Cheat sheet
ASOPE Boiler Operator Cheat Sheet
Boiler Types and Construction
- Not published of exam
- Boiler Types Code Pressure Limits Drums + Heat Recovery BHP Conversions Refractory + Insulation Boiler Type Picker Firetube vs Watertube
Combustion, Fuels and Burners
- Not published of exam
- Combustion Air + Excess Air Flue Gas Readings Fuel Heating Values Burners + Draft Three T's Flue Gas Trim
Fittings, Valves and Controls
- Not published of exam
- Safety Valve Rules Low-Water Cutoff Tests Gauge Glass + Water Column Valves + Fittings Burner Management Timings Dangerous Condition Response Safety Valve vs Relief Valve
Water, Steam and Treatment
- Not published of exam
- Feedwater Chemistry Limits Blowdown + Cycles Steam Table Basics Water Treatment Equipment Water Problem Picker Scale vs Corrosion
Operation, Inspection and Licensing
- Not published of exam
- ASOPE License Facts Codes + Standards Electrical Basics Plant Safety + LOTO Which Code Applies CSD-1 vs NFPA 85
Quick Facts
- Exam ASOPE Third Class
- Format 50 multiple-choice questions
- Time 3 hours
- First Class time 4 hours
- Pass 70 percent minimum
- Fee $45 per attempt
- Renewal $38 each year
- Rules Closed book, formula sheet
- Calculator Non-programmable only
- Retest waits 30, 90, 120 days
- Third Class scope 500 BHP LP, 500 tons
- Weights Not published
Boiler Horsepower CO
- 1 BHP = 34.5 lb/hr = 33,475 Btu/hr
- From and at 212F About 9.8 kW Not shaft horsepower
Firetube vs Watertube CO
Firetube
- Gas inside tubes
- Large water volume
- Slower load response
Watertube
- Water inside tubes
- Small water volume
- Higher pressure, faster steaming
- Gas inside vs water inside
Boiler Type Picker CO
- Steam above 15 psig → Section I power boiler
- Steam at 15 psig → Section IV heating boiler
- Water 160 psig, 250F → Section IV hot water
- High pressure, fast steaming → Watertube design
- Steady load, more water → Firetube design
- High temperature, low pressure → Thermal fluid heater
- Full of water, circulated → Hydronic boiler
- Compact packaged unit → Scotch marine firetube
Boiler Types CO
- Firetube Gas inside, water outside
- Watertube Water inside, gas outside
- Scotch marine Packaged firetube, 2-4 passes
- Steam boiler Waterline with steam space
- Hydronic boiler Runs completely full
- Thermal fluid heater Hot oil, low pressure
- Electric boiler Elements or electrodes
- Cast iron sectional Bolted low-pressure heating sections
Power vs Heating Boiler CO
Power boiler
- Above 15 psig steam
- ASME Section I
- S stamp
Heating boiler
- 15 psig steam maximum
- ASME Section IV
- H stamp
- 15 psig draws the line
Code Pressure Limits CO
- Section IV steam 15 psig maximum Heating
- Section IV water 160 psig, 250F maximum
- Section I steam Above 15 psig Power
- MAWP Maximum allowable working pressure
- S stamp Section I power boiler
- H stamp Section IV heating boiler
- M and E stamps Miniature and electric boilers
- V and HV stamps Section I, Section IV valves
- Heating surface Fire-side area, square feet
- Over 500 sq ft Two valves, two feeds
Drums + Heat Recovery CO
- Steam drum Holds waterline, separates steam
- Mud drum Collects sludge, bottom blowdown
- Downcomer Cooler water descends
- Riser Steam and water ascend
- Economizer Flue gas preheats feedwater
- Superheater Adds heat above saturation
- Air preheater Warms incoming combustion air
- Furnace Where the fuel burns
BHP Conversions CO
- 1 BHP heat 33,475 Btu per hour
- 1 BHP steam 34.5 lb per hour
- 1 BHP power About 9.8 kW
- 1 ton cooling 12,000 Btu per hour
- 1 kW 3,412 Btu per hour
- 1 horsepower 746 watts
- 1 gallon water 8.33 pounds
- 1 cubic foot water 62.4 pounds, 7.48 gallons
- 1 psi head 2.31 feet of water
- Atmospheric pressure 14.7 psi, 29.92 inHg
Refractory + Insulation CO
- Refractory Heat-resistant furnace lining
- Castable Poured cement-like refractory
