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Steam Tables — Properties of Saturated Steam

Thermodynamic properties of saturated steam and water at various pressures and temperatures.

steamtablesData Table

Overview

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Steam tables provide thermodynamic properties of water and steam at saturation and superheated conditions. The data is essential for sizing steam systems, calculating heat transfer, designing condensate return lines, and determining flash steam losses. Two primary tabulations are used: temperature-based (look up properties by saturation temperature) and pressure-based (look up properties by system pressure).

Key Formulas

Steam Quality

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

Mass fraction of vapor in a two-phase mixture. Ranges from 0 (saturated liquid) to 1 (saturated vapor).

Enthalpy of Wet Steam

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

Determines the specific enthalpy of a wet steam mixture from the quality and saturated properties.

Flash Steam Generated from Condensate

mflash=mliquid  hf1hf2hfg2m_{flash} = m_{liquid} \; \frac{h_{f1} - h_{f2}}{h_{fg2}}

Predicts how much steam is produced when high-pressure condensate is discharged to a lower pressure.

Condensate Load from Heat Transfer

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

Estimates the mass flow rate of condensate from a known heat duty and latent heat.

Specific Volume of Wet Steam

v=vf+x  (vgvf)v = v_f + x \; (v_g - v_f)

Used for pipe sizing in two-phase regions.

Variables

8 rows
Common symbols used in steam table calculations
Symbol
Description
Unit
xSteam quality (dryness fraction)
h_fEnthalpy of saturated liquidkJ/kg
h_fgLatent heat of vaporizationkJ/kg
h_gEnthalpy of saturated vaporkJ/kg
v_fSpecific volume of saturated liquidm^3/kg
v_gSpecific volume of saturated vaporm^3/kg
QHeat transfer ratekW
mMass flow ratekg/s

Source: engineeringtoolbox.com

Saturated Steam — Temperature Table

11 rows
Properties of saturated steam — look up by temperature
Temp(°C)
Pressure(bar)
h_f(kJ/kg)
h_fg(kJ/kg)
h_g(kJ/kg)
v_f(m^3/kg)
v_g(m^3/kg)
1001.013419.1225726760.0010441.673
1101.433461.3223026910.0010521.21
1201.985503.7220227060.001060.892
1302.701546.3217427200.001070.668
1403.614589.1214427340.001080.509
1504.76632.2211427460.0010910.392
1606.181675.5208227580.0011020.307
1707.92719.2204927680.0011140.243
18010.03763.2201427780.0011270.194
19012.55807.6197727850.0011410.156
20015.55852.4193927920.0011570.127

Source: engineeringtoolbox.com

Saturated Steam — Pressure Table

10 rows
Properties of saturated steam — look up by pressure
Pressure(bar)
Temp(°C)
h_f(kJ/kg)
h_fg(kJ/kg)
h_g(kJ/kg)
199.6417.522582675
1.5111.4467.122262693
2120.2504.722022707
3133.5561.421632725
5151.8640.121082748
10179.9762.620152778
15198.3844.719472792
20212.4908.618902798
50263.9115416402794
100311140813192727

Source: engineeringtoolbox.com

Saturation Curve — Temperature vs Pressure

Saturation Temperature vs Pressure

Flash Steam Calculator

Use this calculator to estimate the mass of flash steam produced when condensate at one pressure is discharged to a lower pressure.

Flash Steam from Condensate Blowdown

Wet Steam Properties

Unit Converter

Steam Table Unit Converter

Restored Original Source Tables

The corrected original source for this route is the Online Saturated Steam Table Calculator page. That source page contains calculator form fields and external calculator references, but no substantive thermodynamic data table in the cached HTML. The saturated steam pressure and temperature data used by the calculator experience is preserved in the interactive tables above.

3 rows
Source UI artifacts and calculator migration treatment
Source Artifact
Migration Treatment
Search and layout rows containing × / 検索 placeholdersIntentionally not copied as engineering data; represented here as non-substantive source UI artifacts.
Online Saturated Steam Table Calculator form fieldsMigrated as saturated steam, wet steam, flash steam, and unit-conversion calculators above.
External Spirax Sarco saturated steam calculator referencePreserved in References.

Source: engineeringtoolbox.com

Engineering Notes

  • Interpolation is often required. Steam table data is tabulated at discrete intervals; use linear interpolation between adjacent rows for intermediate conditions.
  • Latent heat decreases with pressure. At higher pressures the difference between liquid and vapor enthalpy narrows, which means less energy per kilogram is available for heating in a condensing process.
  • Superheated steam tables are separate from saturated tables. Once steam is superheated, its properties depend on both pressure and temperature independently.
  • Flash steam recovery is a major energy-savings opportunity in steam systems. High-pressure condensate discharged to atmospheric pressure can flash off roughly 10–15 % of its mass as low-pressure steam.
  • Pipe sizing for steam distribution must account for specific volume, which increases dramatically at lower pressures. Using saturated vapor specific volume (vgv_g) is conservative for header sizing.
  • Steam quality matters for heat transfer. Wet steam with quality below 0.95 can cause water hammer and reduce heat exchanger performance. Aim for quality ≥ 0.98 at the point of use.
  • All values in these tables are based on the IAPWS-IF97 industrial formulation, which is the internationally accepted standard for industrial steam properties.

References