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Steam Boiler Stress

Reference data and engineering information about steam boiler stress for steam and condensate applications.

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Overview

Engineering reference data for Steam Boiler Stress in steam condensate.

Key Formulas

Steam Quality

x=mvmtotalx = \frac{m_v}{m_{total}}

Mass fraction of vapor in two-phase mixture.

Enthalpy of Wet Steam

h=hf+xhfgh = h_f + x \cdot h_{fg}

Specific enthalpy of wet steam.

Flash Steam

mflash=mliquidhfhf2hfg2m_{flash} = m_{liquid} \frac{h_f - h_{f2}}{h_{fg2}}

Steam generated when condensate flashes to lower pressure.

Condensate Load

mc=Qhfgm_c = \frac{Q}{h_{fg}}

Condensate generated by heat transfer.

Variables

SymbolDescriptionUnit
xxSteam quality
hfh_fEnthalpy of saturated liquidkJ/kg
hfgh_{fg}Latent heat of vaporizationkJ/kg
hhSpecific enthalpykJ/kg
QQHeat transfer ratekW

Hoop Stress Derivation & Application

The hoop stress (circumferential stress) formula for a thin-walled cylindrical pressure vessel like a steam boiler shell is a fundamental equation in mechanical engineering. It can be derived from a static equilibrium analysis of a half-cylinder section.

Derivation Principle: For a cylindrical shell of internal diameter DD, thickness tt, and internal pressure PP:

  1. The total force acting on the projected area (the rectangular section of the half-cylinder) is F=P×D×LF = P \times D \times L (where LL is the length of the cylinder segment).
  2. This force is resisted by the tensile hoop stress σ\sigma acting over the two rectangular cross-section areas of the shell wall: A=2×(t×L)A = 2 \times (t \times L).
  3. Equating force to resistance: PDL=σ(2tL)P \cdot D \cdot L = \sigma \cdot (2 \cdot t \cdot L).
  4. Simplifying yields the core formula: σ=PD2t\sigma = \frac{P \cdot D}{2t}

Key Applications & Limitations:

  • Design Criterion: This stress is the primary parameter used to size the shell thickness tt to ensure it remains below the material's allowable stress.
  • Thin-Wall Assumption: The formula is valid for "thin-walled" vessels, typically defined as D/t>20D/t > 20. For thicker vessels, more complex formulas (Lamé's equations) must be used to account for the stress variation across the wall thickness.
  • Stress State: This is the principal (largest) stress in the boiler shell. Longitudinal (axial) stress is generally half this value (σlong=PD/4t\sigma_{long} = PD/4t).

References