- Plastic refractory Rammed into place
- Insulating firebrick Light, low conductivity
- Spalling Cracking from thermal shock
- Dry-out Slow controlled first heat-up
- Hot spot Failed lining, hot casing
- Lagging Outer insulation jacket
Three T's CO
- Time, Temperature, Turbulence make complete combustion
- Time: residence Temperature: ignition Turbulence: mixing Miss one: carbon monoxide
Combustion Air + Excess Air CO
- Three T's Time, temperature, turbulence
- Stoichiometric air Exact theoretical air
- Excess air Air beyond theoretical
- Gas excess air About 10-15 percent
- Too little air Carbon monoxide, smoke, soot
- Too much air Heat lost up stack
- Complete combustion Carbon dioxide, water vapor
- Incomplete combustion CO, soot, unburned hydrocarbons
Flue Gas Trim CO
- Lowest oxygen that still shows zero CO
- Oxygen up: air up CO present: air short Never trim into CO
Flue Gas Readings CO
- Oxygen rising Excess air climbing
- Carbon dioxide falling Excess air climbing
- Any carbon monoxide Air starved, dangerous
- Trim target Lowest oxygen, zero CO
- High stack temperature Fouling or excess air
- Smoke spot Poor oil atomization
- Draft gauge Inches of water column
- Oxygen trim Automatic excess air control
Fuel Heating Values CO
- Natural gas About 1,000 Btu cubic foot
- Propane About 2,500 Btu cubic foot
- No. 2 oil About 140,000 Btu gallon
- No. 6 oil About 150,000 Btu gallon
- Bituminous coal About 12,000 Btu pound
- Flash point Vapors ignite momentarily
- Pour point Lowest temperature oil flows
- Viscosity Resistance to flow
- Heavy oil preheat Needed for proper atomization
Burners + Draft CO
- Atomizing burner Steam or air shears
- Pressure-atomizing burner Pump pressure, narrow turndown
- Turndown ratio Maximum to minimum firing
- Air register Directs and swirls air
- Natural draft Stack effect only
- Forced draft Fan pushes air in
- Induced draft Fan pulls gas out
- Balanced draft Both fans, slight vacuum
Low Water Response SA
- Secure fuel, never feed, cool, then inspect
- Fuel off first No cold water Cool slowly Inspect before restart
Safety Valve vs Relief Valve SA
Safety valve
- Steam service
- Pops fully open
- Steam heating boilers
Relief valve
- Liquid service
- Opens gradually
- Hot water boilers
- Steam pops, liquid creeps
Dangerous Condition Response SA
- No water in glass → Secure fuel now ( Never feed water )
- Level unproven or doubtful → Blow down the glass ( Try cocks confirm )
- Pressure above high limit → Secure fuel, check controls
- Safety valve lifting → Cut firing, find cause
- Flame failure lockout → Purge before relight ( Never bypass )
- Repeated lockouts → Stop, call service ( Never jumper interlocks )
- Tube leak suspected → Controlled shutdown, cool slowly
- Water hammer in line → Close valve, drain condensate
- Priming into steam line → Lower level, blow down
- Smoke or furnace puff → Secure fuel, purge fully
- Fuel gas odor → Secure fuel, ventilate, evacuate
Safety Valve Rules SA
- Safety valve Steam, pops full open
- Relief valve Liquid, opens gradually
- Safety relief valve Built for either service
- Lowest set pressure At or below MAWP
- Accumulation limit 6 percent over MAWP
- Shutoff valve ban None before or after
- Discharge piping Safe point, drained low
- Try lever test Proves valve still free
- Valve blowdown Pop minus reseat pressure
Cold Startup Order SA
- Water, vent open, low fire, vent closed
- Check level first Vent until steady steam Fire at low rate Heat metal slowly
Operating vs High-Limit Control SA
Operating control
- Cycles the burner
- Automatic reset
- Normal setpoint
High-limit control
- Backup trip only
- Manual reset
- Set above operating
- Auto reset vs manual
Low-Water Cutoff Tests SA
- Low-water fuel cutoff Stops burner on low
- Float type Float switch in chamber
- Probe type Conductivity through the water
