Inflection Point Engineering Piping Design Guide

Thermosiphon Hydraulics

Chapter from the Piping Design Guide.

THERMOSIPHON REBOILER HYDRAULIC DESIGN

Thermosiphon Circulation Principles

Natural circulation (thermosiphon) reboilers operate by density difference between the two-phase mixture in the riser (outlet) and the liquid in the downcomer (inlet). No pump is needed — gravity drives circulation.

Driving Force = ρ_liquid × g × H - ρ_mixture × g × H
Where H = elevation difference between column liquid level and reboiler outlet nozzle

Circulation Rate determined by balance:
• Driving force = total friction losses (inlet piping + exchanger + outlet piping + exit loss into column)

Key Parameters:
• Circulation ratio: 3:1 to 10:1 (mass liquid recirculated / mass vaporized per pass)
- Low ratio (3:1): high % vaporization per pass, risk of dryout
- High ratio (10:1): low % vaporization, more like liquid flow, stable
- Typical design: 4:1 to 6:1
• Vaporization per pass: 10-35% (typical), never >40% (dryout risk)
• Liquid level in column: MUST be above reboiler return nozzle + static head for circulation

Vertical vs. Horizontal Thermosiphon

Parameter Vertical Horizontal Decision Factor
Orientation Tubes vertical, shell or tube side boiling Tubes horizontal, shell-side boiling Column geometry, maintenance
Elevation Required High (tubes must be submerged) Lower (bundle below column) Plot plan constraints
Tube Length 6-12 ft typical Per shell diameter Head available drives length
Fouling Service Good (easy to rod tubes) Moderate (shell-side fouling harder) Cleaning requirements
Circulation Ratio 4:1 to 8:1 5:1 to 10:1 Higher for horizontal (lower driving head)
Max Vaporization/Pass 30-35% 20-25% Lower for horizontal
Surface Area Limited by single shell Can be larger (longer tubes) Duty requirement
Common Type BEM, BEU (tube-side boiling) AES, AET, G-shell Maintenance vs. performance

Source: Piping_Design_Guide_v1.xlsx · sheet “Thermosiphon Hydraulics”