Boilers & Package Units

Steam Generators

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Steam Performance Extends Beyond the Boiler

A steam system includes generation, distribution, end use, and condensate return. Assessing only boiler efficiency can miss losses or operating problems elsewhere in the system.

Define the useful output and fuel-input basis before calculating efficiency. State whether the fuel heating value is higher/gross or lower/net, and keep the basis consistent when comparing equipment or operating periods.

Reference: DOE — Improving Steam System Performance.

Worked Example: Direct Boiler Efficiency

Illustrative example: these assumed values demonstrate arithmetic, not actual plant results or recommended operating targets.

For a simplified steady-state steam-output calculation:

Efficiency = steam mass flow × (steam enthalpy − feedwater enthalpy) ÷ fuel energy input.

Assume 5,000 kg/h of steam and an illustrative enthalpy increase of 2,400 kJ/kg. Useful output is 12,000,000 kJ/h, or 3,333 kW.

If fuel energy input is 15,000,000 kJ/h on a stated heating-value basis, calculated efficiency is 80%.

Obtain actual enthalpies from suitable steam-property data at the measured conditions. This simplified example does not account separately for blowdown output, transients, or every boundary correction. A formal assessment must use a defined method.

Record Conditions That Explain the Result

Keep steam flow and conditions, feedwater temperature, fuel consumption and quality, operating load, condensate return information, and relevant water-chemistry records together. Use measurements covering the same period.

Use Trends to Form Questions

Does fuel consumption rise at the same useful steam output? Has feedwater temperature changed? Has the production pattern shifted toward more startup or standby operation? Did an instrument or fuel specification change?

These questions produce a better investigation than assigning a fault from one efficiency number.

Protective trips require the site's approved response. Do not bypass interlocks or use this general explanation as a restart procedure.

Next step: Choose a consistent calculation boundary and compare representative operating periods.

Record observations only where it is safe. Inspection inside equipment, electrical testing, chemical work and changes to protective controls require qualified personnel, approved isolation and the installed equipment manual. Never bypass a trip or repeatedly restart unsafe equipment. Engineering disclaimer

Measurements To Record

  • Steam pressure, temperature and mass flow
  • Fuel flow and declared heating-value basis
  • Feedwater conditions and chemistry
  • Condensate return and blowdown measurements

Maintenance Checklist

  • Log pressure, water level, fuel and steam flow.
  • Maintain water-quality and blowdown records.
  • Plan steam-trap and insulation surveys.
  • Maintain statutory inspections and OEM safety-device tests.

Evidence-Based Diagnosis

Low steam pressure

Possible Causes
High demand; insufficient firing; distribution loss; control problem.
Evidence To Collect
Compare generator and header pressures, demand, fuel supply and alarm records.
Qualified Follow-Up
Have an authorised operator diagnose capacity and controls. Never bypass burner or boiler safety devices.

Wet steam or carryover

Possible Causes
Water-level instability; unsuitable chemistry; load fluctuations.
Evidence To Collect
Review level trends, chemistry and steam-quality observations with the boiler specialist.
Qualified Follow-Up
Correct confirmed causes through the approved operating procedure; do not make unapproved level-control changes.

High fuel use per unit steam

Possible Causes
Fouling; combustion inefficiency; losses; reduced condensate return.
Evidence To Collect
Compare fuel/steam measurements at similar loads and inspect the wider steam system.
Qualified Follow-Up
Prioritise verified losses and have qualified personnel assess combustion and heat-transfer performance.

Record The Confirmed Result

Keep the asset model, time, load, ambient conditions, alarm code and relevant readings together. Compare with the last healthy baseline. Record the confirmed cause, approved corrective action and readings after restoration; check that the improvement persists before closing the investigation.

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How It Works

  1. 1

    Feed water is pumped from deaerator into the boiler drum.

    Treated feed water is deaerated at 105 °C to strip oxygen and CO₂, dosed with oxygen scavenger and amines, then pumped by the multistage boiler feed pump through the economizer into the steam drum. Level is controlled by a three-element scheme (drum level + steam flow + feed flow) so swell and shrink during load changes do not trip the boiler.

  2. 2

    Fuel (gas/oil/solid) burns in the furnace, heating water in tubes.