- Blowdown test Flush float chamber routinely
- Slow drain test Lower level, watch trip
- Annual service Dismantle and inspect internals
- Auxiliary cutoff Second, manual reset device
- Top accident cause Low water, poor maintenance
Feed Line Order SA
- Pump, check valve, stop valve, boiler
- Check stops backflow Stop nearest boiler Service check under pressure
Gauge Glass + Water Column SA
- Gauge glass Shows actual water level
- Blow down glass At least once per shift
- Fast return Connections clear, level true
- Slow or no return Plugged line, false level
- False high level Classic dry-fire setup
- Two glasses Above 400 psi MAWP
- Remote indicators May replace one glass
- Try cocks Independent check on level
- Water column Chamber holding level devices
Valves + Fittings SA
- Gate valve Fully open or closed
- Globe valve Throttles, flow under seat
- Check valve Prevents reverse flow
- Feed line order Pump, check, stop, boiler
- Two stop valves Shared header requirement
- Free-blow drain Proves outboard valve holding
- Steam trap Drains condensate, holds steam
- Nonreturn valve Automatic stop-check on header
Burner Management Timings SA
- Flame failure response 4 seconds maximum
- NFPA 85 valve closure Within 1 second
- CSD-1 valve closure Within 5 seconds
- CSD-1 purge At least 4 air changes
- NFPA 85 purge 8 watertube, 4 firetube
- Purge airflow 70 percent full-load minimum
- Post-purge Clears fuel after shutdown
- Interlock string Wired in series
- Operating control Automatic reset, cycles burner
- High-limit control Manual reset backup trip
Priming vs Carryover WA
Priming
- Sudden water slugs
- High level or surge
- Mechanical cause
Carryover
- Any water leaving
- Includes foaming
- Umbrella term
- Priming is one carryover
Water Problem Picker WA
- Hard white deposits → Scale, soften feedwater
- Pits and tubercles → Oxygen corrosion, deaerate
- Rusty water in glass → Acid corrosion, raise pH
- Grooved condensate pipe bottom → Carbonic acid, dealkalize
- Stable foam on surface → High solids, blow down
- Water slugs into header → Priming, lower level
- TDS climbing steadily → Increase surface blowdown
- Sludge in mud drum → Bottom blowdown
Feedwater Chemistry Limits WA
- Boiler water pH Maintain about 11 NB-410
- Condensate pH 7.5 to 8.5 NB-410
- Carbonic acid pH 6.9 down to 4.4
- TDS rule of thumb About 1,000 ppm maximum
- Hardness Dissolved calcium and magnesium
- Oxygen at 70F About 8.6 ppm
- Oxygen at 150F About 4.3 ppm
- Oxygen at 212F About zero ppm
- Deaerator outlet About 0.005 cc per liter
- Oxygen scavenger Sodium sulfite catches traces
Scale vs Corrosion WA
Scale
- Hardness deposits
- Insulates and overheats
- Fix by softening
Corrosion
- Oxygen and acid
- Pits and tubercles
- Fix by deaerating
- Deposit adds, corrosion removes
Blowdown + Cycles WA
- Bottom blowdown Short dump, clears sludge
- Surface blowdown Continuous, controls dissolved solids
- Cycles of concentration Boiler TDS over feedwater
- 200 ppm feedwater Five cycles reaches 1,000
- 25 ppm feedwater Forty cycles reaches 1,000
- Blowdown percent 100 divided by cycles
- Excess blowdown Wastes heat and chemicals
- Blowdown tank Cools and vents discharge
Bottom vs Continuous Blowdown WA
Bottom blowdown
- Short intermittent dump
- Lowest point or drum
- Removes settled sludge
Continuous blowdown
- Steady surface draw
- Just below waterline
- Controls dissolved solids
- Sludge below, solids surface
Steam Table Basics WA
- Sensible heat Changes temperature only
- Latent heat Changes state only
- 32F to 212F 180 Btu per pound
- Latent at 212F About 970 Btu pound
- Total heat 0 psig About 1,150 Btu pound
- Saturation 15 psig About 250F
- Saturation 100 psig About 338F
- Saturation 150 psig About 366F
- Steam expansion About 1,600 times volume
- Superheat Heat above saturation temperature
Water Treatment Equipment WA
