U: 140 W/(m²·K) | Scraped Film hp: 153 W/(m²·K)
4 Blades @ 280 RPM
Product Outlet Temperature (Tout)
92.4 °C
Inlet = 95 °C | Jacket = 15 °C
Scraper Motor Power Demand
5.75 kW
7.71 HP Mechanical Drive
Rotational Reynolds (Rer)
86
Boundary layer renewal
Heat Transfer Area (A)
1.26 m²
L = 2 m, D = 200 mm
📈 Heat Duty Q̇ (kW) vs Scraper Rotor Speed N (rpm)
📊 Scraped Film Coeff hp [W/(m²·K)] vs Blades Count Nb
================================================================= THERMOFLUIDCALC — SCRAPED SURFACE HEAT EXCHANGER REPORT ================================================================= Case Title : Aseptic Tomato Paste SSHE Cooler Product Type : Tomato Paste / Puree (High Viscosity Non-Newtonian) Product Flow & Temp : m_dot = 1.50 kg/s, Tin = 95.0 C, Jacket = 15.0 C SSHE Geometry & Scraper : D = 200.0 mm, L = 2.00 m, N = 280 rpm, Blades = 4 ----------------------------------------------------------------- THERMAL HEAT DUTY (Q) : 13.82 kW Scraped Film Coeff (hp) : 152.5 W/(m2.K) Overall Heat Transfer (U) : 139.8 W/(m2.K) Product Outlet Temperature : 92.44 deg C Heat Transfer Area : 1.26 m2 Rotational Reynolds (Re_r) : 86 Scraper Drive Motor Power : 5.75 kW (7.71 HP) =================================================================
📘 Calculation Methodology & SSHE Standards
Continuous Boundary Layer Renewal
Spring-loaded or centrifugal scraper blades continuously scrape the heat exchange cylinder wall, preventing fouling and burning of sticky, heat-sensitive or crystallizing food and chemical products.
Trommelen & Beek Heat Transfer Model
Evaluates the unsteady heat conduction into the liquid film between successive blade passes, scaling with $\sqrt{N \cdot N_b}$.
Key Engineering Assumptions
- Uniform jacket temperature (evaporating refrigerant or condensing steam).
- Power law and high-shear viscous friction dissipation included in shaft load.
- Applicable to ice cream slush freezers, tomato paste, margarine, peanut butter, and gelatin.