    Fuel and combustion air mix at the burner (or on the grate) and burn in the furnace at 1200–1600 °C. Radiant heat passes to the water walls; the risers carry the steam-water mixture up to the drum while the downcomers return water, driving natural circulation. Flue gas O₂ is trimmed to 3–4 % — excess air cools the furnace and wastes fuel, too little makes CO and soot.

  3. 3

    Steam separates in drum; superheater raises temperature.

    Inside the drum, cyclone separators and chevron dryers separate water droplets from steam so that only dry saturated steam leaves. In a water-tube boiler it then passes through the superheater to 400–540 °C, with an attemperator (spray desuperheater) holding final temperature within ±5 K. Continuous blowdown from the drum controls dissolved solids and prevents carryover.

  4. 4

    Economizer preheats feed water using flue gas.

    The economizer recovers flue gas heat into the feed water, typically lifting it 40–70 K and adding 4–6 % to boiler efficiency. It is placed after the superheater where gas is cooler; skin temperature must stay above the acid dew point to avoid cold-end corrosion.

  5. 5

    Air preheater improves efficiency; ID/FD fans handle draft.

    The air preheater (tubular or regenerative) heats combustion air with the remaining flue gas, raising furnace temperature and efficiency by another 2–4 %. The FD fan supplies air, the ID fan maintains furnace draft slightly negative (−2 to −5 mm WC) so hot gas cannot puff out, and both are interlocked so the ID always leads.

Key Components

Burner / Grate
Combustion source

Gas/oil burner with pilot, flame scanner, air register and modulating fuel valve, or a solid-fuel grate/FBC bed. Purge and light-off sequence, flame failure trip and low/high fuel pressure trips are the mandatory burner management interlocks.

Steam Drum
Steam-water separation

Thick-walled pressure vessel holding the water/steam interface, internal cyclones and dryers, feed distribution pipe, chemical dosing line and continuous blowdown pipe. Two independent level gauges plus low-water trips — the low-water trip is the single most important protection on any boiler and must never be bypassed.

Water Walls & Tubes
Heat transfer surface

Membrane-welded tube panels forming the furnace enclosure, plus riser and downcomer circuits for natural circulation. Failures come from waterside scale (poor feed water), overheating and flue-side erosion; ultrasonic thickness surveys at every annual shutdown map the wear.

Superheater
Raises steam temperature

Convective and/or radiant tube banks that dry and heat steam above saturation, with an interstage spray attemperator for temperature control. Superheated steam raises turbine efficiency and prevents condensate erosion in long steam lines.

Economizer & APH
Heat recovery

Finned or bare-tube economizer for feedwater preheat, tubular or rotary (Ljungström) air preheater for combustion air. Together they typically pull stack temperature from 300 °C to 150–170 °C. Watch for cold-end corrosion and soot blocking — rising stack temperature is the alarm.

Deaerator
Removes O₂/CO₂ from feed

Spray/tray or spray-only vessel at 0.2 bar(g) / 105 °C that heats condensate with steam and vents non-condensables, cutting dissolved oxygen to <7 ppb before the chemical scavenger. Also acts as the feed water storage tank giving NPSH to the BFP.

Typical Operating Parameters

These reference ranges are illustrative context, not approved operating limits. Verify the installed model, duty, fuel or water conditions and applicable site requirements before use.

Pressure Range
10 – 110 bar
Feed Water pH
8.5 – 9.5
Blowdown
1 – 3 % of steam
Efficiency
82 – 92 %

Safety Notes

  • •IBR compliance mandatory (India).
  • •Test safety valves, level gauges & interlocks per schedule.
  • •Never bypass low-water trip.

Maintenance Schedule

  • •Daily: TDS, pH, hardness, blowdown log.
  • •Weekly: burner tuning, flue gas O₂/CO.
  • •Annual: hydro test, IBR inspection, tube thickness.

Problem Solving Matrix

Listed causes are hypotheses, not confirmed findings. Any corrective work requires qualified assessment, approved procedures and follow-up measurements.

IssueLikely causeFix
CarryoverHigh TDS / level swingBlowdown, tune level control
Low efficiencyExcess air / foulingTune burner, clean tubes

Equipment Running-Cost Estimate

Use measured electrical input, operating hours and your actual electricity tariff to estimate energy costs for steam generators. Compare replacement options before setting a project budget.

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