- Zeolite softener Swaps hardness for sodium
- Brine regeneration Restores resin exchange capacity
- Dealkalizer Cuts alkalinity, carbon dioxide
- Reverse osmosis Membrane strips dissolved solids
- Deaerator Heats and vents gases
- Feedwater tank Stores condensate and makeup
- Chemical feed pump Doses treatment continuously
- Condensate return Cuts makeup and fuel
CSD-1 vs NFPA 85 LI
CSD-1
- Below 12.5 MMBtu input
- Automatically fired boilers
- 4 air changes purge
NFPA 85
- 12.5 MMBtu and above
- Larger fired units
- 8 air changes, watertube
- Fuel input picks code
Which Code Applies LI
- Power boiler construction → ASME Section I
- Heating boiler construction → ASME Section IV
- Auto-fired below 12.5 MMBtu → ASME CSD-1
- 12.5 MMBtu and above → NFPA 85
- Inservice repair or alteration → NBIC
- Worker safety in plant → OSHA general industry
- License to operate → ASOPE or local board
Codes + Standards LI
- ASME Section I Power boiler construction
- ASME Section IV Heating boiler construction
- ASME CSD-1 Auto-fired below 12.5 MMBtu
- NFPA 85 12.5 MMBtu input and above
- NBIC Inservice inspection and repair
- NBIC parts Installation, inspection, repairs, valves
- OSHA General industry safety
- Jurisdiction State or city board
ASOPE License Facts LI
- Third Class scope 500 BHP low pressure, 500 tons
- Exam length 50 multiple-choice questions
- Third Class time 3 hours
- First Class time 4 hours
- Pass mark 70 percent minimum
- Exam fee $45 per attempt
- Annual renewal $38 per year
- Age and school 18, diploma or GED
- Training required 6 months or 3 credits
- Retest waits 30, 90, 120 days
- Result reported Pass or fail only
- Curriculum list 19 minimum topics published
Electrical Basics LI
- Ohm's law Volts equal amps times ohms
- Current Volts divided by ohms
- Power Watts equal volts times amps
- Series circuit One path, all close
- Parallel circuit Many paths, same voltage
- Interlock string Any open contact trips
- Motor starter Contactor plus overload relay
- Fuse or breaker Protects conductors from overload
Plant Safety + LOTO LI
- Lockout/tagout Isolate, lock, tag, verify
- Energy sources Fuel, electric, steam, feedwater
- Personal lock Only the owner removes
- Confined space Permit required for drums
- Blanking Blind off connected lines
- Atmosphere test Oxygen, flammables, toxics
- Attendant Outside with rescue means
- PPE Gloves, glasses, hearing protection
Common Traps
Safety valve vs relief valve
- Safety pops on steam ≠ Relief creeps on liquid
Section I vs Section IV
- Section I above 15 psig ≠ Section IV 15 psig maximum
Bottom vs surface blowdown
- Bottom clears settled sludge ≠ Surface controls dissolved solids
Priming vs foaming
- Priming is level surge ≠ Foaming is dissolved solids
Never feed a dry boiler
- Cold water cracks metal ≠ Secure fuel and cool
CSD-1 vs NFPA 85
- CSD-1 below 12.5 MMBtu ≠ NFPA 85 at 12.5 up
Boiler horsepower is not shaft
- BHP is 33,475 Btu ≠ Shaft hp is 2,545 Btu
Scale is not corrosion
- Scale insulates and overheats ≠ Corrosion pits and thins
Gate valve never throttles
- Gate: open or closed ≠ Globe: throttles the flow
Last Minute
- 1. Section IV steam: 15 psig
- 2. Section IV water: 160 psig, 250F
- 3. Section I: above 15 psig
- 4. Over 500 sq ft: two valves
- 5. Accumulation: never over 6 percent
- 6. Two gauge glasses above 400 psi
- 7. Flame failure 4 seconds, close 1
- 8. Purge: 70 percent airflow minimum
- 9. 1 BHP = 34.5 lb, 33,475 Btu
- 10. Low water: secure fuel, never feed
- 11. Boiler water pH 11; condensate 7.5-8.5
- 12. TDS rule of thumb: 1,000 ppm
- 13. CSD-1 below 12.5 MMBtu; NFPA above
- 14. ASOPE: 50 questions, 70 percent
- 15. Third Class: 500 BHP, 500 tons
- 16. Retest: 30, 90, 120 days
ASOPE Boiler Operator
- Practice Questions 145 questions Study Guide 33 topics Cheat Sheet 193 facts Flashcards 50 cards Shorts 1 short 1 Job Wiki Free CE Podcast